ANN - A Executive Summary in English…………………………………………………. I to XX
ANN - B Executive Summary in Gujarati…………………………………………………. XXI to XLIII
ANN – C Accreditation Certificate ………………………………………………………… XLIV to XLVIII
CHAPTER-1
PREAMBLE 1-31
1.1 Preamble.................................................................................... 01 1.2 Identification of Project and Project Proponent………………………. 01 1.3 Objective of EIA Study………………………………………………….. 03 1.4 Location ……………………………………………………………………. 04 1.5 Study Area…………………………………………………………………. 11 1.6 Nearest Location from the Project Site……………………………… 11 1.7 Scope and methodology of EIA………………………………………. 12 1.8 Structure of EIA…………………………………………………………… 15 1.9 Compliance of TOR……………………………………………………… 17 1.10 Regulatory Frame work………………………………………………….. 29 1.11 Photographs of the Existing & Proposed Plant Site 30
CHAPTER – 2 PROJECT DESCRIPTION
32-205
2.1 Prelude…………………………………………………………………………….. 32 2.2 Location……………………………………………………………………………. 32 2.3 Justification of Proposed Activity……………………………………………… 33 2.4 Promoters and their background……………………………………………….. 33 2.5 Infrastructure Facilities ………………………………………………… 34 2.6 Land Use Breakup for Total Plot Area………………………………. 35 2.7 Product Details…………………………………………………………… 36 2.8 Packing & Final Application of Products………………………….. 38 2.9 Raw material Requirements……………………………………………. 39 2.10 Chemical Name, Physical form of Raw Materials…………………. 55 2.11 Physical and Chemical properties of the Hazardous Raw material 59 2.12 Manufacturing Process, Mass balance & Chemical Reaction… 64 2.13 Plant water Requirement & Waste Water generation……………… 164 2.14 Characteristics of effluent……………………………………………… 169 2.15 Details of Effluent Treatment Plant…………………………………. 170 2.16 Flue Gas Emission…………………………………………………………….. 171 2.17 Process Gas Emission………………………………………………………… 173 2.18 Fuel Requirement…………………………………………………………....... 173 2.19 Fugitive Emission Control……………………………………………………… 174 2.20 Hazardous waste management…………………………… 174 2.21 Noise Pollution…………………………………………………………….. 177
2.22 List of Hazardous Chemicals……………………………………………. 178 2.23 Safety & Occupational measure for storage & handling of the Raw Material
& product………………………………………………………… 186
2.24 Action Plan for Transportation of Raw Material & product including hazardous Chemicals…………………………………………………………
191
2.25 Details Of Fire Fighting Equipments…………………………………….. 192 2.26 Cost of project…………………………………………………................ 192 2.27 Power Requirement……………………………………………………….. 193 2.28 Man Power Details………………………………………………………… 194 2.29 Green Belt Development………………………………………………..... 194 2.30 Scheme for Rain water Harvesting……………………………………… 195 2.31 Solvent Recovery System……………………………………………….. 202
CHAPTER – 3 BASELINE ENVIRONMENTAL STATUS
206-299
3.1 Introduction .................................................................... 206 3.2 Study Area........................................................................ 206 3.3 Environmental Standards Of The Region................................ 211 3.4 Air Environment…………………………………………………………… 211
3.4.1 Ambient Air Quality (Aaq) In The Study Area 211 3.4.1.1 The Location Of Aaq Stations 212 3.4.1.2 Base Line Data 212 3.4.1.3 Sample Analysis 223
10.6 Greenbelt Development…………………………………… 446 10.7 Health and Safety………………………………………….. 450 10.8 Occupational health hazards…………………………….. 450 10.9 Details Of Occupational Health Surveillance………….. 457
10.10 Hazardous Identification And Preventive Measures… 458 10.11 Expenditure On Environmental Matters………………… 467 10.12 Concept Of Waste Minimization, Recycle / Reuse / Recover
Techniques, Energy Conservation And Natural Resources Conservation…………………………………………………
468
10.13 Checklist In The Form Of Do’s And Don’t ……………. 470 10.14 Socio Economic Development Activity………………… 473 10.15 Infrastructure Facilities To The Labours During Construction Phase 473 10.16 Odour Control Measures…………………………………… 474
CHAPTER –11 SUMMARY OF ENVIONMETAL IMPACTS AND CONCLUSION
476-480
11.1 Salient Features of The Project…………………………….. 476 11.2 Air Environment……………………………………………….. 478 11.3 Water Environment……………………………………………. 478 11.4 Noise Environment……………………………………………. 478 11.5 Hazardous wastes…………………………………………….. 479 11.6 Ecology………………………………………………………….. 479 11.7 Socio Economic Environment……………………………….. 479 11.8 Land Use………………………………………………………… 479 11.9 Topography…………………………………………………….. 480
CHAPTER - 1 1.1 Map of Gujarat State……................................................. 05 1.2 Map of Gandhinagar District.................................................. 06 1.3 5 Km & 10 KM radius Map of the project site…………………. 07 1.4 Plant Layout ……………………………………………………………. 08 1.5 Goggle Image of M/s. BHIMANI DYECHEM INDUSTIRES 09 1.6 Topography map of M/s. BHIMANI DYECHEM INDUSTIRES 10 1.7 Methodology of EIA study………………………………………… 14
CHAPTER-2
2.1. Water Balance Diagram................................................. 168 2.2 Effluent Treatment Plant Flow Diagram..................................... 170 2.3 Fire Hydrant Diagram………………………………………………….. 189 2.4 Systematic Design of the RW harvesting structure……. 199 2.5 Solvent Recovery System……………………………………… 205
CHAPTER -3
3.1 Study Area Map of Base line Study for 5 KM Radius and 10 KM Radius in Google Map………………………………………………..
208
3.2 Study Area Map of Base line Study for 5 KM Radius and 10 KM Radius with Topo Sheet No…………………………………………….
209
3.3 Sampling Location Map…………………………………………………….. 210 3.4 Wind Rose Diagram...................................................... 225 3.5 Wind Class Frequency Distribution……………………………… 228 3.6 Geological Structure of Gujarat State................................ 250 3.7 Land use / land cover map of 10 km radius area around project site… 258 3.8 Forest Vegetation map of Gujarat…………………………………………. 269 3.9 National park and Sanctuaries of Gujarat………………………………… 269
3.10 Population Details…………………………………………. 278 3.11 Literacy details……………………………………………….. 278 3.12 Employment pattern……………………………………………. 282 3.13 Main Worker Employment pattern……………………………… 282
CHAPTER - 4
4.1 Isopleths of SPM..................................................................... 326 4.2 Isopleths of SO2……………………………………………………….. 327 4.3 Isopleths of NOx……………………………………………………….. 328 4.4 Isopleths of HCl……………………………………………………….. 329 4.5 Isopleths of NH3……………………………………………………….. 330
10.2 Schematic Diagram of Proposed Waste Water Treatment- ZLD System
441
TABLES
TABLE NO. TOPICS PAGE NO.
CHAPTER –1
1.1 Nearest locations from the Project Site.................................... 11 1.2 Nearest Industries from the project Site…………………………... 12 1.3 Compliance of Terms of Reference……………………………….. 17
CHAPTER –2
2.1 Location of the project site………………………………………….......... 32 2.2 Details of Sources…………………………………………………………. 34 2.3 List of plant machinery for proposed project………………………… 34 2.4 Land use breakup for total Plot area…………………………………….. 35 2.5 List of Product with Chemical name and QTY …………………… 36 2.6 Packing & Final Application of Products………………………………… 38 2.7 Details of Raw Material …………………………………………………… 39 2.8 Details of water consumption & Wastewater Generation……………… 164 2.9 Product wise water consumption & Effluent Generation……………….. 165
2.10 Characteristics of Industrial Effluent……………………………………… 169 2.11 Details of Proposed Effluent Treatment Plant Units………………… 170 2.12 Flue gas Stack details……………………………………………………. 171 2.13 Emission Rate of Pollutants……………………………………………… 172 2.14 Process Gas stack Details………………………………………………. 173 2.15 Fuel Details…………………………………………………………. 173 2.16 Details of Hazardous waste………………………………………. 174 2.17 Typical Noise level of equipment………………………………. 177 2.18 List of Hazardous chemicals………………………………….. 178 2.19 Details of fire and Safety Equipment…………………………. 188 2.20 Antidotes of Chemicals…………………………………………. 190 2.21 Capital Cost & Recurring cost of the project……………………….. 192 2.22 Power Requirement…………………………………………………… 193 2.23 Details of Man Power…………………………………………… 194 2.24 Details of Solvent Recovery System…………………………………. 203
CHAPTER – 3
3.1 Name of villages in the study area……………………………… 206 3.2 Location of ambient air quality monitoring stations…………. 212
3.3 Ambient Air quality Results (Min, Max, Avg and 98%) for Individual Locations………………………………………………….
213
3.4 Ambient Air Quality Analysis Report ……………………………… 215 3.5 Details of Ambient Air quality monitoring and analysis
procedure……………………………………………………. 223
3.6 Wind Rose Frequency Distribution…………………………… 226 3.7 Wind Rose Frequently Count……………………………………… 227 3.8 Relative Humidity – Project Site Meteorology data ………… 229 3.9 Rainfall pattern at Gandhinagar Rain gauge Station 230
3.10 Hourly mixing depth over Indian Region…………………….. 231 3.11 Ambient Noise Levels within Study Area…………………… 233 3.12 Noise Level in the study area…………………………… 235 3.13 Location of water quality monitoring station………………... 244 3.14 Water quality Analysis………………………………………….. 246 3.15 Analysis Results of Soil Sample……………………………………. 252 3.16 Standard Soil Classification……………………………………… 255 3.17 Landuse distribution in study area (10 Km Radial Zone) ……. 257 3.18 Hydro geological Characteristics of the Aquifers 261 3.19 List of Commonly found flora in the study area……………….. 263 3.20 Bird species reported during the study……………………… 265 3.21 Mammals species reported during the study…………………….. 267 3.22 Population Details…………………………………………………… 275 3.23 Literacy Details………………………………………………………. 279 3.24 Employment pattern and Main worker Employment pattern….. 284 3.25 Main worker Employment pattern………………………………… 286 3.26 Availability of basic Amenities Activities………………………… 289 3.27 Main Commodities in the Study Area…………………………… 293 3.28 Name of village for survey in the Study Area………………… 297
CHAPTER -4
4.1 Impact identification matrix………………………………………… 303 4.2 Impact Prediction Matrix……………………………………………. 304 4.3 Basis of Emission Rate calculations…………………………….. 308 4.4 Maximum Computed Ground Level Concentration……………. 312 4.5 Cumulative Conc. Due to Incremental GLC’s………………… 313 4.6 The 1st highest 24 Hr average Concentration values of
SPM………………………………………………………………… 316
4.7 The 1st highest 24 Hr average Concentration values of SOx……………………………………………………………………….
318
4.8 The 1st highest 24 Hr average Concentration values of NO2……………………………………………………………………….
320
4.9 The 1st highest 24 Hr average Concentration values of NH3……………………………………………………………………….
322
4.10 The 1st highest 24 Hr average Concentration values of HCl ……………………………………………………………………….
324
4.11 Total Water Requirement for Proposed Project………………… 333 4.12 Total Waste Water Generation………………………………… 333 4.13 Solid/Hazardous Waste Generation and Disposal MODE 335 4.14 Traffic study………………………………………………………….. 346 4.15 Assessment of Proposed Traffic Load………………………… 346
10.1 Budgetary Expenditure for GBD 449 10.2 Plant Species for Green Belt Development 449 10.3 Details of Fire Extinguisher 454 10.4 Details of Fire water pump 454 10.5 Details of provision for fire-fighting system 454 10.6 Expenditure on Environmental Matters 457
ANNEXURES
ANNEXURE
NO. Topics
Page No.
1. APPROVED TOR FOR EIA STUDY FROM MOEF&CC, NEW DELHI. 483
2. RISK ASSESMENT STUDY REPORT………………………………… 492
3. NATIONAL AMBIENT AIR QUALITY STANDARDS……………………….. 601
4. ICMR STANDARD FOR DRINKING WATER………………………………. 603
5. NATIONAL AMBIENT NOISE QUALITY STANDARDS AND OSHA’S PERMISSIBLE LIMIT FOR NOISE………………………………………….. 604
6. LAND SUPPORTING DOCUMENTS……………………………………….. 605
7. UNDERTAKING OF M/S. BHIMANI DYECHEM INDUSTIRES……. 618
8. UNDERTAKING OF BECPL…………………………………………………. 619
9. MEMEBRSHIP CERTIFICAT……………………………………………. 620
10. MATERIAL SAFETY DATA SHEET……………………………………….. 621
11. ADEQUACY REPORT OF SCHEDULE II………………………………… 890
M/s. BHIMANI DYECHEM INDUSTRIES Proposed to start Dyes and dyes intermediates manufacturing unit at Plot No.:2, Survey No. 316, Opp. Dharti industries Estate, At: Dhanot, Tal: Kalol, Dist.: Gandhinagar, Gujarat. In their proposed unit, they will manufacture Synthetic Organic Chemical (Dyes and dyes intermediates) @ 225 MT/M. The proposed project cost is about Rs. 4.50 Crore. As per the EIA Notification S.O. 1533 dated 14th September 2006 and its amendments from time to time, by Ministry of Environment , Forest & Climate Change (MoEF &CC), Government of India, their Proposed manufacturing activity is falls under Synthetic Organic Chemicals – Schedule 5(f)) & cat -A. For that unit needs Environmental clearance from Ministry of Environment, forest and climate change. The industry engaged the services of Bhagwati Enviro care Pvt. Ltd., Ahmedabad to prepare and submit the necessary documents. The consulting firm has submitted an application in prescribed FORM-I along with necessary enclosures for obtaining Terms of Reference to Ministry of Environment, forest and climate change, on dated 22/10/2018. The Ministry of Environment, forest and climate change has given Terms of Reference vide Ref No. IA-J-11011/349/2018-IA-II(I) Dated on 29-11-2018, to carryout EIA Study. The Environmental monitoring and analysis were carried out by Bhagwati Enviro care Pvt. ltd. (Having NABL Accreditation and MoEF&CC Registration) during the period of March –April – May 2018 and Final EIA Report was prepared and submitted for Public Consultation.
Total plot area is 3344 Sq. meter. From that they will do gardening and plantation for 1105 Sq. Meter which is 33 % of the total plot area.
2. SALIENT FEATURE OF THE PROJECT:- 1. Name of project : M/s. BHIMANI DYECHEM INDUSTRIES 2. Location : Plot No.:2, Survey No. 316, Opp. Dharti
3. Latitude & Longitude : 23° 17' 14.1684'' N (23.287269) 72° 25' 1.0704''E (72.416964)
4. Existing / Proposed : Proposed Unit 5. Schedule & category of Unit : Schedule – 5(f), Cat: A 6. Type of Unit : Dyes and dyes intermediates Unit 7. Land acquired for the plant : 3344 Sq. meter 8. Green belt Area : 1105 Sq. meter (33 % of the total Plot Area) 9. Project Cost : 450 lac 10. Capital Cost of the project : 99.5 lac 11. Recurring cost of the project : 369.9 lac 12. CSR Budget : 2.25 lac per Year (11.25 lac for 05 Yr)
i Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
13. CER Budget : 1.8 Lac per Year (9.0 lac for 05 yr) 14. Man Power Requirement : 40 Nos. 15. Source of Electricity & Power
Requirement : UGVCL (Uttar Gujarat Vij Co. Ltd.)
75 KVA 16. Total No. of Product and Qty : 51 Products, 225 MT /M 17. Types of Solvents to be used : Benzene, TNBA, Methanol, ODCB, Butanol 18. Source of Water : Water Tanker 19. Total Water requirement : 85 KLPD
: 44.5 KLPD industrial effluent will be treated in In-house primary Effluent treatment plant and finally it will be sent to Chhatral Environment Management Systems Pvt. ltd. For Spray drying to achieve ZLD.
22. Domestic Effluent generation & Disposal
: 5.0 KLPD to Soak Pit System
23. No. of flue gas stacks : 1. Steam Boiler-1 – 3 MT (Stack height- 30 m)
2. Steam Boiler-2 – 3 MT (Stack height- 30 m)
3. Hot air generator- 10 Lac K cal (Stack height -30 m)
4. DG set – 125 KVA (Stack height -11 m) 24. Air Pollution Control System
Attached to flue gas stacks : Multi Cyclone Dust Collector followed by bag
filter attached to Steam Boiler and Hot air generator separately.
25. No. of Process gas stacks : 1. Stack attached To reaction vessel of N.W Acid – (Stack height- 11 m)
2. Stack attached To reaction vessel of N.W Acid – (Stack height- 11 m)
3. Stack attached To reaction vessel of K Acid – (Stack height- 11 m)
4. Stack attached To reaction vessel of K Acid – (Stack height- 11 m)
5. Stack attached To reaction vessel of Direct blue 86 – (Stack height- 11 m)
6. Stack attached To reaction vessel of Reactive Blue G – (Stack height- 11 m)
7. Stack attached To Spray dryer – (Stack height- 11 m)
26. Type of process gas emission : Ammonia, HCl,SO2,SPM
ii Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
Group 2. Dyes (Alternative Production) Reactive Dyes 120 1. Reactive Black 8/HN Reactive Black 8 12225-26-2 2. Reactive Black WNN
/ Black Mix Black CNN ----
3. Reactive Black 5/B Remazol Black GF 17095-24-8 4. Reactive Blue 222/BF Reactive Blue FBN 93051-44-6 5. Reactive Blue 194/
Navy Blue ME2GL Reactive Blue M-2GE 93050-78-3
6. Reactive Orange 12/Golden Yellow HR
Reactive orange 12 35642-64-9
7. Reactive Orange 13/H2R
Reactive Orange 13 12225-85-3
8. Reactive Yellow 15/GR
Reactive Yellow GR 12226-47-0
9. Reactive Yellow 18/H4G
Reactive Yellow 18 12226-48-1
10. Reactive Yellow 42/FG
Reactive Yellow 42 12226-63-0
11. Reactive Yellow 145/Golden Yellow MERL
Reactive Yellow 145 93050-80-7
12. Reactive Yellow 160/ME4GL
Reactive Yellow 160 129898-77-7
13. Reactive Red 195/ ME4BL
Reactive Red 195 93050-79-4
14. Reactive Red 198/ RB Reactive Red 198 145017-98-7 15. Reactive Turquoise
Blue 21/G Reactive Turquoise Blue 21 12236-86-1
16. Reactive Orange 122/ ME2RL
Reactive Orange 122 12220-12-1
2. Direct Dyes 1. Direct Black 22/ VSF Direct Black 22 6473-13-8 2. Direct Red 31/ 12B Direct Red 31 5001-72-9 3. Direct Orange 39 Direct Orange 39 1325-54-8 4. Direct Yellow 86 Direct Yellow 86 50925-42-3 5. Direct Yellow 11/
Paper Yellow R Direct Yellow 11 1325-37-7
6. Direct Violet 9/ BRILL Direct Violet 9 6227-14-1
4. WATER CONSUMPTION & WASTEWATER GENERATION/ DISPOSAL
Table: 02 Water Consumption and Wastewater Generation:
• Total Water consumption will be 85 KLPD. From which 5 KLPD for Domestic Purpose, 2
KLPD for Gardening purpose & 78 KLPD for Industrial Purpose.
• Total Waste water generation will be 49.5 KLPD. From which 5 KLPD domestic waste water will goes to soak pit via septic tank. 44.5 KLPD waste water will generate from industrial purpose activity.
• Total waste water generated from industrial activity will treat in Effluent treatment plant with primary treatment and then it will send to Common Spry Dryer (Chhatral Enviro management System Pvt. Ltd.) to achieve zero discharge.
Application Water Consumption
(KL/Day)
Waste water generation (KL/Day)
Domestic 5 5 Gardening 2 0 Industrial Process 27 30 Washing 10 10 Boiler 30 3 Cooling 5 0.5 Scrubber 6 1 Total (C) 78 44.5 Total (A+B+C) 85 49.5
vii Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
1. ENVIRONMENTAL PARAMETER MONITORING STUDY AREA/ STUDY PERIOD
The study area for detailed studies is an area within a radius of 10 Kms. Ambient air quality monitoring were carried out at 08 locations within the study area of 10 km aerial coverage from project site as the Center. The ground water monitoring, noise level monitoring, Soil analysis were carried out at 08 location for once in the study period. The monitoring activities were carried out at 08 sampling sites for the Month of March 2018 – May 2018.
2. AIR ENVIRONMENT
Baseline study indicates that AAQ in the surrounding study area with respect to PM2.5, PM10, SO2, NOX, and VOC are well within the stipulated permissible limits as prescribed by the latest National Ambient Air Quality (NAAQ) Standards for the respective industrial residential rural areas.
Maximum evaluated 24 hourly GLC from the ISCST-3, when added to the 98-percentile concentration of each parameter monitored during March 2018 – May 2018 season of the ambient air it indicates that due to Proposed project of M/s. BHIMANI DYECHEM INDUSTRIES., ambient air quality of the surrounding study area will be well within the NAAQ standards for the respective Industrial, residential rural areas. Company will use Coal/ lignite/ agro wastee/ Diesel as a fuel. There will be process gas emission from process Reaction as mention in table no.5 which is SO2, NH3 and HCl. For that unit will provide adequate Air Pollution Control System.
It is concluded that there will be no long term impacts on the surrounding ambient air environment.
3. WATER ENVIRONMENT
M/s. BHIMANI DYECHEM INDUSTRIES is a proposed unit and the source of water for proposed activity will be Tanker. Water Consumption and Wastewater Generation &Disposal:
• Total Water consumption will be 85 KLPD. From which 5 KLPD for Domestic Purpose, 2 KLPD for Gardening purpose & 78 KLPD for Industrial Purpose.
• Total Waste water generation will be 49.5 KLPD. From which 5 KLPD domestic waste water will be goes to soak pit via septic tank. 44.5 KLPD waste water will generate from industrial purpose activity.
Total waste water generated from industrial activity will treat in Effluent treatment plant
with primary treatment and then it will be sent to Common Spray Dryer to achieve zero
discharge.
xi Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
Base line data indicates that noise levels in the ambient air environment are within the prescribed norms. The industry will provide adequate noise control measures such as mufflers & silencers at the air inlet/outlet, anti vibration pad for equipment with have extreme vibration etc. Ear plugs & ear muffs will be provided to the workers where noise level will remain extremely high. Thus, there will be short term, reversible impact on the noise environment due to the proposed project. 5. LAND ENVIRONMENT
Air pollution, water pollution and solid waste pollute soil and causes direct/indirect effect on soil. Since all necessary air pollution control measures have been provided and based on the results of the dispersion model for the ground level concentration of various pollutants after the commissioning of the Proposed Project, there will not be any adverse impact of air pollution on soil. All necessary control measures will be provided for handling, storage and safe disposal of solid/hazardous waste, which will be generated from the proposed project. Thus, there will not be any significant impact of solid waste on the soil Environment.
6. ECOLOGY
Impacts on terrestrial ecosystem due to the operation of plant occur mainly from air emissions. Air pollutants can impact adversely on the biotic and abiotic components of the ecosystem and may include injurious effects when concentration of these pollutants exceed from permissible limit. The unit will provide appropriate APCM to control air pollution, so, there will be no adverse impact on the ecological environment of the study area. Total plot area is 3344 Sq. meter. From that they will do proposed gardening and plantation for 1105 Sq. meter. So, after expansion total area for gardening and plantation will be 1105 Sq. Meter i.e. 33.00 % of the total Plot Area.
The company will also develop plantation as per the MoEF guidelines all along the periphery of plant so that these trees perform as natural barrier for bring down the fugitive emission and also stop carryover of dust along with wind current.
xii Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
7. SOCIO-ECONOMIC ENVIRONMENT Due to Proposed project, 20 nos. of local people and outside people will get employment during the construction phase and 40 people will be employed during the operation phase.
The indirect employment will also be generated by way of transportation, shopkeepers and other casual employment for many people. Thus, the proposed project will have long term- irreversible positive impact on the employment pattern of the study area. 8. ENVIRONMENTAL PARAMETER MONITORING
Environmental parameter monitoring facility of the proposed project is as given below:
Sr. No. Aspect Source of Impact
Monitoring Method and it’s Parameters
Frequency Executing Agency
Monitoring Agency
1.0 Construction Phase (As the construction area is small so, steel structure will be used in the existing unit, hence the impact will be very less)
1.1 Local Manpower Absorption
Construction Work
Contractor’s report No. of people working in the project
Daily Contractor BHIMANI DYECHEM INDUSTRIES
1.2 Air Quality transportation of construction materials
Survey & observations; Levels of SPM, RSPM, SO2 and NOx
Weekly BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
1.3 Public Health Dust, Noise, Movement of labours
Regular medical checkup
Monthly Contractors BHIMANI DYECHEM INDUSTRIES
2.0 Operation Phase 2.1 Water Quality
& Quantity Surface & Ground water quality within the Project Area
Surveys, sample collection & field measurement;
Quarterly BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
2.2 Effluent Quality
Quality of Treated effluent Send to common spray drying facility.
ETP sample collection & quality analysis
Daily (Internal); Monthly (Third Party)
BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
xiii Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
Generation of spent Acid (40-45 %) from manufacturing process.
Maintain Records Daily BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
Generation of Glauber Salt from manufacturing process.
Maintain Records Daily BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
Generation of Dilute HCl (25%) from manufacturing process.
Maintain Records Daily BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
Generation of Sodium Bi Sulphite (28%) from manufacturing process.
Maintain Records Daily BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
Generation of Ammonium Hydroxide (25%) from manufacturing process.
Maintain Records Daily BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
Generation of Distillation Residue from manufacturing process.
Maintain Records Daily BHIMANI DYECHEM INDUSTRIES
GPCB/ Recognized Env. Agency
9. ADDITIONAL STUDIES
We have carried out socio-economic study of the study area to evaluate impact of proposed project on them. Since the Proposed project is a large scale unit so, it is beneficial to local people. We have carried out Risk Assessment report for Chloro Sulfonic Acid, Hydrochloric Acid, Sulphuric Acid, Ammonia, Acetic Anhydride, Oleum (65%), Sodium Hydroxide, Aniline, Acetic Acid, Alpha Naphthylamine, Methyl Alcohol, Formaldehyde, Benzene, ethyl acetate, PCl3 and Butanol. Detailed possible accident scenarios of that chemical is described in Risk Assessment Report (Annexure- 02 of EIA report).
xv Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
The environmental management plan is the plan for effective environmental management prepared by project proponents. Environmental Management Plan of the company is given in the following table:
OPERATIONAL PHASE:
M/s. BHIMANI DYECHEM INDUSTRIES has planned all the necessary steps to control Water Pollution, Air Pollution, noise pollution as well as Hazardous Waste Pollution. The detailed mitigation measures planned during operation phase of the project are as follows:
Activity Environmental Impacts
Mitigation measures Remarks
Manufacturing of Products
• Air • Land • Water • Noise
• Ensure proper handling of all chemical by introducing spill control procedures.
• Ensure usages of PPE’s by workers.
• Strictly following the appropriate spill control procedures.
• The charging of the hazardous chemical will be done through very carefully.
Proposed Budget For Environmental Management Plan [EMP]
Sr. No
System Approximate recurring cost
per annum (in Lac)
Approximate capital cost (Rs. In Lac)
Basis for cost estimates
1 Air pollution control
12.0 45.0 The capital cost would include cost of providing adequate height of the stack, ladder and platform, Air Pollution Control Systems and recurring cost would include cost of monitoring of air environment.
2 Water pollution control
335 40 Capital cost would include cost of ETP, Evaporation cost of Spray Drying etc. In capital cost civil work, mechanical work, Electrical work and piping work is included. Recurring cost is for operational phase.
3 Noise pollution monitoring
0.25 0.0 The recurring cost would include cost of noise monitoring.
4 Solid and hazardous waste management
15.0 12.0 Capital cost would include cost of providing storage space for hazardous waste and membership of TSDF Fee. Recurring cost would include cost of land filling and transportation.
5 Environment monitoring and management
2.0 0.0 The recurring cost would be incurred on hiring of consultants and payment of various statutory fees to regulatory agencies.
6 Green belt 0.8 1.5 Development of Greenbelt including Gardening and Plantation.
7 Occupational health (OHC)
0.8 1.0 Occupational health check up of Employees and workers
8 CSR 2.25 0 2.5 % of the project cost. Recurring cost will include cost allocated for the CSR activity like Educational, Drinking facility, Infrastructure facility, Green belt development, Tribal development, health and medical services etc.
9 CER 1.8
0 2% of the proposed project cost. Green belt development, Drinking water facility, solar Lighting etc.
Total 369.9 99.5
xix Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
Annexure: A Executive Summary of Final Environmental Impact Assessment Report of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2 Survey No. 316, Opp. Dharti Industrial Estate,
CONCLUSION The study brings out the followings: • The proposed project will have easy access to basic infrastructure facilities,
availability of land, fuel, transportation network, power availability, environmental compatibility and well developed pollution control systems.
• Environmental Impact Assessment shows that proposed project activity will not
have any significant impact on ambient air quality, ground water quality and noise level.
• Risk to flora, fauna and soil is negligible due to location of project activity and
proposed effective environmental management plan for management and handling of air pollution, hazardous wastes and wastewater.
• Greenbelt on available open land area will be developed within the plant
premises; there will be positive impact on the ecological environment of the study area.
• There will be Socio-economic benefits due to creation of direct/indirect
employment. Thus, it is concluded that proposed project of M/s. BHIMANI DYECHEM INDUSTRIES. Will have negligible impact on environment and will become beneficial to the local people after implementation of the mitigation measures and environmental management plan.
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Annexure-B
મેસસર્. ભીમાની ડાયક�મ ઇન્ડસ્ટ્ર�ઝ ના ��ૂચત �િુનટમા ંસીન્થેટ�ક ઓગ�નીક
ક�િમકલના ંઉત્પાદનની પયાર્વરણ પર થનાર� અસરો �ગેના અહ�વાલનો મહત્વ�ણૂર્
સારાશં
(સવ� ન ં:૩૧૬, પ્લોટ ન:ં ૦૨, ધરતી ઈન્ડસ્ટ્ર�યલ એસ્ટ�ટ ની સામે, ગામ:ધનોટ, તા:કલોલ, �.ગાધંીનગર,
�જુરાત)
અહ�વાલ તૈયાર કરનાર
ભગવતી એન્વાયરો ક�ર પ્રા.લી.
(આઈએસઓ ૯૦૦૧, આઈએસઓ૧૪૦૦૧ અને OHSAS: ૧૭૦૦૧ થી પ્રમા�ણત કંપની)
મેસસર્. ભીમાની ડાયક�મ ઇન્ડસ્ટ્ર�ઝ દ્વારા ��ૂચત ઉત્પાદન પ્ર�ક્રયા કરવા માટ�નો કાયર્કાર� સારાશં
સવ� ન.ં૩૧૬ , પ્લોટ નબંર: ૦૨. ધરતી ઇન્ડસ્ટ્ર�યલ એસ્ટ�ટની સામે
ગામ:ધાનોટ, તા:કલોલ,�.ગાધંીનગર, �જુરાત.
૧. પ્રસ્તાવના:
મેસસર્. ભીમાની ડાયક�મ ઇન્ડસ્ટ્ર�ઝ � ડાયઝ અને ડાયઝ ઈન્ટરમીડ�એટ્સ ના ��ૂચત ઉત્પાદન સવ� નં : ૩૧૬ , પ્લોટ
ન:ં ૦૨, ધરતી ઈન્ડસ્ટ્ર�યલ એસ્ટ�ટ ની સામે, ગામ:ધાનોટ, તા:કલોલ,�.ગાધંીનગર, �જુરાત ખાતે શ� કરવા માટ�ની
દરખાસ્� કર�લ છે. ��ૂચત �નૂીટ મા ંતેઓ િસન્થેટ�ક ઓગ�િનક (ડાય ઝ અને ડાય ઝ ઈન્ટરમીડ�એટ્સ) �ુ ંઉત્પાદન
૨૨૫ મે. ટ્ન પ્રિત માસ કરશે. આ એકમ �સ્થાિપત કરવાની �ક�મત �. ૪.૫૦ કરોડ થશે.
અતે્ર ન�ધનીય છે ક� િમિનસ્ટ્ર� ઓફ એન્વાયર્રમેન્ટ ફોર�સ્ટ તથા ક્લાઈમેટ ચને્જ , ભારત સરકાર ના ઈ.આઈ.એ
નો�ટફ�ક�શન એસ.ઓ ૧૫૩૩ તાર�ખ ૧૪ સપ્ટ�મ્બર ૨૦૦૬ અને તેના �ધુારા �તગર્ત, તેમની ��ુચત ઉત્પાદનની
પ્ર�કયા િસન્થેટ�ક ઑગ�િનક ક�િમકલ્સ-િવભાગ-૫-(એફ)-ક�ટ�ગર�. -એ મા ંઆવે છે. તેના માટ� પ્રો�ક્ટ� િમિનસ્ટ્ર� ઓફ
એન્વાયર્રમેન્ટ ફોર�સ્ટ તથા ક્લાઈમેટ ચને્જ ખાતેથી એન્વાયર્રમેન્ટ ક્લીયરન્સ લેવા� ુરહ�શે. મેસસર્ ભગવતી એન્વાયરો ક�ર પ્રા. �લ. , અમદાવાદ ને પ્રસ્થાિપત એકમનો પયાર્વરણીય �થુ્થ્કરણ અસર નો અભ્યાસ
(EIA) કરવા માટ� િનમ�કૂ કરવામા ંઆવેલ છે. કન્સલટ�ગ ફમર્ દ્વારા TOR મેળવવા માટ� , ફોમર્-૧ તથા તેની સાથે
સામેલ જ�ર� દસ્તાવેજો િમિનસ્ટ્ર� ઓફ એન્વાયર્રમેન્ટ ફોર�સ્ટ તથા ક્લાઈમેટ ચને્જ ખાતે ૨૨/૧૦/૨૦૧૮ ના રોજ જમા
કરાવવામા ં આવ્યા હતા. આ ��ૂચત પ્રો�ક્ટની િમિનસ્ટ્ર� ઓફ એન્વાયર્રમેન્ટ ફોર�સ્ટ તથા ક્લાઈમેટ ચેન્જ , ભારત
સરકાર એ EIA ર�પોટર્ બનાવવા માટ� ર�ફરન્સ ન ં IA-J-11011/349/2018-IA-II(I) થી તા ૨૯/૧૧/૨૦૧૮ ના રોજ TOR
આપ્યો હતો.ભગવતી એન્વાયરો ક�ર પ્રા. �લ (NABL Accreditation and MoEF & CC Registration) દ્વારા પયાર્વરણીય
દ�ખર�ખ તથા �થુ્થ્કરણ માચર્-અિપ્રલ-મે-૨૦૧૮ દરમ્યાન કરવામા ંઆવ્�ુ ંહ� ું તથા ડ્રાફ્ટ EIA ર�પોટર્ બનાવીને લોક
�નુાવણીની પ્ર�ક્રયા માટ� જમા કરવામા આવેલ છે. પ્લોટ � ુ �ુલ ક્ષેત્રફળ ૩૩૪૪ ચો. મી. છે. તે પૈક� ૧૧૦૫ ચો.મી, નો િવસ્તાર �કૃ્ષારોપણ અને બાગકામ માટ� નો રહ�શે.�
M/S. BHIMANI DYECHEM INDUSTRIES is a proposed unit located at Plot no.2, Survey No. 316, Opp. Dharti Industrial Estate, At: Dhanot , Ta: Kalol, Dist: Gandhinagar, Gujarat In their proposed unit, they will manufacture Synthetic Organic Chemical (Dyes and Dyes Intermediates )@ 225 MT/M. The manufacturing of Synthetic organic chemical (Dyes and Dyes Intermediates) falls under Category “A” of EIA Notification issued in September – 2006. For this the unit needs Environmental clearance from Ministry of Environment Forest Climate Change.
The Final EIA studies are carried out as a part of process to obtain Environmental Clearance Certificate for the proposed project. Unit believes in sustainable development and equally concern about environment preservation and pollution control and proposes to provide adequate Environmental Management System to meet desired norms prescribe by statutory authority.
In order to assess the Environmental Impacts of the proposed project, M/S. BHIMANI DYECHEM INDUSTRIES Entrusted Bhagwati Enviro Care Pvt. Ltd, Ahmedabad (NABET Accredited) to undertake Final Environmental Impact Assessment Study for various components of the Environment viz., Air, Water, Noise, Land and Socio-economics. This Report presents base line data collected for March - April – May 2018 for Air, Water, Noise, Land etc., for identification and assessment of the impacts.
1.2 IDENTIFICATION OF PROJECT AND PROJECT
PROPONENT
Environment Impact Assessment or EIA is a study to predict the effect of a proposed projection or its expansion activity on the environment. It is a management tool to facilitate appropriate decision; an EIA compares various alternatives for a project and seeks to identify the one, which represents the best combination of economic and environmental costs and benefits.
It helps to identify possible environmental effects of the proposed project, proposes measures to mitigate adverse effects and predicts whether there will be significant adverse environmental effects, even after the mitigation is implemented.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
By considering environmental effects and mitigation early in the project planning cycle, environmental assessment has many benefits, such as protection of environment, optimum utilization of resources and saves overall time and cost of the project.
On 27th January 1994, the Union Ministry of Environment and Forests (MoEF), Government of India, under the Environmental (Protection) Act 1986, promulgated EIA Notification making Environmental Clearance (EC) mandatory for expansion or modernization of any activity or for setting up new projects listed in Schedule of the notification and its subsequent amendments.
On 14th September 2006, a new legislation was passed, which has objectives such as “To formulate a transparent, decentralized and efficient regulatory mechanism; to incorporate necessary environmental safeguards at planning stage; to involve stakeholders in the public consultation process and to identify developmental projects based on impact potential instead of the investment criteria”
The developmental activities requiring Environmental Clearance (EC) are:
• All new projects/activities listed in Schedule;
o Expansion and modernization of existing projects or activities listed in the Schedule to this Notification with addition of capacity beyond the limits specified for the concerned sector, that is, projects or activities which cross the threshold limits given in the Schedule, after expansion or modernization;
o Any change in product - mix in an existing manufacturing unit included
in Schedule beyond the specified range.
The projects or activities shall require prior environmental clearance from the concerned regulatory authority, as the Central Government in the Ministry of Environment and Forests for matters falling under Category ‘A’ in the schedule and at State level the State Environment Impact Assessment Authority (SEIAA) for matters falling under Category ‘B’ in the said Schedule, before any construction work, or preparation of land by the project management except for securing the land, is started on the project or activity. As per the provisions of the new re-engineered EIA Notification of 2006, the company requires to obtain prior Environmental Clearance from the State Level Environmental Appraisal Authority or from the Ministry of Environment & Forests, New Delhi as stated in the said Notification. This Proposed project falls under Synthetic organic Chemical Industry which is listed in Schedule and falls under Clause No. 5 (f) of Category “A” (Located outside notified industrial area / estate) of
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
Schedule as stated in Environmental Impact Assessment Notification published on 14th September 2006 and its vide amendment.
As specified in sub paragraph (ii) of paragraph 2, of the stated Notification of the Government of India, Proposed project requires prior environmental clearance from the Ministry of Environment Forest Climate change as, Proposed project is located outside the notified industrial area [Clause No. 5 (f)] of Category “A”. For this the industry is required to submit draft Environmental Impact Assessment Study report to State Pollution Control Board, Gujarat for Public hearing and final EIA report to Ministry of Environment Forest & Climate change, New Delhi. In order to assess the Environmental Impacts arising due to the proposed project, the company has appointed M/s. Bhagwati Enviro Care Pvt. Ltd., Ahmedabad to undertake the Environmental Impact Assessment for various components of the Environment.
The growing demand of the various kinds of Dyes and Dyes Intermediates in the domestic as well as international markets has provided a strong basis to M/S. BHIMANI DYECHEM INDUSTRIES for their proposed unit located at Plot no.2, Survey No. 316, Opp. Dharti Industrial Estate, At: Dhanot , Ta: Kalol, Dist: Gandhinagar, Gujarat.
The proposed project will help in the following aspects.
• To earn a substantial amount of foreign exchange through business development, manufacturer & sales of fine chemical products.
• To generate adequate employment for people in neighbouring areas. • To generate indirect employment.
1.3 OBJECTIVES OF EIA STUDY The project activities are listed in serial No. 5 (f) of the schedule of EIA
Notification, 2006 (synthetic Organic Chemical industries). Since the proposed project is coming up outside the notified industrial area, it is categorized as category ‘A’ and needs the Environmental clearance from Ministries of Environment Forest Climate Change.
The Environmental study undertaken is aimed at identifying existing
Environmental conditions; predicting Environmental impacts associated with the proposed unit and suggesting mitigation measures to mitigate the adverse Environmental impacts. The different activities that are likely to take place have been analyzed and proposed mitigation measures are assessed for their adequacy. Proposed mitigation measures have been considered where necessary.
The study also aims at reflecting the acceptability of the project to different stockholders and at incorporating the concerns raised by them into impact assessment and of the subsequent comprehensive Environmental management Plan and suggest the preventive and mitigative measures to
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
To decide whether proposed action is likely to cause significant adverse environmental effects; the concept of EIA is practiced. Before proceeding the baseline Environmental status, it is important to know the boundary limits and framework where data can be effectively utilized in impact assessment. In keeping with the nature and size of the industry, based on our submitted TOR and additional terms of Reference Issued by Ministry of Environment Forest and Climate Change the study area for detailed studies is an area within a radius of 10 Kms with the Project Site at the centre. A Map of the Study Area is presented in Figure No. 1.3
1.6 NEAREST LOCATION FROM THE SITE
Table: 1.1
Nearest locations from the Site
Sr. No.
Features Description Distance (Km)
1 Nearest village Dhanot Bileshwarpura Indrad
1.59 km, NE 2.62 km, NW 1.75 km, NW
2 Nearest town Chhatral 2.73 Km, ESE 3 Water Body Creek / Nalah /
Table: 1.2 Nearest Industries from the Project Site
1.7 SCOPE & METHODOLOGY OF EIA:
An attempt has been made to carry out a Final Environmental Impact Assessment Study for M/s. BHIMANI DYECHEM INDUSTRIES.The Scope of EIA adopted for BHIMANI DYECHEM INDUSTRIES is based on the TOR approved by Ministry of Environment Forest & Climate Change. The copy of the same is attached here with. Under the scope of EIA, it covers:
• A brief description of project site, its surrounding environment and proposed project facilities.
• To endow with detail description of the raw materials and manufacturing process for proposed products.
• Collection and Assessment of existing environmental baseline status based on the project information, field survey relating to air quality, meteorology, water quality, socio-economic aspects, flora & fauna, existing land use pattern etc. within study area.
• Identification of Impacts due to the proposed project. • Prediction and evaluation of the environmental impacts that may result
from project development. • Outline the Environmental Management Plan (EMP) to mitigate the
adverse impacts due to the proposed project. • Preparation of Risk Assessment Report.
Sr. No.
Name of Industries Address Type of Unit
1 Zenith Aromas Plot no 20, Shubhlaxmi Estate, Opposite Golden Estate, Near Somani Godown, Chhatral-Kadi Road, Gam: Dhanot, Taluka: Kalol, District: Gandhinagar - 382729, Gujarat, INDIA
The methodology adopted for carrying out the Environmental Impact Assessment for the proposed project has been based on the Guidelines issued by Ministry of Environment and Forest & Climate Change (MOEF). An effective EIA calls for identification of environmental parameters likely to be impacted, depending on the activities to be carried out during construction and operation phase of the project.
• Generation and collection of baseline data for valued Environmental components as per approved TOR.
• Identification and quantification of significant Environmental impacts due to the project and associated activities.
• Evaluation of impacts due to proposed activities and preparation of an Environmental impact statement.
• Preparation of appropriate Environmental Management Plan (EMP) surrounding strategies for minimizing identified adverse impacts along with budgetary provisions to be made by the project authorities for implementation of mitigation measures.
• Delineation of post Environmental Quality Monitoring Programme (EQMP) along with organizational setup required for monitoring the effectiveness of mitigation measures.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
This EIA report has been prepared on the basis of available on-site primary data (survey/ monitoring) and secondary/literature data. The EIA report contains project features, baseline environmental setup, assessment of environmental impacts, and formulation of mitigation measures, environmental management and monitoring plan with risk & assessment Report. The report includes 12 Chapters. The structure of the EIA Report with necessary tables, drawings and annexure is as follows: Chapter 1: Introduction This chapter provides background information on need of project, need of EIA study and brief of the project. The scope and EIA methodology adopted in Preparations of EIA report have also been described in this Chapter. It also covers the identification of project & project proponent, brief description of nature, size, location of the project and its importance to the country and the region. Scope of the study details about the regulatory scoping carried out as per the generic structure given in the EIA Notification, 2006. Chapter 2: Project Description This chapter deals with the project details of the proposed products, with type of project, need for the project, location, size & magnitude of operation including associated activities required by and for the project, proposed schedule for approval and implementation, including technical details of raw material, quality and quantity etc. Chapter 3: Description of the Environment This chapter presents the existing environmental status of the study area around the proposed project including topography, drainage pattern, water environment, geological, climate, transport system, land use, flora & fauna, socio-economic aspects, basic amenities etc. Environmental assessment of the project site in regard to its capability to receive the proposed project is also discussed in this Chapter.
Chapter 4: Anticipated Environmental Impacts and Mitigation
Measures This chapter describes the overall impacts of the proposed project activities and underscores the areas of concern, which need mitigation measures. It predicts the overall impact of the proposed project on different components of the environment viz. air, water, land, noise, biological, and socio-economic.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
Chapter 5: Analysis of Alternatives (Technology & site) This chapter describes the site selection criteria and analysis of proposed alternative technologies. Chapter 6: Environmental Monitoring Program Technical aspects of monitoring the effectiveness of mitigation measures have been given in this Chapter. Chapter 7: Additional Studies This chapter deals with the Public consultation & Risk assessment carried out for the proposed manufacturing plant. Unit is not located in notified area so, public consultation is required. Chapter 8: Project Benefits This chapter deals with the benefits to the local surrounding people due to proposed project.
Chapter 9: Environment cost benefit Analysis
During the scoping stage; no recommendation of environmental cost benefit analysis is suggested by the appraisal committee.
Chapter 10: Environmental Management Plan This chapter details the inferences drawn from the environmental impact assessment exercise. It describes the overall impacts of the proposed activities during construction and operation phases and underscores the areas of concern, which need mitigation measures. It also provides mitigation and control measures for environmental management plan (EMP) for minimizing the negative environmental impacts and to strengthen the positive environmental impacts of the proposed project.
Chapter 11: Summary & Conclusion This chapter provides the summary and conclusions of the EIA study of the Proposed project with overall justification for implementation of the project and also explanation of how, adverse effects will be mitigated. Chapter 12: Disclosure of Consultants Engaged This chapter provides the disclosure of consultants engaged to carry out the EIA study along with other additional studies.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
GENERIC TERMS OF REFERENCE (TOR) IN RESPECT OF INDUSTRY SECTOR 1. Executive Summary (Generic
Structure as per Appendix III A)
Please Refer Annexure A ---
2. Introduction
i. Details of the EIA Consultant including NABET accreditation
Please Refer Annexure – C
XLIV
ii. Information about the project proponent
Please Refer Section 2.4 of Chapter 2
33
iii. Importance and benefits of the project
Please Refer Section 1.2 & 1.10 of Chapter 1. Section 2.3. of Chapter 2
01 29 33
3. Project Description
i. Cost of project and time of completion.
Please Refer Section 2.26 of Chapter 2. Time of Completion: 06 months after obtaining EC & CTE.
192
ii. Products with capacities for the proposed project.
Please Refer Section 2.7 of Chapter 2.
36
iii. If expansion project, details of existing products with capacities and whether adequate land is available for expansion, reference of earlier EC if any.
For product details, please refer table No. 2.5 For Land breakup, please refer Table No.2.4
36
35
iv. List of raw materials required and their source along with mode of transportation.
Please Refer Section 2.9 of Chapter 2.
39
v. Other chemicals and materials required with quantities and storage capacities.
Please Refer Section 2.10 of chapter 2
55
vi. Details of Emission, effluents, hazardous waste generation and their management.
For Air Emission: Please Refer Section 2.16 – 2.19 of Chapter 2. For Water consumption
171-174
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
& Effluent Generation: Please Refer Section 2.13 – 2.15 of Chapter 2. For Hazardous Waste Generation: Please Refer Section 2.20 of Chapter 2.
164-170
174
vii. Requirement of water, power, with source of supply, status of approval, water balance diagram, man-power requirement (regular and contract).
Please Refer Table 2.2 of Chapter 2, For water balance Diagram, Please Refer Fig 2.1 of Chapter 2, For manpower details, Please Refer table 2.23 of Chapter 2.
34
168
194
viii. Process description along with major equipments and machineries, process flow sheet (quantities) from raw material to products to be provided.
For Process Description & for Process flow diagram, Please Refer Section 2.12 of chapter 2.
64
ix. Hazard identification and details of proposed safety systems.
Please Refer Section 10.10 of Chapter 10.
458
x. Expansion/modernization Proposals:
Proposed unit. ---
a. Copy of all the Environmental Clearance(s) including Amendments thereto obtained for the project from MOEF/SEIAA shall be attached as an Annexure. A copy of the compliance of conditions stipulated in all the existing Environmental clearances including Amendments shall be provided. In addition, status of compliance of Consent to Operate for the ongoing /existing operation of the project from SPCB shall be attached with the EIA-EMP report.
Proposed Unit ---
b. In case the existing project has not obtained Environmental clearance, reasons for not taking EC under the
Proposed Unit ---
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
provisions of the EIA Notification 1994 and/or EIA Notification 2006 shall be provided. Copies of Consent to Establish/No Objection Certificate and Consent to Operate (in case of units operating prior to EIA Notification 2006, CTE and CTO of FY 2005-2006) obtained from the SPCB shall be submitted. Further, compliance report to the conditions of consents from the SPCB shall be submitted.
4. Site Details
i. Location of the project site covering village, Taluka/Tehsil, District and State, Justification for selecting the site, whether other sites were considered.
Please Refer Fig 1.1 to 1.3 of chapter 1 For Justification for selecting the site, Please Refer Section 2.3 of Chapter 2.
5 – 7
33
ii. A Topo sheet of the study area of radius of 10km and site location on 1:50,000/1:25,000 scale on an A3/A2 sheet. (Including all eco-sensitive areas and Environmentally sensitive places).
Please Refer Fig 3.2 of chapter 1
209
iii. Details w.r.t. option analysis for selection of site.
Not done. ---
iv. Co-ordinate (lat long) of all four corners of the site.
1. 23017’13.37”N , 72024’58.24”E
2. 23017’12.49”N , 72025’00.49”E
3. 23017’13.82”N , 72025’01.52”E
4. 23017’14.79”N , 72025’00.01”E
v. Google map-Earth download Please Refer Fig 1.5 of chapter 1
09
vi. Layout maps indicating existing unit as well as proposed unit indicating storage area, plant area, greenbelt area, utilities etc. If located within industrial area/Estate/Complex, lay
Please Refer Fig 1.4 of chapter 1.
08
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
out of industrial area indicting location of unit within the Industrial area/ Estate.
vii. Photographs of the proposed and existing (if applicable) plant site. If existing, show photographs of plantation/greenbelt, in particular.
Please Refer Section 1.11 of Chapter 1.
30
viii. Land use break-up of total land of the project site (identified and acquired), government/private - agricultural, forest, wasteland, water bodies, settlements, etc shall be included. (not required for industrial area).
Please Refer table 2.4 of Chapter 2.
35
ix. A list of major industries with name and type within study area (10km radius) shall be incorporated. Land use details of the study area.
For list of major industries, Please Refer Table 1.2 of Chapter 1. For Land Use Details, Please Refer section 3.12 of Chapter 3.
12
256
x. Geological features and Geo-hydrological status of the study area shall be included.
For Geological features, Please Refer Section 3.10.1 of Chapter 3 and For Geo-hydrological status of the study area, Please Refer Section 3.13 of Chapter 3.
249
259
xi. Details of Drainage of the project up to 5km radius of study area. If the site is within 1 km radius of any major river, peak and lean season river discharge as well as flood occurrence frequency based on peak rainfall data of the past 30 years. Details of Flood Level of the project site and maximum Flood Level of the river shall also be provided. (Mega green field projects).
Treated Effluent sent to Chhtral Enviro Management Service Pvt. Ltd.
---
xii. Status of acquisition of land. If acquisition is not complete, stage of the acquisition process and expected time of complete
Land Supporting Document is enclosed in Annexure 06.
605
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possession of the land. xiii. R&R details in respect of land in line
with state Government policy. Not Applicable
---- 5. Forest and wildlife related issues (if
applicable):
i. Permission and approval for the use of forest land (forestry clearance), if any, and recommendations of the State Forest Department. (If applicable).
Not Applicable
ii. Land use map based on High resolution satellite imagery (GPS) of the proposed site delineating the forestland (in case of projects involving forest land more than 40 ha).
For land Use details of the study Area, Please Refer Section 3.12 of Chapter 3.
256
iii. Status of Application submitted for obtaining the stage I forestry clearance along with latest status shall be submitted.
Not Applicable -----
iv. The projects to be located within 10 km of the National Parks, Sanctuaries, Biosphere Reserves. Migratory Corridors of Wild Animals, the project proponent shall submit the map duly authenticated by Chief Wildlife Warden showing these features vis-à-vis the project location and the recommendations or comments of the Chief Wildlife Warden-thereon.
Not Applicable. No, National Parks, Sanctuaries, Biosphere Reserves. Migratory Corridors of Wild Animals, located within 10 Km of the Study Area.
-----
v. Wildlife Conservation Plan duly authenticated by the Chief Wildlife Warden of the State Government for conservation of Schedule I fauna, if any exists in the study area.
Not Applicable -----
vi. Copy of application submitted for clearance under the Wildlife (Protection) Act, 1972, to the
Not Applicable -----
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Standing Committee of the National Board for Wildlife.
6. Environmental Status
i. Determination of atmospheric inversion level at the project site and site-specific micrometeorological data using temperature, relative humidity, hourly wind speed and direction and rainfall.
Please Refer Table No. 4.6, 4.7, 4.8, 4.9, 4.10 of Chapter 4. Please Refer Fig No. 4.1, 4.2, 4.3,4.4,4.5 of Chapter 4. For Micrometeorology data Please Refer Section 3.6 of Chapter 3.
316-324
326-330
224
ii. AAQ data (except monsoon) at 8 locations for PM10, PM2.5, SO2, NOX, CO and other parameters relevant to the project shall be collected. The monitoring stations shall be based CPCB guidelines and take into account the pre-dominant wind direction, population zone and sensitive receptors including reserved forests.
For Monitoring Station, Please Refer table No. 3.2 of Chapter 3. AAQ data of 8 locations is given in table No. 3.4 of Chapter 3.
212
215
iii. Data of all AAQ measurement for 12 weeks of all stations as per frequency given in the NAQQM Notification of Nov. 2009 along with - min., max., average and 98% values for each of the AAQ parameters from data of all AAQ stations should be provided as an annexure to the EIA Report.
AAQ data of 8 locations is given in table No. 3.4a to 3.4d of Chapter 3. Min., Max., Average and 98% values for each of the AAQ parameters from data of all AAQ stations is shown in table No. 3.3 of Chapter 3.
215
213
iv. Surface water quality of nearby River (100m upstream and downstream of discharge point) and other surface drains at eight locations as per CPCB/MoEF & CC guidelines.
Please refer Table no.3.14 of chapter 3.
246
v. Whether the site falls near to Not Applicable ---
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polluted stretch of river identified by the CPCB/MoEF & CC, if yes give details.
vi. Ground water monitoring at
minimum at 8 locations shall be included.
Please Refer Table No. 3.14 of Chapter 3.
246
vii. Noise levels monitoring at 8 locations within the study area.
Please Refer Table No. 3.12 of Chapter 3.
235
viii. Soil Characteristic as per CPCB guidelines.
Please Refer Table No. 3.15 of Chapter 3.
252
ix. Traffic study of the area, type of vehicles, frequency of vehicles for transportation of materials, additional traffic due to proposed project, parking arrangement etc.
Please Refer Section 4.14 of Chapter 4.
345
x. Detailed description of flora and fauna (terrestrial and aquatic) existing in the study area shall be given with special reference to rare, endemic and endangered species. If Schedule-I fauna are found within the study area, a Wildlife Conservation Plan shall be prepared and furnished.
Please Refer Section 3.14 of Chapter 3.
262
xi. Socio-economic status of the study area.
Please Refer Section 3.15 of Chapter 3.
270
7. Impact and Environmental Management Plan
i. Assessment of ground level concentration of pollutants from the stack emission based on site-specific meteorological features. In case the project is located on a hilly terrain, the AQIP Modeling shall be done using inputs of the specific terrain characteristics for
Please Refer Section 4.4 of Chapter 4.
305
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determining the potential impacts of the project on the AAQ. Cumulative impact of all sources of emissions (including transportation) on the AAQ of the area shall be assessed. Details of the model used and the input data used for modeling shall also be provided. The air quality contours shall be plotted on a location map showing the location of project site, habitation nearby, sensitive receptors, if any.
For Air Quality Contours, Please refer Fig. 4.1, 4.2, 4.3, 4.4, 4.5 of Chapter 4.
326-330
ii. Water Quality modeling - in case of discharge in water body
Not Done.
iii. Impact of the transport of the raw materials and end products on the surrounding Environmental shall be assessed and provided. In this regard, options for transport of raw materials and finished products and wastes (large quantities) by rail or rail-cum road transport or conveyor cum-rail transport shall be examined.
Please Refer Section 4.14 of Chapter 4.
345
iv. A note on treatment of wastewater from different plant operations, extent recycled and reused for different purposes shall be included. Complete scheme of effluent treatment. Characteristics of untreated and treated effluent to meet the prescribed standards of discharge under E(P) Rules.
Please Refer Section 2.13 – 2.15 of Chapter 2.
164
v. Details of stack emission and action plan for control of emissions to meet standards.
Please Refer Section 2.16 – 2.18 of Chapter 2.
171
vi. Measures for fugitive emission control.
Please Refer Section 2.19 of Chapter 2.
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vii. Details of hazardous waste For Details of hazardous Prepared By M/s. Bhagwati Enviro Care Pvt. Ltd.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
generation and their storage, utilization and management. Copies of MOU regarding utilization of solid and hazardous waste in cement plant shall also be included. EMP shall include the concept of waste-minimization, recycle/reuse/recover techniques, Energy conservation, and natural resource conservation.
waste generation and their storage, utilization and management, Please Refer Section 2.20 of Chapter 2. For, concept of waste-minimization, recycle/reuse/recover techniques, Energy conservation, and natural resource conservation - Please Refer Section 10.12 of Chapter 10.
174
468
viii. Proper utilization of fly ash shall be ensured as per Fly Ash Notification, 2009. A detailed plan of action shall be provided.
Generated fly ash will be mixed with Solid waste and send to TSDF site.
--
ix. Action plan for the green belt development plan in 33 % area i.e. land with not less than 1,500 trees per ha. Giving details of species, width of plantation, planning schedule etc. shall be included. The green belt shall be around the project boundary and a scheme for greening of the roads used for the project shall also be incorporated.
Please Refer Section 10.6 of Chapter 10. Please Refer Section 2.29 of chapter 2
446
194
x. Action plan for rainwater harvesting measures at plant site shall be submitted to harvest rainwater from the roof tops and storm water drains to recharge the ground water and also to use for the various activities at the project site to conserve fresh water and reduce the water requirement from other sources.
Please Refer Section 2.30 of Chapter 2.
195
xi. Total capital cost and recurring cost/annum for Environmental pollution control measures shall be included.
Please Refer table No.2.21 of Chapter 2.
192
xii. Action plan for post-project Environmental monitoring shall be
Please Refer table No. 6.1 of Chapter 6.
352
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xiii. Onsite and Offsite Disaster (natural and Man-made) Preparedness and Emergency Management Plan including Risk Assessment and damage control. Disaster management plan should be linked with District Disaster Management Plan.
Please Refer Section 7.10 of Chapter 7. Risk Assessment Report is enclosed in Annexure -02.
405
492
8. Occupational health
i. Plan and fund allocation to ensure the occupational health & safety of all contract and casual workers.
Please Refer table 10.6 of Chapter 10.
467
ii. Details of exposure specific health status evaluation of worker. If the workers' health is being evaluated by pre designed format, chest x rays, Audiometry, Spirometry, Vision testing (Far & Near vision, color vision and any other ocular defect) ECG, during pre placement and periodical examinations give the details of the same. Details regarding last month analyzed data of above mentioned parameters as per age, sex, duration of exposure and department wise.
Please Refer Section 10.7 of Chapter 10.
450
iii. Details of existing Occupational & Safety Hazards. What are the exposure levels of hazards and whether they are within Permissible Exposure level (PEL). If these are not within PEL, what measures the company has adopted to keep them within PEL so that health of the workers can be preserved.
Please Refer Section 10.8 of Chapter 10.
450
iv. Annual report of heath status of workers with special reference to Occupational Health and Safety.
After Proposed activity of the project, all the data of the medical checkups of workers will be kept as per Form 37 as per existing
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
i. Does the company have a well laid down Environmental Policy approved by its Board of Directors? If so, it may be detailed in the EIA report.
Please Refer Section 6.7 of Chapter 6.
358
ii. Does the Environmental Policy prescribe for standard operating process / procedures to bring into focus any infringement / deviation / violation of the Environmental or forest norms / conditions? If so, it may be detailed in the EIA.
Please Refer Section 6.7 of Chapter 6.
358
iii. What is the hierarchical system or Administrative order of the company to deal with the Environmental issues and for ensuring compliance with the Environmental clearance conditions? Details of this system may be given.
Please Refer Figure 10.1 of Chapter 10.
430
iv. Does the company have system of reporting of non compliances / violations of Environmental norms to the Board of Directors of the company and / or shareholders or stakeholders at large? This reporting mechanism shall be detailed in the EIA report.
Please Refer Section 6.7 of Chapter 6.
358
10. Details regarding infrastructure facilities such as sanitation, fuel, restroom etc. to be provided to the labour force during construction as well as to the casual workers including truck drivers during operation phase.
Please Refer Section 10.15 of Chapter 10.
473
11 Enterprise Social Commitment (ESC)
i. Adequate funds (at least 2.5 % of The industry will provide Prepared By M/s. Bhagwati Enviro Care Pvt. Ltd.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
the project cost) shall be earmarked towards the Enterprise Social Commitment based on Public Hearing issues and item-wise details along with time bound action plan shall be included. Socio-economic development activities need to be elaborated upon.
2.5 % of the project cost Towards the Enterprise Commitment. Socio Economic development activities.
-----
12. Any litigation pending against the project and/or any direction/order passed by any Court of Law against the project, if so, details thereof shall also be included. Has the unit received any notice under the Section 5 of Environmental (Protection) Act, 1986 or relevant Sections of Air and Water Acts? If so, details thereof and compliance/ATR to the notice(s) and present status of the case.
There was no any litigation pending against the project and/or any direction/order passed by any Court of Law against the project.
------
13. 'A tabular chart with index for point wise compliance of above TOR.
Given herewith in Section 1.9 of Chapter 1.
17
Specific TORs 1. Details on solvent to be used,
measures for solvent recovery and for emission control.
For solvent details, Refer Section 2.31 of chapter 2.
202
2. Details of process emissions from the proposed unit and its arrangement to control.
For process gas emission, Please refer 2.17 of chapter 2.
173
3. Ambient air quality data should include VOC, other process Specification pollutants like; NH3, Chlorine, HCl, HBr, H2S, HF, etc. (As applicable)
Please refer Table 3.4 of chapter 3.
215
4. Work zone monitoring arrangements for hazardous chemicals.
Please refer section 6.3 of chapter 6.
354
5. Detailed effluent treatment scheme including segregation of effluent streams for unit adopting Zero liquid discharged.
Please refer Section 2.13 & 2.14 of chapter 2.
164
6. Action plan for odour control to be submitted.
Please refer Section 10.16 of chapter 10.
474
7. A copy of the Memorandum of undertaking signed with cement manufacturing indicating clearly that
Not Applicable --
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they co process organic Solid / hazardous waste generated.
8. Authorization/Membership for the disposal of liquid effluent in CETP and solid /hazardous waste in TSDF site, if any.
Please refer Annexure: 9 620
9. Action plan for utilization of MEE/Dryers salts.
Unit will install spray dryer for convert liquefied dyes material in to powder form so there will no spray dryer salt.
--
10. MSDS for all the chemical are being used / will be used.
Please refer Annexure: 10 621
11. Authorization/membership for the disposal of solid/hazardous waste in TSDF.
Unit will become member of nearest TSDF site.
--
12. Details of incinerators if to be installed.
No any incinerator to be installed.
--
13. Risk Assessment for storage and handling of hazardous chemical/solvent. Action plan for handling & Safety to be incorporated.
Please refer Annexure: 2 492
14. Arrangement for ensuring health & Safety of workers engaged in handling of toxic material.
Please refer Section 7.4 of chapter 7.
390
1.10 Regulatory Frame work
The proposed project is yet at its technical investigation stage. Prior to its implementation, it will be necessary to acquire all the necessary clearance from the Government of India, as per the applicable national regulations. Key clearances include obtaining the No Objection Certificate from the Gujarat Pollution Control Board (GPCB) under The Water (Prevention and Control of Pollution) Act, 1974 and Rules, 1975; The Air (Prevention and Control of Pollution) Act, 1981 and Rules, 1982. In addition to that Manufacture, Storage and Import of Hazardous Chemicals (MSIHC) Rules, 1989 and amendments thereafter, Hazardous Waste (Management, Handling and Transboundary Movement) Rules, 2008 will also be applicable to the industry. The purpose of the study is to comply with legal requirements as per Environmental Impact Assessment (EIA) Notification, 14th September 2006 (and subsequent amendments) of Ministry of Environment and Forests (MoEF) Since the proposed project involves manufacture of Dyes and Dyes Intermediates located at Plot no.2, Survey No. 316, Opp. Dharti Industrial Estate, At: Dhanot , Ta: Kalol, Dist: Gandhinagar, Gujarat. The proposed project falls under Category: 5(f) A. As per the Environmental Impact Assessment notification, dated September 14, 2006 the project requires prior environmental clearance from The State Level Environment
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As per the requirements of the notification, an application in Form 1 was submitted to Ministry of Environment and Forest Climate Change on 22/10/2018. The ‘TOR’ was issued on 29/11/2018 for preparation of EIA/EMP. A copy of the TOR is included in chapter 1 of this EIA Report. As per TOR project was considered under “A” category. (Based on the additional information, in view of the MoEF & CC’s OM vide No.IA-J-11011/387/2017-IA-II(I) committee asked to prepare EIA – EMP report as per the EIA notification 2006.)
As per the requirements of the TOR DTD 22/10/2018 and to estimate the environmental impacts arising due to its proposed project, M/s. BHIMANI DYECHEM INDUSTRIES retain M/s. Bhagwati Enviro Care Pvt. Ltd., Ahmedabad, to carry out Environmental Impact Assessment study for various environmental components including air, noise, water, land and biological components along with parameters of human interest which may be affected and to prepare Environmental Management Plan (EMP) for mitigating adverse impacts. The environmental impact assessment report has been prepared for obtaining environmental clearance for the proposed activity for M/s. BHIMANI DYECHEM INDUSTRIES.
1.11 Photographs of the proposed site.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
M/S. BHIMANI DYECHEM INDUSTRIES is a proposed unit located at Plot No.2, Survey No. 316, Opp. Dharti Industrial Estate, Village: Dhanot, Ta: Kalol, Dist: Gandhinagar Gujarat. In their proposed unit, they will manufacture Synthetic Organic Chemical (Dyes and Dyes Intermediates) @ 225 MT/M. Considering scale of unit and its categorization, according to EIA notification dated 14th September 2006, by Ministry of Environment & Forest (MoEF), Government of India, their proposed manufacturing activity is falls under Synthetic Organic Chemicals – Schedule 5(f) & cat -A. For that unit needs Environmental clearance from Ministry of Environment Forest Climate Change. In order to assess the Environment Impacts of the proposed project, M/s BHIMANI DYECHEM INDUSTRIES entrusted Bhagwati Enviro Care Pvt Ltd, Ahmedabad (NABET Accredited) to undertake Final Environmental Impact Assessment Study for various components of the Environment viz., Air, Water, Noise, Land and Socio-economics. This Report presents base line data collected for March-April-May-2018 for Air, Water, Noise, Land etc., for identification and assessment of the impacts.
2.2 LOCATION
The location of the project is as shown here in Table 2.1. TABLE 2.1
LOCATION OF THE PROJECT SITE
Sr. No. Description Information 1 Latitude 23° 17' 14.1684'' N (23.287269) 2 Longitude 72° 25' 1.0704''E (72.416964) 3 Plot. No. Plot No.2, Survey No: 316 5 Village Dhanot 5 Ta Kalol 6 Dist Gandhinagar 7 State Gujarat
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In our country, we had found the high quality of material with low rate compare to others so due to that respective India is having large Market demand in India as well as abroad. Based on our informal survey of the market with our current customers and various traders, we have found that there is a big potential for the range of the products we are planning. To meet the current market requirement M/s BHIMANI DYECHEM INDUSTRIES has intended to do proposed manufacturing activity at Plot no.2, Survey No. 316, Opp. Dharti Industrial Estate, Village: Dhanot, Ta: Kalol, Dist: Gandhinagar, Gujarat. Specific site selection criteria of the unit have been given below.
• Plot size is suitable for proposed project. • Availability of the set up and the utility and support facilities within the
same premises. • The project site is well connected by road to Kadi-Chhatral State
highway 0.72 km, S away from project site & Ahmedabad-Mehsana National Highway 2.32 km, E away from project Site.
• The proposed unit is located in Industrial Estate, including Availability of infrastructure facility like power, water supply, road drainage, manpower etc.
• There are no ecological sensitive areas located within 10 km radius of the project site.
• No any national park or wild life sanctuary located within 10 km radius of the project site.
• Availability of good communication and transport facilities. 2.4 PROMOTERS & THEIR BACKGROUND
Because of availability of open area for project in the premises itself it becomes easy for the unit. The other supporting factor for justifying the location is mentioned as under:
• Due to Sufficient land area and residential area is away from the site. • Availability of basic facilities like water, fuel, power, man power and raw
materials. • Nearest town Chhatral is 2.73 km away from the location, which is having
connectivity with other parts of the country by road. • Availability of good communication and transportation facilities.
No national park, reserved forest or wild habitats as well as site of archeological significance or ecological importance fall within 10 km radius of the project site.
The details of resources are mentioned in Table No. 2.2:
TABLE NO. 2.2 DETAILS OF SOURCES
TABLE NO. 2.3
LIST OF PLANT MACHINERIES FOR PROPOSED PRODUCTION ACTIVITY:
Sr. no.
Project Requirements
Total Source/Remarks
1. Total Fresh Water
85 KL/Day Tanker
2. Power 75 KW Uttar Gujarat Vij Co. Ltd.
3. Fuel Requirement A Coal/ lignite/
wood/ agro waste
11 MT/Day Trader
B Diesel 20 Lit/hr Trader
Type Equipment Status Quantity (Total nos. to be provide)
Capacity of each
Vessel (1) M S R L 1 5000 Ltr Vessel (2) M S R L 1 10000 Ltr Vessel (3) M S R L 1 20000 Ltr Vessel (4) M S R L 1 30000 Ltr Pulverizer C.I 1 70 kgs/Hour R.O. Plant S.S. 1 120 Ltr / Hour Filter Press S.S. 1 200 Ltr / Hour
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
ultimate) 1 Plant facilities 900 26.91 2 Storage Area (Raw
material, Finished good, Tank farm area)
310 9.27
3 Administrative, other buildings, Security cabin, Fire water tank
129 3.86
Utilities 200 5.98 4 ETP area 240 7.18 5 HW storage area 150 4.49 6 Roads, Parking 110 3.29 7 Green Belt / space 1105 33.04 8 Open Area 200 5.98
Total 3344 100
Tray Dryer M.S. 3 200 Tray Small Boiler M.S. 1 600 kgs Ball mill – 1 M.S. 1 2000 Kgs Ball mill – 2 M.S. 1 500 Kgs Hot Air Generator S.S. 1 2.0 Lacs Kcal Ball mill – 3 M.S. 2 5000 Kgs Steam Boiler M.S. 1 1000 Kgs Spin Flash Dryer S.S. 1 200 Ltr. / Hour Spray Dryer M.S. 1 700 Ltr / Hour Air Compressor M.S. 1 10 H.P. Hot Air Generator S.S. 1 10 Lacs KCal Vessel (5) M S R L 1 50000 Ltr Vessel (6) M S R L 1 60000 Ltr
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2. Direct Red 31/ 12B Direct Red 31 5001-72-9 3. Direct Orange 39 Direct Orange 39 1325-54-8 4. Direct Yellow 86 Direct Yellow 86 50925-42-3 5. Direct Yellow 11/
Paper Yellow R Direct Yellow 11 1325-37-7
6. Direct Violet 9/ BRILL Violet B
Direct Violet 9 6227-14-1
7. Direct Blue 86/ Turquoise Blue GL
Direct Blue 86 1330-38-7
8. Direct blue 1/ FF Direct Blue 1 2610-05-1 3. Acid Dyes
1. Acid Blue 193/ Blue MTR
Acid Blue 193 12392-64-2
2. Acid Brown75/CR Acid Brown75 8011-86-7 3. Acid black
194/MSRL Acid black 194 61931-02-0
4. Acid Blue 113 Acid Blue 113 3351-05-1 5. Acid green 68 Acid green 68 61901-32-4 6. Acid Red 131 Acid Red 131 12234-99-0 7. Acid Yellow 36 Acid Yellow 36 587-98-4,377 8. Acid Violet 90/
Bordeaux MB
Acid Violet 90 6408-29-3
9. Acid Black 210/NT Acid Black 210 99576-15-5 4. Solvent Dyes 1. Solvent Blue 36 1,4-
Bis(isopropylamino)anthracene-9,10-dione
14233-37-5
2. Solvent Red 24 Solvent Red 24 85-83-6 3. Solvent Yellow 33 Solvent Yellow 33 8003-22-3 4. Solvent Green 3 Solvent Green 3 128-80-3
5. Food Colors:
1. Tartrazine Tartrazine 1934-21-0
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* We will maintain as minimum inventory as possible. Mode of Transportation: Road Source: Chemical Mfg. Units located in Kalol, Ahmedabad, Ankleshwar, Vapi, Vadodara etc, various Traders and Export from other Countries. 2.10 CHEMICAL NAME AND PHYSICAL FORM OF ROW MATERIAL
2.12 MANUFACTURING PROCESS DETAILS, CHEMICAL REACTION
AND MASS BALANCE
Group2. Reactive Dyes:
1. Reactive Black 8/HN: 4 Nap Is diazotized and coupled with H-Acid solution in alkaline medium. Coupling mass obtained is then chrominated and cobalting is done. The resultant mass is then cyanurated and hot brandings done with liquid ammonia. The final product spray dried to get dry powder.
Chemical Reaction for Reactive Black HN:
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
Vinyl Sulfone Diazo: Charge water and Vinyl Sulfone in MSRL vessel. Stir for good slurry. Charge HCL and Ice followed by Sodium Nitrite gradually till diazotization completed, which can confirmed by starch iodide paper. Any access nitrite will be removed by adding sulfamic acid just before coupling.
Coupling: Charge J. Acid into the first couple mass. And add soda bi carb/Soda Ash to adjust pH. Add Ice. Stir the couple mass for some time. Third Coupling: Increase pH by adding Soda Bi Carb / Soda Ash. Then charge MPDSA. Stir it for dissolved. Spray Drying: The liquid transferred to the spray drying holding tank and spray dry. Standardization: The spray dried powder is then charged to the Blender and de-dusted by antidusting oil if necessary. Packing: The final product is then packed in HDPE bags / M.S. Drums / Plastic Carboys / Paper Carton Boxes for ready to dispatch.
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
First Diazotization: VS charged to a MSRL reaction vessel along with water and ice to maintain temperature between 0 ºC to 5ºC. Then Hydrochloric Acid will be added followed by Sodium Nitrite powder gradually till diazotization completed, which can be confirmed by starch iodide paper. Any excess nitrite will be removed by adding Sulfamic Acid just before coupling. Keep temperature between 0 ºC to 5ºC throughout the diazotization reaction. First Coupling: Charged H-Acid to the diazotized BNTS and stir it keeping the temperature between 0 ºC to 5ºC by adding ice. Second Coupling: OAVS charged to a MSRL reaction vessel along with water and ice to maintain temperature between 0 ºC to 5ºC. Then Hydrochloric Acid will be added followed by Sodium Nitrite powder gradually till diazotization completed, which can be confirmed by starch iodide paper. Any excess nitrite will be removed by adding Sulfamic Acid just before coupling. Keep temperature between 0 ºC to 5ºC throughout the diazotization reaction. Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags / MS Drums / Plastic Carboys / Paper carton boxes.
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4. Reactive Blue 222/BF Manufacturing Process: MPDSA is condensed with Cynuric chloride and which is further condensed with MBVS Ester and then the product obtained is diazotized and coupled with H-Acid to get Coupling Mass-1. S.T A is diazotized and further coupled with coupling mass-1 to get coupling Mass-2, which is spray dried and dry PDR is obtained.
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MPDSA is condensed with cycle and condensed product is again 2nd condensed with Sulfamic acid, which is then diazotized and coupled with H-Acid to give coupling mass-1. V.S. Ester Diazo is prepared and then condensed with coupling mass-1 to give coupling mass-2, which then spray dried and dry powder is obtained.
Chemical Reaction for Reactive Blue 194/Navy Blue ME2GL:
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K-Acid is diazotized and coupled with Meta uriedo aniline. The coupled mass is cyanurated with Cyanuric chloride. The Cyanuration mass is hot branded with liquid ammonia to get final product, which is then isolated, filtrated and wet cake is obtained. The wet cake solution is prepared and then spray dried to get dry powder.
Chemical Reaction for Reactive Orange 12
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First Acetylation N Methyl J-Acid Charge to a MSRL reaction vessel along with water and ICE to maintain Temperature between 0 oC to 5ºC. Then Acetic Anhydride will be added followed by Caustic Flacks powder gradually till reaction completed, which can be confirmed by Congo Red paper. Keep Temperature between 20 oC to 25ºC throughout the Acetylation. First Diazotization ST Acid charged to a MSRL vessel along with water and ICE to maintain temperature between 0 oC to 5ºC. Then Hydrochloric Acid will be added followed by sodium Nitrite powder gradually till diazotization completed, which can be confirm by starch iodide paper. Keep temperature 0 oC to 5ºC throughout the diazotization reaction. First Coupling Charge Acetylation mass to the first diazotization BNTS and stir it keeping the temperature between 0 oC to 5ºC by adding Ice. Hydrolysis Charge caustic Flacks gradually keeping Temperature 85ºC throughout the Hydrolysis. Cyanuration In Hydrolysis mass charge ICE to maintain temperature 5ºC. Then Cynuric Chloride will be added followed by Soda Ash powder gradually till reaction Completed. Condensation Charge VS Powder gradually keeping Temperature 55ºC throughout the Reaction Completed. Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags / MS Drums / Plastic Carboys / Paper Carton boxes.
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First Cyanuration & Diazotization MPDSA Charge in MSRL reaction Vessel along with water and ICE to maintain Temperature between 0 ºC to 5ºC. Then add Cyanuric Chloride in the mass. Then Hydrochloric Acid will be added followed by Sodium Nitrite powder gradually till diazotization completed, which can be confirmed by starch iodide paper. Keep temperature between 0 ºC to 5ºC throughout the diazotization reaction. First Coupling Charge SPCP Powder to the diazotization BNTS and stir keeping the temperature between 0 ºC t o 5ºC by adding ICE. Condensation Charge Metanilic Acid Powder with soda ash for condensation purpose to the coupler mass and stir it keeping the temperature between 45ºC to 50 ºC. Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags / MS Drums / Plastic Carboys / Paper carton boxes.
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Diazotization of Vinyl Sulphone by Hydro Chloric Acid, Sodium Nitrite, Ice & water. This mixture is known as diazotization of VS. Make solution of SPCP with water. Coupling of Diazo -1 with SPCP solution. This is known as coupler 1. Then add caustic soda up to required pH. Send the liquefied material of coupler I for spray drying activity. Finally the powder material is packed into bags.
Chemical Reaction for Reactive Yellow FG/42: (1) VINYL SULPHONE DIAZOTIZATION:-
+ 2HCl + NaNO2 + NaCl + 2H2O
(2) COUPLING I WITH SPCP:-
+
NH2
SO2CH2CH2OSO3H
(M.W. 281)
N=N-Cl
SO2CH2CH2OSO3H
(M.W. 328.5)
N=N-Cl
SO2CH2CH2OSO3H
S.P.C.P. (M.W. 284)
(M.W. 328.5)
Reactive Yellow FG +
(M.W. 576)
HCl. (M.W. 36.5)
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First Diazotization K-Acid Charge in MSRL reaction Vessel along with water and ice to maintain temperature between 0ºC to 5ºC C. Then Hydrochloric Acid will be added followed by Sodium Nitrite powder gradually till diazotization completed, which can be confirmed by starch iodide paper. Keep temperature between 0ºC to 5ºC throughout the diazotization reaction. First Coupling Charge MUA Powder to the diazotization BNTS and stir keeping the temperature between 0ºC to 5ºC C by adding ice. 1st Cyanuration Charge Cyanuric Chloride to maintain Temperature between 0ºC to 5ºC C. Then Charge Soda Ash powder gradually till Cyanuration completed which can be confirmed by PC. Condensation Charge VS Powder with soda ash for condensation purpose to the coupler mass and stir it keeping the temperature between 45ºC to 50ºC Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags/MS Drums/Plastic Carboys/Paper carton boxes.
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MPDSA is condensed with Cyanuric chloridr and condensed product is diazotized and coupled with 2-Pyridone. The coupling mass obtained is further condensed with Vinyl Sulfone Ester to give final product, which is spraying dried to give dry powder.
Chemical Reaction for Reactive Yellow 160/ ME4GL:
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First Cyanuration VS Charge to a MSRL reaction vessel along with water and ICE to maintain Temperature between 0 ºC to 5ºC. Then Cyanuric Chloride will be added followed by Soda Bicarbonate powder gradually till reaction completed, which can be confirmed by Congo red paper. Keep Temperature between 0 ºC to 5ºC throughout the Cyanuration. Second Cyanuration Charge H-Acid Powder to the first Cyanuration BNTS and stir it keeping the temperature between 0 ºC to 5ºC by adding Ice. First Diazotization ST Acid charged to a MSRL vessel along with water and ICE to maintain temperature between 0 ºC to 5ºC. Then Hydrochloric Acid will be added followed by sodium Nitrite powder gradually till diazotization completed, which can be confirm by starch iodide paper. Keep temperature 0 ºC to 5ºC throughout the diazotization reaction. First Coupling Charge second Cyanuration to the first diazotization BNTS and stir it keeping the temperature between 0 ºC to 5ºC by adding ICE. Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags / MS Drums / Plastic Carboys / Paper carton boxes
93
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First Cyanuration VS Charge to a MSRL reaction vessel along with water and Ice to maintain temperature between 0ºC to 5ºC. Then Cyanuric Chloride will add followed by Sodium Bicarbonate powder gradually till reaction completed, which can be confirmed by Congo red paper. Keep Temperature between 0ºC to 5ºC throughout the Cyanuration. Second Cyanuration Charge H-Acid Powder to the first Cyanuration BNTS and stir it keeping the temperature between 0ºC to 5ºC by adding ice. First Diazotization ST Acid charged to a MSRL vessel along with water and Ice to maintain temperature between 0ºC to 5ºC. Then Hydrochloric Acid will be added followed by sodium Nitrite powder gradually till diazotization completed, which can be confirm by starch iodide paper. Keep temperature 0ºC to 5ºC throughout the diazotization reaction. First Coupling Charge second Cyanuration to the first diazotization BNTS and stir it keeping the temperature between 0ºC to 5ºC by adding ice. Condensation Charge Metanilic Acid Powder with soda ash for condensation purpose to the coupler mass and stir it keeping the temperature between 45ºC to 50ºC
Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags / MS Drums / Plastic Carboys / Paper carton boxes.
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Charge Chloro Sulphonic Acid in MS Reactor plus charge CPC Blue gradually, heat up this mixture by boiler by 120 °C -130 °C and maintain this temperature for 3Hrs and cool it down to 40 °C- 45 °C. After that dump this mixture in to dumping vessel with ice. Then filter this mixture into filter press and was it off with water. Then add VS Solution and maintain the pH by adding material. Sprays dry this material in spray dryer.
Chemical Reaction for Reactive Blue G/ 21:
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First Acetylation J-Acid Charge to a MSRL reaction vessel along with water and ICE to maintain Temperature between 0 oC to 5ºC. Then Acetic Anhydride will be added followed by Caustic Flacks powder gradually till reaction completed, which can be confirmed by Congo red paper. Keep Temperature between 20 ºC to 25ºC throughout the Acetylation. First Diazotization ST Acid charged to a MSRL vessel along with water and iceto maintain temperature between 0 ºC to 5ºC. Then Hydrochloric Acid will be added followed by sodium Nitrite powder gradually till diazotization completed, which can be confirm by starch iodide paper. Any excess nitrite will be removed by adding Sulfamic Acid just before coupling. Keep temperature 0 ºC to 5ºC throughout the diazotization reaction. First Coupling Charge Acetylation mass to the first diazotization BNTS and stir it keeping the temperature between 0 ºC to 5ºC by adding ice. Hydrolysis Charge caustic Flacks gradually keeping Temperature 85ºC throughout the Hydrolysis. Cyanuration In Hydrolysis mass charge ICE to maintain temperature 5ºC. Then Cynuric Chloride will be added followed by Soda Ash powder gradually till reaction Completed. Condensation Charge VS Powder gradually keeping Temperature 55ºC throughout the Reaction completed. Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization.
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Diazotization: F C Acid charged to a reaction vessel along with water. Then Hydrochloric Acid will be added followed by stirring. Charge ice then charge Sodium Nitrite. Maintain it for some time. Remove excess Nitrite by adding sulphamic acid Keep temperature between 0 to 50C throughout the diazotization reaction. Gamma acid clear solution: Charge Gamma Acid with water. Raise the pH of the mass by addition soda ash and caustic flakes up to the 6.5 – 7.0. Stir it for 30 minutes. Add ice to drop temp around 00C. First coupling: Transfer Gamma Acid clear solution in to F C Diazo slowly with temp 5 to 100C. Stirr for 2 hr. Diazo of coupler mass: Charge ice with HCL in coupler mass. Then dump sodium nitrite. Stir the solution for 0.5 hr. Add ice to set temp 0C. Remove excess nitrite by adding sulphamic acid. MPD clear solution: Charge water and heat it up to 500C. Then charge MPD and stir for 30 minutes. Second coupling: Transfer first coupled mass in to MPD clear solution. After completion of addition adjust pH 8.5 by charging Soda ash solution. Stir the solution for 8 hrs. Do the filtration of coupling solution after raising the temp up to 400C. Then Charge with water to make slurry. Spray Drying: The liquid transferred to the spray drying holding tank and spray dry.
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4. Direct Yellow 86: First Diazotization C-Acid charge to a MSRL reaction vessel along with water and ICE to maintain temperature between 00C to 50C. Then Hydrochloric Acid will be added followed by Sodium Nitrite powder gradually till diazotization completed, which can be confirmed by starch iodide paper. Any excess nitrite will be removed by adding sulfamic acid just before coupling. Keep temperature between 00C to 50C throughout the diazotization reaction. First Coupling Charge Meta Toluidine Hydrochloride to the diazotization BNTS and stir keeping the temperature between 00C to 50C by adding ICE. Isolation & Filtration Charge Refined Salt and stir keeping temperature 50C to 100C by adding ICE till good spot. Filter in Filter Press. W/C Charge in Water & Proceed for Cynuration. 1st Cynuration Cynuric Chloride Charge in MSRL reaction Vessel along with water and ICE to maintain Temperature between 00C to 50C. Then Cyanuric Chloride in the mass. Then Base solution will be added followed by Sodium Carbonate powder gradually till Reaction completed, which can be confirmed by Paper Chromatogram. Any excess Base will be removed by adding Cynuric Chloride. Keeping temperature between 00C to 50C throughout the 1st cyanuration reaction completed. Condensation Raise temperature between 400C to 450C by adding Soda Carbonate powder gradually till reaction completed, which can be confirmed by paper chromatogram. Any excess Base will be removed by adding Cynuric Chloride keeping temperature 400C to 450C temperature through the 2nd condensation reaction completed. Spray Drying The Standardized dye liquid will be transfer to the spray drying holding tank and spray dried. Standardization The Spray dried powder is then charged to the ball-mill and standardization. Packing The Final product is then packed in HDPE bags / MS Drums / Plastic Carboys / Paper carton boxes.
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Charge Chloro Sulphonic Acid into reactor vessel. Slowly add CPC powder into the reactor. Maintain temperature during this reaction. Dump Sulpho mass into salted ice and filter it. Make liquid of w/c by addition of Caustic flakes. This liquid is dried by direct spraying.
Chemical Reaction for Direct Blue 86: C32H10N8Cu + 2H2SO4.SO4→C32H10N8CuS2O8 + 2H2SO4 C32H10N8CuS2O8 + 2NaOH →C32H10N8CuS2O82Na + 2H2O 2H2SO4 +4NaOH→2Na2SO4+4H2O
Chloro-Sulphonation
Drowning
Spray Drying
1500 kg Finish Product
ChloroSulphonic acid: 500 kg CPC Blue: 280 kg
ICE: 1500 kg Water: 1100 lit
Water: 1100 lit NaOH: 300 kg
Glauber Salt: 500 kg
Evaporation: 2200 kg
Filtration Spent Acid: 2500 L
HCl: 80 kg for scrubber
Dil. HCl (25 %):320 kg
Water: 1000 Kg
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1-Diazo 2-Naphthol 4 Sulphuric Acid coupling with Beta Naphthol. Clear Sold at 50ºC temp. in alkaline medium in presence of catalyst. Stir for 3 hours after 3 hours Chromination with Salicylic Acid & B.C.S at 95ºC temp. PHP maintain so for 4 hours. After 4 hours check test completion of Chromination. If o then spray dry it.
Chemical Reaction for Acid Blue 193/ Dark Blue MTR:
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H-Acid Diazotized with HCL & Nitrite at 0ºC temp. Stir 1-1/2" hours after 1-1/2 hours coupling with resorcinol in alkaline medium and stir. After 2hours Na picramate diazo coupling with first coupling in alkaline medium. Stir for 2 hours. After 2 hours PNA Diazo coupled with second coupling at 6.5 pH, stir 6 hours then RO and spray dryer it.
Chemical Reaction for Acid Brown75/CR:
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• Metanilic acid diazotized with HCl, Nitrite and with ice at 0°C temperature stir for 1 hour. Alpha Naphthyl Amine coupled with Metanilic acid in acidic medium. Stir for 8 hours. After 8 hours ANA diazo with HCl & Nitrite at 18 °C temp. Stirrer 3 hours and then coupled with Phenyl Peril Acid. At neutral pH, stir for 3 hours, then isolated & spray dryer it.
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• PNA (Para Nitro Aniline) Diazotized with HCl, Nitrite at 50°C temp, Stir for 2 hour. H- Acid Clear Solution coupled with PNA Diazo in Acidic Medium at 100°C temperature. Stir 8 hours DASA Tetrazosited and with first coupling in alkaline medium coupled at 70°C temperature. Stir 2 hour third coupling resorcinol with second coupling in alkaline medium at 100°C temperature. Stir for 6 hours. After 6 hours heat 50V clarify/filter, Spray Drying it.
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Manufacturing Process: Metanilic Acid, Soda Ash, Caustic Flakes and NaNO2 are diazotised in presence of water and Ice. Diphenyl Amine, Caustic, Emulsifier and Soda Ash are dissolved in presence of Ice & water.above both diazotised and dissolved mass are coupled in coupling vessel. The mass is than Isolated and filtered followed by drying and pulverisation to obtain finished product. Chemical reaction:
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1 Diazo 2 Naphthol 4 Sulphonite Acid coupling with PMP. Diazoxide is coupled in near Alkaline medium with Parazolone and the coupling product converted into 1:2 metal complexes with Basic Chrome Sulphate.
Chemical Reaction for Acid Violet 90/ Bordeaux MB:
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First make PNA Diazo coupled with H Acid in acidic medium at 5ºC stir foe hour then DASA Tetrazo coupled with first coupling in alkaline medium at 10ºC stir for 2 hour & then last above coupling with make Phenyl Diamine in alkaline pH at 10º then clarify & Filter and spray dry it.
Chemical Reaction for Acid Black 210/NT:
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In clean reaction charge methanol, quinizerene propan-2-amine.Heat the reaction mass to reflux temp. And maintain for 8 hrs. Cool the reaction mass to Room temp, for isolation. Filter the reaction mass and wash with water. Dry the wet cake and pulverize and sent for packing.
Chemical Reaction for Solvent Blue 36:
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Diazotization:- Take approximate water in vessel. Take Garnet GBC and Stirrfor15minures.Add Hydrochloric Acid. Add Ice to bring temperature 0-5ºC. Add Sodium Nitrite under stirring Maintain temperature 0-5ºC. Coupler:- In another vessel take approximate water. Charge B-Naphthol and stir solution for 15minutes. Add Caustic Flakes and stir the solution for 30minutes. Clear the solution and Ice to bring temperature 0-5ºC. Coupling:- Receive diazo solution to coupler solution. Stir over night. Maintain pH 7.0 Next day heat to 40ºC. Filter in filter press. Unload and dry the wet cake at 80-90ºC.
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In vessel take O.D.C.B and add Quinaldine, Phthalic Anhydride. Close the vessel. Heat to 175oC. Separate the water from receiver and maintain this temperature for 5hours. Cool to room temperature and dump to Nutch filter. Wash with Methanol. Dry wet cake at 100 oC.
Chemical Reaction for Solvent Yellow 33:
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A mixture of Quinizarine & Leuco Quinizarine is reacted with Para Toluidine using Butanol as a solvent. The product is isolated by distilling off the Butanol; it is then filtered and washed with HCl. The wet cake is dried, pulverized and sieved to get the finished product.
Chemical Reaction for Solvent Green 3:
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STAGE 01: Take water in reaction vessel 01.Now charge Sulphanilic Acid in it. Then stir it. Add Ice to maintain temperature. Add HCl and Sodium Nitrite. STAGE 02: Couple vessel 01 mass with DMAS in reaction vessel 02. Charge Sodium Carbonate and water in it. Then stir it. SPRAY DRYING: Sent the liquor for spray drying. Pack the Final product.
STAGE 01: Take water in reaction vessel 01.Now charge Sulphanilic Acid in it. Then stir it. Add Ice to maintain temperature. Add HCl and Sodium Nitrite STAGE 02: Couple vessel 01 mass with Schaffer’s Acid in reaction vessel 02.Charge Sodium Carbonate and water in it. Then stir it. SPRAY DRYING: Sent the liquor for spray drying. Pack the Final product.
Stage 1: Take Water in a reaction vessel. Now charge Sodium Naphthonate in it. Then stir it, Add ice to maintain the temperature. Add HCl and Sodium Nitrite. Stage 2: Couple vessel 1 mass with Resorcinol in Reaction Vessel 2. Charge Sodium Hydroxide and Formaldehyde and stir it. Stage 3: Then clarifying the mass and add salt to it. Again filtrate it and then Spray drying it. Pack the final product.
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STAGE 01: Take water in reaction vessel 01.Now charge Sodium Napthonate in it. Then stir it. Add Ice to maintain temperature. Add HCl and Sodium Nitrite STAGE 02: Couple vessel 01 mass with G-Salt in reaction vessel 02.Charge Sodium Carbonate and water in it. Then stir it. SPRAY DRYING: Sent the liquor for spray drying. Pack the Final product.
Manufacturing Process: DNBrPNA is diazotized & coupled with M-5A.Then Coupled mass is Filtered. Wet cake is washed by water & make slurry in dispersing agent & water Then is grinded & standardized in sand mills, Then Slurry is dried in spray dried for powder product. Then Directly Packed. Chemical Reaction:
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In a MS Jacketed Sulphonator take Benzene. Check moisture test and charge Di Ethyl Oxalate. Check moisture test and charge Ethyl Acetate. Heat to 45oC and then charge Sodium Metal in 4-parts. After metal charging again heat for 3hours. In another reactor take water and charge real PHPSA the charge Caustic Lye. Then heating is started and get temperature 95-100 oC and maintain for 4hrs. Filter above solution in filter press and Nutch filter and take into MS/RL/BL vessel and charge Sulfanilic Acid. Drawn this solution into Nutch filter and then centrifuge it.
Chemical Reaction of SPCP (1, 4 Sulphophenyl 3 Carboxy 5- Pyrazolone)
SO3H
NH2
HCl
NaNO2
SO3HNa
N=N-Cl
NaHSO3
Na2CO3
+H2O
N-SO3 Na
NH-NH2
+NaCl
SO3HNa
SO3HNa
SO3 + H2 O +
N
N
O
CH2
SO3H
H2 O +CH3OH
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Process Description:- Sodium Naphthionate is condensed with sodium Bisulphite at reflux temp for 48 hrs.Followed by Hydrolysis with sulphuric acid to remove SO2.SO2 is scrubbed in soda ash solution and reuse for further batch.Hydrolysed mass is neutralize and alkaline with sodium Hydroxide(Caustic Lye) boile for removal of Ammonia.Cool it remove isolated salt.Than Isolate N.W.acid with dil sulphuric acid/Hydrochloric acid.Filter it.Collect W/C and than dry the mass as N.W.Acid.
+ NaHSO3
NH2 OH
H2SO
NaOH
SO3H SO3H
3. Chemicals Reaction:-
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Manufacturing Process: Alpha Naphthyl Amine is Sulphonated with Sulphuric Acid in ODCB at higher temp convert Naphthionic Acid. Distill ODCB with water as azeotropic mixtures, followed by neutralization with sodium Carbonate (Soda Ash). Collect 1st cut ODCB from bottom and sand for acid treatment(AT). Filter the mass. Collect in isolation vessel and cool the mass. Filter it in Nutch and CF it gives cold water wash to get Sodium Naphthionate. Collect filtrate take in Naphthionate isolation vessel add dil. Sulphuric acid. Filter the mass and collect W/C as NA.Charge collected NA in a vessel.
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B-Naphthol is sulphonated by 98% Sulphuric acid and 65% Oleum. Then sulpho mass dump in ice & water. Then salted out with Sodium Sulphate. Then filter it and get cake then amidation by 24% Ammonia & Sodium bisulphite. Then isolate the material with 98% Sulfuric acid. Filter it and centrifuge it & the final product is known as K-acid.
Chemical Reaction for K-Acid:
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M/s BHIMANI DYECHEM INDUSTRIES is proposed unit and the source of water for proposed activity will be Tanker Water Supply. Water Balance Diagram is shown at Figure No. 2.8
TABLE NO. 2.8
DETAILS OF WATER CONSUMPTION & EFFLUENT GENERATION
Application Water Consumption (KL/Day)
Waste water generation (KL/Day)
Domestic(A) 5 5 Gardening(B) 2 0 Industrial(C) Process 27 30 Washing 10 10 Boiler 30 3 Cooling 5 0.5 Scrubber 6 1 Total (C) 78 44.5 Total (A+B+C) 85 49.5
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• Total Water consumption will be 85 KLPD. From which 5 KLPD for Domestic
Purpose, 2 KLPD for Gardening purpose & 78 KLPD for Industrial Purpose.
• Total Waste water generation will be 49.5 KLPD. From which 5 KLPD domestic waste water will goes to soak pit via septic tank. 44.5 KLPD waste water will generate from industrial purpose activity.
• Total waste water generated from industrial activity will treat in Effluent treatment plant with primary treatment and then it will send to Common Spry Dryer (Chhatral Environment management System Pvt. Ltd.) to achieve zero discharge.
2.14 CHARACTERISTICS OF EFFLUENT:
The characteristics of wastewater & final outlet would be as follows:
TABLE 2.10
CHARACTERISTICS OF INDUSTRIAL EFFLUENT
Sr. No.
Parameter Before Treatment
After Treatment
Disposal
1 pH < 2 6.5 Treated effluent will be send to Spray Dryer (Chhatral Environment Management System Pvt. Ltd.).
2 Total Suspended Solid
240 82
3 Total Dissolved Solid
70000 74000
4 Oil & Grease 10.0 7.0 5 COD 31000 29000 6 BOD 8000 7500 **All the parameter except pH is in mg/L
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Fugitive emission could occur from the storage yard of raw materials and finished products. The storage quantity is low since only 6 days inventory will be maintained at site and proper handling methods will be adopted. Emissions from transport of vehicles would occur to a certain extent. The emissions from traffic movements will be controlled by proper planning of the transport of raw materials and finished products to and fro from the factory premises. All the roads inside the plant will be concreted to reduce any dust emissions. Proper planning and maintenance will control the extent of fugitive emissions. During the production, the industry will carry out regular monitoring of fugitive emissions as per the factories Act. Measures taken for fugitive emission control:
• Proper storage of raw materials, products and fuels. • Ensuring closed feeding and sampling. • Establishing SOPs for start-up, shut down and maintenance operational
procedures. • Regular work place monitoring and ambient air quality monitoring as per
post project monitoring plan. 2.20 HAZARDOUS WASTE MANAGEMENT
The hazardous wastes generated by the industry & Method of Management and Handling is given In Table No. 2.16
TABLE NO. 2.16
DETAILS OF HAZARDOUS WASTES
Sr. No
Type of Hazardous Waste
Source Cat. No.
Quantity Management
1. ETP Sludge ETP 35.3 300 MT/Year
Collection, Storage, Transportation, Disposal to TSDF site
2. Discarded Bags/Containers/Drums
R.M Storage 33.1 80 MT/Year Used for packing of ETP waste or return back to supplier.
3. Used Oil D.G Set 5.1 20 Liter /Year
Storage into carboys and ultimately Reuse or sell to
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The various sources of noise in the Industry have been identified as under:
• Pumps • Compressor The typical Noise levels of equipment. As indicated by the Equipment manufacturers are given in Table No. 2.17
TABLE NO. 2.17 TYPICAL NOISE LEVELS OF EQUIPMENT
Sr. No.
Name of Machinery/Unit Noise level in Db
1. Pumps 60-65 2. Compressor 65-75
The following measures have been taken to reduce the noise levels to acceptable limits: i) Sound producing equipment are enclosed in the sound proofing
enclosure to give residual sound pressure level of 85 dB(A) and ii) Providing suitable ear protecting devices for working personnel.
Details of measures proposed for noise pollution abatement & its monitoring.
• Noise levels will be monitored and records of same will be maintained, at day
and night at 4-6 locations, fortnightly internally and monthly by third party (GPCB recognized Env. Agency).
• Also periodically workers will be examined for their hearing ability and accordingly corrective actions will also made if required.
• Good working conditions will be developed to avoid chances of Noise Pollution.
• Regular maintenance of machineries, machine guarding and enclosures for the Noisy machines will be done to avoid Noise Pollution.
• Even though Noisy machines will be strictly be operated in day time only. • Effective green belt will be developed to minimize effect of Noise Pollution to
surroundings. • Required PPEs will be given to workers.
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The Raw Materials, which are termed as Hazardous Chemicals as per the "Manufacturing, Storage and Import of Hazardous Chemicals Rules, 1989", are as listed in Table No. 2.18
Table No. 2.18 LIST OF HAZARDOUS CHEMICALS
Hazardous Chemicals
Reference The Manufacturer, storage & Import of Hazardous chemical Rules 1989
Maximum quantity that can
be stored at a time (MT)
Threshold Quantity in MT
Chloro Sulfonic Acid Sr. No. 136(Part II, Sch. 1 of MSCIR, 1989)
15 Not Listed
HCl Sr. No. 313(Part II, Sch. 1 of MSCIR, 1989)
30 Not Listed
Sulphuric Acid Sr. No. 591(Part II, Sch. 1 of MSCIR, 1989)
40 Not Listed
Liq. Ammonia Sr. No. 31(Part II, Sch. 1 of MSCIR, 1989)
40 50
Acetic Anhydride Sr. No. 3(Part II, Sch. 1 of MSCIR, 1989)
5 Not Listed
Oleum(65%) Sr. No. 444(Part II, Sch. 1 of MSCIR, 1989)
40 Not Listed
Sodium Hydroxide Sr. No. 571(Part II, Sch. 1 of MSCIR, 1989)
1 Not Listed
Aniline Sr. No. 37(Part II, Sch. 1 of MSCIR, 1989)
7 Not Listed
Acetic Acid Sr. No. 2(Part II, Sch. 1 of MSCIR, 1989)
2 Not Listed
Alpha Naphthylamine
Sr. No. 418(Part II, Sch. 1 of MSCIR, 1989)
10 Not Listed
Methyl Alcohol Sr. No. 377(Part II, Sch. 1 of MSCIR, 1989)
30 Not Listed
Formaldehyde Sr. No. 285(Part II, Sch. 1 of MSCIR, 1989)
3 Not Listed
DETAILS OF HAZARDOUS CHEMICALS
Name of Hazardous Chemicals
Toxicity (Oral LD50) mg/kg
Hazardous Characteristics
Chloro Sulfonic Acid
Not Available
Flammability of the Product: Non-Flammable. Auto-Ignition Temperature: Not Applicable Flash Points: Not Applicable
Precautions: Keep container dry. Do not breathe gas/fumes/ vapour/spray. Never add water to this product In case of insufficient ventilation,
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Flammable Limits: Not Applicable Products of Combustion: Not Available. Explosion Hazards in Presence of Various Substances: Explosive in presence of reducing materials. Non-explosive in presence of open flames and sparks, of shocks, of heat, of oxidizing materials, of combustible materials, of organic materials, of metals, of acids, of alkalis, of moisture. Fire Fighting Media and Instructions: Not Applicable.
wear suitable respiratory equipment If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes Keep away from incompatibles such as reducing agents, organic materials, metals, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package Storage: May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Corrosive materials should be stored in a separate safety storage cabinet or room.
Sulphuric Acid 2140 mg/kg [Rat.]
Flammability of the Product: Non-flammable. Auto-Ignition Temperature: Not applicable. Flash Points: Not applicable. Flammable Limits: Not applicable. Products of Combustion: Products of combustion are not available since material is non-flammable. However, products of decomposition include fumes of oxides of sulfur. Will react with water or steam to produce toxic and corrosive fumes. Reacts with carbonates to generate carbon dioxide gas. Reacts with cyanides and sulfides to form poisonous hydrogen cyanide and hydrogen sulfide respectively. Fire Hazards in Presence of Various Substances: Combustible materials Explosion Hazards in Presence of Various
Precautions: Keep locked up. Keep container dry. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, combustible materials, organic materials, metals, acids, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Storage: Hygroscopic. Reacts. violently with water. Keep container tightly closed. Keep container in a cool, well-ventilated area. Do not store above 23°C (73.4°F).
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Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of oxidizing materials.
Hydrochloric Acid
3124 mg/kg [Rat].
Flammability of the Product: Non-flammable Auto-Ignition Temperature: Not applicable Flash Points: Not applicable Flammable Limits: Not applicable Products of Combustion: Not Available Fire Hazards in Presence of Various Substances: of metals Explosion Hazards in Presence of Various Substances: Non-explosive in presence of open flames and sparks, of shocks. Fire Fighting Media and Instructions: Not Applicable
Precautions: Keep locked up.. Keep container dry. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, organic materials, metals, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area
Liq. Ammonia 350 mg/kg [Rat].
Flammability of the Product: Flammable. Lower Flammable Limit: 15.5 % Volume in Air (for NH3) Upper Flammable Limit: 27.0 % Volume in Air (for NH3) Auto-Ignition Temperature: 1204°F (651°C) (for NH3)
Handling: Avoid contact with either liquid or vapors. Direct contact with mercury must be avoided. Use proper PPE when working with or around aqua ammonia (See section 8). Storage: Ambient temperature. Store in dry, well- ventilated area away from incompatible materials. Protect against physical damage. Keep out of direct sunlight and away from heat sources.
Acetic Anhydride
1780 mg/kg
Flammability of the Product: Flammable.
Precautions: Keep container dry. Keep away
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316°C (600.8°F) Flash Points: CLOSED CUP: 49°C (120.2°F). OPEN CUP: 51°C (123.8°F). Flammable Limits: LOWER: 2.7% UPPER: 10.3% Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Flammable in presence of heat. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available Fire Fighting Media and Instructions: Flammable liquid. SMALL FIRE: Use DRY chemical powder. LARGE FIRE: Use alcohol foam, water spray or fog. Cool containing vessels with water jet in order to prevent pressure build-up, auto ignition or explosion. Special Remarks: Not available
from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Oleum(65%) 2140 mg/kg [Rat.].
Flammability of the Product: Non-flammable. Auto-Ignition Temperature: Not applicable. Flash Points: Not applicable. Flammable Limits: Not applicable. Products of Combustion: Not available. Fire Hazards in Presence of Various Substances: Not applicable. Explosion Hazards in
Precautions: Keep locked up.. Keep container dry. Keep away from heat. Keep away from sources of ignition. Keep away from direct sunlight or strong incandescent light. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. Avoid shock and friction. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical
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Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of heat, of oxidizing materials.
advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, combustible materials, organic materials, metals, acids, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area. Hygroscopic; keep container tightly closed. Will react with water or steam to produce heat and toxic fumes.
Sodium Hydroxide
2140 mg/kg [Rat.].
Flammability of the Product: Non-flammable. Auto-Ignition Temperature: Not applicable. Flash Points: Not applicable. Flammable Limits: Not applicable. Products of Combustion: Not available. Fire Hazards in Presence of Various Substances: of metals Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of heat.
Precautions: Keep container dry. Do not breathe dust. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If you feel unwell, seek medical attention and show the label when possible. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, metals, acids, alkalis, moisture. Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area. Do not store above 23°C (73.4°F).
Aniline 250 mg/kg [Rat.].
Flammability of the Product: Combustible Auto-Ignition Temperature: 615°C (1139°F) Flash Points: CLOSED CUP: 70°C (158°F).
Precautions: Keep locked up. Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/
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Flammable Limits: LOWER: 1.3% UPPER: 23%. Products of Combustion: These products are carbon oxides (CO, CO2), nitrogen oxides (NO, NO2...). Fire Hazards in Presence of Various Substances: Flammable in presence of open flames and sparks, of heat. Non-flammable in presence of shocks. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available.
vapor/spray. Wear suitable protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, metals, acids, alkalis. Storage: Air and light sensitive. Store in light-resistance container. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Acetic Acid 3530 mg/kg [Rat.].
Flammability of the Product: Flammable. Auto-Ignition Temperature: 463°C (865.4°F) Flash Points: CLOSED CUP: 39°C (102.2°F). OPEN CUP: 43°C (109.4°F). Flammable Limits: LOWER: 4% UPPER: 19.9% Products of Combustion: These products are carbon oxides (CO, CO2) Fire Hazards in Presence of Various Substances: Flammable in presence of open flames and sparks, of heat. Slightly flammable to flammable in presence of oxidizing materials, of metals. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available.
Precautions: \Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, metals, acids, alkalis. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
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Slightly explosive in presence of oxidizing materials.
Alpha Naphthylamine
Not available
Flammability of the Product: May be combustible at high temperature. Auto-Ignition Temperature: Not available. Flash Points: CLOSED CUP: 112°C (233.6°F). Flammable Limits: Not available Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Slightly flammable to flammable in presence of heat. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available.
Precautions: Keep away from heat. Keep away from sources of ignition. Empty containers pose a fire risk, evaporate the residue under a fume hood. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable p. 3 protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, moisture. Storage: MOISTURE SENSITIVE. Keep container tightly closed. Keep container in a cool, well-ventilated area. Do not store above 23°C (73.4°F).
Methyl Alcohol 5628 mg/kg [Rat.].
Flammability of the Product: Flammable Auto-Ignition Temperature: 464°C (867.2°F) Flash Points: CLOSED CUP: 12°C (53.6°F). OPEN CUP: 16°C (60.8°F). Flammable Limits: LOWER: 6% UPPER: 36.5% Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Highly flammable in presence of open flames and sparks, of heat. Non-flammable in presence of shocks. Explosion Hazards in Presence of Various Substances:
Precautions: Keep locked up.. Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, metals, acids. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and
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Risks of explosion of the product in presence of mechanical impact: Not available. Explosive in presence of open flames and sparks, of heat.
sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Formaldehyde 100 mg/kg [Rat].
Flammability of the Product: Flammable. Auto-Ignition Temperature: 430°C (806°F) Flash Points: CLOSED CUP: 50°C (122°F). OPEN CUP: 60°C (140°F). Flammable Limits: The greatest known range is LOWER: 6% UPPER: 36.5% (Methyl alcohol) Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Flammable in presence of open flames and sparks, of heat. Non-flammable in presence of shocks, of oxidizing materials, of reducing materials, of combustible materials, of organic materials, of metals, of acids, of alkalis. Explosion Hazards in Presence of Various Substances: Non-explosive in presence of open flames and sparks, of shocks. Fire Fighting Media and Instructions: Flammable liquid, soluble or dispersed in water. SMALL FIRE: Use DRY chemical powder. LARGE FIRE: Use alcohol foam, water spray or fog. Cool containing vessels with water jet in order to prevent pressure build-up, auto ignition or explosion.
Precautions: Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, acids, alkalis, moisture. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
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To prevent any spillage, accident and impacts of human health for safety measure will be taken while handling the raw material and products:
Occupational control measures for no health hazard to the worker and to keep the risk of accidents to a minimum from our manufacturing activities. Mitigatory measures: For the proposed project, company will make following arrangement within the factory premises for the different hazards:
Storage & Handling of Hazardous Chemicals: • Company will do planning to stock all the necessary material as
minimum as possible. • All containers with hazardous chemicals have labels indicating the
contents and warning of the hazard. • Necessary information on safe handling and first aid measures and
antidotes of major hazardous material will be available on the label. • Workers dealing with hazardous chemicals will be trained on health
risks and safe handling. • Exposure to hazardous chemicals will be minimized. • Liquid Hazardous chemicals will be transferred in closed piping system. • Separate storage section will be provided for storage of hazardous and
non-hazardous raw materials. • Drums / Tanks shall be located and marked in designated area of
hazardous chemical storage. • Tanks / Drums of proper MOC will be selected. • All tanks / Drums shall be uniformly tagged. • Level indicator shall be provided in tanks. • Dyke will be provided. • Industrial type electric fittings shall be provided. • Adequate fire fighting equipments will be provided. • Anti corrosive paint shall be done. • Safety instruction board will be displayed. • Proper earthling shall be provided. • Lightning arrestor will be provided.
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Vessel and other Equipment related: • Checking of process vessels and equipment is carried out regularly. • Records related to maintenance and its planning schedule is
maintained.
Safety Instructions for Transportation of Hazardous Materials:
• The name of the chemical along with pictorial sign denoting the dangerous Goods are marked on the vehicle and the packing material.
• The name of the transporter, his address and telephone number are clearly written on the road tanker and on the vehicle.
• The important safety precautions are mentioned on the tanker as a Warning label.
• Only trained drivers and cleaners are engaged in transport of hazardous Chemicals.
• The transporter and manufacturer must ensure the safe transportation of the material.
Tankers: • The tankers are checked for its fitness and safe condition before
loading. • During loading and unloading, the tanker should be braked and
isolated against any movement, while loading/unloading, use safety appliances.
• Check for leakages from the line connections before starting and stopping the filling operations.
• Drive the vehicles carefully, especially in crowded localities and on bumpy Roads.
• Do not apply sudden break. • The tanker should not be parked for long time on the way and
especially in Crowded Places. Park the vehicle away from residential areas.
Fire control plan: • Overhead water storage tank with adequate capacity is provided to
ensure 24 hr. supply. • Fire water tank with sufficient capacity of 100 KL (02 Nos.) will be
provided with fire pump (02 Nos.) • Fire hydrant system will be provided. • Sprinkler system will be provided at raw material storage area and tank
farm area. • Fire extinguisher will be provided at production plant as per the
requirement. Contact numbers of nearest fire agency will be provided. • Nearest fire station is Kalol. Time required to reach the project site is
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• Unit will appoint qualified and trained fire personnel having qualification
like B.Sc. or Diploma in Fire and Safety. • Flame proof equipments and fittings will be provided for handling of
hazardous chemicals. • Tanks and all pump motors shall be earthed. • Road tanker earthing lines shall provide near the unloading pumps. • Independent dykes will provide for hazardous chemicals storage to
contain leakages. Floors of the dyke area shall of impervious finish. • Housekeeping of the plant shall as per prescribed norms. Floors,
platforms, staircases, passages will be kept free of any obstruction. • All hazardous operations shall explain to the workers. They will
periodically trained on the hazardous processes. • Dedicated supply of firewater shall available in the plant. • Only authorized persons shall be allowed inside the plant. • All instrument and safety devices will be checked and calibrated during
installation. They will also be calibrated, checked at a frequent interval. Calibration records shall maintain.
• All electrical equipments will be installed as per prescribed standards. • All the equipments of the plant shall periodically tested as per standard
and results shall documented. All equipments undergo preventive maintenance schedule.
• The area will fence to isolate the same from all other departments. • Proper Earthing will be provided to each tank. Also earthing would be
taken care during solvent transfer from tanker into the underground vessel.
• Flame arrestors shall provide on each tank. • Flameproof pumps & motors shall provide for solvent transfer. • In addition to fire hydrant system, fire extinguishers will be installed at
different locations within premises. • Adequate ventilation arrangement shall provide for safe and better
working in the plant as per the standard. • Process, equipments, plant involving serious fire hazards are designed
as per prescribed guideline. • Sufficient access for fire fighting shall provide in the plant. • Protection against lightning will be taken care in the plant. • Precautions against ignition will be taken.
Table No. 2.19 Details of Fire and Safety Equipment
Sr. No. Type Total Quantity
1 Dry Chemical Powder 15
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Hydroxide • Wash with plenty of water if eyes or skin is affected. • Do not give chemical antidotes because it increases heat
and injury with reaction. Do not induce vomiting. 8. Aniline • Immediate treatment for aniline overexposure consists of
decontamination and cardiopulmonary support. Symptomatic individuals should be administered supplemental oxygen and the methemoglobin antidote, Methylene blue, as soon as possible
9. Acetic Acid • Milk of magnesia 10. Alpha Naphthyl
amine • IMMEDIATELY flood affected skin with water while
removing and isolating all contaminated clothing. Gently wash all affected skin areas thoroughly with soap and water
11. Methyl Alcohol • Ethanol (30% solution through oral, 5% solution through injection), epicake syrup, if Acidosis than Sodium bicarbonate, if effect of delirium than give10mg diazepam through injection.
12. Formaldehyde • Fresh Air/ Milk / Water • Milk, Activated Charcoal or water.
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2.24 ACTION PLAN FOR TRANSPORTATION OF RAW MATERIALS
AND PRODUCTS INCLUDING HAZARDOUS CHEMICALS:
Following safety precautions are suggested during transportation of hazardous chemicals in tankers / or other vehicles, while unloading, transportation and meeting the emergencies arising out of leakages and spillages of hazardous materials:
Safety Instructions for Transportation of Hazardous Materials:
• The name of the chemical along with pictorial sign denoting the dangerous Goods are marked on the vehicle and the packing material.
• The name of the transporter, his address and telephone number are clearly written on the road tanker and on the vehicle.
• The important safety precautions are mentioned on the tanker as a Warning label.
• Only trained drivers and cleaners are engaged in transport of hazardous Chemicals.
• The transporter and manufacturer must ensure the safe transportation of the material.
Tankers:
• The tankers are checked for its fitness and safe condition before loading.
• During loading and unloading, the tanker should be braked and isolated against any movement, while loading/unloading, use safety appliances.
• Check for leakages from the line connections before starting and stopping the filling operations.
• Drive the vehicles carefully, especially in crowded localities and on bumpy Roads.
• Do not apply sudden break. • The tanker should not be parked for long time on the way and
especially in Crowded Places. Park the vehicle away from residential areas.
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The unit will provide fire extinguishers based on probability and type of fire hazards at strategic locations. The unit will install approximately 05 fire extinguishers (Dry powder type) to tackle the fire hazards of Class A, B & C at different levels of the plant. The unit has also decided to provide fire protection arrangements in the form of fixed water spray system (1 No.) and fire hydrant systems (1 Nos.) to tackle any fire emergency arising due to storage of chemicals.
Details of Fire and Safety Equipment
Sr. No. Type Total Quantity
1 Dry Chemical Powder 15 2 Carbon dioxide 10
TOTAL 25 • Overhead water tank storage capacity: 25 KL ×4 • Underground water tank storage capacity: 100 KL ×2 • No. of Fire Sand Storage: 10 No.
2.26 COST OF THE PROJECT
The total project cost will be 450 lac including Building, machinery & others. Total capital and recurring cost towards Environmental protection Measures per annum will be 99.5 lac & 369.9 lac respectively.
TABLE - 2.21 Capital Cost & Recurring Cost of the Project
Sr. No
System Approximate recurring cost per annum (in Lac)
Approximate capital cost (Rs. In Lac)
Basis for cost estimates
1 Air pollution control
12.0 45.0 The capital cost would include cost of providing adequate height of the stack, ladder and platform, Air Pollution Control Systems and recurring cost would include cost of monitoring of air environment.
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335 40.0 Capital cost would include cost of ETP, Evaporation cost of Spray Drying etc. In capital cost civil work, mechanical work, Electrical work and piping work is included. Recurring cost is for operational phase.
3 Noise pollution monitoring
0.25 0.0 The recurring cost would include cost of noise monitoring.
4 Solid and hazardous waste management
15.0 12.0 Capital cost would include cost of providing storage space for hazardous waste and membership of TSDF Fee. Recurring cost would include cost of land filling and transportation.
5 Environment monitoring and management
2.0 0.0 The recurring cost would be incurred on hiring of consultants and payment of various statutory fees to regulatory agencies.
6 Green belt 0.8 1.5 Development of Greenbelt including Gardening and Plantation.
7 Occupational health (OHC)
0.8 1.0 Occupational health check up of Employees and workers
8 CSR 2.25 0 2.5 % of the project cost. Recurring cost will include cost allocated for the CSR activity like Educational, Drinking facility, Infrastructure facility, Green belt development, Tribal development, health and medical services etc.
9 CER 1.8
0 2% of the proposed project cost. Green belt development, Drinking water facility, solar Lighting etc.
Total 369.9 99.5
2.27 POWER REQUIREMENT
TABLE 2.22 POWER REQUIREMENT
Electricity DG Set Required Proposed Connected Load HP
Source 125 KVA
75 KW The Uttar Gujarat Vij Co. Ltd.
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The requirement of personnel for the Plant is met with keeping in view the following: • Technical support of Plant, including Process Control and
Instrumentation • Smooth and efficient operation of Plant • Effective co-ordination between the various Departments within the
Plant • Optimum organization with well-defined and judicious job distribution • Optimum utilization of different grades of workmen and supervisory
staff and Maximum capacity utilization of facilities. Total Manpower at BHIMANI DYECHEM INDUSTRIES will be summarized in Table No. 2.23
TABLE NO. 2.23 DETAILS OF MAN POWER
2.29 GREEN BELT DEVELOPMENT
The development of Green Belt is an important aspect for any plant because: • It acts as a 'Heat Sink' • It improves the Ambient Air Quality by controlling SPM in air • It helps in noise abatement for the surrounding area • It helps in settlement of new birds and insects within itself and • It increases the aesthetic value of Site.
Total plot area is 3344 Sq. meter. From that they had done planning for gardening and plantation for 1105 Sq. Meter.
Total Workers in all Shifts
Male Female Total
38 02 40
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• Unit will develop 25 trees in 1st year, 35 trees in 2nd year, 40 trees in
3rd year, 50 trees in 4th year, 60 trees in 5th year in and around the premises.
• The tree species selected for the plantation will be pollutant tolerant ,fast growing, wing firm, deep rooted and ever green.
• The company will select pollutant tolerant plant species. For example, Asopalav, Neem Tree, Gulmahor, Julie, etc.
• We will also develop plantation as per the MoEF guidelines all along the periphery of plant so that these trees perform as natural barrier and bring down the fugitive emission and stop carryover of dust along with wind current.
• The tree species selected for the plantation will be pollutant tolerant, fast growing, wing firm, deep rooted, and ever green. The company will select pollutant tolerant plant species.
They will also develop plantation as per the MoEF guidelines all along the periphery of plant so that these trees perform as natural barrier and bring down the fugitive emission and stop carryover of dust along with wind current.
2.30 SCHEME FOR RAIN WATER HARVESTING The source of water for the project is ground water. The unit has also proposed to design & implement rain water harvesting scheme within premises. The parameter considered for designing the Rain water harvesting is as follows:
• The average rainfall of the area considered for the design is 800 mm/year.
• The paved area available in front. • The amount of water collected from the run off. • The roof top area available. • The amount of water collected from the roof top. • Considering one hour of peak rainfall. • Total rain water to be collected.
Hence rain water harvesting pit will be made to collect the rain water from roof top and paved area based on the above data consideration.
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M/s BHIMANI DYECHEM INDUSTRIES.(Proposed project) has assigned M/s Bhagawati Enviro Care Pvt. Ltd. to conduct EIA/EMP study & Comprehensive hydro-geological & rainwater harvesting studies in Survey no.- 316, plot no.-02, Opp. Dharti Industrial estate, village: Dhanot, District Gandhinagar , Gujarat.-382729. The project area details are as under:
S. No. Particulars Area (sq. m )
1 Total Plot Area 3344
2 Roof top area 1929
3 Paved /road area 110
4 Green belt area /Open area 1305
The water supply by tankar of the project is 85.0 m3/day & it falls in city- Kalol
block of Gandinagar District, which falls under “Over-Exploited ” category
according to CGWB Publication “Dynamic Ground Water Resources of India –
2011”. The assignment was given to work out the scope of
geology,Hydrogeological & artificial recharge through detailed survey.
DESIGN OF RAINWATER HARVESTING: For good design of rainwater harvesting, following points are to be kept under
consideration:
(a) Ideal location with good ground slope.
(b) The location has adequate subsurface permeability of the aquifer to
accommodate maximum recharge of rainwater through injection well.
(c) Rate of filtration should exceed average rainfall intensity.
(d) Clogging of filtration media should be cleaned periodically.
(e) Ground water pollution does not take place.
ROOFTOP RAIN WATER HARVESTING: Total rooftop area of project is 1929 m2 that may be connected through pipes and
drains to Rainwater harvesting structures which has storage chamber and the
percolation pits as per sites having rooms for recharge in resonance with average
rainfall, catchment area and peak rainfall intensity. 196
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The total open area of project is 1305 m2 which may be connected through drains to
rainwater harvesting structures which has storage chamber and the percolation pits as per sites having rooms for recharge in resonance with average rainfall, catchment
area and peak rainfall intensity.
Following dimensional parameters are considered for design of open area rainwater harvesting system in the project premises.
Total open area = 1305 m2
Average rainfall = 857 mm = 0.86 m Catchment factor for open area = 0.15 (as per C.G.W.A) Total volume of water to be captured = 1305 x 0.86 x 0.15 = 168.34 m3
The dimension of the structures to be designed for 40 mm/hour peak rainfall intensity. Considering 15 minutes of peak rainfall, runoff volume in a single storm should be:
1305 m2 x 0.15 x 0.04 m/4 = 1.96 m3
DESIGN OF RAINWATER HARVESTING STRUCTURE: The total volume of water generated in project premises from rooftop, road/paved & open area in a single storm on 40 mm peak rainfall intensity would be
= 16.396 m3 + 0.825 m3 + 1.96 m3 = 19.175 m3
It is revealed from recharge test that the aquifer would good accept water to the
order of 0.85 m3/day @3.54 m3/hour continuously in long term through vadose zone.
Considering the space availability, Now, we will proposed percolation tank with 27
KLD capacity and such 1 structures will accommodate up to total rainfall volume of
24.83 m3 in any rainfall event at peak rainfall occurrence.
The individual design is made for accumulation of 27 m3 of water i.e. 18 m3 of water
in collection tank (3 m height x 3 m length x 2 m width and about 9 m3 in the
process of infiltration through filtration media of recharge well. Hence, the
dimensional parameters of collection chamber would be 3 m (length) x 3 m (width) x
2 (depth). The filtration tank dimension would be 3 m (length) x 3 m (width) x 1 m
(depth) with 0.15 m dia recharge well (1 nos.) of 8 m depth depending upon the
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TOTAL RECHARGE POTENTIAL On completion of Rainwater Harvesting & other recharge factors, additional recharge potential in the premises would be as under: 1. Rooftop Rainwater harvesting in the premises
1929*0.85*0.86 = 1410.099
2. Road storm water harvesting in the premises
110*0.86*0.75 = 70.95
3. Recharge due to open area in the premises
1305*0.86*0.15 = 168.34
4. Recharge due to return flow of water used in plantation
2*305*.05 = 30.5
Total 1679.88 (Note - formula =area * run-off coefficients* rain fall {mm/1000}) The recharge potential to be created by artificial measures will be 1679.88 m3/annum
which would help in maintaining groundwater regime in terms of quantity & quality.
RECOMMENDATIONS: The total volume of water generated in project premises from rooftop, road/paved & open area in a single storm on 40 mm peak rainfall intensity would be 19.175 m3. It is revealed from recharge test that the aquifer would good
accept water to the order of 85 m3/day @3.54 m3/hour continuously in long term
through vadose zone. Considering the space availability, Now, we will proposed
percolation tank with 27 KLD capacity and such 1 structures will accommodate up to
total rainfall volume of 24.83 m3 in any rainfall event at peak rainfall occurrence. The
individual design is made for accumulation of 27 m3 of water i.e. 18 m3 of water in
collection tank (3 m height x 3 m length x 2 m width and about 9 m3 in the process of
infiltration through filtration media of recharge well. Hence, the dimensional
parameters of collection chamber would be 3 m (length) x 3 m (width) x 2 (depth).
The filtration tank dimension would be 3 m (length) x 3 m (width) x 1 m (depth) with
0.15 m dia recharge well (1 nos.) of 8 m depth depending upon the formation for
recharge in aquifer through vadose zone.
One piezometers are proposed to be installed in the plant premises as per CGWB
norms for monitoring of season-wise water levels & water quality for ascertaining the
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Preparation of this study needs a datum on which the evaluation can be done. It is necessary to collect data about different environmental attributes that are being affected by the development of the region which, in turn, defines an existing environmental quality of the region to serve as the datum.
Base line data requirement is also necessary to identify environmentally significant issues as well as to enumerate the critical environmental changes that are occurred due to the industrial development of the region.
Here an attempt has been made to collect the information about an existing environment on the below mentioned eight major environmental attributes:
I - Air Environment
II - Meteorology
III - Water Environment
IV - Hydro-geomorphology
V - Noise
VI - Land Environment
VII - Ecology
VIII - Socio-economic
3.2. STUDY AREA
The study area for Baseline Environmental Quality is the area with a radius of 10Kms keeping project site as a centre. The same is shown in Figure No. 3.1 and the villages falls under the same is listed in Table No. 3.1.
Table No. 3.1Name of Villages in Study Area.
Sr. No. Name of village Distance from project Site
National Ambient Air Quality Standards are reproduced in Annexure 3.The State has not promulgated separate Ambient Air Quality Standards.
WATER QUALITY STANDARDS
Standards prescribed by BIS (IS 10500-91) and Indian Council of Medical Research (ICMR) for drinking water are given in Annexure 4.
AMBIENT NOISE QUALITY STANDARDS
National Ambient Noise Quality Standards are presented in Annexure 5.The State has not promulgated separate Ambient Noise Quality Standards.
3.4. AIR ENVIRONMENT
3.4.1. AMBIENT AIR QUALITY (AAQ) IN THE STUDY AREA
The collection of base line information for Air Environment includes identification of specific air pollutants being released into the atmosphere having significant impact on neighborhood. The Ambient Air Quality status, with respect to the identified air pollutants, has been studied at eight majorlocations. This has been done through Air Quality surveillance program and based on TOR.
The back-ground air quality for PM10, PM2.5, Sulphur Dioxide (SO2), Oxides of Nitrogen (NOx), CO, HC, NH3, HCl including VOCs was monitored. The monitoring for these parameters has been done at sites located in different directions and situated within the suspected impact zone, in and around the Proposed project site. We had considered minimum one monitoring station in the upwind direction and minimum one monitoring station in the pre dominant downwind direction at a location where maximum ground level concentration is likely to occur.
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The locations of the AAQ stations are based on prevailing meteorology, pollution source and available infrastructure facilities. One station has been particulary set-up in down wind direction.
Thus, monitoring has been done at eight sampling stations located in different directions and situated within the suspected impact zone in and around the existing project site.
The locations map of the AAQ monitoring station is shown in Figure No. 3.1 and tabulated in Table No. 3.2.
Table No.3.2Locations of Ambient Air Quality Monitoring Stations
At every sampling station, important parameters namely PM10, PM2.5, Sulphur Dioxide (SO2), Oxides of Nitrogen (NOx) including HC, CO,NH3, HCl, andVOCs were monitored. The results are given in Table No.3.4.a to 3.4.c.
The minimum, maximum, Average and 98 % of PM10, PM2.5, SO2 and NOxare as shown in Table No 3.3
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Monitoring and testing of ambient air quality were carried out for various parameters namely PM10, PM2.5, SO2, NOx, HCl, NH3 by using Respirable Dust Sampler (RDS). Twenty four -hourly samples were collected for PM10 ,PM2.5 and for SO2 & NOx 8 hourly samples were collected for the month of March – April – May - 2018.
The sampling and testing of Ambient Air Quality Parameters were carried out as per relevant parts of IS: 5182. The brief details of testing procedures adopted are given in Table No.3.5.
Table No. 3.5Details of Ambient Air Quality Monitoring & Analysis Procedures
Parameter Ambient Air Quality Monitoring & Analysis Procedure
PM10 Gravimatric Method, IS:5182, 11255 & Operational Manual of Instrument
PM2.5 Gravimatric Method & Operational Manual of Instrument
NOx Jacob & Hochheiser Method. Absorption in dilute NaOH and then estimating colorimetric with Sulphanilamide N(1-Nepthyl) Ethylene Diamine Dihydrochloride and Hydrogen Peroxide (IS : 5182 Part II : 1975)
SO2 Improved West & Gaeke Method.Absorption in Mercury Sodium Tetra Chloride followed by colorimetric estimation using P-Rosaniline Hydrochloride and Formaldehyde(IS : 5182 Part II : 1969)
VOC (Benzene, Toluene, Xylene,)
Instrumental manual method
CO and HC Instrumental manual methodNH3 Indophenol blue method, NAAQMS, CPCB Volume –
1HCl Methods of Air sampling and analysis, 2nd Edition
APHA
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3.5. METEOROLOGY Meteorological conditions, of the site, regulates the transport and diffusion of air-pollutants released into the atmosphere. Ambient temperature, wind speed, wind direction and atmospheric stability are called primary or basic Meteorological Parameters because the dispersion and diffusion of pollutants depend mainly on these Parameters. Humidity, precipitation, pressure and visibility are secondary Meteorological Parameters as this control the dispersion of the pollutants indirectly by affecting primary Parameters.
3.6. Baseline DataMeteorological data were obtained from our own meteorological station kept at Chhatral Environment management System Pvt Ltd. for the parameters namely ambient temperature, wind speed, wind direction, relative humidity for the period March, April and May 2018.The Wind Rose diagram for the month of March, April and May 2018. is shown in Figure No. 3.5.
3.6.1. Ambient Temperature
The monthly variations of monthly highest and monthly lowest temperatures recorded are as follows:
Location – Project site Temperature, oCMarch 2018 April 2018 May 2018
Maximum 41.1 41.5 43.0Minimum 20.0 22.0 18.5
3.6.2. Wind Speed
Wind speed determines the rate of diffusion and travel time of air pollutants. The results of monitoring are as follows:
Location – Project Site Wind Velocity, Km/hrMarch 2018 April 2018 May 2018
Maximum 10.1 7.8 33.3Minimum 0.0 0.0 0.0
3.6.3. Wind Direction
This is important in air pollution since it determines the direction of transport of air pollutants. The mean wind direction will be indicative of the direction of travel of the pollutants.
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The meteorological parameters namely: ambient temperature, wind speed, wind direction and stability class were obtained from our own meteorological station kept at Chhatral Environment management System Pvt Ltd. for the Period of March – April – May - 2018. As specific mixing heights were not available, mixing height based on CPCB publication “Spatial Distribution of Hourly Mixing Depth over Indian Region”, PROBES/88/2002-03 has been used.The windrose diagram is shown in Figure No. 3.4
Figure No. 3.4
Windrose Diagram FOR THE MONTH OF March– April – May 2018
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Mean Monthly Relative Humidity for Meteorological station kept at Chhatral Environment management System Pvt Ltd. is given in Table No.3.8
Table No.3.8Relative Humidity
Month Relative Humidity ( % )Minimum Maximum
March 2018 2.4 61.5April 2018 2.0 75.5May 2018 6.3 93.0
3.6.5. Climate & Rain Fall
The district experiences semi-arid type of climate. The rainy season lasts from June to September and coincides with south-west monsoon. Winter season last from November to February and summer season from March to June. About 95% of the annual rainfall is received during south-west monsoon season (June to Sept.), July being the heavy rainfall month. There is no climatological station in Gandhinagar, however, the IMD Station located at Ahmedabad Airport is quite close to Gandhinagar and is representative for the district. The general temperature in Gandhinagar district increases rapidly from February to May, the later being the hottest month with mean daily maximum and minimum temperature as 41° and 26°C respectively. The district is sometimes affected by cold waves due to western disturbances that pass across north India causing minimum temperature to drop the freezing point. In the monsoon months, the relative humidity is generally 65% or more. However, the rest of the year is comparatively dry. March and April are the driest months where the humidity in less than 45% dropping to 20% or less in the afternoons.
Rainfall plays a major role in groundwater availability. Almost 90% of the total annual rainfall is received during the southwest monsoon, The mean annual rainfall of last 5 years (2013 to 2017) for the nearest rain gauge station –Gandinagar is about 857 mm, based on IMD data.
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Table No.3.9Rainfall pattern at Gandinagar Rain gauge Station
Years Rainfall (mm)2013 1048.02014 677.52015 695.82016 653.62017 1207.2
Average
3.6.6. Topography
The topography of the project site and the study area of 10 km radial zone are almost plain. The average elevation of the study area is about 68 m -73 mabove mean sea level. There are no hills or hillocks in the study area. The site area is plain with little undulating at few places. Agriculture and allied activities are most predominant in this area. Fallow land and barren lands were less observed near project site. There was no any Eco Fragile Zone or Natural Forest Observed near project site in study area.
Buffer Zone/Drainage:The study area is a part of kolol, gandhinagar district and having average
elevation of 68 m to 73 m above mean sea level .
Buffer Zone:-The topography of the project site and the study area of 10 km radial zone are
almost plain. The average elevation of the study area is about 71 m above
mean sea level. There are no hills or hillocks in the study area
Core Zone:-The project area has built up and opens part, comprises of soil and has flat
terrain. The open area is covered by alluvium, which is used for grassing and
paved. The project site lies latitude 23° 17' 14.1684'' N and 72° 25' 1.0704''E.
[Toposheet no.- 1) F43A07 2)F43A08 3)F43A11 4)F43A12 ] The average
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ground elevation of the study area is 70 m from mean sea level. Vegetation is
present along the boundary wall. There are no major nalah and river.
3.6.7. Mixing Height
As specific mixing heights were not available, mixing height based on CPCB publication “SPATIAL DISTRIBUTION OF HOURLY MIXING DEPTH OVER INDIAN REGION”, PROBES/88/2002-03 has been tabulated in Table No.3.10
Table No.3.10Hourly Mixing Depth over Indian Region
Noise, often defined as unwanted sound, interferes with speech communication, causes annoyance, distracts from work and disturbs sleep thus deteriorating quality of human environment.
The noise is generated from multiple sources such as medium and heavy industries, urban activities in the commercial and human settlements, and vehicular traffic in the region.
The noise level in the study area has been measured through Leutron sound level meter, for a period of one day for 30 minutes interwal at each monitoring station.
In the study area noise levels were monitored in eight locations at different locations for day and night time and are given Table No.3.11
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Water is the most vital resource for all kinds of life. It should not only be available in sufficient quantity but should be of good quality as well. Defilement of water, as a result of human activities, industrial activities and consequent pollution of water, cause deterioration of the water environment.
3.9.1 BASELINE DATA COLLECTION GW & SW
Physico-chemical Parameters have been used for assessing the base line quality of ground water environment and identification of impacts due to the proposed project.
Methodology for Water Quality Monitoring
The Samples, under all categories, were analysed for various Parameters specified by the Department of Environment. For the collection, preservation and analysis, APHA/IS methods were followed. The requisite Procedures, laid down in APHA/IS methods, were adopted for preserving the Samples with suitable preservative chemicals. The Samples were analysed within the time limits prescribed for each Parameter.
Ground water sources and surface water sources covering 10-km radial distance were examined for physico-chemical, heavy metals and bacteriological parameters in order to assess the effect of industrial and other activities on ground water and surface water. The samples were analyzed as per the procedures specified in 'Standard Methods for the Examination of Water and Wastewater' published by American Public Health Association (APHA).
Samples for chemical analysis were collected in polyethylene carboys. Samples for bacteriological analysis were collected in sterilized glass bottles. Selected physicochemical and bacteriological parameters have been analyzed for projecting the existing water quality status in the study area. Parameters like pH and temperature were analyzed at the time of sample collection.
The details of surface and ground water sampling locations are given in Table 3.13 and sampling locations of ground water quality and surface quality monitoring are shown in Figure 3.3. The physico - chemical characteristics of the ground water samples and surface water samples are presented in the Tables 3.14.
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The monitoring has been done at eight sampling stations located in different directions and situated within the suspected impact zone in and around the project site.
Table No. 3.13Locations of Water Quality Monitoring Stations
Sr. No.
Type of sample Water sample location
1 Ground Water Near Project Site Bore water
2 Ground Water Chhatral tap Water3 Ground Water Budasan Tap well4 Ground Water Ankhol Tap Water5 Ground Water Indrad Tap well6 Ground Water Dhanot Tap Water7 Ground Water Acharasan Tap Water8 Ground Water Karannagar Tap water9 Ground Water Kadi Tap water
10 Surface Water Narmada Canal water11 Surface Water Chhatral Pond12 Surface Water Budasan Pond
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Geological Structure of Gujarat state and Figure no. 3.6 of Geology plan of Study Area. No other rock formations are exposed in the area.
The area forms part of North Gujarat Alluvial Plain with elevations ranging from 40 to 50 m MSL. The area is under lain by post Miocene alluvium comprising sand, gravel, silt and clay. The alluvium is about 400 m thick under lain by tertiary formation. The alluvium mainly consists of palaeo deltaic, fluvial and Aeolian sediments, comprising alternate bands of fine to course grained sand, gravel and yellowish brownish sticky clay.
REGIONAL GEOLOGYThe Quaternaries which comprise mainly alluvial sediments rest on the
Tertiary sediments which in turn lie on the Deccan Traps Himmatnagar
Sandstone of Cretaceous age is exposed along the Seatmate river
The stratigrsphic sequence of the area is given below:
LOCAL GEOLOGY:-In the project side, no out crops are seen. The area belongs to deccan trap
age. The litho logically, the area covered with soil which have 3-5 m thickness.
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Source: Water Resources Dept from http://guj-nwrws.gujarat.gov.in/
3.11 TYPE OF SOILS
Soil may be defined as a thin layer of earth’s crust that serves as a natural medium for the growth of vegetations. It is the unconsolidated mineral matter that has been subjected to and influenced by genetic and environmental factors. Soil serves as a reservoir of nutrients for plants and crops and also provides mechanical anchorage and favourable tilth.
The sub soil condition below the existing ground level is almost uniform in nature. Sub soil is composed of Clay mixed with little fine grained silty sand, moram and Kankar with low resistivity due to clay and soil moisture. The area is covered with recent to sub recent alluvial deposits comprising of brownish clay mixed with little fine grained sand, silty sand. The Soil below ground level consist of top silty low plastic soil layer having no swelling nature. Blockish brown to yellowish brown clayey silt or sand silt layer extends to the depth of 2 to 3 mts.
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The soil samples were collected from different places in the study area. The soil samples are taken from eight villages.
The present study on soil quality establishes the baseline characteristics in the study area surrounding the project site. The study has been addressed with the following objectives.
o To determine the base line characteristics
o To determine the soil characteristics of plant site and surrounding areaswith in 10 km radius.
o To determine the impact of industrialization/Urbanization on soilcharacteristics.
o To determine the impacts on soils from agricultural productivity point ofview.
At each sampling site, the samples were collected at random at a depth of 15 cms and mixed together to form a composite sample. Large stones, gravels and plant roots were removed from soil.
The homogenized soil samples collected at different locations were packed in a polyethylene plastic bag and sealed. The sealed samples were sent to laboratory for analysis. The important physical, chemical parameter concentrations were determined from all samples. The soil was then crushed and water suspension was prepared. The supernatant liquid was then subjected to Physico-Chemical analysis.
Standard Procedures were followed for analysis. The results of soil analysis are tabulated in Table No. 3. 15
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provides a flexible environment and a powerful tool for the manipulation and
analysis of spatial information for land cover feature identification and the
maps of all variables were combined to extract information to better
understand analyzing. Satellite remote sensing, in conjunction with geographic
information systems, has been widely applied and been recognized as a
powerful and effective tool in analyzing land cover/use categories This study
made use of remotely sensed data and GIS technologies; to evaluate
qualitatively and quantitatively outcome of part of land cover/use distribution.
Obtained results were compared, visualized and analyzed, in Geographic
Information System.
The Study Area up to 10 kms radius from the proposed project Site comprises
of 40 villages of Gandhinagar & Mehsana District.The locations of these
villages are shown in Figure No. 3.1.
The important land uses, as classified by the Census Records, are the Forest,
Land irrigated by different water sources, un-irrigaed areas, Cultivable waste
land and areas not available for cultivation.
Landuse and landcover distribution in the study area has been estimated using
the satellite imagery of generated from Landsat ETM+ scene of October 2006
(Refer: Figure 3.7). The landuse and landcover pattern of the study area (10
km radial zone) has been studied by the same. The land use distribution in the
study area (10 km radial zone) is presented in Table 3.16.Table 3.16:
Land Use Distribution in Study Area (10 km Radial Zone)
Area Calculation Sr no Discription Area in Sq.
KmArea in Ha percentage
1 Habitation 21.69 2169.18 6.912 Industrial area 11.10 1110.48 3.533 Agricultural 211.04 21104.00 67.184 Land Without Scrub 3.93 393.11 1.255 Water Body 1.64 164.21 0.52
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Hydrology is the science that deals with the depletion and replenishment of water resources. It deals with surface as well as ground water. The water below the water table is known as ground water and water above the water table is known as soil moisture. The water table map and water quality map of study area is attached as a Figure No. 3.7.
The area forms part of North Gujarat Alluvial Plain with elevations ranging from 40 to 50 m MSL. The area is under lain by post Miocene alluvium comprising sand, gravel, silt and clay. The alluvium is about 400 m thick under lain by tertiary formation. The alluvium mainly consists of palaeo deltaic, fluvial and Aeolian sediments, comprising alternate bands of fine to course grained sand, gravel and yellowish brownish sticky clay..Ground water & Narmada water is the main source of water in the study area. Ground water is utilized for almost all uses in the area. Generally, every village has open wells and hand pumps to draw water for domestic uses. In addition to that, there are rain water storage ponds at each village of the study area, which are used by the villagers for irrigation, domestic applications other than drinking and also for cattle feeding.
The hydrogeology investigation work carried out in the study area, reveals that the litho logical logs of exploratory bore holes, electrical logging results by govt. agencies in and around Kadi taluka have been studied to understand the subsurface geology and the aquifer system. These bore holes have penetrated the thick sequence of post Miocene sediments down to 300 + m depth. The hydro geological cross sections have been prepared by CGWB to study the subsurface geology and aquifer system in the area. It is reveals that the existence of multilayered aquifer system, within a depth of 300 + m bgl. In general three distances confined aquifer with thickness varies from 12 to 30 m can be identified. The aquifer lies between,
i. 45 to 90 mii. 100 to 180 miii. 180 to 260 m bgl, Separated by clays.
The district forms a part of Cambay basin and is occupied by quaternary alluvium comprising mainly of sand, gravel, silt clay and Kankar etc. The Hydro-geological map of the district is presented as figure- . The ONGC has established that the thickness of alluvium in the North Gujarat is about 700 m. However. As per the studies carried out by CGWB under UNDP Project the Miocene formations were encountered within 611 m at the deepest borehole drilled in the district at
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Sardhao. There is a sequence pf alternating layers of granular sandy and clayey horizons, the uppermost granular zone varies in thickness from 5 to 65 m. it is underlain by a thick clay bed followed by alternating sequence of arenaceous and argillaceous horizons.
The granular horizons occurring at various depths forms potential aquifers. The aquifer system of the district is described below. Aquifer System Geological survey of India during its studies had identified three confined aquifers within a depth of 600 m in the adjoining Mahesana district. These were designated as “A”, “B” and “C” aquifers. Subsequently, the studies carried out by CGWB under UNDP project, which also covered the northern part of Gandhinagar district, a multi-aquifer system was established. A total of 7 aquifers zones, each separated by aquiclude of varying thickness, were identified as “A”, “B”, “C”, “D”, “E”, “F” and “G”. Of these first five i.e. “A to E” represents Quaternary alluvium, whereas, last two i.e. “F & G” represents Miocene sediments.
A brief discussion of these aquifers is given in table. The thickness of quaternary alluvium is limited in the eastern part and all the aquifers are not developed in this part. Moreover, identification of different aquifers also becomes very difficult in the eastern part due to limited thickness of aquiclude. However, the aquifer system is well developed in the western part. The aquifers in the entire district are the southward and eastward extension of those identified in the UNDP Project area. The aquifer “A” in the district occurs as phreatic and semi-confined aquifer. The thickness varies from less than 25 m in the east to more than 80 m in the 9 western part.
Most of the dug wells and shallow tubewells tap this aquifer. However, over the years it has gone dry and at present occurs as saturated zone only in the vicinity of Sabarmati River and in the eastern parts of Dahegam & Gandhinagar Talukas. The aquifer “B” and “C” which occurs within a depth of about 225 m, are the most exploited aquifer in the district and most of the tubewells constructed tap these aquifers. Aquifer “D” is also being developed in some parts of the district particularly in Mansa and Kalol Talukas. The deeper aquifers, i.e., “E”, “F” and “G” are required to be properly explored and tested for future use. The depth of most prolific and most exploited aquifers in the district range from about 50 m to more than 300 m. The depth of tubewells gradually increases from east to west. The Dug-cum-bore wells and shallow tubewells (<100m) are feasible in the eastern part. However, in the western part only deep tubewells are feasible. The feasible depth of tube wells ranges from less then 100 m in the eastern part to more than 300 m in parts of Mansa Taluka. The tubewells tap all potential zones upto the depth constructed. The aquifers being tapped are “B and/or C” in major part of the district. However, aquifer “A” and “D” are also being developed either in isolation or in combination of other aquifers in the eastern and western parts respectively.
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There are 4 National Parks and 21 Wildlife Sanctuaries in Gujarat; however, none of them are falling in the study area. The Forest Vegetation Map of Gujarat is shown in Figure 3.8 and National Parks with Wildlife Sanctuaries Map of Gujarat is shown in Figure 3.9:
Figure NO: 3.8
Forest Vegetation Map of Gujarat
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There are no protected areas in the vicinity of the project area. There are alsono monuments of historical and archaeological importance within the studyarea.
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Baseline data such as demographic pattern, occupational status, educational, health and other amenities as existing in the study area have been studied.
The study of socio-economic component of environment incorporates various facets, viz. demographic structure, availability of basic amenities such as housing, education, health and medical services, occupation, water supply, sanitation, communication and power supply, prevailing diseases in the region as well as features such as places of tourist attraction and monuments of archaeological importance. The study of these parameters helps in identifying predicting and evaluating the likely impacts due to project activity in the surrounding region.
M/S. Bhimani Dye Chem Industries is a proposed unit located at Survey No.: 316, Plot No.: 02, Opp/ Dharti Industrial Estate,At: Dhanot,Tal: Kalol, Dist: Gandhinagar Gujarat. In their proposed unit, they will manufacture Synthetic Organic Chemical (dyes & dyes Intermediate) @ 225 MT/M.
Considering scale of unit and its categorization, according to EIA notification dated 14th September 2006, by Ministry of Environment & Forest (MoEF), Government of India, their Proposed manufacturing activity is falls under Synthetic Organic Chemicals – Schedule 5(f)) & cat -A. For that unit needs Environmental clearance from Ministry of environment and forest climate change..
The study area for the project has been considered 10 km peripheral from Gandhinagar & Mehsana district of Gujarat state from the project boundary. Seven villages, two towns and four wards are falling from Kalol Tehsil of Gandhinagar District. Thirty villages and one town are falling from Kadi Tehsil from Mehsana District respectively. Total 37 villages, 02 towns and 04 wards are falling from 02 Tehsil and 02 district in the study area.
On the basis of available census data, 2011 different aspects of socio economic condition of all total 37 villages, 04 wards and 02 towns in the study area have been analyzed and presented in Table 3.1 Study Area map is given at Figure 3.1
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Socio- Economic StatusThe latest available data have been complied to generate the existing socio-
economic scenario of the study area. Information on socio-economic profile was
collected from the Primary Census Abstract CD 2011, including the population
details of the region and Village Directory CD 2011, having the details of basic
amenities available in the region. In the 10km radius study area constitute
Gandhinagar & Mehesana districts from Gujarat state.
The villages surveyed under Study Areas are shown in Table 3.12. The details of village and ward wise (rural and urban) demography and the occupational structure of the Study Areas are appended (Table 3.18) Literacy details in Table 3.19 The Socio-Economic status of the above eleven study areas is mentioned below:
Demographic StructureDetails regarding the demographic structure of the region were collected from
Primary Census Abstract of Gandinagar and Mehesana districts of Gujarat for
the year 2011.
Demographic details such as number of persons per household, total area,
population density, sex ratio, SC and ST population, and literacy rate and
employment pattern are summarized .The salient observations are as follows:
Population Structure
As per 2011 Census, total population of the study area was 338748, out of
which male population was 178376(53%) and female population was
160372(47%)
Total number of households were 70770 with average occupancy of 4.79
persons per household
Total child (below 6 years of age) population was 40791(12%)
Total SC population was 35060(10%) , and ST population is 3025(1%)
available in the study area
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Economic resource base of any region mainly depends upon its economically active group i.e. the working population involved in productive work. Work- Work may be defined as participation in any economically productive activity. Such participation may be physical or mental in nature. Work involves not actual work but also effective supervision and direction of work. It also includes unpaid work on farm or in family enterprise. The employment pattern of worker and Main worker of the study area is described below and presented in Table 3.20 as well as in Figure 3.15
According to 2011 Census, total worker population in the study area was
117899(35%).
Main workers were 104250(31%) and marginal workers were 13649(4%).Total non-
working population was 220849(65%)
Types of main workersMain workers are classified in four categories as cultivators, agricultural
workers, household industry workers and other workers. As per 2011 Census, Out of
total 104250 main workers in the study area, there were total 10310 cultivators (10%),
12967 agricultural workers (12%), 1264 household industry workers (2%) and other
workers 79709(76%). Mostly in main workers population other workers were highly
found in study area.
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Environmental Impact Assessment (EIA) is an activity or an attempt to identify, predict, evaluate and communicate the likely environmental impacts of the Proposed project as well as proposed project on the surrounding environment. The major element involved in the process of Environmental Impact Assessment is the Identification of impacts as it forms the basis for quantification and evaluation of impacts. In this section, the impacts on the environment, either beneficial or deleterious due to the proposed project have been identified. The aspects of the environment, which are likely to be disturbed or damaged due to the proposed project, are represented as parameters. Prediction of impacts is the most important component in the Environmental Impact Assessment studies for quantification and evaluation of impacts. Several scientific techniques and methodologies are available to predict impacts of developmental activities on physical, ecological and socio-economic environments. Such predictions are superimposed over the baseline (pre-project) status of environmental quality to derive the ultimate (post-project) scenario of environmental conditions. The prediction of impacts helps in minimizing the impacts on environmental quality during the post project execution. The identified impacts for various components of environment viz., air, noise, water, land, socio-economy, etc. are presented herewith. EIA is an activity or an attempt to identify, predict, evaluate and communicate the likely environmental impacts of the activity/project on the environment.
ENVIRONMENTAL IMPACT ASSESSMENT STUDY INCLUDES:
• Identification of all the probable impacts (be it positive or negative) of the various
activities involved in the completion of the project. • Classification of the probable impacts i.e. positive or negative, reversible or
irreversible, short term or long term. • Evaluation of the probable impacts i.e. qualitative and quantitative assessment of
the likely impacts. • Communication to the general public, interested parties, controlling authorities
(Government or Municipality) through a Public Hearing process, revealing all the probable impacts, which are likely to occur due to the Proposed project, on the environment. It also includes the mitigation measures of those impacts, which are inevitable.
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This chapter presents the identification, prediction and evaluation of impacts with mitigation measures of the proposed project of M/s. Bhimani DyeChem Industries effected in the baseline environmental status.
4.2 IMPACT IDENTIFICATION
Considering that identification of significant environmental impact is essential in the preparation of EIA report, an attempt has been made here through the use of “Activity Effect” Matrix.
IDENTIFICATION MATRIX
The impact identification matrix is shown in the Table No. 4.1. For simplicity the entire project has been divided into two phases:
1. Construction Phase
2. Operation Phase
Various activities belonging to each phase have been grouped separately and arranged in Columns. The environmental Factor or Parameter, which are anticipated to be impacted, has been arranged in Rows. A preliminary scrutiny has been done and the cells, which fall at the junction of the ‘Activity’ and ‘Factor’, that have possible interaction with each other, have been ‘marked’. The matrix thus establishes the possible ‘cause-effect’ relationship and identifies the environmental factors likely to be impacted and activities responsible for the same. The impact identified may be positive and negative, short term and long term, reversible and irreversible, minor and major. This determination will be done at prediction stage.
A. Construction Phase
Unit needs to do construction activity for installation of plant machineries. The various activities involved in construction phase of a proposed project are listed below: • Construction / foundation. • Erection/Installations of equipment and machinery • Transportation • Material handling • Employment of labour • Green belt development
B. Operational Phase
The activities involved in the operation phase of the proposed project are listed below:
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Land Env. Biological Env. Socio Economics Fuel & Energy
Air Quality
Water Availability
Water Quality
Land Use Pattern
Soil Forest Eco- Logy
Demo-graphic
Eco. Structure
Basic Amenities
Health
PLANT CONSTRUCTION PHASE Construction / Foundation √ √ √ Erection of equipment and machinery √ √ √ Transportation Material handling √ √ √ √ Employment of labour √ GBD √ √ √ √ √ √
This section is devoted to the prediction and assessment of impacts, which are the most important components of EIA. Such predictions are superimposed over the base-line status of the environmental quality to derive the ultimate environmental scenario.
4.3 IMPACT PREDICTION AND ASSESSMENT WITH MITIGATIVE MEASURES:
This section is devoted to the prediction and assessment of impacts, which are the most important components of EIA. Such predictions are superimposed over the base-line status of the environmental quality to derive the ultimate environmental scenario. Prediction involves determination of the nature and extent of the probable impacts due to the proposed Project. Here it is determined, whether the likely environmental impacts are: 1. Positive or Negative 2. Long term or Short term Prediction of impacts during the construction and operational phase is as Shown in Table No 4.2. Based on Environmental Impact Analysis, the Environmental Impacts under this step are quantitatively and qualitatively assessed. Quantitative assessment with the help of a mathematical model has been done wherever possible. In other cases, the impact assessment has been qualitative which is based on available scientific knowledge and judgment. The mathematical model used for prediction in the present study includes “Aermod view” model for ambient air quality. For other cases i.e. Water, Noise, Land/Soil, Ecology, Socioeconomic etc., the available scientific knowledge and judgments have been used.
4.4 AIR ENVIRONMENT
A. Impact during Construction Phase:-
The impacts during construction phase will be short-term impacts as they will be limited to the period of construction. These activities may result in temporary increase in SPM levels, primarily, in the working environment. Following mitigative measures during construction phase have been planned
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Main Impacts during construction period is dusting and Air Pollution from vehicles. There will be impact on Air Environment during construction phase and also during operation phase. The impact during construction phase will be short term and reversible. However impacts during operation phase will have long term impacts due to flue gas emission as well as process gas emission. But suitable air pollution control measures will be adopted to keep the quality of air emission below the prescribed norms so as to have minimal impact on air quality. The main sources of emission during the construction period are the movement of equipment at site and dust emitted during the leveling, grading, earthwork, foundation works and exhaust emissions from vehicles and equipment deployed during the construction phase is also likely to result in marginal increase in the levels of SO2, NOx, SPM and CO.
B. Mitigation measures during Construction Phase :-
The activities like site development, construction and vehicular traffic contribute to increase in SPM and NOx concentrations. The mitigation measures recommended to minimize the impacts are:
o Water sprinkling in construction area.
o Proper maintenance of vehicles and construction equipment.
o Tree plantation in the area earmarked for greenbelt development.
Hence, the impacts on ambient air quality during construction phase will be marginal temporarily and reversible in nature (for short duration) and restricted to small plant area only.
C. Impact during Operational Phase:-
The impacts on air quality from project depend on various factors like design capacity, configuration, process technology, raw material, fuel to be used, air pollution control measures, operation and maintenance. Apart from the above, other activities associated with transportation of fuel, raw materials and finished products, storage facilities and material handling within the plant premises may also contribute to air pollution. 1. Source of Air Pollution
The operational phase activities are expected to have long - term impacts on the air quality. The main sources from project are Flue gas emission, process gas emission, Fugitive emission etc.
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Steam Boiler, Hot Air Generator and DG set will be the main sources of emissions from the plant. BHIMANI DYECHEM INDUSTRIES proposed to use Agro waste / Bio coal/ natural gas in steam boiler of capacity 3 TPH and second boiler capacity 3TPHand HAG capacity 10 lac K. Cal/hr. 125 KVA DG Set will be kept as standby power during power failures. PM, SO2 and NOx are the main air pollutants generated from the only boiler and DG set. The emissions from the boiler stack and DG Set Stack are given in Table 4.6, 4.7 & 4.8. Generally, the operational activities are expected to have long-term negligible impacts on the air quality. The operational activity from proposed project is expected to have long term impact on the air quality. Generally, the operational activities are expected to have long-term impacts on the air quality. Based on the above stated facts, predictions related to the Ground Level Concentrations (GLCs) have taken into account the flue gas emissions from the proposed stack attached to Steam boiler. 3. Process/Fugitive Emissions
The most probable emitted pollutants from process are NH3, HCl ,SO2and SPM. The emission from the process is mainly liberated gases from various reactions. The various gases emanating from reactions shall be scrubbed in two stage scrubber system to control the gaseous emission into the atmosphere, by using the suitable scrubbing media. Apart from this all the reactors are connected with primary and secondary condensers to mitigate the solvent evaporation losses from process. Fugitive emission :
The main sources of fugitive emissions from project are handling of raw materials and Solvents like Benzene, TNBA, Methanol, ODCB, Butanol. The solvents will be stored in drums in elevated flat from under the roof. Bulk quantities will be stored in storage tanks with vent condensers to avoid the fugitive emissions. Solvents are handled in closed conditions thereby reducing the losses in the form of evaporation.
Data used for the evaluation of the Ground Level Concentration for the proposed project is given in the Table No. 4.4. All the suitable precautionary measures will be taken for the control of fugitive emissions.
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4. Prediction of Impacts on Air Environment The concentration of pollutants at the ground level has been computed using computer model to assess the impact of source emissions from the proposed stack which will be installed. Air quality impact assessment is an important study; Mathematical modeling is an established and accepted technique to predict the air quality.
In this study, impact on environment due to the proposed plant has been assessed with the help of Mathematical modeling following the Central Pollution Control Boards Guidelines. The mathematical model used for conducting the study is the latest version of AERMOD developed by the Lakes Environmental Software, which is entirely in line with the requirements of Central Pollution Control Board, New Delhi. A mathematical model developed by the Environmental Protection Agency (EPA) is used for calculating GLCs. This is based, on the original Gaussian Plume Model equation but is defined in terms related to atmospheric phenomenon.. The average and maximum Ground Level Concentrations (GLCs) have been determined for SPM, SO2 and NOx. The average 24hrs. concentrations have been determined in polar grid of 100 up to 3600 for a distance of 100 m, 200m, 300m, 500m, 1000m, 2000 m, 3000 m, 4000m, 5000 m, 7000 m, 8000 m, 9000 m and 10000 m. has been calculated based on the micro-meteorological data collected from the meteorological station kept at the project site of Chhatral Environment Management system Pvt. Ltd. The objective of dispersion modelling is to predict the ground level concentration during the operation of plant and its impact on ambient air quality of the area. Air quality assessment is done by integrating the measurement techniques and modelling tools. The air modelling tools are routinely used in the environmental impact assessments, risk analysis, emergency planning, and source apportionment studies. Recent strategies for air pollution control in industries have largely neglected the emission reduction measures which are the prime polluting sources. To accomplish this, various air dispersion models have been developed and used worldwide so far for different applications under different scenarios. The Gaussian plume model is a standard approach for studying the transport of pollutants due to turbulent diffusion and advection by the wind. Applications of such models have been made mandatory. In this study, the AERMOD (the American Meteorological Society/Environmental Protection Agency Regulatory Model Improvement Committee’s Dispersion Model, Gaussian dispersion model is selected to predict the ground level concentrations (GLC’s) of Particulate Matter (PM) µg/m3, sulphur dioxide (SO2) µg/m3 , and oxides of nitrogen (NOx)- µg/m3, Ammonia- µg/m3, HCl- µg/m3, from point source emissions will be investigated in the study area.
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Prediction of GLC values are made by using AERMOD software approved
by U.S. Environmental Protection Agency (USEPA) and has adopted it as
its regulatory model since 2005. In point source emissions, the stacks are
subjected to plume rise which again is dependent on force of buoyancy
and momentum. The higher is the plume rise or stack, the lesser will be
ground level concentrations (GLC’s).The emissions when released into
the atmosphere are subjected to transportation, dispersion,
transformation, and fall out and wash out and finally reach the ground
level at a particular distance and concentrations. The relationship between
the source of emissions and its magnitude with the ground level
concentrations (GLC’s) at receptor points is governed by air dispersion
models which take into the account by the source strength, plume rise,
atmospheric stability, mixing height, wind velocity, terrain and other
meteorological conditions. The comparison between the predicted and
field sampled downwind concentrations for PM, SO2 & NOX (µg/m3) will
be carried out in this study to predict the average downwind ground
level concentrations (GLC’s)
Data Used for Computation
Stack emissions data have been used HCl & NH3 for prediction of short-term incremental GLC values of PM, SO2 & NOx using the meteorological data collected during the March – April – May 2018. Details of the data used for computations are given below
Meteorological Data
The meteorological data recorded continuously during the month of March 2018 to May 2018, on hourly basis. AERMOD model requires hourly surface data values for wind speed, wind direction, temperature, relative humidity and cloud cover. Both data files for the surface and profile files were then used to generate the meteorological file required by the AERMOD dispersion model using the AERMET meteorological pre-processor. This AERMET has three stages to process the data. The first stage extracts meteorological data and assesses data quality through a series of quality assessment checks. The second stage merges all data available for 24-hour periods and writes these data together in a single
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intermediate file. The third and final stage reads the merged meteorological data and estimates the necessary boundary layer parameters for dispersion calculations by AERMOD.
Dispersion Modeling Results
The 24 hourly average ground level concentration (GLC) values from plant
have been computed for PM, SO2 & NOx, NH3, HCl considering
topographical features around the plant and applicable stability classes.
The maximum 24 hourly average GLC values for PM, SO2 & NOx, HCl.
NH3 from plant are given in Table 4.6 to 4.10. Corresponding isopleths
plotted are shown in Figure 4.1 to Figure 4.5 for SPM, SO2 NOx, NH3
and HCl.
5. Predicted 24-hourly short term incremental ground level
concentration
The results of the GLCs are given in the Table No. 4.4 When the above stated GLCs results are added in to the average ambient air parameters it gives overall AAQ of the surrounding study area. Air quality contours are shown in the Figure No. 4.1 to 4.5
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MAXIMUM COMPUTED GROUND LEVEL CONCENTRATION AT PROJECT SITE
Sr. No
Description Value Concn * ( µg/m3)
Co-ordinates X (m) Y (m)
A PM 1 1st Highest 24 hr. Result 3.48844 848441.21 2581642.92
B SO2 1 1st Highest 24 hr. Result 0.62351 848274.33 2581813.50
C NOx 1 1st Highest 24 hr. Result 0.39625 848436.70 2581591.36
D HCl 1 1st Highest 24 hr. Result 0.17673 848441.21 2581642.92
E NH3 1 1st Highest 24 hr. Result 0.33943 848274.33 2581813.50
Note :-(*) This predicted maximum Ground Level Concentration (GLC) is based on worst case scenario, considering maximum stack emission limit of SPM-150 mg/Nm3, SO2 100 PPM and NOx-50 PPM. As the actual emissions will be well below this predicted GLCs.
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Incremental Concentrations due to Proposed Project
(μg/m3)
Resultant Concentration
(μg/m3)
NAAQ Standards
(μg/m3)
PM 87.38 3.48 90.86 100
SO2 35.07 0.62 35.69 80
NOx 49.51 0.39 49.9 80
HCl <1 0.17 0.17 200
NH3 <2 0.33 0.33 400
With this marginal contribution due to the proposal of the project, the levels
of SPM, SO2 &NOx, HCl, NH3, will remain below the 24 –hourly ambient air
quality standards for SO2 & NOx (80 μg/m3) and PM10 (100μg/m3)
prescribed by CPCB. The operation of plant is not likely to cause any
significant impact on the ambient air quality of the study area. The Dispersion modeling assumptions are considered as follows:
1. The receptor locations for 36 wind directions starting with 10 degrees
and incrementing with 10 degrees for radial distances viz. 100m, 200m, 300m, 500m, 1000m, 2000m, 3000m, 5000m,6000m, 8000m, 9000m and 10000m has been taken for the Air Quality Modeling.
2. The impacts of the pollutants were identified up to 10000 meters. 3. The terrain of the study area was considered as FLAT. 4. Stability Class was evaluated based on Temperature Profile and Cloud
Cover. 5. The mathematical equations used for the dispersion modeling assumes
that the earth surface acts as a perfect reflector of plume and physic-chemical process, such as dry and wet deposition, and chemical transformation of pollutants are negligible.
6. The micro-meteorological data viz. Temperature, Wind Speed, Wind Direction and Cloud Cover has been collected from the meteorological station kept at the project site of Chhatral Environment Management system Pvt. Ltd.
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Base line study reveals that the levels of various pollutants like PM, SO2 and NOx etc., in the ambient air of surrounding study area are well within the limits stipulated by National Ambient Air Quality (NAAQ) Standard for Residential, Rural and other areas. It can be seen from Table No. 4.7 that the maximum predicted 24 hours GLC(s) of all the pollutants i.e., PM, SO2 and NOx, HCl, NH3 and its incremental concentrations on baseline value is below the NAAQS. Thus, it can be concluded that, with proposed emissions from the Plant, the Ambient Air Quality within the industrial premises as well as in the surrounding study area will not exceed the NAAQ standards and hence there is no significant adverse impact on Ambient Air Quality.
D. Mitigation Measures for Air Environment during Operational Phase
• The industry will take measures for reduction of fugitive emissions
emanating out of process reactions by providing vent condensers.
• Good ventilation will be provided to reduce the workroom concentrations.
• Fugitive emissions will be reduced by providing vent condensers to the
all the reactors.
• Adequate stack height of 30 m will be provided to the 3 TPH boiler and 30 m to the Hot Air Generator.
• Stack monitoring facilities for the periodic monitoring of the stack to
verify the compliance of the stipulated norms. Apart from this Mu l t i
Cyclone Dust Collector followed by Bag filter will be provided to the boiler
and HAG.
• In order to minimize the air pollution, unit will develop greenbelt in and
around its premises.
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Impact on water quality during construction phase / foundation work will be marginal and confined to use of water by workers only. The sewage generated will be disposed to Soak Pit and septic tank system & they will take all reasonable precautions for wastewater seepage. This will prevent soil contamination. The water required for construction will be met by Water Tanker sources. The quality of both surface and groundwater may also deteriorate in regard to the labour camps likely to be developed during the construction phase if proper solid waste management practices are adopted. Improper treatment of sewage from labour camps leads to infiltration into soil and finally affects groundwater regime. This will create accumulation dirty water over which mosquitoes and other flies to flourish thereby affecting the health of workers. During the operation phase, irrational disposal of liquid wastes will be avoided. The formation of roads will affect the drainage system as such road laying is to be properly planned protecting the natural drainages by leaving sufficient buffer zone of 7.5 m on either side of natural stream courses. The baseline status of water quality in the core and buffer zone area has been established through sampling and analysis of various water quality parameters as part of the baseline environmental monitoring. Water samples collected from 16 locations in the core and the buffer zone of 10 km radius of the proposed project area during the study period. The prime objective of the baseline water quality study was to establish the existing water quality in the study area and to evaluate the anticipated impact of the proposed project on water quality and to suggest appropriate mitigation measures for implementation. This will also be useful for assessing the conformity to the standards of water quality during the construction and implementation/ operational phase of the project. The contamination of groundwater might occur due to the irrational disposal of liquid wastes.
B. Mitigation measures :
The domestic sewage generated during the construction activity will be
routed to septic tanks followed by soak pit.
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• Domestic Wastewater @ 5 KL/day will be disposed off through Soak Pit / Septic Tank System.
• Industrial Effluent generation @ 44.5 KL/day will be sent to ETP for Primary treatment and then it will be sent to Chhatral Environment Management System Pvt. Ltd. For Spray drying.
• So, unit will achieve Zero Discharge.
TABLE 4.11 TOTAL WATER REQUIREMENT FOR PROPOSED PROJECT
Thus, it can be concluded that negligible impact on surrounding water environment is caused. Further, it is emphasized that all precautionary measures have to be strictly adhered as mentioned in the Environmental Management Plan given in Chapter 10, to maintain ground water quality within norms in the future.
D. Mitigation Measures for Water Environment during Operational Phase :-
• Effluent generated in the plant will be treated in primary Effluent Treatment Plant. Treated effluent will be sent to Chhatral Environment Management System Pvt. ltd. For Spray drying. So, unit will achieve zero discharge.
• Domestic wastewater will be disposed to soak pit system via septic tank.
• Unit is proposed to recharge ground water through roof water harvesting
pits in the project area and rain water harvesting pits outside plant area
wherever possible to balance the water table.
• Minimization of water use providing drip system for gardening.
• Use of high-pressure hoses for cleaning the floor and process
equipment to reduce the amount of wastewater generated during
washings.
4.6 SOLID / HAZARDOUS WASTE :
A. Impact of Solid / hazardous waste during Construction Phase:-
Improper disposal of debris, used oil, faulty and replaced spares, tyres and tubes and diesel for DG sets will result in surface and groundwater contamination and in turn affects the drainage of the area. As such proper housekeeping programme needs to be formulated for proper disposal of solid and liquid wastes.
B. Impact of Solid / hazardous waste during Operation Phase:-
The details of hazardous waste to be generated from the proposed project, is mentioned at Chapter - 2. The proposed practice of storage of generated hazardous waste, in a closed room having an impervious bottom, and disposed of as per the prescribed guidelines will be continued for the generation of hazardous waste. Hence, the impact due to the same will be negligible as the handling of hazardous waste to be
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B Measures for hazardous/solid waste during Operational phase :-
To reduce the quantity of solid / hazardous waste generation as well as
possible contamination of land (soil) due to spillages / leaks from the plant
operations, following Mitigation measures can be implemented:
• There will not be any leakages / spillage from the raw-materials storage
and from the storage of generated effluent from the project.
• The generated Hazardous waste will be stored on floor with suitable
packing and this dedicated area will be covered with the roof.
• The records on quantity of hazardous waste generation and disposal
will be maintained for each category and possibilities will be explored
for minimization and reuse.
• Classification of waste • Collection, Storage, Transportation, & disposed/sale to authorized
recycler or re-user.
• Data Management and Reporting
• Personnel Training to the workers and employees.
• The leakages of oil spills from machinery shall be collected in leak
proof barrels and then disposed off to SPCB authorized dealers.
4.7 NOISE ENVIRONMENT :-
A. Impact during Construction Phase
There will be slightly increase in noise level during construction phase due to erection and installation of machinery. But it is restricted to construction phase only and it will occur during day time, when construction activities will be in progress. Construction equipment and vehicular traffic contribute to the
increased noise level.
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B. Mitigation measures during Construction Phase :-
Recommended mitigation measures are:
• Good maintenance of vehicles and construction equipment.
• Restriction of construction activities to day time only. • Plantation of trees around the plant boundary to attenuate the noise.
C. Impact during Operational Phase :-
As per observations, the Ambient Noise Level is within norms of Industrial Area. With the implementation of the mitigation measures proposed, the noise levels at plant boundaries will be well below the limits specified for industrial areas. The major sources contributing to Noise pollution during the plant operation will be Compressor, Boiler, Pumps, etc. The operation of the equipment will generate noise ranging between 70-80 dB (A). The occasional noise will be attenuated by the development of green belt in and around the industry, which will be taken up right from the construction phase. Also ear protecting devices will be provided for personnel working in high noise generating zone. The main sources of noise pollution in the plant are Boiler, Hot Air Generators, Reactors, DG Set, and other Noise generating units. Vehicular movements during operation phase for loading / unloading of raw materials and finished products and transporting activity may also increase noise level. Noise levels in the ambient air are well within the permissible limits given by the National Ambient Noise level standards as confirmed during baseline study. Leq values of the noise levels within the plant premises will be kept less than 75 – 70 db [A] [during day time and night time] which will be within the permissible limit. Thus, there is practically no impact on surrounding environment.
D. Mitigation Measures for Noise level during Operational Phase :
To minimize the noise pollution the unit proposes the following noise
control measures,
• Noise suppression measures such as enclosures, buffers and / or
protective measures will be provided, if required (wherever noise level
is more than 90 dB (A)).
• Employees will be provided with earplugs or earmuffs where exposure
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• Extensive oiling, lubrication and preventive maintenance will be carried
out for the machineries and equipments to reduce noise generation.
• Green Belt Development.
4.8 LAND /SOIL ENVIRONMENT : A. Impact during Construction Phase
In proposed unit needs to do Excavation for plant activity. Unit will do construction activity for proposed foundation work. Hence there will be minor impact on the surrounding soil environment and there will be no change in Land Use Pattern. Present Land use of the site is open land. Proposed production activity will be done in premises of the unit.. Hence, there will be change of existing land use pattern only for the project site. The activities of proposed products will be confined within the plant site premises. During construction works, top soil generated from various activities like excavation etc. will be stored and preserved to use it during restoration period as far as possible. There will be no disposal of wastewater on land. Hazardous wastes will be stored at earmarked area with impervious flooring, shed and spillage/ leakage collection system to eliminate rainwater contamination, chances of overflow / spillages going on to the land and thus land/ soil contamination.
B. Mitigation measures during Construction Phase :-:
• The earthen material generated during excavations and site grading periods, will be properly dumped and slope stabilization shall be taken. The topsoil generated during construction shall be preserved and reused for plantations.
Hence, no significant negative impact is envisaged on the surrounding soil quality due to presence of solid / hazardous waste within the plant premises.
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Source emission, wastewater and hazardous waste generation from any project activity affects the soil environment. The impact due to air causes direct/indirect effect on soil. The emissions of SPM during operation will be effectively controlled. There will be practically no effect on the soil quality due to air emissions. Domestic effluent will be discharged to soak pit and septic tank system. Wastewater generated from the Industrial activity will be treated in Effluent Treatment Plant and finally it will be send to Chhatral Environment Management System Pvt Ltd and ETP waste will be disposed to TSDF site. As per the Hazardous Waste (Management & Handling) Amendment Rules, 2003, all necessary control steps for each type of Hazardous Wastes generated will be taken for the proposed project. Hence, due to the proposed project the, land use pattern; land cover and topography of the area will be changed only for the project premises.
IMPACT ON SOIL One of the adverse impacts of a project may be enhanced soil
erosion, mainly on account of rain and flood. Soil erosion is due to
heavy rains and floods coupled with improper and unplanned land
use. Physico-chemical changes in soil quality may occur due to
spillage of various chemicals on land around storage area. The
impact will remain confined within the factory premises it will change
the quality of soil and impact will be of irreversible in nature.
D. Mitigation Measures during Operational Phase :
• Flue gases from Boiler stack and HAG stack will be controlled in Multi Cyclone Dust collector Followed By Bag Filter and discharged into the atmosphere through a stack of 30 m. Outlet dust emission from Bag filters
will be below 50 mg/Nm3.
• Effluent water generated from all streams of the proposed project will
be treated in Primary Treatment plant and finally treated effluent will be
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Any construction activity brings changes in some components of the local Terrestrial ecosystem. These adverse impacts are restricted to the project Construction site and to some extent it's immediate surroundings. The proposed project will not involve removal of any vegetation from the soil and loosening of the topsoil generally causes soil erosion as it is. However, such impacts will be confined to the plant site and will be minimized through paving and water sprinkling. However, 33% of greenbelt will be developed in the plant site. The existing trees will be preserved to the extent possible. Thus, there will no major adverse impacts are envisaged on ecological environment due to project activities.
B. Mitigation measures during construction phase :
During construction, small shrubs in the plant premises are required to be cleared. The measures required to be undertaken to minimize the impact on the ecology are:
• The felling of trees will be kept at minimum.
• Adequate Greenbelt will be developed.
C. Impact during Operation Phase :-
Impacts on terrestrial ecosystem can occur due to operation of the any industrial project mainly from air emissions, liquid effluents as well as hazardous wastes generation, which can interfere with the biotic and abiotic components of the ecosystem and may induce injurious effects when concentrations exceed permissible standards. The proposed project will be carried out on land within M/s. BHIMANI DYE CHEM INDUSTRIES without cutting of any trees. The proposed project does not alter the crop pattern and natural vegetation of the surrounding area. Due to the safe control technology of air pollutants, liquid effluents and hazardous wastes disposal, no impact on the surrounding ecology is anticipated. Development of additional greenbelt/green area will improve the ecological Environment of the surrounding areas.
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Prediction of impacts is based both on the direct and indirect; short-term as well as long-term; irreversible and irreversible impacts that are most likely to occur owing to the industrial activity during establishment and operation. The ecological factors that are considered most significant as far as the impact on flora and fauna are concerned: 1. Whether there shall be any reduction in species diversity.
2. Whether there shall be any habitat loss or fragmentation. 3. Whether there shall be any risk or threat to the rare or endangered
or endemic or threatened (REET) species. 4. Whether there shall be any impairment of ecological functions
such as (i) disruption of food chains, (ii) decline in species
population and or (iii) alterations in predator-prey relationships.
Negative Impacts: As there is change in the land use and land cover on account of the proposed project, the proposed action is not going to have any direct and significant negative impacts of flora and fauna or biodiversity. Most probable Scenario: As stated earlier, it is a new project there will be change in the land use and land cover within the project site. No damage is going to be done to the existing green cover within the project site. Except for a few weeds, there are only cultivated plants and no RET species in the core area. No species is going to be lost on account of the proposed project. No direct or indirect damage is expected to the flora and fauna of the buffer zone. Further, as there are no rare or endangered or endemic or threatened (REET) species, the project does not pose any threat to the flora and fauna of the study area. As the industry is required to operate and maintain the emissions and effluents within the limits specified by the CPCB / SPCB, the effects of the industry on the flora and fauna of the buffer zone may be negligible. Neither the storm water nor the effluent water nor any other kind of rain or waste water from the industry shall get in to the drinking water resources. D. Mitigation Measures during Operational Phase :-
The measures required to be undertaken to minimize the impact on the ecology are:
• The felling of trees will be kept at minimum.
• Adequate Greenbelt will be developed.
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Like any other project, the proposed project is also expected to have certain positive and negative impacts on socio-economic environment. A. Impact during Construction Phase
Local people involved as contract laborers will have benefits of getting employment. Proposed project will generate temporary employment for personnel during operational phase.
Impact on Socio-Economic Environment Due to proposed project there is no major negative impact on socio economic environment. The proposed Project will require workforce of 40 persons during plant operations. Thus industrial activity will boost up the commercial and economical status of the locality to some extent. And, the overall impacts on socio- economic environment due to the proposed expansion are positive in nature and accrue to the community on the long-terms basis. B. Impact during Operational Phase :-
The proposed project will generate direct employment. The indirect employment will be generated by way of transportation, shopkeepers and other casual employment. Implementation of this plant will also reduce production loss due to shortage of power. Thus, the Proposed project will have significant positive impacts on the employment pattern of the study area. During the erection phase short term direct or indirect employment will be generated. Project Proponent shall give first preference to the Local people wherever found suitable for all the jobs in the plant operations. Economic status of the local people will improve due to the increased employment & business opportunities, thereby, making a positive impact to the Local Economy. Educational, medical and housing facilities in the study area will considerably improve. Thus, the proposed project will have significant positive impact on the socio-economic environment. C. Mitigation Measures for Socio-Economy :-
• Due to proposed activity the employment generation will be around 40
persons including, skilled, semi-skilled & unskilled labour and office
staff. Local qualified personnel can be employed.
• Under CSR Budget, the proponent has allotted 0.11 lac to take up
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Health problems are also likely to be experienced in the area as a result of Immigrant labour being careless about personal hygiene and also mosquito and fly-borne infections usually prevalent in the rural areas. Such Problems will be minimized by provision of adequate sanitary and health services.
B. Impact during Operational Phase :-
The impact on health and safety hazard is due to Fire, handling of raw material and products, . The company will provide sufficient fire fighting system. Therefore, no adverse impact is anticipated. C. Mitigation measures for Health & Safety :-
1. Provision of periodic medical checkup for all the employees is
necessary first aid facilities.
2. Protective equipments will be regularly checked and will be
kept easily accessible and easily workable during emergency.
3. Various types of fire extinguishers such as (Foam type, DCP,
water, CO2 type) will be providing inside the factory premises.
4. Provide sufficient fire fighting system
5. Health Problems will be minimized by provision of adequate
sanitary and health services
4.14 TRAFFIC STUDY & ITS IMPACT:
Traffic study is important to calculate the existing and proposed load on the existing Road due to Proposed Project. There is only one main junction nearby the proposed project i.e. M/S. BHIMANI DYECHEM INDUSTRIES. Traffic counts were collected at two Directions (1) From A to B – (Up) Kadi – Ankhol - Chhatral and (2) From B to A – (Down) Chhatral– Ankhol– Kadi on 22/05/2018. Details regarding the traffic survey are: • Traffic counts were collected and recorded in 4 hours intervals.
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• Morning period (pick hours) survey was carried out from 8:00 to 12:00
hrs. • Evening period (pick hours) survey was carried out from 16:00 to 20:00
hrs. Traffic counts observed during the above survey are tabulated in Table 4.14
Table No.: 4.14 Traffic Study
Based on the above mentioned traffic study given in above Table, hourly vehicular traffic has been calculated. Considering worst case scenario, average number of vehicles observed during 4 hours has been taken as hourly counts. Passenger Car Unit (PCU) has been calculated by applying PCU factor. Proposed load of trucks due to the movement of raw materials, fuel and products has been calculated. Design capacities of both the routes have been taken from the Indian Road Code. Assessment of proposed traffic load is described in Table 4.15
Table No.: 4.15 Assessment of Proposed Traffic Load
Type of Vehicles
Direction -1 From A to B – (Up)
Kadi – Ankhol – Chhatral)
Direction 2 From B to A – (Down) Chhatral–
Ankhol – Kadi
PCU factor as per Indian Road Code Avg. vehicle
per Hr. (Worst case)
Equivalent PCU (Passenger Car Unit per Hr.)
Avg. vehicle per Hr. (Worst case)
Equivalent PCU (Passenger Car Unit per Hr.)
Type of Vehicles
Direction -1 From A to B – (Up)
Kadi – Ankhol – Chhatral)
Direction 2 From B to A – (Down) Chhatral–
Ankhol – Kadi Timings of Survey(hrs) Timings of Survey(hrs)
22-05-2018 22-05-2018 8:00 to 12:00
hrs.
16:00 to 20:00 hrs.
8:00 to 12:00 hrs.
16:00 to 20:00 hrs.
Large Trailer 22 32 39 31 Heavy (Bus, Truck, etc)
12 14 21 24
Medium (Tractors, light commercial vehicles etc)
14 12 26 09
Light (Car, Jeep, Pickup Van etc.)
30 34 26 44
3 Wheeler (Rickshaw)
24 29 26 45
2 Wheeler (Scooter, motorcycle, cycle etc)
72 89 64 44
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Large Trailer 27 121.5 35 157.5 4.5 Heavy (Bus, Truck, etc)
13 39 23 69 3
Medium (Tractors, light commercial vehicles etc)
13 19.5 18 27 1.5
Light (Car, Jeep, Pickup Van etc.)
32 32 35 35 1
3 Wheeler (Rickshaw)
27 27 36 36 1
2 Wheeler (Scooter, motorcycle, cycle etc)
80 40 54 27 0.5
Total PCU /Hr 279 351.5 Width of Road in m
6.0 6.0
Design PCU per Hr
2000 2000
Existing PCU per Hr.
279 351.5
Proposed Load Trucks / Day
20 20
Proposed PCU per day
60 60
Total PCU per Hr after the proposed Expansion
339 411.5
From the above table no. 4.9, it can be concluded that even for considering the worst case; there will be minor increase in vehicular load due to the proposed project. However, the total traffic load even after the proposed project will be very low compare to the design capacity of roads.
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The proposed unit is in an area of 3344 SQ. M., will have the infrastructure facilities
very near to the plant area. Land, water sources, material transportation, and power
etc are available without any difficulty and the site is also near to Ahmedabad –
Mehsana Highway. Since land for proposed unit is adequate so, there is no need to
analyze any alternate site for expansion.
The supporting factors for site selection:
1. There is no protected area notified under the Wild Life (Protection) Act (1972) & Eco-sensitive area notified under Section 3 of the Environment
(Protection) Act- 1986 exists within 10 Km radius areas from the Plant Site.
2. The raw materials required for the production of all the proposed products is easily available in the vicinity of the project site, because of the proximity to the industrial chemical markets at Ahmedabad, Kalol, Chhatral, Ankleshwar, Panoli, Jhagadia and Dahej. This will reduce both the cost of raw material transportation and the associated risk.
3. Plant is 2.76 km, W from SH 41 at Chhatral Junction, which is having good
transportation facility
4. All required common environmental infrastructure are in existence in the area namely Common effluent Spray drying facility at Chhatral Environment Management System Pvt ltd. Nearest TSDF site is in the area of 150 - 200 Km.
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5. Availability of trained and skilled manpower nearby because of the proximity to
various industrial areas and city/town.
5.2 ALTERNATIVES FOR TECHNOLOGIES: The technology proposed by M/s. BHIMANI DYECHEM INDUSTRIES for
manufacturing of Synthetic Organic (dyes & dyes intermediates) is one of the best
and proven technologies; hence no alternative technology has been analyzed. Thus,
no new or untested technology will be used and will be based on Zero liquid
Discharge.
Particulars
Proposed Technology
Alternatives
Manufacturing Process
The unit will adopt latest and best Technology available so far in the market for the manufacturing of proposed products to achieve maximum yield with minimum pollution generation and fugitive emission.
The unit is very concerned and Conscious about the product quality and equally about the environmental protection & resource conservation. Hence, unit will put continuous efforts for replacing/ upgrading plant and machineries from time to time with the best available technology with continuous research through its state of the art R&D facility.
Wastewater Industrial Effluent of 44.5 KL/day will be sent to ETP for primary treatment and then it will be sent to Chhatral Environment Management System Pvt. Ltd. So, our unit will achieve Zero Discharge. Domestic wastewater will be send to Soak pit via septic tank system.
No alternatives are required since, proposed technology is adequate for the industrial wastewater treatment to achieve Zero Liquid Discharge by sending treated effluent to Chhatral Environment management System Pvt Ltd.
Air Air Pollution Control System of Multi Cyclone Dust collector followed by common bag filter for flue gas emission will be installed for Steam Boiler and Hot air generator.
No alternatives required since Proposed equipment is suitable and adequate to achieve prescribed norms of SPCB.
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Adequate scrubbing system (Alkali Scrubber system & Water Scrubber system and acid scrubber system) for the control of process gases emission from proposed project.
Proposed technology is suitable To control emission of process gases & adequately designed, considering the pollution load, to maintain prescribed norms of GPCB.
Hazardous waste
On-site temporary storage of different type of hazardous waste separated with proper labeling and demarcation will be provided.
Unit will obtain necessary permission for disposal of additional hazardous waste by SPCB
As all proposed Technology/ methods are safe disposal facilities and also guided by authority, no alternative is required.
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ENVIRONMENTAL MONITORING PROGRAMME 6.1 PREAMBLE Based on the findings of the Environmental Impact Assessment study, various mitigation measures have been proposed, which have been detailed out in Environmental Management Plan (EMP). In order to monitor the impacts and efficacy of these plans monitoring of various environmental attributes have been proposed during and after the completion of the management plans. A well defined environmental monitoring programme would be employed with trained and qualified staff of Environmental Management Cell of the proposed project to monitor the environmental attributes of the area with respect to EMP as well as the guidelines of the GPCB/CPCB. Environmental monitoring schedule proposed to be adopted by the project. The post project environmental monitoring program serves as the key tool to keep track on performance of mitigation measures implemented & pollution control technologies installed to prevent impacts associated with various operations of the project. Environmental monitoring is the repetitive and systematic measurement of the characteristics of environmental components to test specific hypotheses of the effects of human activity on the environment. Environmental monitoring will be undertaken primarily to determine the environmental effects of human activities, and secondarily to increase understanding of cause-effect relationships between human activity and environmental change. Thus, environmental monitoring is the effective observation of site conditions and work activities; and identification of potential non-compliance situations and initiation of corrective or remedial actions. Monitoring is as important as that of control of pollution, since the efficiency of control measures can only be determined by monitoring. 6.2 MONITORING OF ENVIRONMENT From the monitoring point of view, the important components are air, water, soil and noise. Unit will carry out regular monitoring by NABL/MOEF approved laboratory. Regular monitoring of all significant environmental parameters is essential to check the compliance status vis-à-vis the environmental laws and regulation. The objective of the monitoring will be as follows.
To verify the results of the impact assessment study with respect to the
proposed project.
To study the trend of concentration values of the parameters, which have
been, identified as critical and planning the mitigate measures.
To check and assess the efficacy of pollution control equipment.
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Controlling activities inside the plant, until the environmental problem
has been corrected.
Suitably responds to emergency situations
The industry will engage recognized laboratories to carry out all necessary
monitoring parameters. Qualified staff has been appointed for the purpose of
Operation and maintenance of the pollution control facilities. Stand-by facilities
are provided to all the facilities so as to ensure fail proof treatment.
6.3 Work zone monitoring arrangement for Hazardous chemicals.
Arrangement for monitoring in the work zone. Sources: Operators may be exposed due to mechanical failure of hoses or seals
and failure to ensure all hatches and chutes are closed. Exposure could also occur during the following activities or events: sample collection and testing, truck loading and unloading, filling of drums, equipment cleaning and maintenance, opening of tanks and equipment, and spills. All activities from glue spreading, pre-lay and hot press operating.
Method of Testing: NIOSH, National Institute for Occupational Safety and Health Method 2541
Duration of sampling: 6-10 hours Benefit of monitoring:
1. To control potential risk to health. 2. To provide controls measures by using following.
• Elimination • Substitution • Engineering controls • Safe work practices (Administrative practices) • Personal protective equipment
Requirements Plan for Compliance
Gujarat factories rules want the occupier of the premises to carry out the required monitoring under Section 7 A (2) e and Rule -12 B in Form 37 prescribed therein.
As seen from the foregone discussions it is clear that the airborne contaminants and their concentrat ions including the composit ion are l ikely to vary a lot. Hence, portable sampling equipment capable to sample dif ferent contaminants shall have to be procured.
Records for location of operation, contaminant, sampling instrument, concentrat ion of air borne contamination, method of analysis followed and the number of workers exposed to the process are supposed to be maintained by the occupier
The dragger make or similar equipment is best f itted for the purpose and will be arranged for with necessary absorbing media tubes for expected contaminants.
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The following emergency equipment shall be present on site:
1. Fire Extinguishers. 2. Industrial First Aid Kit. 3. Portable Eye wash station, Capable of Supplying 15 minutes of water. 4. Emergency Shower. 5. Vehicle Suitable for emergency Transport. 6. Emergency Communication like Land Line Phones, Mobile Phones. Etc.
6.4 CHEMICALS WHICH ARE EXPOSED TO WORKERS DIRECTLY OR INDIRECTLY
Hazardous Chemicals
Reference The Manufacturer, storage & Import of Hazardous chemical Rules 1989
Maximum quantity that can
be stored at a time (MT)
Threshold Quantity in MT
Chloro Sulfonic Acid Sr. No. 136(Part II, Sch. 1 of MSCIR, 1989)
15 Not Listed
HCl Sr. No. 313(Part II, Sch. 1 of MSCIR, 1989)
30 Not Listed
Sulphuric Acid Sr. No. 591(Part II, Sch. 1 of MSCIR, 1989)
40 Not Listed
Liq.Ammonia Sr. No. 31(Part II, Sch. 1 of MSCIR, 1989)
40 50
Acetic Anhydride Sr. No. 3(Part II, Sch. 1 of MSCIR, 1989)
5 Not Listed
Oleum(65%) Sr. No. 444(Part II, Sch. 1 of MSCIR, 1989)
40 Not Listed
Sodium Hydroxide Sr. No. 571(Part II, Sch. 1 of MSCIR, 1989)
1 Not Listed
Aniline Sr. No. 37(Part II, Sch. 1 of MSCIR, 1989)
7 Not Listed
Acetic Acid Sr. No. 2(Part II, Sch. 1 of MSCIR, 1989)
2 Not Listed
Alpha Naphthylamine
Sr. No. 418(Part II, Sch. 1 of MSCIR, 1989)
10 Not Listed
Methyl Alcohol Sr. No. 377(Part II, Sch. 1 of MSCIR, 1989)
30 Not Listed
Formaldehyde Sr. No. 285(Part II, Sch. 1 of MSCIR, 1989)
3 Not Listed
Pre-employment medical checkup and periodically medical examination will be done. Liver function test will be done during pre-placement and periodical examination. Raw materials, by-products and finished products involved in the process. Hazardous chemicals are within the TLV/PEL as per ACGIH recommendation by using gas monitor & work place ambient air monitoring. FORM NO.37 should be prepared & submitted.
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SCHEDULES Looking to the Zero Effluent Discharge by complete evaporation of collected and neutralized effluent at Chhatral Environment Management System Pvt Ltd., there is no need to establish full fledge laboratory for ETP. However, unit will regularly check pH of the raw effluent. Flow meter will be provided at the ETP inlet and outlet for regular monitoring of wastewater quantity. In addition to this, regular monitoring will be carried out for wastewater, gaseous emission, fugitive emission and noise by NABL / MOEF approved laboratory as proposed in monitoring program. 6.6 CORPORATE ENVIRONMENTAL RESPONSIBILITY Management of BHIMANI DYECHEM INDUSTRIES not only carries out business but
also understands the obligations towards the Environment. The company believes in
sustainable development and equally concern about environment preservation and
pollution control. The Proposed Unit will have a well organized Environmental
Management Cell (EMC) which performs all the environmental management activities.
The will have Environment, Health & Safety Policy.
The EHS Policy prescribes to comply with statutory norm with regards to the
Environment, Health & Safety, to prevent pollution by adopting cleaner production
techniques, identification and management of operational hazards and risks and to
ensure the safety of people. All employees at each cadre of the proposed unit will be
educated about the EHS Policy of the company and policy pasted at various prominent
places in the unit. The company will have EHS policy for standard operating procedures
to bring into focus any infringement / deviation / violation of the environmental or forest
norms/conditions with regards to the Environment, Health & Safety and to take further
corrective actions. Hierarchical system and administrative order of the company to deal
with the environmental issues and for ensuring total environmental compliance are
described in the subsequent topics with relevant headings.
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Does the company have a well laid down Environmental policy approved by its board of directors? If so, it may be detailed in the EIA report
Company will adopt Environmental policy.
B
Does the Environmental policy prescribes for standard operating process / procedures to bring into focus any in fragment/deviation/violation of the Environmental or forest norms/conditions If so, it may be detailed in the EIA report.
Environmental policy and standard operating procedures will be implemented and displayed.
C
What is the hierarchical system or administrative order of the company to deal with the environmental issues and for ensuring compliances with the EC conditions. Details of this system may be given
Detail of this system is given in Figure-6.1
D
Does the company have a system of reporting of non compliance / violations of environmental norms to the board of directors of the company and / or shareholders or stake holders at large? This reporting mechanism should be detailed in the EIA report.
Non compliance reports will communicated to all directors in a systematic manner
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Director Approve environment policy and give directions to succeeding component of the cell
2
EHS Manager
Responsible for overall environmental management. Regularly coordinate with Officer-EHS and take feedback regarding all the activities performed under EMC, keep aware the Director of the unit about all the activities performed under EMC, any major issue/accidents / incident take place, any noncompliance / violation of environmental norms
3
Executive - EHS
Establish EHS Policy, Development of EHS SOP, EHS Plan, Manual, Evolutes EHS program & training, Legal complacencies of SPCB & other Authorities. Execute and follow-up for routine monitoring, cleaning and maintenance work of environmental Management systems. Observe regularity, discipline and working strength of ETP operator. Property Loss Prevention activities, Work permit, Plant equipment changes, Mock drill activity, Safety Inspection & audit work, EHS Incidents/Accident investigation, Employee observations/near misses along with corrective action, Develop safety Committee & take quarterly its meeting Review & compliance report. Reporting the general manager about all the activities performed under EMC, any major issue/accidents/incident take place, any noncompliance/ violation of environmental norms
4
Supervisors & Operator
To coordinate with production department, Utility, Engineering department to run ETP smoothly, carry out daily effluent analysis & take necessary actions if required & maintain & update all documents & records on daily basis, Routine cleaning & maintenance of ETP, Maintain minimum stock of required chemicals / materials, Give indent for spare components and follow up for it, maintain hazardous waste storage area in good condition & Record of it, Observe regularity, discipline, working strength of helpers.
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7.1 PUBLIC CONSULTATION As per the EIA notif ication 2006 and its subsequent amendments, “Public Consultation” refers to the process by which the concerns of local affected persons and others who have plausible stake in the environmental impacts of the project or activity are ascertained with a view to taking into account all the material concerns in the project or activity design as appropriate. Al l Category ‘A’ and Category B1 projects or activit ies shall undertake Public Consultation, except the following:-
(a) Modernizat ion of irr igation projects (item 1(c) ( i i ) of the Schedule). (b) All projects or act ivit ies located within industrial estates or parks
(item 7(c) of the Schedule) approved by the concerned authorit ies, and which are not disal lowed in such approvals.
(c) Expansion of Roads and Highways (item 7 (f) of the Schedule), which
do not involve any further acquisit ion of land. (d) All Building /Construct ion projects/Area Development projects and
Townships (item 8). (e) All Category ‘B2’ projects and act ivit ies. (f) All projects or activit ies concerning national defense and security or
involving other strategic considerations as determined by the Central Government. M/s. Bhimani Dye Chem Industries is Considering scale of unit and its categorization, according to EIA notif ication dated 14th September 2006, by Ministry of Environment & Forest (MoEF), Government of India, their proposed manufacturing activity is falls under Synthetic Organic Chemicals – Schedule 5(f) & cat -A. For that unit needs Environmental clearance from Ministry of Environment Forest Climate Change. So, as per notif icat ion, Public Consultat ion is required for proposed project.
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Risk assessment may be broadly categorized as under: Design and Pre-modification review: Improper layout l ike location of plant in downwind side of tank farm, f ire stat ion near process area, process area very close to public road and wrong material of selection can cause severe damages to the work and outside environment. Chemical Risk Assessment: It is being assessed for chemicals from the point of view of compatibi l ity, storage, f ire protect ion, toxicity, hazard index rating, f ire and explosion hazards. Process Safety Management: Before effecting major process changes, lack of Management of Change procedure (MOC) like rel iabil ity assessment of process equipment, incorporating safety t ips and interlocks, scrubbing system, etc. Electrical Safety: Ignorance of hazardous area classif ication, protect ion against static electricity, improper maintenance of specialized equipment l ike f lameproof etc. Safety Audits: Lack of Periodical assessment of safety procedures and practices, performance of safety systems and implementation of the same along with follow up measures. Emergency Planning: Lack of comprehensive risk analysis indicat ing the impact of consequences and specif ic writ ten down and practiced emergency procedures along with suitable faci l it ies had increased the severity of the emergency situations.
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Training: Lack of safety induction and periodical refresher training for the regular employees and contract workmen. Risk Management & Insurance Planning: Lack of identif ication and analysis of all risks and insurance planning so that interruption risks and public l iabi l i ty r isks could also be managed effectively.
To assess f ire risk assessment in the industrial unit following steps shall be considered and measures shall be taken. FIRE RISK ASSESSMENT
o Identif ication & assessment of f ire r isks during operat ions in receipt, storage, transfer and handling of chemicals (raw materials and f inished products).
o Identif ication & control of ignit ion sources in areas where f lammable chemicals wil l be stored/handled/transferred.
o Review of chemical compatibi l ity in storage areas and to suggest appropriate f ire loss control measures.
o Review of f ire detection measures adopted in the plant & to suggest suitable improvement measures.
o Review of the various act ive (f ire hydrant, sprinkler, portable f ire ext inguishers) and passive f ire protection requirements for chemical storage and handling areas and to suggest improvements as necessary.
o Review of contractor safety awareness (chemical spi l l, f ire f ighting, emergency communication, knowledge of plant hazards & safety regulat ions) and to recommend suitable improvement measures to enhance contractor safety.
o Review of safety awareness and safety training requirements (training identif icat ion and eff icacy) of plant employees with respect to hazards present in the plant.
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o Identif ication of scenarios of potential disasters/emergencies leading to loss of l ife, property damage etc. and qualitat ive assessment of their l ikel ihood.
o Recommendations for risk control measures wherever applicable.
o Preparat ion of onsite emergency preparedness plan.
RISK MANAGEMENT & INSURANCE PLANNING
• Identif ication of all major internal and external pure r isks including the natural r isks and analysis of the impact of above risks.
• Scrut iny of all exist ing major insurance policies in respect of:
1. Rationalization of basic rate of premium and widening of covers.
2. Applicabil ity/el igibil ity of discounts in premium.
3. Applicat ion of suitable clauses, warranties and conditions.
• Identif ication of possible areas for refund of premium and suggestions regarding procedure for the same.
• Select ion of insurance coverage on the basis of r isk analysis.
• Evaluation of business interruption exposure due to identif ied risks.
• Providing guidelines on documentation requirements, procedures for claims under various policies, evaluation of insurers.
• Risk Assessment including prediction of the worst case scenario and maximum credible accident scenario should be carried out. The worst case scenario has been taken into account the maximum inventory of storage at site at any point in t ime. The risk contours should be plotted on the map clearly showing which of the facil it ies and surrounding units would be affected in case of an accident taking place.
• The Risk Assessment report is enclosed herewith. Please Refer Enclosure : 02
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The following parameters are considered to prepare Risk Assessment.
1. Design data, built in safety systems were studied. Discussions were held with officials on individual safety systems.
2. Hazard Identification exercise was conducted taking into consideration the materials, operating parameters and proposed safety measures.
3. Containment failure scenarios related to flammable chemicals and Corrosive Chemicals/Toxic chemicals Storage /handling and reactions involved in proposed products manufacturing have been considered for Risk Assessment and consequences in detail. Thus, this study is mainly oriented towards acute risks rather than chronic risks.
4. Discussed on proposed Raw materials Hazards and their Risks in handling.
7.3 IDENTIFICATION OF HAZARDS • Hazard identification is carried out to ascertain the controls required and
available in order to mitigate the risk of exposure to the hazards. This would substantially help in overcoming costly errors and prolonged delays that may be caused due to the design changes that may be required on a later date.
• Hazard assessment is carried out at the equipment design stage and the control / mitigation measures will be put in place to overcome them to avoid costly errors at a later stage.
• Hazard assessment in the plant is carried out examining the, Liquid and solid chemicals storage in the ware house, production operations, Storage of Flammable liquid chemicals Chloro sulphonic acid, HCl, H2SO4,Ammonia, Acetic Anhydride, Ethylene Oxide, Oleum, Sodium Hydroxide, Aniline, Acetic Acid, Alpha naphthylene, Methyl Alcohol, Formaldehyde locations to find out the adequate facilities in place to overcome the Risks of exposure to the Hazards.
• After a critical analysis of the chemicals used, stored, defined safe operating procedures and the different manufacturing processes, the following table lists the safety measures / installations in place and mitigation measures to overcome the hazards.
Following are the Hazards identified in proposed plant activities: • Fire & Explosion: Heat produces vapors and can cause violent rupture of
containers. Vapors may travel long distances and can flash back. • Can undergo auto-oxidation in air & generate heat which can build up in a
confined space to cause spontaneous combustion which in turn release of hazardous decomposition products Carbon dioxide, carbon mono oxide.
• Inhalation can cause dizziness, headache and nausea, depresses central
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nervous system and has anesthetic effects. Breathing of liquid droplets may
let to chemical pneumonia. In case of excessive inhalation of vapors move the victim to fresh air, obtain medical assistance
• Fire Hazards due to Flammable chemicals leakage from storage tanks, pipe line ruptures during transfer of material which may get ignited due to any spark.
• Fire Hazard due to improper earthing of storage tanks and material transfer lines, Spillage of Hazardous chemicals - Solvents, dilute HCl, which leads to Water pollution, soil pollution and Air pollution due to increase in respective chemical TLV Limits.
• Explosion Hazards due to high pressure in the process reactors.
Storage and Handling of Liq. Ammonia:- • Handling: Avoid contact with either liquid or vapors. Direct contact with mercury
must be avoided. Use proper PPE when working with or around aqua ammonia . • Storage: Ambient temperature. Store in dry, well- ventilated area away from
incompatible materials. Protect against physical damage. Keep out of direct sunlight and away from heat sources.
Storage and Handling of Chloro sulphonic Acid:- • Prior to working with Chloro sulphonic Acid you should be trained on its proper
handling and storage. • Chloro sulphonic Acid Must Be Stored To Avoid Contact With Water; Moist Air;
Strong Acids (Such As Hydrochloric, Sulfuric And Nitric); Strong Bases (Such As Sodium Hydroxide And Potassium Hydroxide); Combustibles; Alcohols; Cresols; And Aldehydes Since Violent Reactions Occur.
• Chloro sulphonic Acid Is Not Compatible With Oxidizing Agents (Such As Perchlorates, Peroxides, Permanganates, Chlorates, Nitrates, Chlorine, Bromine And Fluorine); Finely Divided Metals; Amines; Organics; Plastics; And Rubber.
• Store in tightly closed containers in a cool, well-ventilated area. • Wherever Chloro sulphonic Acid is used, handled, manufactured, or stored, use
explosion-proof electrical equipment and fittings. Personal Protective Equipment
Clothing
• Avoid skin contact with Chloro sulphonic Acid. Wear acid-resistant gloves and clothing. Safety equipment suppliers/manufacturers can provide recommendations on the most protective glove/clothing material for your operation.
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• All protective clothing (suits, gloves, footwear, headgear) should be clean,
available each day, and put on before work. • Safety equipment manufacturers recommend Polyethylene as a protective
material. Eye Protection • Wear indirect-vent, impact and splash resistant goggles when working with
liquids. • Wear a face shield along with goggles when working with corrosive, highly
irritating or toxic substances. • Contact lenses should not be worn when working with this substance. Respiratory Protection • Where the potential exists for overexposure to Chlorosulphonic Acid, use a
NIOSH approved supplied- air respirator with a full face piece operated in a pressure- demand or other positive-pressure mode. For increased protection use in combination with an auxiliary self- contained breathing apparatus operated in a pressure- demand or other positive-pressure mode.
• Storage and Handling of Hydrochloric Acid :- FIELD HANDLING AND USE:
Because of the potential to release toxic vapors, hydrochloric acid should never be opened, mixed, or transferred to other containers at any time while inside a vehicle or in any other small enclosure without a mechanism to vent all fumes to the outside. A Materials Safety Data Sheet (MSDS) should be in the possession of the user at all times and made available to those working with this chemical. The MSDS for hydrochloric acid is to be in the laboratory and field files containing all pertinent MSDS. The MSDS files should be clearly labeled and readily accessible to all personnel.
Transportation
Hydrochloric acid should never be transported in other than a plastic coated glass container, accurately labeled, and properly stored within the vehicle to prevent shifting, spillage, or breakage. Containers of hydrochloric acid carried in vehicles in warm climates should be placed in coolers to protect them from excessive heat. Although hydrochloric acid has a boiling point of 110 degrees C (230 degrees F) it should be transported at room temperature to minimize a buildup of gas pressure in the container.
Contingency Spills and Response
During operational use, transportation, and wherever an accidental spill is likely to occur, each laboratory and field unit should have, as part of their required
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emergency equipment, sufficient absorbent materials, such as sodium bicarbonate, soda ash or lime, to handle small spills. Shovel chemical waste into a container and properly label as "used hydrochloric acid." Wash residue from spill are with copious amounts of water. Do not allow run-off to contaminate water supplies or nearby creeks or rivers. Do not attempt cleanup unless wearing skin, eye, and respiratory protection. Since hydrochloric acid has a pH less than 1, discarded material is a hazardous waste (Environmental Protection Agency (EPA) Hazardous Waste No. D002, 40 CFR 261.22) including empty hydrochloric acid containers. Waste material should be stored in a safe area and clearly marked for special disposal by a recycling contractor. Record how much of the chemical was spilled and the method of clean up and proper disposal, as required by hazardous waste regulations.
PERSONAL PROTECTIVE EQUIPMENT:
Because hydrochloric acid is a strong corrosive, an acid-resistant apron, gloves, and face shield or protective eyewear should be worn at all times while pouring, mixing, or transferring this chemical. Handling of hydrochloric acid must be in a well-ventilated area or under a fume hood for approved acids. Because of its nature to induce severe chemical burns, an eyewash station and quick drench shower should be made available within the work area.
STORAGE:
Hydrochloric acid should be kept in a tightly closed container and stored in chemical area that is compatible with other chemicals. Store in a secure, well-ventilated area, that is well marked, and away from the general work population. Do not store near oxidizing materials.
DISPOSAL:
Spilled or used hydrochloric acid is considered a hazardous waste and must be handled accordingly. It must be properly labeled and disposed of by a hazardous waste contractor. Storage should be in an assigned area that is away from general worker population, and well-marked, well ventilated and not subject to heat cycles. Records must be maintained on the amounts of waste hydrochloric acid, the storage time, and the contractor involved in hazardous waste recycling. Used hydrochloric acid is considered a hazardous waste because of its corrosive properties. By diluting hydrochloric acid to 5 percent volume to volume or less, and neutralizing it with NAHCO3 to a neutral pH, the solution is no longer corrosive and can, in some jurisdictions, be disposed of down the drain. Before this is practiced as a means of disposal, permission must be obtained from the local waste water treatment facility and be in compliance with local and State environmental regulations.
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• Storage and Handling of Sulphuric Acid :- Precautions: Keep locked up. Keep container dry. Do not ingest. Do not breathe gas/fumes/
vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, combustible materials, organic materials, metals, acids, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package.
container in a cool, well-ventilated area. Do not store above 23°C (73.4°F). Personal Protection Face shield. Full suit. Vapor respirator. Be sure to use an approved/certified
respirator or equivalent. Gloves. Boots. Personal Protection in Case of a Large Spill: Splash goggles. Full suit. Vapor respirator. Boots. Gloves. A self contained
breathing apparatus should be used to avoid inhalation of the product. Suggested protective clothing might not be sufficient; consult a specialist BEFORE handling this product.
First Aid Measure: Eye Contact: Check for and remove any contact lenses. In case of contact, immediately flush
eyes with plenty of water for at least 15 minutes. Cold water may be used. Get medical attention immediately.
Skin Contact: In case of contact, immediately flush skin with plenty of water for at least 15
minutes while removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.
Serious Skin Contact: Wash with a disinfectant soap and cover the contaminated skin with an anti-
bacterial cream. Seek immediate medical attention. Inhalation: If inhaled, remove to fresh air. If not breathing, give artificial respiration. If
breathing is difficult, give oxygen. Get medical attention immediately. Serious Inhalation:
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Evacuate the victim to a safe area as soon as possible. Loosen tight clothing such
as a collar, tie, belt or waistband. If breathing is difficult, administer oxygen. If the victim is not breathing, perform mouth-to-mouth resuscitation. WARNING: It may be hazardous to the person providing aid to give mouth-to-mouth resuscitation when the inhaled material is toxic, infectious or corrosive. Seek immediate medical attention.
Ingestion: Do NOT induce vomiting unless directed to do so by medical personnel. Never
give anything by mouth to an unconscious person. Loosen tight clothing such as a collar, tie, belt or waistband. Get medical attention if symptoms appear.
• Storage and Handling of Acetic Anhydride :- Precautions: Keep container dry. Keep away from heat. Keep away from sources of ignition.
Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this
product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes.
Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated
area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Personal Protection: Face shield. Full suit. Vapor respirator. Be sure to use an approved/certified
respirator or equivalent. Gloves. Boots. Personal Protection in Case of a Large Spill: Splash goggles. Full suit. Vapor respirator. Boots. Gloves. A self contained
breathing apparatus should be used to avoid inhalation of the product. Suggested protective clothing might not be sufficient; consult a specialist BEFORE handling this product.
First Aid Measures: Eye Contact: Check for and remove any contact lenses. In case of contact, immediately flush
eyes with plenty of water for at least 15 minutes. Get medical attention immediately.
Skin Contact: In case of contact, immediately flush skin with plenty of water for at least 15 minutes while removing contaminated clothing and shoes. Cover the irritated skin
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with an emollient. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.
Serious Skin Contact: Wash with a disinfectant soap and cover the contaminated skin with an anti-
bacterial cream. Seek immediate medical attention. Inhalation: If inhaled, remove to fresh air. If not breathing, give artificial respiration. If
breathing is difficult, give oxygen. Get medical attention immediately. Serious Inhalation: Evacuate the victim to a safe area as soon as possible. Loosen tight clothing
such as a collar, tie, belt or waistband. If breathing is difficult, administer oxygen. If the victim is not breathing, perform mouth-to-mouth resuscitation. WARNING: It may be hazardous to the person providing aid to give mouth-to-mouth resuscitation when the inhaled material is toxic, infectious or corrosive. Seek immediate medical attention.
Ingestion: Do NOT induce vomiting unless directed to do so by medical personnel. Never
give anything by mouth to an unconscious person. If large quantities of this material are swallowed, call a physician immediately. Loosen tight clothing such as a collar, tie, belt or waistband.
• Storage and Handling of Oleum:- Keep containers closed. Store in a dry and well- ventilated location away
from combustibles, oxidizers, bases or metallic powders. Storage tanks should be protected from water ingress and maintained structurally in a safe and reliable condition. Wear appropriate personal protective equipment (PPE). Use only with adequate ventilation. Do not breathe sprays or mists and wash hands thoroughly after handling. Do not allow the product to get into the eyes, on skin or on clothing.
Individuals working with this chemical should be properly trained regarding its hazards and safety. Always refer to the Safety Data Sheet (SDS) for detailed information on storage and handling.
Precautions: Keep locked up.. Keep container dry. Keep away from heat. Keep away from
sources of ignition. Keep away from direct sunlight or strong incandescent light. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. Avoid shock and friction. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, combustible materials, organic materials, metals, acids, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package.
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Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area.
Hygroscopic; keep container tightly closed. Will react with water or steam to produce heat and toxic fumes
Safety Wear personal protective equipment (PPE) such as goggles, full - body suit, safety
shoes and gloves. Always wear a self - contained breathing apparatus or a full - face airline respirator to avoid inhalation of the product. Prevent breathing of mist or vapours. Prevent contact with skin, eyes and clothing. Ensure adequate ventilation. Always refer to the Safety Data Sheet (SDS) for detailed information on safety.
First Aid Measure: Eye Contact: Immediately flush eyes with running water for at least 20 minutes. If irrita tion
persists, Repeat flushing. Get immediate medical aid. Skin contact: Wash affected area (s) with running water for at least 20 minutes. If irritation
persists, repeat flushing. If medical treatment is delayed, immerse the affected area (s) in cold water. Remove contaminated clothing and wash thoroughly before reuse. Get immediate medical aid.
Ingestion: Do not induce vomiting. If the person is alert and not convulsing, rinse mouth and
give ½ to 1 glass of water to dilute material. If spontaneous vomiting occurs, have the person lean forward with the head down to avoid breathing in. Get immediate medical aid.
Inhalation: Shift the person to fresh air. If the person is not breathing, give artificial
respiration. If breathing is difficult, give oxygen. Call a physician. Spills and disposal Personnel handling this material should be thoroughly trained to handle spills and
releases. In case of spills, dike by using absorbent or impervious materials such as sand or clay. Stop leakage if possible without risk. Flush spilled area with water and neutralize the site with soda ash, sodium bicarbonate or lime. Do not allow it to contaminate the ground water system. Waste must be disposed of in accordance with federal, state or local regulations, as applicable.
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• Storage and Handling of Sodium Hydroxide: Precautions: Keep container dry. Do not breathe dust. Never add water to this product. In case
of insufficient ventilation, wear suitable respiratory equipment. If you feel unwell, seek medical attention and show the label when possible. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, metals, acids, alkalis, moisture.
Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area. Do
not store above 23°C (73.4°F). Work place Exposure limits: OSHA: The legal airborne permissible exposure limit (PEL) is 2 mg/m3 averaged
over an 8 - hour work shift. NIOSH: The recommended airborne exposure limit (REL) is 2 mg/m3, which should
note exceeded at any time. ACGIH: The threshold limit value (TLV) is 2 mg/m3, which should not be exceeded at
any time. Note: The above exposure limits are for air levels only. When skin contact also
occurs, you may be overexposed, even though air levels are less than the limits listed above.
Accidental Release Measure: Small Spill: Use appropriate tools to put the spilled solid in a convenient waste disposal
container. If necessary: Neutralize the residue with a dilute solution of acetic acid. Large Spill: Corrosive solid. Stop leak if without risk. Do not get water inside container. Do not
touch spilled material. Use water spray to reduce vapors. Prevent entry into sewers, basements or confined areas; dike if needed. Call for assistance on disposal. Neutralize the residue with a dilute solution of acetic acid. Be careful that the product is not present at a concentration level above TLV. Check TLV on the MSDS and with local authorities.
Personal Protection: Splash goggles. Synthetic apron. Vapor and dust respirator. Be sure to use an
approved/certified respirator or equivalent. Gloves. Personal Protection in Case of a Large Spill: Splash goggles. Full suit. Vapor and
dust respirator. Boots. Gloves. A self contained breathing apparatus should be used to avoid inhalation of the product. Suggested protective clothing might not be sufficient; consult a specialist BEFORE handling this product.
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First Aid Measure: Eye Contact: Check for and remove any contact lenses. In case of contact, immediately flush
eyes with plenty of water for at least 15 minutes. Cold water may be used. Get medical attention immediately.
Skin Contact: In case of contact, immediately flush skin with plenty of water for at least 15
minutes while removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.
Serious Skin Contact: Wash with a disinfectant soap and cover the contaminated skin with an anti-
bacterial cream. Seek medical attention. Inhalation: If inhaled, remove to fresh air. If not breathing, give artificial respiration. If
breathing is difficult, give oxygen. Get medical attention immediately. Serious Inhalation: Evacuate the victim to a safe area as soon as possible. Loosen tight clothing such
as a collar, tie, belt or waistband. If breathing is difficult, administer oxygen. If the victim is not breathing, perform mouth-to-mouth resuscitation. WARNING: It may be hazardous to the person providing aid to give mouth-to-mouth resuscitation when the inhaled material is toxic, infectious or corrosive. Seek immediate medical attention.
Ingestion: Do NOT induce vomiting unless directed to do so by medical personnel. Never
give anything by mouth to an unconscious person. If large quantities of this material are swallowed, call a physician immediately. Loosen tight clothing such as a collar, tie, belt or waistband.
• Storage and Handling of Aniline: Precautions: Keep locked up. Keep away from heat. Keep away from sources of ignition.
Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable protective clothing. In case of insufficient ventilation, wear uitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, metals, acids, alkalis.
Storage: Air and light sensitive. Store in light-resistance container. Keep container in a cool,
well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
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Personal Protection: Splash goggles, Lab-coat, Vapor respirator. Be sure to use an approved/certified
respirator or equivalent, Gloves. Personal Protection in Case of a Large Spill: Splash goggles, Full suit, Vapor respirator, Boots, Gloves. A self contained
breathing apparatus should be used to avoid inhalation of the product. Suggested protective clothing might not be sufficient; consult a specialist BEFORE handling this product.
First Aid Measure: Eye Contact: Check for and remove any contact lenses. Immediately flush eyes with running
water for at least 15 minutes, keeping eyelids open. Cold water may be used. Get medical attention. Finish by rinsing thoroughly with running water to avoid a possible infection.
Skin Contact: In case of contact, immediately flush skin with plenty of water. Cover the irritated
skin with an emollient. Remove contaminated clothing and shoes. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention.
Serious Skin Contact: Wash with a disinfectant soap and cover the contaminated skin with an anti-
bacterial cream. Seek immediate medical attention. Inhalation: If inhaled, remove to fresh air. If not breathing, give artificial respiration. If
breathing is difficult, give oxygen. Get medical attention immediately. Serious Inhalation: Evacuate the victim to a safe area as soon as possible. Loosen tight clothing such
as a collar, tie, belt or waistband. If breathing is difficult, administer oxygen. If the victim is not breathing, perform mouth-to-mouth resuscitation. WARNING: It may be hazardous to the person providing aid to give mouth-to-mouth resuscitation when the inhaled material is toxic, infectious or corrosive. Seek immediate medical attention.
• Storage and Handling of Acetic Acid: Precautions: Keep away from heat. Keep away from sources of ignition. Ground all equipment
containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the
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container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, metals, acids, alkalis.
Storage: Store in a segregated and approved area. Keep container in a cool, well-
ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Personal Protection: Splash goggles, Lab coat, Vapor respirator. Be sure to use an approved/certified
respirator or equivalent, Gloves. Personal Protection in Case of a Large Spill: Splash goggles, Full-suit, Vapor respirator, Boots, Gloves. A self contained
breathing apparatus should be used to avoid inhalation of the product. Suggested protective clothing might not be sufficient; consult a specialist BEFORE handling this product.
First Aid Measure: Eye Contact: Check for and remove any contact lenses. In case of contact, immediately flush
eyes with plenty of water for at least 15 minutes. Cold water may be used. Get medical attention immediately.
Skin Contact: In case of contact, immediately flush skin with plenty of water for at least 15
minutes while removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.
Serious Skin Contact: Wash with a disinfectant soap and cover the contaminated skin with an anti-
bacterial cream. Seek immediate medical attention. Inhalation: If inhaled, remove to fresh air. If not breathing, give artificial respiration. If
breathing is difficult, give oxygen. Get medical attention immediately. Serious Inhalation: Evacuate the victim to a safe area as soon as possible. Loosen tight clothing such
as a collar, tie, belt or waistband. If breathing is difficult, administer oxygen. If the victim is not breathing, perform mouth-to-mouth resuscitation. WARNING: It may be hazardous to the person providing aid to give mouth-to-mouth resuscitation when the inhaled material is toxic, infectious or corrosive. Seek immediate medical attention.
• Storage and Handling of Alpha Naphthylamine:
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Precautions: Keep away from heat. Keep away from sources of ignition. Empty containers pose
a fire risk, evaporate the residue under a fume hood. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable p. 3 protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, moisture.
Storage: MOISTURE SENSITIVE. Keep container tightly closed. Keep container in a cool,
well-ventilated area. Do not store above 23°C (73.4°F). • Storage and Handling of Methyl Alcohol: Precautions: Keep locked up. Keep away from heat. Keep away from sources of ignition.
Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, metals, acids.
Storage: Store in a segregated and approved area, Keep container in a cool, well-ventilated
area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flae).
• Storage and Handling of Formaldehyde Precautions:
Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, acids, alkalis, moisture.
Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
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Liquid Raw materials will be transferred from the drums to the day tank situated at the production block with the help of leak proof drum pumps / pumps /Vacuum through pipe lines from day tank to reaction vessel unloading by gravity.
7.4.2 MEASURES TO AVOID EVAPORATION
All liquid chemicals/solvents stored in containers will be tightly closed. Will Keep away from heat, sparks, and flame Will Keep away from sources of ignition
7.4.3 SAFETY SYSTEMS
1. Designated areas with proper indication & safety sings
2. Double earthling systems for all solvent storage tanks & process reactors
3. Flame arrestor to the vent of Solvent(Benzene, TNBA, Methanol, ODCB, Butanol) storage tanks
4. Flame proof transferring pumps for all flammable chemicals
5. Handling precautions/sop protocol
6. Pressure Gauges and temperature gauges on each reactor
7. Level indicators on all solvent storage tanks(Benzene, TNBA, Methanol, ODCB,
Butanol)
8. Flame proof lighting to solvent storage yard
9. Safety valve & Rupture disc on each process reactor.
10. Well ventilated warehouse with suitable fire extinguishers will be used for storage of liquid flammable chemicals HCl /Oleum/ Benzene/ Ethyl Acetate/ Acetic Acid.
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1. Company will do planning to stock all the necessary material as minimum as
possible. 2. All containers with hazardous chemicals have labels indicating the contents
and warning of the hazard. 3. Necessary information on safe handling and first aid measures and antidotes
of major hazardous material will be available on the label. 4. Workers dealing with hazardous chemicals will be trained on health risks and
safe handling. 5. Exposure to hazardous chemicals will be minimized. 6. Liquid Hazardous chemicals will be transferred in closed piping system. 7. Separate storage section will be provided for storage of hazardous and non-
hazardous raw materials. 8. Drums / Tanks shall be located and marked in designated area of hazardous
chemical storage. 9. Tanks / Drums of proper MOC will be selected. 10. All tanks / Drums shall be uniformly tagged. 11. Level indicator shall be provided in tanks. 12. Dyke will be provided. 13. Industrial type electric fittings shall be provided. 14. Adequate fire fighting equipments will be provided. 15. Anti corrosive paint shall be done. 16. Safety instruction board will be displayed. 17. Proper earthling shall be provided. 18. Lightning arrestor will be provided.
7.4.5 TRANSPORTATION / UNLOADING
Highly inflammable chemicals will be transported by road. Therefore, adequate safety precautions for transportation will be followed. During transportation of hazardous chemicals, MSDS & TREM card will be provided to driver. As per Motor Vehicle Rules, PESO rules and Factory Rules all safety precautions will be followed during transportation of hazardous chemicals. The following safety precautions are suggested during transportation of toxic, inflammable and corrosive chemicals in tankers, while loading and unloading, transportation and meeting the emergencies arising out of leakages and spillages of hazardous materials:
1. Park the vehicle at designated place.
2. Stop the engine.
3. Check-up spark arrester.
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• The tanker / vehicle should not be parked for long time on the way and especially in crowded places. Park the vehicle away from residential areas
7.5 SPILL CONTROL
• For all chemicals spill control procedures will be displayed. Spillage shall be controlled as per concerned spill control procedure.
• Like any spilled materials to contain, absorb spilled liquid by dry absorbent clay or vermiculite.
• Collect most of the contaminated absorbent with shovel for further disposal/incineration.
• If material spills directly on the ground, dig up and remove saturated soil for disposal/incineration.
• In case liquid chemicals spills on to the ground use dry absorbent clay/vermiculate and neutralize with sodium carbonate
• In case of Raney Nickel catalyst spillage clear instruction will be given to operating personnel not to touch the material and it should be covered with wet earth and sand and eliminate all ignition sources.
7.6 EFFECT AND CONSEQUENCE ANALYSIS
In a plant handling hazardous chemicals, the main hard due to storage, handling of solvents, HCl/Chloroform/Chlorine/ Ammonia. If these chemicals are released into the atmosphere, they may cause damage due to resulting fires.
7.6.1 OPERATING PARAMETERS
1. Potential vapor release for the material depends significantly on the operating conditions especially for any liquefied gas, operating conditions are very critical to assess the damage potential.
7.6.2 INVENTORY
1. Inventory analysis is commonly used in understanding the relative hazards and short listing of release scenarios.
2. Inventory plays an important role in regard to the potential hazard.
3. Larger the inventory of a vessel or a system, larger the quantity of potential release.
4. The potential vapor release [source strength] depends upon the quantity of liquid release, the properties of the materials and the operating conditions [pressure, temperature].
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5. If all these influencing parameters are combined into a matrix and vapor
source strength estimated for each release case, a ranking should become a credible exercise.
7.6.3 LOSS OF CONTAINMENT
1. Plant inventory can get discharged to environment due to Loss of Containment. 2. Certain features of materials to be handled at the plant need to the clearly
understood to firstly list out all significant release cases and then to short list release scenarios for a detailed examination.
3. Liquid release can be either instantaneous or continuous.
4. Failure of a vessel leading to an instantaneous outflow assumes the sudden appearance of such a major crack that practically all of the contents above the crack shall be released in a very short time.
5. The more likely event is the case of liquid release from a hole in a pipe connected the vessel. The flow rate will depend on the size of the hole as well as on the pressure, which was present, in front of the hole, prior to the accident. Such pressure is basically dependent on the pressure in the vessel.
6. The vaporization of released liquid depends on the vapor pressure and weather conditions.
In the study the largest potential hazard inventories have been considered for its consequence Risk estimation how vulnerable the organization is to a specific incident consequence.
7.7 General safety measures and specific safety measures
adopted for transportation, storage & handling (spillage and leakage) of hazardous chemicals are listed as follows.
A. General safety measures for transportation, storage & handling
(spillage & leakage) • Layout and location of hazardous chemical storage tank as per natural and
mechanical ventilation. • Storage of hazardous chemicals based on their compatibility characteristics.
• Provision of display boards on all storage tanks showing name of chemicals, material of construction, calibration of tanks and date of painting.
• Installation of level indicators on all storage tanks to know the exact liquid level inside the tank and to avoid the accidental spillage or overflow.
• Provision of dyke walls and transferring pumps on all the storage area for the hazardous chemicals which helps to reduce the risk of tank leakages.
• Provision of spare barrels/tanks of sufficient quantity for any emergency spillage
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• Regular inspection of all the drums/tanks of hazardous chemicals and damaged drums for separation and disposal to avoid the possibility of catastrophic rupture.
• Provision of double earthing to all storage tanks to prevent the firing due to static charges. Regular inspection of earthing pit.
• Installation of on-site detectors for fire, based on heat &/or smoke detection, with alarm system are provided as required.
• Installation of breather valves and flame arrestors on flammable liquid storage tanks to prevent firing. Regular inspection / testing of the same.
• Periodic calibration and maintenance of all equipments related to hazardous chemical storage.
• Installation of NRV on all pump discharge lines.
• Insertion of heavy duty gaskets to all pipe joints to prevent any leakage.
• Thorough examination of piping for transfer of hazardous chemicals on yearly basis for finding out any defects and rectify the same in due time. Maintain record of such examination.
• Use of drum trolley for the movement of drums of hazardous chemicals to avoid accident due to manual error.
• Display SOP for handling of hazardous chemicals in local language for safe operating procedure.
• Maintain proper inventory of hazardous chemical and keep buffer stock as minimum as possible.
• Implement standard procedure for safe unloading of road tanker.
• Provision of static earthing for tanker unloading.
• Mount muffler on silencer of tanker during entering in factory premises.
• Provision of water showering system (Automated sprinkling system) to the flammable liquid storage tanks, wherever required to avoid vaporization due to increase in ambient temperature
• Provision of adequate firefighting system. • Provision of first aid boxes at prominent places in the plant.
• Declare entire plant area as “NO SMOKE ZONE.”
In addition to the above listed safety measures, following measures are recommended and to be implemented for the proposed project.
• Installation of VOC detectors and implementation of LDAR programme.
• On-site detectors for fire based on heat &/or smoke detection with alarm system as required.
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Specific safety measures for storage and handling of hazardous chemicals to be followed and implemented are as follows.
7.8 OCCUPATIONAL HEALTH & SAFETY PROGRAM
The main ill-effects anticipated to the health of workers are due to the exposure of toxic chemicals. No other source of adverse effects on occupation health & safety is likely to occur. However, MSDS of hazardous chemicals will be prepared and made available with the management as well as concerned personnel working with materials or area likely to be affected by materials.
Following are the key safety measure to be followed and implemented.
• Provision of all necessary equipment like portable detector, online detectors
and other laboratory equipments as proposed for regular monitoring of workplace air and other conditions.
• Implementation of safety policy.
• Provision of proximity suits and self- breathing apparatus.
• Provision and compulsory use of necessary PPEs like helmate, safety goggles, face mask, hand gloves and safety shoes etc. for all workers.
• Provision of ear muffs/ ear plugs to the workers exposed to higher noise level.
Soframycin (ointment), Sterilized cotton wool, Band-aid, Antiseptic Solution (Sevlon), Bandage, Rose Water, etc) at various places in the premises.
• Organize training program for information on accident prevention, proper control and maintenance of equipment, first aid training and safe material handling practices.
Following are the measures followed and implemented for Occupational Health of the workers. • Pre medical checkup at the time of employment and regular medical checkup
of employees. • Maintain all the records in Form 33 certifying fitness for employment in
hazardous process and operation as per Factories Act guidelines. • Maintain health register of all the employees in Form 32. • Monitoring of occupational hazards like noise, ventilation, chemical
exposure at frequent intervals and maintain all records as per Factories Act guidelines.
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• Provision of occupational health center (OHC) and part time qualified medical
officer as per factories act guidelines • Provision of drinking water supply for the employees as per standard of the
drinking water as per WHO guidelines. • Availability of proper sanitary facilities for the employees so that they do not
suffer from any health ailments.
7.9 MONITORING PROGRAM Based on analysis of the existing plant, the important components for the monitoring of occupational health and safety performance are identified as follows. The same will be augmented and implemented for the proposed project. Details of monitoring program for occupational health & safety are given in following Table 7.2.
Table 7.2: Monitoring Program for occupational health and safety
Sr. No.
Components
Locations
Parameters
Frequency
1. Work Place Air Quality
3-5 within plant area
VOC, NH3, HCl and as specified under Gujarat Factory Rules
Monthly
Gas detector for VOC, NH3 and HCl
Continuous
2.
Noise
All prominent locations within the process plant area
Noise levels
Quarterly
3.
Ventilation & Illumination
Process plant & Chemical storage area
Volumetric Air change, Room Temperature, Light Intensity
people away, isolate hazard area and deny entry. Stay upwind, out of low areas, and ventilate closed spaces before entering. Evaluate the affected area to determine whether to evacuate or shelter- in-place by taping windows and doors, shutting off outside air intake(attic fans, etc.), and placing a wet towel or cloth over the face (if needed). Self-contained breathing apparatus (SCBA) and structural firefighter’s protective clothing used in conjunction with water spray will provide limited protection in outdoor releases for short term exposure. Fully encapsulating, vapor-protective clothing should be worn for spills and leaks with no fire. Use water spray to control vapors.
B. Mitigation measures for leakage of solvents and hazardous
organic chemicals • Allow only trained personnel to handle leakage and spillage.
• Prohibit entry of any personnel to the prone area, If flammable vapor level of solvent is above 10% of the LFL in a confined area.
• Provision of Leak detection system to control leakage from source only.
• Respirators is not as effective as ventilation in protecting workers in most situations.
• However, allow use of respirators in case of insufficient ventilation.
• Use of DCP, CO2 and/ or water type fire extinguisher in case of fire.
C. Mitigation measures for leakage of concentrated acids
• Neutralize acid leakage by using lime, sodium bicarbonate and soda ash etc.
• Absorb leakage by using dry earth, sand or other non-combustible materials.
• Allow only trained personnel to handle leakage and spillage.
• Use of water spray to divert vapor drift and to reduce vapors. D. General Mitigation Measures
• Installation of all the equipment as per guidelines of provision of The Gujarat
Factories Rules, 1963. • Storage of hazardous chemicals in small sized multiple containers so as to
avoid
• major hazard associated with large sized containers.
• Proper Control of the operating parameters, mainly temperature, vacuum, cooling media circulation, during plant operation and solvent recovery.
• Availability of common antidotes like milk of magnesia, banana, jiggery, glucose and
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• milk etc. in case of exposure to toxic chemicals. Details of antidotes for other hazardous chemicals are given in MSDS .
• For any case of fire emergency, availability of standard type of fire fighting
• equipments and fire extinguishers in the storage area as well as required places
in the plant. • Strictly prohibit smoking inside the factory.
• Provision of adequate and suitable personnel protective equipments to operators and workers. Availability of First-Aid facility and First-aid trained person at the time of handling operation.
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• Identify the spillage material and refer MSDS for control plan.
• Segregate leakage drum from the area.
• Inform the Site Main Controller (SMC) in detail.
• Open all doors and windows in this area.
• Take decision to declare onsite emergency.
• Spill control and neutralization team member try to control spread material in more area by absorbing material and dry sand.
• If material is toxic or any other flammable and toxic chemical, special precautions needs to be taken as per chemical expert Key person guide line.
• Do not spray water or Foam on spilled material.
• Conductive drum pallets shall be provided.
• Drum handling trolley / stackers/fork lift shall be used for drum handling.
• Materials shall be stored as per its Compatibility study and separate area shall be made available for flammable, corrosive and toxic chemical drums storage.
• Dyke wall will be provided to area where hazardous chemicals will be stored.
• Smoking and other spark, flame generating items shall be banned from the entry Gate.
• NFPA & GHS labels shall be provided on
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material in close container and send to ETP for further neutralization of the residual contents.
• Administer first aid to the victim.
• Make arrangement to send injured person/s to Hospital.
• If off site emergency situation occurs, inform to following agencies Request for Mutual aiders, local authorities like DISH office, Collectorate office, Disaster management cell, Police, fire brigade, nearby hospital, local GPCB office
drums for hazard Identification of the chemicals.
• Exhaust shall be provided at ground level in drum storage area.
• Drum loading unloading procedures are prepared and implemented. Liquid chemicals will be transferred by mechanical seal pump through closed pipeline.
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Remedial measures to prevent recurrence of such incident
Chemical Storage Area Process Plant area
Potential injury / fatality from large release
Toxic Gas Release Reactor / Heater Failure, Leakage in Process Line, Plugging of reactor outlet, leakage in pipeline
• Activate audio visual alarm • Evacuate the area immediately. • Inform the area incharge. • Inform Incident Controller in detail. • Call fire department immediately and help
them in fire fighting. • Try to control situation at department level
with available resources with full PPEs. • If it is found uncontrollable condition by
department level inform Site Main Controller for onsite emergency situation.
• Declare on site emergency if required. • All hazardous activates stop at site. • Inform nearby company to remove
hazardous material or inventory from the compound wall.
• Ensure search and rescue and causalities receive attention.
• Administer first aid to the victim. • Make arrangement to send injured person/sto
Hospital and inform victim’s family. • If off site emergency situation occur –Inform
to following agencies. Request for Mutual aiders, local authorities like – DISH office, Collectorate office, Disaster management cell, Police, fire brigade, nearby hospital, local GPCB office.
• Provide accurate gas monitoring system on site.
• Minimize on-site storage • Develop procedure for tank
inspection and maintenance • Develop purge system to remove
gas to another tank. • Provide temperature control inside
reactor with automatic shut-down of gas flow to the reactor.
• Design collection system to remove and purify/recycle or discard unreacted gas.
• Design control system to detect excess gases in exhaust and shut down gas flow.
• Provide control system to detect extreme temperature variations and activate backup cooling system.
• Diver flow to temporary storage tank • Provide relief valve on reactor with
outlet to a temporary storage tank • SOP for handling will be displayed in
local language for safe operating procedure.
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EMERGENCY MANAGEMENT PLAN OF THE INDUSTRY Risk leads to disasters & disasters have great impact on the prof itabi l ity, stabil ity & reputat ion of an industry. Disaster occurs when a hazard or a threat rises in vulnerable condit ion and the trend ref lects an increase in both. To uphold righteous image of an organization, Disaster Management is of prime importance. For tackling the major consequences inside the port and in the vicinity of port DMP has to be formulated and this planned emergency document is cal led ‘DISASTER MANAGEMENT PLAN’. Indian industry of late has begun to be aware of the necessity to apply more systematic approaches to safety part icularly in plant design. Primari ly, safety in the design of plant extends to the applicat ion of various codes of pract ice or design codes, which are based on the wide experience and knowledge of professional experts and specialists in the industry. Such applicat ion is backed by the experience of local plant managers and engineers who have been involved in similar plants and who have direct experience in their operation over a number of years. The main objective of evolving this emergency and disaster control plan is to create a procedure and infrastructure based on combined resources of the factory and the outside services with a view to minimize emergencies and disaster. This may arise as a result of usage, handling and storage of certain toxic, corrosive, inf lammable and explosive materials used in the manufacturing process and any other emergencies which may direct ly or indirect ly affect the employees, property and local community. Objectives are further classified as under:
• Rescue operation and treatment of persons affected by the emergency.
• Safeguard of other persons not affected by the emergency.
• Keep the damage to property and environment at a minimum level.
• Init ially contain the impact of incident and ult imately bring the incident under control.
• Provide authentic information to outsiders and media.
• Rehabil itat ion of affected person.
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• Inquiry into the cause of emergency situat ions and then analysis to prevent recurrence.
PURPOSE OF PLAN:
• To save lives and injuries,
• To prevent or reduce property losses,
• For protect ion of environment,
• For protect ion of instal lation & restoration of production,
• To provide help for quick continuation of normal situat ion or operat ion.
More specif ically the elements that will form the backbone of the emergency preparedness organizat ion are: o Availabil ity organizat ion and ut i l ization of resources for facil ity
emergencies. o Accident evaluation procedures. o The command, coordination and responsible organization structure. o Notif icat ion and communication mechanism. o Training exercises and plans maintenance. Emergencies and disasters can happen at any moment - and, they usually occur without warning. When an emergency str ikes, immediate safety and prompt recovery are depends on the exist ing levels of preparedness among workers and management. Emergency incidents that may occur, including • Earthquakes • Fires or Explosions • Hazardous Materials Releases • Extended Power or Uti l i ty Outages • Floods • Mass Casualty Events
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As discussed in earl ier chapters, emergencies are classif ied as minor or major, according to their severity and potential impact. The Disaster management of any f irm mainly covers steps l ike PREPAREDNESS, RESPONSE and RECOVERY PREPAREDNESS is a f irst step to assemble appropriate human and physical resources before any emergency occurs, So the industry shall have a designated an “Emergency Coordinator” with the management experience and f inancial authority to deal with the Disaster plan. The person shall arrange related staff safety education and training; Purchase department emergency supplies and equipment and give quick response on occurrence of any emergency- disaster. The company wil l have the following essentials in an accessible location:
• First aid supplies, with instruct ions
• Flashlights/batteries, approved power str ips and extension cords, emergency power supply
• Portable AM/FM radios/batteries
• Laboratory spi l l kits
• Portable emergency water supply
• Eyeglasses, medications and personnel protective measures
• Personal’s emergency contact numbers. The company wil l be in direct contact with the offsite Disaster plan of Distr ict Disaster Management authority. The important telephone numbers including Protect ive Services i.e. Fire station, Hospital, Police department, factory inspector etc. shall be made readily available and in updated forms. A brief onsite emergency plan shall be readily available to all.
FIRE PREVENTION The fire accident may take place because of the electrical spark or static electricity. All the precautionary measures will be taken by the industry to prevent fire in any part of the plant as per the followings: • The company will identify the sources of accidents.
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• Adequate fire extinguishers is provided and additional will be provided as
per requirement.
• Mechanical rooms or utility rooms will not be used for storage.
• All the chemicals will be stored with recommendation storage and handling practice.
• Storage and process area will be posted with “No Smoking” signs.
• All the Personnel Protective equipment will be easily available to all the
workers.
• The company will provide firewater reservoir, fixed water monitors/foam monitor, foam trolley, sand bucket, eye wash shower, flame arrester and fire extinguisher to prevent from any causalities.
LABORATORY SAFETY & PREPAREDNESS The company will maintain clean work environment; post laboratory safety work rules, train all personnel; carry out inventory and label chemicals; not purchasing excess quantities of chemicals; segregates incompatible chemicals; keeps flammables in flammable storage cabinets with copies of Material Safety Data Sheets; installs seismic restraints on chemical storage tanks and reactors and disposed off chemical waste properly. In case of occurrence of disaster, the company gives training to all workers and personnel to react as under: MINOR release in the laboratory. • Follow laboratory eyewash, rinse or shower procedures • Flush affected area continuously for 15 minutes • Vacate persons in immediate area if necessary • Clean spill • Wear protective equipment • Use appropriate kit to contain, neutralize and absorb • Collect, containerize, and label waste MAJOR release in the industry and vicinity area
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• Report factory name, location, phone number, the material spilled, possible
injuries to concerned department for emergency help and measures. • Assist injured persons. • Isolate contaminated persons and area. • Avoid contamination or chemical exposure further. • Close doors or control access to spill site MATERIAL SAFETY DATA SHEETS As part of quality for Hazard Communication Standard, all company is required to have Material Safety Data Sheets (MSDS) available to al l employees working with hazardous chemicals. The concept is “that employees have both a need and a r ight to know the hazards and identit ies of the chemicals they are exposed to when working. They also need to know what protect ive measures are available to prevent adverse effects from occurring.” Information that can be found in a MSDS includes: • The ident ity of the chemical substance • Physical and chemical character ist ics • Physical and health hazards • Primary routes of entry • Permissible Exposure Limits (PELs) • Carcinogenic status • Precaut ions for safe handl ing and use ( including personal protect ive
equipment) • Spi l l response • Emergency and f irst aid procedures • Date of the MSDS • Although not required, it is highly recommended for the company to
maintain a f i le of MSDS sheets for all of the chemicals used in lab/work area. A central f i le is maintained at the of f ice.
ON SITE EMERGENCY PLAN Emergency Response Room (Safety officer room) The place identified as Emergency Response Centre will be considered as the Security Gate Office. The location of the Emergency Response Centre may change in future as
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per convenience. The facilities available at the Emergency Response Centre shall include:
1. Internal Telephone 2. External Telephone 3. Manual Fire/Emergency Siren 4. Siren Actuation Switch 5. Important Address and Telephone Numbers 6. Emergency Vehicles 7. Confined Space Entry Procedure 8. List of Antidote/actions to be taken in case of hazardous chemical/materials. 9. Material Safety Data Sheets of chemicals 10. A copy of On-Site Disaster Management Plan
All communications after General Shift working hours and on Sundays/ Holidays are to be routed through the Security Gate Office. General Rules:
1. Follow sense of discipline and do not pain. 2. Do not rush and endanger your personnel safety 3. Use personnel protective equipment according to the situation 4. Do not block any passages, which may hinder the movement of emergency
vehicles. 5. In case you have to shut down your plant operation, do it in an orderly manner
as per standard operating procedures. 6. In situation when you have to leave your work and evacuate to identify places
out of operating areas, do it in an orderly manner. 7. Follow instructions of the Safety officer. 8. Understand the Disaster Management Plan well and take interest in practice
mock drill. An emergency in the premises has the potential to cause serious injury or loss of lives or extensive damage to the property and/or environment and serious disruption both inside and outside the plant. In such cases sometimes outside agencies are required to call for help in handling the situation. The causative factors like plant/equipment failure, human error, earth quake, sabotage etc. will normally manifest in various forms viz. Fire, Explosion, Toxic release, structure collapse etc. This OEP lays down the code of conduct of all personnel in the Plants and the procedures to be adopted by them in the event of an "Emergency". These procedures have been prepared taking into account the minimum strength of manpower available at all times in
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the premises. The individuals under the direction of the respective Team Leaders shall carry out the responsibilities assigned. The emergency procedures outlined are suitable for round the clock coverage including holidays. These emergency procedures shall be followed as outlined in the OEP during general shifts as well. OBJECTIVES: The overall objectives of OEP are:
• To control the situation and if possible eliminate as quickly as possible. • To avoid confusion/panic and to attend the emergency with clear-cut line of action. • To minimize the loss of property to the plant as well as to our neighbourhood. • To safe guard the non-affected areas. • To alert the neighbourhood. • To arrange head-count and rescue operations. • Treatment of the injured. • To safeguard others by timely evacuation. • To prevent any cascade of emergencies.
EMERGENCY: An emergency is the situation, which has potential to cause a large-scale damage or destruction to life or property or Environment or combination of these within or outside the factory. Therefore it is essential to have a laid down procedure to meet emergency systematically. In any industry, emergency can arise at any moment and this depends on the type of:
• Structure • Raw materials • Machines • Nearby Industries • Location of the Industry etc.
NATURE OF EMERGENCY: The "Emergency" specified in this plan will refer to occurrence of one or more of the following natural/manmade events.
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• Earthquakes • Fires or Explosions • Hazardous Materials Releases • Extended Power or Uti l i ty Outages • Floods • Mass Casualty Events
MEDICAL HELP: First Aid Boxes have been provided at various strategic locations. Requisite number employees are trained about First Aid, Liaison with nearest hospitals. COMMUNICATION SYSTEM:
• Alarm Rising for Emergency by blowing the sirens installed • The siren will be used for raising the emergency alarm and also for all clear
signals. • Emergency Siren: The wailing alarm will be sounded intermittently at fixed interval
of 30 seconds for a period of two minutes in case of emergency, such alarm will signify the employees that an emergency has occurred and that the emergency services should be put into operation.
• Incident Controller after assessing the situation will declare that emergency is over. Till the Incident Controller issues the declaration, all the leaders will adhere to the task and be present at the prescribed location.
• All clear signal will be sounded through continuous siren for 1 minute. Even after the emergency is over a skeleton staff of the Rescue/Evacuation Team will be available at the site of emergency for at least 30 minutes to ensure that the situation is absolutely free from danger.
• After the emergency is over, all the team leaders should meet at the Emergency Control Center and each team leader should submit a report to the Incident Controller about team performance and other details observed.
• In addition to the above systems, Internal telephones, P.A.System, Mobile telephones, Computer System etc. will be used for communication.
• If situation is beyond the control, the external agencies will be informed accordingly and asked for the help. Direct telephone, cell phone or messengers / runners may achieve this.
ASSEMBLY POINT: In case of emergency some locations are considered as Assembly Points. Depending on the wind direction and location of emergency, Assembly Point will be declared. The employees should run across the wind direction and not against the wind direction.
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Depending upon the location of the emergency the Incident Controller will fix the Assembly Point and Officer will announce the location of the Assembly Point. Employee’s attendance, visitors and contractors workmen register will be made available at the Assembly Point for head count. Emergency control centre: Factory Manager Office will be declared as an Emergency control centre. Emergency control centre is facilities with:
I. Address and Telephone numbers of the Factory Inspectorate, Gujarat Pollution Control Board, Police, Fire Brigade, Hospitals and OEP Team Members
II. Plant layout-indicating storage of hazardous materials, layout of fire Hydrants/extinguishers, entrances/exits, roads etc.
IV. Fire Blankets / Fire Proximity Suit, Breathing Apparatus, First Aid Box etc. V. List of employees with address, telephone number, blood group etc.
VI. Material Safety Data Sheets of all chemicals handled. WIND SOCKS: Wind direction will be determined with the help of installed windsocks. MOCK DRILL: Mock drills are carried out regularly to familiarize the staff with their roles, fire protection equipment/system installed in the plant and use of personnel protective equipment. Senior officials monitor this and shortcomings are thoroughly studied and necessary corrective measures are taken. PROCEDURES FOR MOCK DRILLS
A. Inform all the employees about mock drills and the signal to be given. B. Fix the date and location of the emergency for mock drills. C. Mock drills will be monitored by observers. D. Raise the siren for emergency.
PROCEDURE ON NOTICING AN EMERGENCY
1. If anybody notices any situation, which may lead to a disaster, should be immediately inform the Shift In-charge / site controller / Incident Controller / Fire & Safety Supervisor / Security.
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2. Take charge of the situation as Incident Controller. 3. Rush to the site of emergency to get the correct picture and then to Emergency
Control Center for speedy control over the situation by making an arrangement for raising the alarm.
4. On arrival of Team members, he shall assign duties as required and activate the On-Site Emergency Plan.
5. Ensure safety of the plant and the personnel in the plant. He will make an assessment of the emergency and decide on external assistance.
6. Communicate and Coordinate among the Incidents Controller/ Site Controller/ Factory manager/ fire safety supervisor etc. and will be the final authority on all matters related with management of emergency such as:
Fire fighting. Welfare and rescue operations. Arrange for Civil/Mechanical/Electrical work during emergency. Transport.
INCIDENT CONTROLLER / SITE CONTROLLER: Rush immediately to the scene of the fire/emergency, select and set out appropriate fire/emergency equipment. He will take the below mentioned actions at the earliest opportunity, if the fire/emergency is not controlled. He will Call the security personnel from their residences for additional manpower if
required. Regulate entry and exit of personal required for controlling the fire/emergency. Restrict exit of personal required for controlling the fire/emergency. Arrange for Personnel Protective Equipment required for the emergency. Call, the local Fire Brigade, Police in case of necessity in consultation with the
Incident controller. Arrange transport facilities for removal of causalities to dispensary / hospital. Take responsibility of law and order. Keep detailed records of the incident and progress of operations to fight the
emergency. FACTORY MANAGER: He will rush to the Emergency Control Centre and collect the information from the Incident Controller. Further he will,
• Announce the location of the Assembly Point after getting information from Incident Controller / site controller.
• Take the list of persons to be communicated internally and externally.
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• Maintain liaison with the press, government agencies i.e. Police, Fire Brigade etc.
and the neighbourhood regarding the emergency under instructions from Incident Controller.
• Courteously Receive officers from the State Government or neighbours to the Administration Block only and inform to Incident Controller that they can be taken care off.
• Take all the steps required for the welfare such as providing tea, snacks, emergency temporary Medical Center in consultation with the incident controller/site controller.
• Disclose all the necessary information in the plant and media so as to avoid rumours and Confusion.
• Also be responsible for the head counts at the Assembly Points. FIRE & SAFETY SUPERVISOR/ SHIFT INCHARGE & SECURITY:
o Proceed to the scene; establish contact with firemen and incident controller to supplement efforts in fire fighting.
o Assist in searching casualties and help to remove them to the medical centre. o Organize outside assistance in fire fighting and rescue operations if required. o Mobilize personal protective equipment and safety appliances and assist personnel
handling emergency in using them. o Keep and check on any new development of unsafe situation and report the same
to Site Main Controller. o Collect and preserve evidence to facilitate future inquiries.
o Effectively cordon off the emergency area and will prevent unauthorized people
entering the scene. o Permit the Fire tenders or Ambulance requisitioned by Incident Controller to the
plant. o Ensure that vehicles and trolleys are sent out of the plant premises. o Ensure that all the employees are conducted out of plant and assembled at
Assembly Point. o Control Traffic Movement. o Remove tankers, tanker drivers outside. o Entry of unauthorized public to be prevented. o Arrange for vehicles for shifting casualties and essential workers to safe assembly
points. ENGINEERING/ OPERATION & MAINTENANCE:
o Ensure the safety of the remaining part of the plant. o Take necessary steps for plant shutdown in consultation with the site controller.
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o Ensure that an Operator is immediately available at the Water Pump House for fire
fighting. o Mobilize with necessary tools and tackles to handle any repair work on an
emergency basis. OFFSITE EMERGENCY PREPAREDNESS PLAN The task of preparing the Offsite Emergency Plan lies with the District Collector; however the offsite plan will be prepared with the help of the local district authorities. The proposed plan will be based on the following guidelines. Introduction
o Offsite emergency plan would follow the onsite emergency plan. When the consequences of an emergency situation go beyond the plant boundaries, it becomes an offsite emergency.
o Offsite emergency is essentially the responsibility of the public administration. However, the plant management will provide the public administration with the technical information relating to the nature, quantum and probable consequences on the neighbouring population.
o The offsite plan in detail will be based on those events, which are most likely to
occur, but other less likely events, which have severe consequence, will also be considered. Incidents which have very severe consequences yet have a small probability of occurrence would also be considered during the preparation of the plan.
o However, the key feature of a good offsite emergency plan is flexibility in its
application to emergencies other than those specifically included in the formation of the plan.
o The roles of the various parties who will be involved in the implementation of an
offsite plan are described below. Depending on local arrangements, the responsibility for the offsite plan would either rest with the plant management or with the local authority.
o Either way, the plan would identify an emergency coordinating officer, who would
take the overall command of the offsite activities. As with the onsite plan, an emergency control centre would be setup within which the emergency coordinating officer can operate.
o An early decision will be required in many cases on the advice to be given to
people living
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o "Within range" of the accident - in particular whether they should be evacuated or
told to go indoors. In the latter case, the decision can regularly be reviewed in the event of an escalation of the incident.
o Consideration of evacuation may include the following factors: In the case of a
major fire. Only houses close to the fire are likely to need evacuation, although a severe smoke hazard may require this to be reviewed periodically; and if a fire is escalating and in turn threatening a store of hazardous material, it might be necessary to evacuate people nearby, but only if there is time; if insufficient time exists, people should be advised to stay indoors and shield them from the fire.
o This later case particularly applies if the installation at risk could produce a fireball
with very severe thermal radiation effects. Aspects Proposed to be considered in the Offsite Emergency Plan The main aspects, which should be included in the emergency plan, are: Organization Detail of command structure, warning systems, and implementation procedures, emergency control centres. Names and appointments of incident controller, site main controller, their deputies and other key personnel. Communications Identification of personnel involved, communication centre, call signs, network, list of telephone numbers. Specialized Knowledge Details of specialist bodies, firms and people upon whom it may be necessary to call e.g. those with specialized fuel knowledge, laboratories. Voluntary Organizations Details of organizers, telephone numbers, resources etc Fuel Information Details of the hazardous substances stored and a summary of the risk associated with them.
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Meteorological Information Arrangements for obtaining details of weather forecasts and weather conditions prevailing at that time. Humanitarian Arrangements Transport, evacuation centres, emergency feeding, treatment of injured, first aid, ambulances and temporary mortuaries. Responsibility of the Emergency Co-ordinating Officer The various emergency services would be co-ordinated by an Emergency Coordinating Officer (ECO), who will be designated by the district collector. The ECO would liaison closely with the site main controller. Again depending on local arrangements, for very severe incidents with major or prolonged offsite consequences, the external control would be passed to a senior local authority administrator or even an administrator appointed by the central or state government. The ECO will be equipped with address and phone numbers of important agencies. Responsibility of Police Formal duties of the police during an emergency include protecting life and property and Controlling traffic movements. Their functions should include controlling bystanders, evacuating the public, identifying the dead and dealing with casualties, and informing relatives of death or injury. Responsibility of the Local Authority
The duty to prepare the offsite plan lies with the local authorities. The emergency planning Officer (EPO) appointed should carry out his duty in preparing for a whole range of different emergencies within the local authority area. The EPO should liaison with the plant, to obtain the information to provide the basis for the plan. This liaison should ensure that the plan is continually kept up to date. It will be the responsibility of the EPO to ensure that all those organizations which will be involved offsite in handling the emergency, know of their role and are able to accept it by having for example, sufficient staff and appropriate equipment to cover their particular responsibilities. Rehearsals for offsite plans should be organized by the EPO. Responsibility of Fire Authorities The control of a fire should be normally the responsibility of the senior fire brigade officer
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who would take over the handling of the fire from the site incident controller on arrival at the site. The senior fire brigade officer should also have a similar responsibility for other events, such as explosions. Fire authorities in the region should be appraised about the location of all stores of flammable materials, water and foam supply points, and fire fighting equipment. They should be involved in onsite emergency rehearsals both as participants and, on occasion, as observers of exercises involving only site personnel. Responsibility of Health Authorities Health authorities, including doctors, surgeons, hospitals, ambulances and so on, should have a vital part to play following a major accident, and they should form an integral part of the emergency plan. For major fires, injuries should be the result of the effects of thermal radiation to a varying degree, and the knowledge and experience to handle this in all but extreme cases may be generally available in most hospitals. Major off site incidents are likely to require medical equipment and facilities additional to Those available locally, and a medical "mutual aid” scheme should exist to enable the Assistance of neighbouring authorities to be obtained in the event of an emergency. Responsibility of Government Safety Authority This will be the factory inspectorate available in the region. Inspectors are likely to satisfy themselves that the organization responsible for producing the offsite plan has made adequate arrangements for handling emergencies of all types including major emergencies. They may wish to see well documented procedures and evidence of exercise undertaken to test the plan. In the event of an accident, local arrangements regarding the role of the factory inspector will apply. These may vary from keeping a watch, to a close involvement in advising on operations.
7.11 SOCIAL IMPACT ASSESSMENT
Operational phase of the proposed unit cover the entire l ife span of the project. The proposed project wil l generate direct employment for local persons. The indirect employment will also be generated by way of transportation, shopkeepers and other casual employment for many people.
Local people wil l be given training and preference for almost all the jobs in the plant, direct as well as indirect. Economic status of the local people wil l be improved due to the increased business opportunit ies, thereby, making a posit ive impact. Educational, medical and housing faci l it ies in the study area wil l considerably improve.
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CHAPTER - 8 PROJECT BENIFITS The proposed activities will become beneficial to the surrounding area or community
in terms of employment, social development and other benefits as described hereunder;
8.1 EMPLOYMENT OPPORTUNITY Due to Proposed project, 20 nos. of local peoples and outside peoples will get employment during the construction phase and 40 peoples will be employed during the operation phase. Local people will be given preference for almost all the jobs in the Plant, direct as well as indirect. Economic status of the local people will be improved due to the increased business opportunities, thereby, making a positive impact. Educational, medical and housing facilities in the study area will considerably improve. Therefore, social infrastructure of the study area will be improved. The company will also do following developmental activities in the area: The proposed Project does not involve any displacement of villages; however it will lead to development of the region and increase in infrastructure facility. During the operation phases of the project a work force will be needed which will include both skilled and unskilled people. Due to the proposed project direct employment for local employees will be generated. Existing ancillary as well as auxiliary industries would be benefited by way of getting additional work. In addition to direct employment, indirect employment will generate ancillary business to some extent for the local population.
For the proposed unit, persons will be employed for skilled, semi-skilled and unskilled
category. The preference will be given to local population for employment in the semi-
skilled and unskilled category; this will increase the employment opportunity in the
surrounding area. The ideology of the company is to give employment opportunity to
nearby villagers and this is the most positive aspect of company regarding
enhancement of the society. Secondary jobs and indirect employment are also bound to
be generated to provide day-to-day needs and services to the work force and industrial
activity. This will also increase the demand for essential daily utilities in the local market.
Due to proposed project there will be development of communication facilities in the
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area. The employed people will be benefited financially. This financial gain will fulfill
their monetary requirements, which in turn will increase their standard of living.
8.2 CORPORATE SOCIAL RESPONSIBILITY (CSR) & SOCIO-ECONOMIC DEVELOPMENT
Due to the proposed Project, facilities are likely to grow with the development. There is a positive effect due to improved communication and health services, which have lead to economic prosperity, better educational opportunities and access to better health and family welfare facilities. There will be beneficial effect on human settlement due to employment opportunities from the industry. Local quality of life will be improved. This factor combined with all other mitigation measures like proper treatment and disposal of wastewater, hazardous waste and gaseous emission has minimized the adverse impact on ecology and had a beneficial impact on human settlement and employment opportunities. There has been a beneficial impact on the local socio-economic environment. The increasing industrial activity will boost the commercial and economical status of the locality up to some extent. BHIMANI DYECHEM INDUSTRIES is not only carries out business but also
understands the obligations towards the society. The Project proponent is well aware
of the obligations towards the society and to fulfill the social obligations, unit will
employ semi-skilled and skilled labor from the nearby villages for the proposed project
as far as possible. Unit will also try to generate maximum indirect employment in the
nearby villages by appointing local contractors during construction phase as well as
during operation phase. Unit will be contributed reasonably as part of their CSR
activity. Unit will spend about 2.5% of the project cost for CSR activities in nearby
villages. CSR activities identified and planned at present are described below Table.
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Any industrial development is associated with certain positive impacts as well as some negative impacts on the environment. However, the negative or adverse impacts cannot possibly rule out scientific development. At the same time, adverse impacts cannot be neglected.
An Environmental Management Plan has been formulated for mitigation of the adverse impacts and is based on the present environmental conditions and the environmental impact appraisal. This plan helps in formulating, implementing and in monitoring the environmental parameters during and after commissioning of the project.
The Environmental Management Plan describes, in brief, the management's plan for proper and adequate implementation of treatment and control system for air and liquid pollutants and for maintaining the environment. It also includes development of green belts around the Plant, proper safety of the workers, noise control, fire protection systems and measures. This chapter provides mitigation and control measures to attenuate or eliminate environmental impacts, which are likely to be caused by the proposed project. An Environmental Management Plan (EMP) has been developed to mitigate the potential adverse impacts and to strengthen the beneficial environmental impacts as well as to create positive environmental footprints during the construction and operation phases. The institutional capacity of BHIMANI DYE CHEM INDUSTRIES as the owner & facility developer and the reporting requirement to fully implement the mitigation measures have also been described in this chapter. In addition to that during the operation phase, the company will have an additional responsibility to comply with the statutory requirements as per the guidelines of Central/ State Government.
10.2 The EMP
The Environmental Management Plan (EMP) consists of a set of mitigation, monitoring and institutional measures to be taken during the design, construction and operation (post construction) stages of the project. The plan also includes the actions needed for implementation of these measures. Overall objective of EMP:
• Prevention: Measures aimed at impeding the occurrence of negative
environmental impacts and/or preventing such an occurrence having harmful environmental impacts.
• Preservation: Preventing any future actions that might adversely affect an
environmental resource or attribute.
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. • Minimization: Limiting or reducing the degree, extent, magnitude, or
duration of adverse impacts.
The major components of the Environmental Management Plan are:
• Mitigation of potentially adverse impacts. • Monitoring during project implementation and operation. • Implementation schedule and environmental cost estimates. • Integration of EMP with project planning, design, construction and operation. The EMP has been designed keeping in view the regulatory and other requirements to ensure the following: • Minimum disturbance to the native flora and fauna. • Compliance with the air, water, soil and noise quality norms. • Conservation of water to the extent possible. • Encourage the socio-economic development.
10.3 OBJECTIVES OF EMP
The main objectives in formulating this environmental management plan are:
To treat all the pollutants viz., liquid and gaseous which contribute to the degradation of the environment, with appropriate technology.
To comply with all regulations stipulated by the Central / State Pollution Control Boards related to air emissions and liquid effluents discharges as per air and water pollution control laws
To handle hazardous wastes as per the Hazardous Waste (Management and Handling Rules, 1989 of the Environment (Protection) Act, 1986
To encourage support and conduct developmental work for the purpose of achieving environmental standards and to improve the methods of environmental management.
To promote further afforestation in the surrounding areas of the Plant To create good working conditions (devoid of air and noise pollution) for
employees To reduce fire and accident hazards. Perspective budgeting and allocation of funds for environment management
expenditure. Dissemination of technological solutions on Commercial basis to interested
parties and Continuous Development and search for innovative technologies for a cleaner and better environment.
The Potential Environmental Impacts from the construction and operational
activities of the industry are summarized below.
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. The site will be secured by fencing and manned at entry points.
Adequate and effective environment protection measures will be planned and designed to minimize the impacts due to activities related to preconstruction (preparatory phase) of the project, machinery installation and commissioning stages and end with the induction of manpower and start up. The impacts during the construction phase on the environment will basically be very insignificant as the project construction area is very small. Only foundation for RCC structure will be made. Ready mix Concrete will be used and therefore no possibility of fugitive emission due to material handling. In view of the above, the following measures are recommended to reduce the impact during this period:
• Due provision of necessary infrastructural services like water and power supply
etc., for the construction area.
• All possible care will be taken to reduce the noise level due to construction activity. As planned, no such noise generating machineries will be used. Also, noise prone activities shall be restricted to the extent possible during night particularly during the period 10 PM to 6 AM in order to have minimum environmental impact.
10.5 ENVIRONMENTAL MANAGEMENT DURING OPERATION The detailed mitigation measures planned during operation phase of the project are as follows:
Activity Environmental Impacts
Mitigation measures Remarks
Construction Phase: Erection of Plant Machineries
• Air • Noise • Socio
Economic
• Well maintained vehicles will be used.
• Metalled Road for Vehicle Movement
• Well maintained equipment will be utilized to prevent noise generation.
• Local labour will be hired for the work so that housing arrangement will be avoided.
• Proper storage of raw materials, products and fuels.
• Ensuring closed feeding and sampling.
• Establishing SOPs for start-up, shut down and maintenance operational
procedures.
• Regular work place monitoring and ambient air quality monitoring as per
post project monitoring plan.
• Various types of solvents will be used in the manufacturing process. The
solvents will be stored in storage tanks with vent condensers. These are
handled in closed conditions.
• The industry will take measures for reduction of fugitive emissions by providing chilled brine circulation to the condensers which, ensures the recovery of 95%. Good ventilation will be provided to reduce the workroom concentrations. The reactor generating solvent vapors will be connected to condensers with reflux system. Dyke walls will be provided to the solvent storage tanks. The solvents like Benzene, TNBA, methanol, ODCB, Butanol etc will be recovered up to 95 % by using distillation and the remaining 5% will be the loss.
10.5.4 SOLVENT MANAGEMENT PLAN
Solvent management consists of the following: Unloading Storage Handling / transferring Process / Reaction Recovery i) Unloading Solvents are received in drums / tankers
Drums • Before unloading the drums from the truck, check the drums condition. • Drums may be MS or HDPE Carboys • Drums / barrels will be unloaded from the vehicles onto the unloading
platform by using the drum lifter provided for the purpose. Under no circumstances drums shall be dropped or rolled on the ground or on any
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• Carboys will not be dropped or allowed to strike against each other and shall be unloaded on the pallets
• Personal protective equipments like safety goggles, hand gloves, PVC aprons and safety shoes will be used while handling chemicals.
Road tankers • Security will ensure that vehicle personnel shall not carry any match box /
lighters • The store personnel, has to check the paper work before unloading to
confirm that the correct chemical received as well as discharged into the dedicated tank.
• Barriers and flags should be positioned to warn personnel at the unloading. • Brakes should be set and the wheels chocked. • The truck should be earthed. • Tanker should be kept under inert gas flushing through vent while unloading • Make sure that the inert gas valve remains open during the entire unloading
period of delivery is by gravity or by pumping. • Connect the flexible hose to the tanker and to the transfer pump • Check liquid level gauge on storage tank to ensure liquid is being transferred • When tanker is empty, stop pump and close valves on tanker, close valves in
transfer line. • [For flammable material, stop inert gas purge] • Disconnect flexible hose and put into proper catch container to ensure no
product is lost on to the ground. • Remove choked warning signs, earthing and switch locks • Read storage tank liquid level gauge and record reading ii) Storage/ handling/ transferring Storage Tanks
• 2 or 3 Square meter condenser [depends on solvent volatility] with cooling water circulation is connected to each solvent storage tank to prevent solvent vapors escaping from tank surface in to atmosphere. The condensed solvent will go to respective tank. This results in recovery of solvent and prevention of VOCs into the atmosphere.
• The solvent pump which is having mechanical seal will be used for transferring the solvent to the Day Tank of the respective reactor as and when required. The entire solvent transfer takes place in a closed system. There is no manual handling.
The above management will results in recovery of solvent more than or
equal to 95%.
Drums
• As and when required the solvent drums in closed condition will be transferred to the respective reactor.
• By using AODD pump the solvent will be transferred in to the reactor. Hence,
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• During reaction stage the solvent vapors will be sent to a primary condenser having cooling water circulation and later to secondary condenser having temperature < 50 0C chilled brine circulation.
• Above system will eliminate solvent losses during reaction stage and recovery will be the maximum extent possible.
The above management will results in recovery of solvent more than or
equal to 95%. System will eliminate solvent losses during reaction and recovery will
be the maximum extent possible. The above management will results
in recovery of solvent more than or equal to 95%.
10.5.5 NOISE POLLUTION
All the equipment in the plant would be designed to have a total noise
level not exceeding 70-75 dB (A) as per the requirement of CPCB
standards.
NOISE ENVIRONMENT HAG, Boiler and DG set will be the major noise generating units in the
plant, of which generator will be functioning only at the time of power
failure. There is no need for the workers to be near the DG set & Utility
units continuously. The Generator sets will be placed in acoustic
enclosures to maintain the noise levels as permitted by CPCB.
NOISE POLLUTION CONTROL / MANAGEMENT • The noise levels in the work place environment will be monitored periodically
and if necessary action will be taken in the form of regular maintenance schedule to reduce noise and vibration in generating sources.
• The effects of the vibrations coming out of the base of the body over the surrounding civil structures are minimized by providing Damping pads/Resilient mounting at the time of installation.
• Under the general health check up scheme as per factory act, the workers will however be checked up for any Noise induced Hearing Loss (NIHL) by a trained ENT Doctor.
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• Water is essentially used in process, Boiler, cooling tower, washing, Scrubber along with domestic purpose. The total water required for the plant operations will be met from Tanker facility.
WATER POLLUTION CONTROL / MANAGEMENT • Domestic Wastewater @ 5.0 KL/day will be disposed off through Soak Pit /
Septic Tank System. • Industrial Waste water @44.5 KL/D treat in Effluent treatment plant with
primary treatment and then it will sent Common Spry Dryer • So, unit will achieve Zero Discharge.
Treatment system:-
DETAILS OF PROPOSED EFFLUENT TREATMENT PLANT UNITS Sr. No.
Name of Unit Quantity Nos.
Capacity
1. Collection Tank 2 50 KL (Each) 2. Neutralization Tank 1 75 KL (Each) 3. Hoper Bottom Settling
Tank 1 75 KL
4. Sludge Drying Bed 4 ---- 5. Final Collection Tank 3 100 KL (Each)
Strategic Control / Management
• Minimizing water usage. • Segregation and collection of effluent for proper treatment and to minimize
waste generation at treatment facility and to recover water for recycle and reuse.
• Reducing the water consumption for the process by way of developing the process and operation methods.
• Prepare SOPs for handling and treatment of effluent water. • Minimize spillage and leakage of effluent to avoid Land pollution.
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-- 5 MT/Year Collection, Storage and send to CHWIF.
Resource Conservation / Waste Minimization The unit will also implement the concept of waste minimization circle including: • Volatile raw materials will be separated by rectification and these can be
recycled into process.
• Good House Keeping practices make the system easier and less costly. Some of these are as follows: • Solid wastes e.g. powders, spills, etc. in process, and packaging will be
separately collected and disposed off instead of allowing these to join
effluent streams. This will reduce load and increase the efficiency of
treatment system.
• Search for future recycling schemes and evaluate their worth and
implement such schemes wherever a promise of economic feasibility
exists.
Discarded Container / Barrels/ Liners Management • Discarded containers/ barrels/ liners will be kept at a designated place
with paved surface.
• These will be decontaminated (washed/ cleaned) and stored in the
designated area in scrap yard. Washed water sent to ETP.
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. and disposal of all toxic and hazardous chemicals, no additional safety
methods are required especially to prevent contamination of soil.
Liberal use of locally available farmyard manure will be used for the
plants in the greenbelt and block plantations for improving the productivity,
fertility and health of soils.
The project does not have any impact on the soils beyond the boundaries of
the project site since it is a zero liquid discharge unit.
10.5.13 [RISK & HAZARDS MANAGEMENT]:
All the provisions as per the Factories act, 1948 manufacture, storage
and import of hazardous chemicals [MSIHC] Rules, 1989 and
amendments thereafter and also, the Hazardous Waste (Management,
Handling and Transboundary Movement) Rules, 2016 will be followed.
Work environment monitoring as well as noise monitoring will be carried
out on regular interval through third party.
Following hazards may occur during the operation. Fire Hazards Chemicals handling and Storage Road accidents Process hazards Health hazards Following procedures will be followed for effective management of any
disaster in the plant.
• Identification of Hazards and Risk assessment • Identification of persons at risk • Mitigation measures to minimize or elimination of Risk • Disaster management plan
10.6 GREENBELT DEVELOPMENT
OBJECTIVE
The purpose of a green belt around the plant site is to capture the fugitive emissions
emanating from Plant operations, attenuate the noise generated and improve the
aesthetics.
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The choice of trees species, suitable for plantation at the Industry Site, has been governed by the following guiding factors:
1. As per guidelines issued by Ministry of environment & Forests for greenbelt
development. 2. As per the study carried out by our FAE in Ecological & Biodiversity.
3. The tree must be tolerant to all the pollutants present in the area. 4. The tree should be able to grow and thrive on soil of the areas, be
evergreen, in habitat, having minimum of leaf fall. 5. The tree must be tall in peripheral curtain plantation and with large and
spreading canopy in the primary and secondary attenuation zones. 6. The tree should possess extensive foliar area to provide maximum impinge
surface for continued efficient adsorption and absorption of pollutants. 7. The tree should be fast growing and indigenous. 8. The tree should maintain ecological, land and hydrological balance of the
region.
Total plot area is 3344 Sq. meter. From that they had done planning for gardening and plantation for 1105 sq. meter. ; which is 33 % of the total plot area. • Unit will develop 25 - 30 trees every month for the period of five years in the
premises and outside premises.
• The tree species selected for the plantation will be pollutant tolerant ,fast growing, wing firm, deep rooted and ever green.
• The company will select pollutant tolerant plant species. For example, Asopalav, Neem Tree, Gulmahor, Julie, etc.
• We will also develop plantation as per the MoEF guidelines all along the periphery of plant so that these trees perform as natural barrier and bring down the fugitive emission and stop carryover of dust along with wind current.
• The tree species selected for the plantation will be pollutant tolerant, fast growing, wing firm, deep rooted, and ever green. The company will select pollutant tolerant plant species.
They will also develop plantation as per the MoEF guidelines all along the periphery of plant so that these trees perform as natural barrier and bring down the fugitive emission and stop carryover of dust along with wind current.
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. Budgetary expenditure for the greenbelt development has been depicted in the Table No. 10.1
TABLE NO:10.1
BUDGETARY EXPENDITURE FOR GBD
Wind breaker plant species will be (eg. Polyanlthia, Eucalytus, Casuarina, etc.) Planted around the periphery of near boundary walls. Grass mat along with combination flowering shrubs will be planned along the rest rooms. Potted plants and climbers will be used on the roof tops. All the corners inside the rooms of administration building and along the stair case, potted shrubs will be put and change time to time for watering, pruning and fertilizing. Fast growing species with more calorific value is preferable. Necessary help will be taken from the local DFO in development of green belt. Money plants like climbers will be used and make them to hang to avoid penetration dust inside the working areas. These climbers will be sprinkled regularly to remove adhered dust particles. Based on the demand of nutrients by soil the fertilizer input shall be given. These trees will be planted in about different rows. The interspaces will be planted with grasses, bushes and hedges. Choosing native plant species which suits to local environmental conditions will be encouraging (percentage survival) and also for sustainable ecosystem development. Plants with flowering will give good aesthetic look. 1 meter width will be kept for tree plantation around the project boundaries. The plant species for green belt is given below in Table- 10.2
Table 10.2 Plant Species for Green Belt Development
Sr.No Botanical name English name Habitat
1 Abutilon indicum Indian Mallow Shrub 2 Acacia arabica Gum arabic tree Tree 3 Acacia ferruginea Rusty Acacia Tree 4 Acacia mearnsii black wattle Tree 5 Acacia melanoxylon Sally Wattle Tree 6 Acacia nilotica Babool Tree 7 Ageratum conyzoides Goat weed Shrub 8 Albizia lebbeck Flea tree Tree
Sr. No. Parameter Amount in Rs.
1 Site Development 100000.00
2 Plants/ Seeds 75000.00
3 Plant Care & Reg. 100000.00
TOTAL 275000.00
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10 Barringtonia acutangula Indian putat Tree 11 Bidens pilosa Beggar tick Herb 12 Butea frondosa Flame of the forest Tree 13 Calotropis gigantean Crown Flower Shrub 14 Cassia surattensis Scrambled Egg Shrub 15 Cleistanthus collinus Garari Shrub 16 Cleome viscose Asian spider flower Herb 17 Drypetes sepiaria Wild Caper Bush Shrub 18 Eucalyptus globules Eucalyptus Tree 19 Ficus benghalensis Banyan Tree 20 Ficus religiosa Pee pal Tree 21 Magnifera indica Mango Tree 22 Pongamia pinnata Indian beech Tree 23 Techtona grandis Teak Tree
10.7 HEALTH AND SAFETY
Following measures will be adopted in the plant: • Inspection and maintenance of pollution control systems regularly. • All safety measures such as safety appliances, training, safety awards,
posters, slogans related to safety. • The workers exposed to noisy sources will be provided with ear muffs/plugs. • Adequate facilities for drinking water and toilets insufficient numbers will be
provided to the employees. • Fire proof aprons and necessary personnel protective appliances and
equipment will be provided to the concerned personnel.
10.8 OCCUPATIONAL HEALTH HAZARDS
To prevent any spillage, accident and impacts of human health for safety measure will be taken while handling the raw material and products:
Occupational control measures for health hazard to the worker and to keep the risk of accidents to a minimum from our manufacturing activities.
Mitigatory measures:
For the proposed project, company will make following arrangement within the factory premises for the different hazards:
Storage & Handling of Hazardous Chemicals:
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. • Company will do planning to stock all the necessary material as minimum as
possible. • All containers with hazardous chemicals have labels indicating the contents
and warning of the hazard. • Necessary information on safe handling and first aid measures and antidotes
of major hazardous material will be available on the label. • Workers dealing with hazardous chemicals will be trained on health risks and
safe handling. • Exposure to hazardous chemicals will be minimized. • Liquid Hazardous chemicals will be transferred in closed piping system. • Separate storage section will be provided for storage of hazardous and non-
hazardous raw materials. • Drums / Tanks shall be located and marked in designated area of hazardous
chemical storage. • Tanks / Drums of proper MOC will be selected. • All tanks / Drums shall be uniformly tagged. • Level indicator shall be provided in tanks. • Dyke will be provided. • Industrial type electric fittings shall be provided. • Adequate fire fighting equipments will be provided. • Anti corrosive paint shall be done. • Safety instruction board will be displayed. • Proper earthling shall be provided. • Lightning arrestor will be provided.
Vessel and other Equipment related:
• Checking of process vessels and equipment is carried out regularly. • Records related to maintenance and its planning schedule is maintained.
Safety Instructions for Transportation of Hazardous Materials:
• The name of the chemical along with pictorial sign denoting the dangerous Goods are marked on the vehicle and the packing material.
• The name of the transporter, his address and telephone number are clearly written on the road tanker and on the vehicle.
• The important safety precautions are mentioned on the tanker as a Warning label.
• Only trained drivers and cleaners are engaged in transport of hazardous Chemicals.
• The transporter and manufacturer must ensure the safe transportation of the material.
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• The tankers are checked for its fitness and safe condition before loading. • During loading and unloading, the tanker should be braked and isolated against any
movement, while loading/unloading, use safety appliances. • Check for leakages from the line connections before starting and stopping the filling
operations. • Drive the vehicles carefully, especially in crowded localities and on bumpy Roads. • Do not apply sudden break. • The tanker should not be parked for long time on the way and especially in
Crowded Places. Park the vehicle away from residential areas.
Electrical related:
• All electrical fitting and motors in the storage areas will be flameproof. • Checking of all earthings, wiring & connection will be carried out regularly. • Proper earthing will be provided at all equipments and will be provided for
additional equipment. Adequate Nos. of earth pits will be provided.
Safety related:
• Adequate types of personal protective equipment will be provided and also safety training will be provided to workers.
• Emergency showers and eye wash stations will be available at the worksite. • Arrangement for 24 hr. medical facilities by contact with nearest health care
centre/ hospital. • Pre-employment medical check-up and annual medical check-up will be
carried out and its records will be maintained properly.
Fire control plan:
• Overhead water storage tank with adequate capacity is provided to ensure 24 hr. supply.
• Fire water tank with sufficient capacity of 100 KL (50 KL x 02 Nos.) will be provided with fire pump (02 Nos.)
• Fire hydrant system will be provided. • Sprinkler system will be provided at raw material storage area and tank farm
area. • Fire extinguisher will be provided at production plant as per the requirement.
Contact numbers of nearest fire agency will be provided. • Nearest fire station is Kalol. Time required to reach the project site is 15
minutes. • Unit will appoint qualified and trained fire personnel having qualification like
B.Sc. or Diploma in Fire and Safety.
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. • Flame proof equipments and fittings will be provided for handling of
hazardous chemicals. • Tanks and all pump motors shall be earthed. • Road tanker earthing lines shall provide near the unloading pumps. • Independent dykes will provide for hazardous chemicals storage to contain
leakages. Floors of the dyke area shall of impervious finish. • Housekeeping of the plant shall as per prescribed norms. Floors, platforms,
staircases, passages will be kept free of any obstruction. • All hazardous operations shall explain to the workers. They will periodically
trained on the hazardous processes. • Dedicated supply of firewater shall available in the plant. • Only authorized persons shall be allowed inside the plant. • All instrument and safety devices will be checked and calibrated during
installation. They will also be calibrated, checked at a frequent interval. Calibration records shall maintain.
• All electrical equipments will be installed as per prescribed standards. • All the equipments of the plant shall periodically tested as per standard and
results shall documented. All equipments undergo preventive maintenance schedule.
• The area will fence to isolate the same from all other departments. • Proper Earthing will be provided to each tank. Also earthing would be taken
care during solvent transfer from tanker into the underground vessel. • Flame arrestors shall provide on each tank. • Flameproof pumps & motors shall provide for solvent transfer. • In addition to fire hydrant system, fire extinguishers will be installed at
different locations within premises. • Adequate ventilation arrangement shall provide for safe and better working in
the plant as per the standard. • Process, equipments, plant involving serious fire hazards are designed as
per prescribed guideline. • Sufficient access for fire fighting shall provide in the plant. • Protection against lightning will be taken care in the plant. • Precautions against ignition will be taken.
Fire fighting System: -
Adequate fire fighting system will be provided in the proposed plant.
Sufficient numbers of Fire extinguishers will be installed in all plants and
storage area and details of existing fire control equipments are given in Table
10.3.
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. 4. Heat Detector Hazardous chemical storage area
5. VOC Detector Process Plant
Hazardous chemical storage area
Hazardous waste storage area
6. Automatic Sprinkling Admin building, hazardous chemical storage area,
Utility
Proposed DG Set of 01 Nos. x 125 KVA will be installed for emergency power supply.
Mock drill and training will be scheduled and conducted once in six months. Respiratory PPEs like self contained breathing apparatus, bubble hood point
with air compressor, online respirator and non-respiratory PPEs like PVC
apron, gum boot, goggles, rubber hand gloves are provided in case of fire.
Nearest fire station Kalol is located at a distance of 10 km from project site.
Safety related
• Adequate types of personal protective equipment will be provided and also safety training wil l be provided to workers.
• Emergency showers and eye wash stations is available at the worksite.
• Arrangement for 24 hr. medical facil it ies by contact with nearest health care centre/ hospital.
• Pre-employment medical check-up and annual medical checkup is carried out and its records is maintained properly.
DETAILS OF OCCUPATIONAL HEALTH PROGRAMME:
• Worker can be directly or indirectly exposed by chemical like Chloro Sulfonic
Acid, Hydrochloric Acid, Sulphuric Acid, Ammonia, Acetic Anhydride, Oleum, Sodium Hydroxide(Caustic lye) and other liquid chemicals as mentioned in chapter 2, during process or material handling.
COMAPANY HAVE TAKEN FOLLOWING ACTION TO KEEP CHEMICALS WITHIN PEL/ TLV:
• Process should be carried out in isolated area or closed system.
• Dilution ventilation/local exhaust ventilation system should be provided.
• Chemical handled by competent person.
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• MSDS of hazardous substance must be maintained by company.
• Quantity of substance should kept to absolute minimize.
• Flame proof electric fitting should be provided.
• Safety devices like temp. Control and pressure control must be provided to vessel.
• Labeling and sign board should be provided.
• Fire fighting, sprinkling system and emergency exit should be provided.
• PPE must be used during handling of chemicals.
EVALUATION OF EXPOSURE OF CHEMICAL DURING REPLACEMENT AND PERIODICAL MEDICAL MONITORING.
• Emergency /exposure examination and test should be carried out.
Examination is based on irritation, sensitization of skin, respiratory system, eye, shortness of breath
• Test must be carried out as per handling of chemicals as per OSHA
guideline.
• Check the previous medical opinion of worker/employee as well as history.
TREATMENT OF WORKERS AFFECTED BY ACCIDENTAL SPILLAGE OF CHEMICALS: Hazards with Acute Exposure • Contact with skin may cause severe burns or systemic poisoning. • Systemic effects may occur from any route of exposure, especially after skin
absorption. Hazards with Chronic Exposure • Repeated or prolonged exposure may harm the respiratory system. Can
irritate and inflame the airways. • Hazardous material affects the central nervous system, liver, and kidneys.
Special Safety Precautions • Prevent contact with skin by wearing neoprene gloves, lab coat, and
resistant apron. • Wear safety glasses or a face shield if splashing may occur. • Store in a cool, dry, well-ventilated area, away from heated surfaces or
ignition sources. • Skin contact requires immediate washing of the affected area with soap and
water. • Remove contaminated clothing and launder before wearing again.
Procedure for treating workmen after skin contact.
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. • Skin contact requires immediate flushing of the contaminated area with soap
and water at a sink or emergency shower for a good fifteen minutes. Remove contaminated clothing. In case of eye contact, promptly flush the eyes with copious amounts of water for 15 minutes (lifting upper and lower lids occasionally) and obtain medical attention. If methanol is ingested, obtain medical attention immediately. If large amounts of methanol are inhaled, move the person to fresh air and seek medical attention at once. It is recommended to provide the safety shower and eyewash station in plant.
10.9 DETAILS OF OCCUPATIONAL HEALTH SURVEILLANCE
PROGRAMME: Aim:
• Workplace injuries, illness can be prevented and hazard should be identified.
• Evaluations of accident analysis due to unsafe act and condition as well as identified the health and safety problems in workplace.
• Effective Preventive measures strategies can be prepared.
• New technologies, educational activities, public awareness and
regulatory and policy changes can be achieved.
The overall mission of the Occupational Health Surveillance Program is to promote the health, safety and quality of life of working people will be achieved:
Surveillance program can be improved by following action.
• Pre-placement examination and periodic examination must be carried out at Work place.
• Maintain the work profile and medical history of employee/workers.
• Pulmonary function test must be carried out in case handling of hazardous
chemicals.
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. 10.10 HAZARDOUS IDENTIFICATION AND PREVENTIVE MEASURES
Raw Material Storage hazardous and controls:
Name of Hazardous Chemicals
Toxicity (Oral LD50) mg/kg
Hazardous Characteristics
Chloro Sulfonic Acid
Not Available
Flammability of the Product: Non-Flammable. Auto-Ignition Temperature: Not Applicable Flash Points: Not Applicable Flammable Limits: Not Applicable Products of Combustion: Not Available. Explosion Hazards in Presence of Various Substances: Explosive in presence of reducing materials. Non-explosive in presence of open flames and sparks, of shocks, of heat, of oxidizing materials, of combustible materials, of organic materials, of metals, of acids, of alkalis, of moisture. Fire Fighting Media and Instructions: Not Applicable.
Precautions: Keep container dry. Do not breathe gas/fumes/ vapour/spray. Never add water to this product In case of insufficient ventilation, wear suitable respiratory equipment If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes Keep away from incompatibles such as reducing agents, organic materials, metals, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package Storage: May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Corrosive materials should be stored in a separate safety storage cabinet or room.
Sulphuric Acid 2140 mg/kg [Rat.]
Flammability of the Product: Non-flammable. Auto-Ignition Temperature: Not applicable. Flash Points: Not applicable. Flammable Limits: Not applicable. Products of Combustion: Products of combustion are not available since material is non-flammable. However, products of decompostion include fumes of oxides of sulfur. Will react with water or steam to produce toxic and corrosive fumes. Reacts with carbonates to
Precautions: Keep locked up.. Keep container dry. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, combustible materials, organic materials, metals, acids,
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. generate carbon dioxide gas. Reacts with cyanides and sulfides to form poisonous hydrogen cyanide and hydrogen sulfide respectively. Fire Hazards in Presence of Various Substances: Combustible materials Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of oxidizing materials.
alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Storage: Hygroscopic. Reacts. violently with water. Keep container tightly closed. Keep container in a cool, well-ventilated area. Do not store above 23°C (73.4°F).
Hydrochloric Acid
3124 mg/kg [Rat].
Flammability of the Product: Non-flammable Auto-Ignition Temperature: Not applicable Flash Points: Not applicable Flammable Limits: Not applicable Products of Combustion: Not Available Fire Hazards in Presence of Various Substances: of metals Explosion Hazards in Presence of Various Substances: Non-explosive in presence of open flames and sparks, of shocks. Fire Fighting Media and Instructions: Not Applicable
Precautions: Keep locked up.. Keep container dry. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, organic materials, metals, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area
Liq. Ammonia NH4O4.NH3
350 mg/kg [Rat].
Flammability of the Product: Flammable. Lower Flammable Limit: 15.5 % Volume in Air (for NH3) Upper Flammable Limit: 27.0 % Volume in Air (for NH3)
Handling: Avoid contact with either liquid or vapors. Direct contact with mercury must be avoided. Use proper PPE when working with or around aqua ammonia (See section 8).
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Storage: Ambient temperature. Store in dry, well- ventilated area away from incompatible materials. Protect against physical damage. Keep out of direct sunlight and away from heat sources.
Acetic Anhydride
1780 mg/kg [Rat].
Flammability of the Product: Flammable. Auto-Ignition Temperature: 316°C (600.8°F) Flash Points: CLOSED CUP: 49°C (120.2°F). OPEN CUP: 51°C (123.8°F). Flammable Limits: LOWER: 2.7% UPPER: 10.3% Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Flammable in presence of heat. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available Fire Fighting Media and Instructions: Flammable liquid. SMALL FIRE: Use DRY chemical powder. LARGE FIRE: Use alcohol foam, water spray or fog. Cool containing vessels with water jet in order to prevent pressure build-up, auto ignition or explosion. Special Remarks: Not available
Precautions: Keep container dry. Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Oleum(65%) 2140 mg/kg [Rat.].
Flammability of the Product: Non-flammable. Auto-Ignition Temperature: Not applicable. Flash Points: Not applicable.
Precautions: Keep locked up.. Keep container dry. Keep away from heat. Keep away from sources of ignition. Keep away from direct
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. Flammable Limits: Not applicable. Products of Combustion: Not available. Fire Hazards in Presence of Various Substances: Not applicable. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of heat, of oxidizing materials.
sunlight or strong incandescent light. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. Avoid shock and friction. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, combustible materials, organic materials, metals, acids, alkalis, moisture. May corrode metallic surfaces. Store in a metallic or coated fiberboard drum using a strong polyethylene inner package. Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area. Hygroscopic; keep container tightly closed. Will react with water or steam to produce heat and toxic fumes.
Sodium Hydroxide
2140 mg/kg [Rat.].
Flammability of the Product: Non-flammable. Auto-Ignition Temperature: Not applicable. Flash Points: Not applicable. Flammable Limits: Not applicable. Products of Combustion: Not available. Fire Hazards in Presence of Various Substances: of metals Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of heat.
Precautions: Keep container dry. Do not breathe dust. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If you feel unwell, seek medical attention and show the label when possible. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, metals, acids, alkalis, moisture. Storage: Keep container tightly closed. Keep container in a cool, well-ventilated area. Do not store above 23°C (73.4°F).
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Flammability of the Product: Combustible Auto-Ignition Temperature: 615°C (1139°F) Flash Points: CLOSED CUP: 70°C (158°F). Flammable Limits: LOWER: 1.3% UPPER: 23%. Products of Combustion: These products are carbon oxides (CO, CO2), nitrogen oxides (NO, NO2...). Fire Hazards in Presence of Various Substances: Flammable in presence of open flames and sparks, of heat. Non-flammable in presence of shocks. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available.
Precautions: Keep locked up. Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, metals, acids, alkalis. Storage: Air and light sensitive. Store in light-resistance container. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Acetic Acid 3530 mg/kg [Rat.].
Flammability of the Product: Flammable. Auto-Ignition Temperature: 463°C (865.4°F) Flash Points: CLOSED CUP: 39°C (102.2°F). OPEN CUP: 43°C (109.4°F). Flammable Limits: LOWER: 4% UPPER: 19.9% Products of Combustion: These products are carbon oxides (CO, CO2) Fire Hazards in Presence of Various Substances: Flammable in presence of open flames and sparks, of heat. Slightly flammable to flammable in presence of oxidizing materials, of metals. Explosion Hazards in Presence of Various Substances: Risks of explosion of the
Precautions: \Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Never add water to this product. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, metals, acids, alkalis. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid
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. product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available. Slightly explosive in presence of oxidizing materials.
all possible sources of ignition (spark or flame).
Alpha Naphthylamine
Not available
Flammability of the Product: May be combustible at high temperature. Auto-Ignition Temperature: Not available. Flash Points: CLOSED CUP: 112°C (233.6°F). Flammable Limits: Not available Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Slightly flammable to flammable in presence of heat. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Risks of explosion of the product in presence of static discharge: Not available.
Precautions: Keep away from heat. Keep away from sources of ignition. Empty containers pose a fire risk, evaporate the residue under a fume hood. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable p. 3 protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, moisture. Storage: MOISTURE SENSITIVE. Keep container tightly closed. Keep container in a cool, well-ventilated area. Do not store above 23°C (73.4°F).
Methyl Alcohol 5628 mg/kg [Rat.].
Flammability of the Product: Flammable Auto-Ignition Temperature: 464°C (867.2°F) Flash Points: CLOSED CUP: 12°C (53.6°F). OPEN CUP: 16°C (60.8°F). Flammable Limits: LOWER: 6% UPPER: 36.5% Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Highly flammable in presence of open flames and sparks, of heat. Non-flammable in presence of shocks.
Precautions: Keep locked up. Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. Wear suitable protective clothing. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, metals, acids. Storage: Store in a segregated and
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. Explosion Hazards in Presence of Various Substances: Risks of explosion of the product in presence of mechanical impact: Not available. Explosive in presence of open flames and sparks, of heat.
approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
Formaldehyde 100 mg/kg [Rat].
Flammability of the Product: Flammable. Auto-Ignition Temperature: 430°C (806°F) Flash Points: CLOSED CUP: 50°C (122°F). OPEN CUP: 60°C (140°F). Flammable Limits: The greatest known range is LOWER: 6% UPPER: 36.5% (Methyl alcohol) Products of Combustion: These products are carbon oxides (CO, CO2). Fire Hazards in Presence of Various Substances: Flammable in presence of open flames and sparks, of heat. Non-flammable in presence of shocks, of oxidizing materials, of reducing materials, of combustible materials, of organic materials, of metals, of acids, of alkalis. Explosion Hazards in Presence of Various Substances: Non-explosive in presence of open flames and sparks, of shocks. Fire Fighting Media and Instructions: Flammable liquid, soluble or dispersed in water. SMALL FIRE: Use DRY chemical powder. LARGE FIRE: Use alcohol foam, water spray or fog. Cool containing vessels with water jet in order to prevent pressure build-up, auto ignition or explosion.
Precautions: Keep away from heat. Keep away from sources of ignition. Ground all equipment containing material. Do not ingest. Do not breathe gas/fumes/ vapor/spray. In case of insufficient ventilation, wear suitable respiratory equipment. If ingested, seek medical advice immediately and show the container or the label. Avoid contact with skin and eyes. Keep away from incompatibles such as oxidizing agents, reducing agents, acids, alkalis, moisture. Storage: Store in a segregated and approved area. Keep container in a cool, well-ventilated area. Keep container tightly closed and sealed until ready for use. Avoid all possible sources of ignition (spark or flame).
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
• Annual inspections • Safety interlocks to be provided • Safety and pressure gauge valves fitted • Properly supported and protected against
corrosion • Testing of jackets and joints of tubes
regularly.
Reactor Vessel
Chloro Sulfonic
Acid, Hydrochlori
c Acid. Sulphuric
Acid, Ammonia,
Acetic Anhydride,
Oleum & other solvents
• Exothermic Reaction.
• Raw Materials quantity must be controlled either volumetrically or gravimetrically.
• Process control devices must be installed includes the use of sensors, alarms, trips and other control systems that either take automatic action or allow for manual intervention to prevent the conditions for uncontrolled reaction occurring
• High Temperature indicator valve and alarm system must be provided
• Auto cutoff system must be provided after reaching of predetermined maximum safe temperature.
• Pressure gauge is must provided. • Safety Control valve is must be provided. • The Vessel Emergency Relief vent should
discharge to a suitably designed catch pot or should be so positioned that people working in the area and members of the public will not be in danger if the contents of the vessel are discharged.
• Use skilled worker • Proper selection of MOC • Mechanical seal in all pumps and reactors • Transportation of finished product from
vessel to storage tank through General Hazards & controls:
Type of Emergency
Identification of area
Possible Causes
Possible Result
Preventive/control Measures
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The Table No. 10.6 table gives the expenditure to be incurred by M/s. BHIMANI DYECHEM Industries On environmental matters.
Table No.10.6
Expenditure on Environmental Matters
Sr. No
System Approximate recurring cost per annum (in Lac)
Approximate capital cost (Rs. In Lac)
Basis for cost estimates
1 Air pollution control
12.0 45.0 The capital cost would include cost of providing adequate height of the stack, ladder and platform, Air Pollution Control Systems and recurring cost would include cost of monitoring of air environment.
2 Water pollution control
335 40.0 Capital cost would include cost of ETP, Evaporation cost of Spray Drying etc. In capital cost civil work, mechanical work, Electrical work and piping work is included. Recurring cost is for operational phase.
3 Noise pollution monitoring
0.25 0.0 The recurring cost would include cost of noise monitoring.
4 Solid and hazardous waste management
15.0 12.0 Capital cost would include cost of providing storage space for hazardous waste and membership of TSDF Fee. Recurring cost would include cost of land filling and transportation.
5 Environment monitoring and management
2.0 0.0 The recurring cost would be incurred on hiring of consultants and payment of various statutory fees to regulatory agencies.
6 Green belt 0.8 1.5 Development of Greenbelt including Gardening and Plantation.
7 Occupational health (OHC)
0.8 1.0 Occupational health check up of Employees and workers
8 CSR 2.25 0 2.5 % of the project cost. Recurring cost will include cost allocated for the CSR activity like Educational, Drinking facility, Infrastructure facility, Green belt development, Tribal development,
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Cleanup spills and leaks off’s any type quickly and properly.
Follow up preventive predictive maintenance.
ENERGY CONSERVATION: Energy Conservation and Energy Efficiency are separate, but related concepts. Energy conservation is achieved when growth of energy consumption is reduced, measured in physical terms. Energy Conservation can, therefore, be the result of several processes or developments, such as productivity increase or technological progress. On the other hand Energy efficiency is achieved when energy intensity in a specific product, process or area of production or consumption is reduced without affecting output, consumption or comfort levels. Promotion of energy efficiency will contribute to energy conservation and is therefore an integral part of energy conservation promotional policies. Energy efficiency is often viewed as a resource option like coal, oil or natural gas. It provides additional economic value by preserving the resource base and reducing pollution. For example, replacing traditional light bulbs with Compact Fluorescent Lamps (CFLs) means you will use only 1/4th of the energy to light a room. Pollution levels also reduce by the same amount nature sets some basic limits on how efficiently energy can be used, but in most cases our products and manufacturing processes are still a long way from operating at this theoretical limit. Very simply, energy efficiency means using less energy to perform the same function. Inadequate control of steam supply wastes energy. So, we will investigate the
possibility of installing automatic controls. Monitoring drying operations enables energy consumption to be assessed and
possibly reduced. Monitor parameters by us Heat losses from dryers by radiation and convection will be minimized. And we will
improve the insulation of dryers to save energy costs.
Routine cleaning and maintenance programme for the combustion system will improve efficiency and reduce energy costs.
Investigate the possibility of changing any upstream processes in order to decrease
the water content before drying operations. Relatively minor modifications of upstream operating procedures may significantly reduce energy costs.
We will check, if it is possible to use heat recovered from the dryer exhausts in the drying process.
Waste Heat Recovery System Understanding the process is essential for development of Waste Heat Recovery system. This can be accomplished by reviewing the process flow sheets, layout diagrams, piping
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Final Environment Impact Assessment of Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At
. isometrics, electrical and instrumentation cable ducting etc. Detail review of these documents will help us in identifying: a) Sources and uses of waste heat b) Upset conditions occurring in the plant due to heat recovery c) Availability of space d) Any other constraint, such as dew point occurring in an equipments etc. After identifying source of waste heat and the possible use of it, our next step is to select suitable heat recovery system and equipments to recover and utilize the same. Economic Evaluation of Waste Heat Recovery System It is necessary to evaluate the selected waste heat recovery system for our unit on the basis of financial analysis such as investment, depreciation, payback period, rate of return etc. In addition the advice of experienced consultants and suppliers must be obtained for rational decision. Natural Resources Conservation: Renewable energy is energy obtained from sources that are essentially inexhaustible. Examples of renewable resources include wind power, solar power, geothermal energy, tidal power and hydroelectric power. The most important feature of renewable energy is that it can be harnessed without the release of harmful pollutants. Non-renewable energy is the conventional fossil fuels such as coal, oil and gas, which are likely to deplete with time. 10.13 CHECKLIST IN THE FORM OF DO’S AND DON’T.
The checklist in the form of Do’s and don’t of preventive maintenance, strengthening of HSE, manufacturing utility staff for safety related measures are as follows. DO’S
1) Check the raw material availability as per the job on hand required for all stages.
2) Check the vessels expected to be used in the process for good physical condition.
3) Check the availability of utilities required till the end of the batch / job.
4) Check for proper manpower available till the entire operation in over.
5) All equipments including the stand-by should be in operable condition.
6) Verify the test certificates of materials being taken for process.
7) Prepare time schedule of material flow on basis of the process.
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. 30) Don’t ever even thinking of evading safety instructions.
10.14 SOCIO ECONOMIC DEVELOPMENT ACTIVITY:
Unit has done various kinds of socio economic development activities including community welfare programme. At present unit is doing following socio Economic Development Activities.
1. They are interested to donate in schools, hospitals and where ever actual needed. 2. They are ready to provide the needful services required for the nearest villages.
Socio-Economic Development activities will be implementing in coordination with the
NGOs, Village Panchayat, and other Governmental Entities.
A. Social Activities:
• Health check up camps and Medical facilities to Infants and senior citizens,
free medicine supply etc., will be provide on regular basis.
• Help Implement and Run a Safe Drinking Water in Rajpur village where the
project site is located to facilitate Healthy Water for both Drinking & Cooking
Purposes.
• Contribution towards any development activity useful for village development.
B. Economic Activities:
• The company will give preference to the local people for employment.
• The company will be giving contract works like civil, machine repair,
transportation, canteen, etc. to the local people / parties.
• The proposed project will create jobs for at least 20 persons. 10.15 INFRASTRUCTURE FACILITIES TO THE LABOURS DURING
CONSTRUCITON PHASE:
During the construction period, there will be increase in floating population. The project will provide temporary employment of skilled and highly skilled manpower. Most of the people will be employees of contractors/sub-contractors. Additional strain on civic amenities like road, transport, communication, drinking water, sanitation and other facilities will take place, to meet the work force requirement. During the construction phase there will be increased demand of services, as most of the employees deployed during the construction period will be from local area. These include
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. hotels, lodges, public transport (including taxis), etc. There will also be ample opportunities for providing these services. In addition to the opportunity of getting employment as construction laborers, the local population would also have employment opportunities in related service activities like petty commercial establishments, small contracts/sub-contracts and supply of construction materials for buildings and ancillary infrastructures etc. Consequently, this may lead to economic up liftman of the area. The movement of work force to and from the place of work and the movement of vehicles carrying equipment and construction material is expected to increase the stress on the local transport and road network. However, considering the number of people deployed, the impact on road/traffic is marginal and temporary. Consumer Prices: Usually the local population will be affected by inflationary trend sometime later, when prices of local services and produce, egg, fish, vegetables, milk, etc. start rising. This will happen only when a sizeable staff of the project and other associate companies settle permanently in the area. However any such rise in consumer prices is anticipated because the influx of population due to the project activities is minimal. Transport and Civil Construction: The transport companies would benefit from the construction of the plant. Services: The services like retail shops, banks, and automobile workshops; health care, etc. will expand in and near the plant. Employment: Large-scale influx of material and money tend to increase the employment opportunities. Transport: Transport services on the connecting road will improve further. Traffic: The plant construction phase will also see a moderate increase in traffic. Development of Slums: The contractors have to necessarily provide basic amenities like water supply, sanitation, electricity etc. at the labor camp to maintain hygienic condition and aesthetics.
10.16 ODOUR CONTROL MEASURES
The chance of odours within premises is mainly due to
Raw materials
• Storage / Handling • Transportation of raw materials
Process
• Raw materials transportation • During reaction • Drying
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• Industry will provide adequate and proper storage facilities for all the raw materials and finished products.
• Corrosive substances will be stored away from the moisture. • Solid raw material will be stored in covered area and Liquid raw
material will be stored in closed Horizontal / Vertical tanks. • Hazardous chemicals and solid wastes will be stored away from other
plant activities. Handling
• All the raw materials and finished products will be handled as per the standard practice.
• For proper handling, company will adopt good housekeeping technology to entire shed.
• To avoid any leakage or spillage of chemicals from all storage tanks, third party will inspects transfer lines, valves, fittings and every joint periodically.
Transportation of Raw materials
• All the necessary precautions will be taken while carrying out transport of the above materials as per the Hazardous Rules of transportation.
• The vehicles for transportation of raw materials and products will be parked at specified loading facilities where there will be a provision of fire extinguishers.
• The finished product will be transported by road, rail and ship route in closed containers.
Other sources of odour nuisance are as follows
• Leaks from pressurized process equipment generally occur
through valves, pipe connection, mechanical seals or related
equipment.
Control measures
• To minimize & control leaks at process facilities operators carry out
regular leak detection test and repair activities.
• Routine inspections of process equipment with gas detectors can be
used to identify leaks & estimate the leak rate in order to decide an
appropriate corrective action.
• Proper routine maintenance of equipment reduces the likelihood of
leaks.
• Solvents will be transferred through the closed pipe line system.
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The environmental impacts of projects or actions generally encompass a broad range of impact from Air and Noise pollution to affect on employment and neighborhood as well as on social structure. All of these impacts vary in magnitude as well as in their beneficial or adverse classification. As a result, a natural question arises as to what is the “collective” or “overall” environmental impact of the project or action taken. Is the project beneficial or is it adverse? To answer such a question requires a comparison of these impacts and to some extent subjective evaluation of those impacts which are more important than others. M/s. BHIMANI DYECHEM INDSUTRIES proposed to manufacture synthetic organic chemical (Dyes & Dyes Intermediate) manufacturing unit for 225 MT/M.
11.1 SALIENT FEATURES OF THE PROJECT S. No Contents Details
Details of Applicant Mr. Jigneshbhai Jayeshbhai Bhimani
(Partner)
3
Status
M/s. BHIMANI DYECHEM INDUSTRIES Proposed to manufacture Synthetic Organic Chemical (Dyes & Dyes Intermediate) manufacturing unit for 225 MT/M. at Survey No. 316, Plot No.: 02, Opp. Dharti Industrial Estate, At: Dhanot, Tal: Kalol, Dist: Gandhinagar, For that they have applied for obtaining Environment Clearance from MoEF&CC, New Delhi.
4
Type of Land & Status Non Agriculture (Industrial) land. Proposed Land – 3344 Sq.m).
5 Capital Investment of the Project, Rs. in Crore
4.50 Crore
6 Capital cost for EMP, Rs. in Lac
99.5 lac
7 Recurring cost for EMP, Rs. in Lac
369.5 lac
8 Employment opportunity 40 persons
9
Green belt Development
It is envisaged to develop greenbelt on all sides of the industry in an area of about 1105 SQM). – 33 % of the total plot area
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Final Environment Impact Assessment of
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Pollution control measures adopted Effluent water disposal
• Domestic Wastewater is 5 KL/day will be disposed off through Soak Pit/Septic Tank System.
• Industrial Effluent of 44.5 KL/day will be sent to ETP for primary treatment and then it will be sent to Chhatral Environment Management System Pvt. Ltd. So, our unit will achieve Zero Discharge.
Flue gas emission control
• Adequate stack height of 30 Mtrs will be
provided to the 3 TPH boiler and HAG.
Stack monitoring facilities for the periodic monitoring of the stack to verify the compliance of the stipulated norms. Apart from this Cyclone Separator, Bag filters will be provided to the boiler and HAG
Process gas emission control
Two stage water scrubbers installed for process gas emissions i.e. HCl and NH3 &SO2.
Fugitive emission control
Vent condensers to the storage tanks and reactors
Solvents and chemicals are handling in closed system
Hazardous waste management
All the hazardous waste will be collected, stored, handled, transported and disposed as per the Hazardous Waste (Management, Handling and Transboundary Movement) Rules, 2016, amended time to time etc are major Act/rules/notification applicable to industry.
11
Expenditure for CSR & CER activities
11.25 Lac & 9 Lac
Environment Impact Assessment as detailed in previous chapter can now be concise to impact statement given below.
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Final Environment Impact Assessment of
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11.2 AIR ENVIRONMENT Meteorological data collected during the study period March – April – May 2018 confirms that climatic Status of the study area is consistent with the regional meteorology. Average concentration of ambient air quality parameters such as PM10, PM 2.5, SO2, NOx, NH3, HCl in the surrounding study area are well within the permissible limits as prescribed in the National Ambient Air Quality (NAAQ) Standards for respective residential rural areas and industrial areas. Evaluated GLCs due to the proposed air pollution load. When added to the monitored existing ambient air quality, provides the expected ambient air quality when the fuel qty will increase in proposed utility and the same indicates that expected AAQ are well within the permissible limit of National Ambient Air Quality Standards for residential rural areas as well as industrial areas. It is concluded from the above that there will be a minor impact on the AAQ of the surrounding environment due to operation of the proposed project.
11.3 WATER ENVIRONMENT
M/s. BHIMANI DYECHEM INDUSTRIES is a proposed unit and the source of water for proposed activity will be by water tanker. The quality of the water was tested at eight locations in the study area. The ground water norms were compared to IS: 10500 (1991) for evaluation. The Industry generates process effluent apart from process, washing, Cooling Tower blow down and domestic effluent.
Wastewater Generation & Disposal:
• Domestic Wastewater @ 5.0 KL/day will be disposed off through Soak Pit / Septic Tank System.
• Industrial Effluent generation @ 44.5 KL/day will be sent to ETP for Primary treatment and then it will be sent to Chhatral Environment Management System Pvt. Ltd. For Spray drying.
• So, unit will achieve Zero Discharge.
11.4 NOISE ENVIRONMENT
Base line data indicates that noise levels in the study area are not on higher sides. Noise level in and around plant site were measured. Measured noise levels within premises indicate that overall noise levels are within the Damage Risk Criteria. The company will provide ear-protecting devices/ earplugs for
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Final Environment Impact Assessment of
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working personnel exposed to high noise level. It can be concluded that there will be no impact on the noise level of the surrounding environment.
11.5 HAZARDOUS WASTES
As per the Hazardous Waste (Management & Handling) Amendment Rules, 2003, all necessary control steps for each type of Hazardous Wastes generated from the proposed project will be taken. Therefore, no impact of hazardous wastes generation on surrounding soil environment is anticipated.
11.6 ECOLOGY
The proposed project will be carried out on land within their premises without cutting of any trees. Also, the project site is located in non-agricultural land devoid of any permanent eco-system. So it does not alter the crop pattern and natural vegetation of the surrounding area. Due to the safe control technology of air pollutants, liquid effluents and solid/hazardous wastes disposal, no impact on the surrounding ecology is anticipated.
11.7 SOCIO - ECONOMIC ENVIRONMENT
The proposed project will generate direct employment for employment persons. The indirect employment will be generated by way of transportation, shopkeepers and other casual employment. Implementation of this plant will also reduce production loss due to shortage of power. Thus, the proposed project will have significant positive impacts on the employment pattern of the study area.
11.8 LAND USE
Source emission, wastewater and hazardous waste generation from any project activity affects the soil environment. The impact due to air causes direct/indirect effect on soil. The emissions of SPM during operation will be effectively controlled. There will be practically no effect on the soil quality due to air emissions. Domestic effluent will be discharged to soak pit and septic tank system. Wastewater generated from the Industrial activity will be treated in Effluent Treatment Plant and finally it will be send to Chhatral Environment Management System Pvt. Ltd and ETP waste will be disposed to TSDF site. As per the Hazardous Waste (Management & Handling) Amendment Rules, 2003, all necessary control steps for each type of Hazardous Wastes generated will be taken for the proposed project. Hence, due to the proposed project the, land use pattern; land cover and topography of the area will be changed only for the project premises.
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Final Environment Impact Assessment of
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It is a proposed project, does involve changes in topography and project activities include excavation of soil in the plant area and construction of buildings and facilities limited to the project site area. During construction, excavated soil will be restored to its original shape. Thus the impact during the construction is reversible, for short term and insignificant. During the operation phase of the project, no impact is envisaged on the topography. There will be a change in topography of the land in the project site, but there will be no change in drainage pattern.
11.10 CONCLUSION It can be concluded on a positive note that due to the adequate provision and
efficient operation of Environmental Management Systems and after the
implementation of the proposed mitigation measures and environmental
management plans, the project activities during the construction and operation
phase would have manageable & largely have reversible impacts on the
environment, and on balance the project would be beneficial to surrounding
communities and the region.
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Final Environment Impact Assessment of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2, Survey No. 316, Opp. Dharti Industrial Estate,
CHAPTER 12 DISCLOSURE OF CONSULTANT Bhagwati Enviro care Pvt. Ltd. is one of the leading environmental consulting organizations based at Ahmedabad, Gujarat. engaged in providing consulting, engineering, designing, auditing, monitoring & testing and other regulatory compliance services. It was established in January 98 and consists of the highly qualified and well-experienced engineers, scientists, chemists. This technical team is supported by a pool of highly qualified and experienced associated experts from various disciplines. We have successfully completed more than 1500 projects in the field of consulting, auditing, monitoring & testing, pollution control i.e. Design, Installation and commissioning of wastewater treatment plants and air pollution control equipments, during last 20 years. We are also dealing in the projects of waste minimization and cleaner production technology. We are having a strong team of Technocrats and Scientists. We have well equipped MOEF and NABL approved analytical laboratory facility including facilities to analyze physical, chemical and biological parameters as per the requirements of the State Pollution Control Board and our clients. Our team of technocrats and scientists are well experienced to deal with the Design, Installation and Commissioning of wastewater treatment plants and air pollution control equipments and also well conversant to the projects of Waste Minimization and Cleaner Production Technology. The organization has obtained below mentioned recognition and accreditations to
provide you competent and efficient services.
• QCI-NABET accreditation as an EIA Consultant Organization
• QCI-NABL accreditation for Chemical Testing Laboratory under ISO/IEC 17025:2005 standards
• Reorganization as Environmental Auditor by Gujarat Pollution Control
Board.
• ISO 9001:2008 certificate for the Management System. • ISO 14001:2015 certificate for the Management System. • ISO 18001:2007certificate for the Management System. • MOEF Recognized Environmental laboratory under the Environment Protection Act
1986.
The organization has been engaged in carrying out EIA studies and preparation of
EIA/EMP report for the varied range of industries and developmental activity since
Prepared By M/s. Bhagwati Enviro Care Pvt Ltd.
481
Final Environment Impact Assessment of
Proposed Manufacturing unit by M/s. BHIMANI DYECHEM INDUSTRIES At Plot no.2, Survey No. 316, Opp. Dharti Industrial Estate,
2003. Besides the EIA study the organization is prepared and confident to render the
following services in the field of environmental engineering,
• Technical consultation & assistance to ensure & assure complete Environ-Legal compliance including liaison with statutory bodies in order to get the
required permits, clearances & consents.
• Assessment of Environmental Pollution Load.
• Guidance to get water consent, Air consent and Solid Waste Authorization.
• O & M contracts for ETP, STP and CETP. • New project consultancy for Environmental Management System. • After careful study of the existing effluent treatment plant if required we suggest
suitable addition/up gradation/modification in existing Effluent Treatment Plant so as to meet with the standards as specified by the state pollution control board as per the mode of disposal.
• Preparation of application form to get NOC for Establishment of the unit and
Consent for Operation from the state pollution control board Providing technical guidance to the clients to do the technical correspondence and also consulting work with state pollution control board.
• Designing and executing turnkey project of Effluent Treatment Plant (ETP), Solid & Liquid Waste Incinerator and Air Pollution Control Equipment
• Schedule II Environmental Audit as per the order and guidelines of Honorable High Court of Gujarat and GPCB.
• Details Process study to reduce the pollution at source and to reuse / recycle effluent.
• Preparing adequacy and efficacy report on Environmental management System for the existing unit as well as proposed unit.
• Conducting laboratory scale experiments to study treatability of industrial effluent and preparing Treatability report.
• Preparing Feasibility report on the Effluent Treatment Plant. • Performance study of existing pollution control facility and suggesting scheme
for the optimization of the facility.
• Monitoring and analysis of Water, Wastewater, Air Pollution (Stack & Ambient), Solid Waste and soil.
• Monitoring and analysis of Work Area Environment and filling-up Form-37 as per the requirements under Factory Act-1948 and Gujarat Factory Rules.
• Services of chartered Engineers for chemical projects.
