Unilex Colours And Chemicals...

Unilex Colours And Chemicals Ltd. Nov. ‐2017

1. Executive Summary

Name of the Project Proponent : Mr. Mathew Kavalam

PPrree -- ffeeaassiibbiilliittyy RReeppoorrtt

FFoorr

Unilex Colours And Chemicals

Ltd.

PPlloott NNoo.. EE--1100//22,, MMIIDDCC TTaarraappuurr,, TTaall.. && DDiisstt.. PPaallgghhaarr,, PPiinn -- 440011550066..

Consultant:

M/s. SADEKAR ENVIRO ENGINEERS PVT. LTD.

Accredited by QCI – NABET

Lab. Recognized by MoEF, Govt. of India NABL Accredited Certificate No. T- 2190,

Certified by ISO 9001:2008 Certified by BS OHSAS 18001:2007

Plot No. A-95, Road No. 16, Wagle Estate MIDC Area,

Palghar (W) - 400604 Telephone : 022 -2583321/22/23/24

Email : [email protected] / [email protected]

Web site:- www.sadekarenviro.com November, 2017


Sadekar Enviro Engineers Pvt. Ltd. Page 2

Summary of the project

Salient Features of Project Name & Address of Company

M/s Unilex Colours And Chemicals Ltd. Plot No. E-10/2, MIDC Tarapur, Tal. & Dist. Palghar, Pin - 401506.

Schedule of project as per EIA Notification, 2006

5(f)

Category of Project 'B1' Total Plot Area

Particulars Existing (M2)

Proposed (M2)

Total (M2)

Total Plot area 1275.00 -- 1275.00 Built-Up area 949.91 -- 949.91 Parking area -- 153.00 153.00

Green belt area (adjacent to the factory premises)

-- 3037.00 3037.00

Production details Existing: 24.80 MT/M Proposed: 1) Manufacturing products: 100 MT/M 2) Blending products: 40.0 MT/M Total: 164.8 MT/M

Water Requirement of Project

Existing water requirement : 20.5CMD Proposed water requirement: 72.87 CMD Total water requirement (after expansion): 93.37CMD

Effluent generation Total quantity of effluent to be generated after expansion: 23.57 CMD Total quantity of effluent to be recycled after expansion: 13.37 Total quantity of effluent to be sent to CETP after expansion: 10.2 CMD Total quantity of water to be recycled after expansion: 60.13 CMD

Hazardous waste generation

Sr. No.

Hazardous Solid Waste

Total quantity (Existing)

Total quantity (Proposed)

Total Disposal

1 ETP sludge 2.8 11.2 kg/A

14.0 kg/A

Mumbai Waste Management Ltd. - CHWTSDF at Taloja

2 Mechanical Evaporator Residue

-- 133.7 kg/day

133.7 kg/day



3 Empty bags

0.5 nos./M

2.0 nos./M

2.5 nos./M

Sold to authorized recycler

4 Empty drums

5 nos./M

20 nos./M

25 nos./M

5 Empty carboys

7 nos./M

28 nos./M

35 nos./M

Effluent treatment The sewage generation will be 2.0 CMD and effluent form industrial activity will be 23.57 CMD. 13.37 CMD effluent from manufacturing process will be subjected mechanical evaporator from which 0.1337 m3/day residue will be generated which will be sent to CHWTSDF & condensate water will be 13.2363 CMD which will be reused 2.0 CMD sewage will be subjected to soak pit and the 10.2 CMD effluent generated as cooling tower & boiler blow down, scrubber & reaction washing water will be treated in existing ETP of 20 CMD capacity comprising of primary treatment scheme & will be further discharged to TIMA CETP as per the valid MPCB Consent No: Format 1.0/BO/AS(T)/TN-5855-15/E/GEN- 14705 dt. 24.11.2015 hence except the consented quantity of treated effluent there will be no additional effluent load on the CETP thereby the proposed expansion activity will be a Zero Liquid Discharge project.

ETP Details LCOD/LTDS effluent: 10.2 CMD effluent will be treated in ETP of 20 CMD capacity comprising of Primary treatment scheme which will be further sent to CETP. LCOD/HTDS effluent: 13.37 CMD effluent will be subjected to Mechanical Evaporator from which 0.1337 m3/day residue will be generated which will be sent to CHWTSDF & condensate water will be 13.2363 CMD which will be reused

Power Requirement Existing connected load: 379 KW, Existing maximum demand: 297 kVA Proposed connected load: 77KW, Proposed additional demand: 108 kVA Total connected load (after expansion): 456 kVA, Total demand after expansion: 405 kVA Source: MSEDCL

Boiler Details Existing: 1 x 0.6 TPH steam boiler - Existing boiler will be sale out after expansion Proposed: 1x 850 kg/hr. steam boiler

Thermic Fluid Heater Existing: 1 X 2.0 lakh kilo calorie./hr. - Existing thermic fluid heater will be sale out after exapnsion Proposed: 1 X 4.0 lakh kilo calorie/hr. thermic fluid heater

Fuel requirement Existing:



Indonesian Coal: 1507.5 kg/day Total fuel requirement after expansion: Indonesian Coal: 3508.9 kg/day

Stack details Stack No. 1 : 30.0 m stack for proposed steam boiler Stack No. 2 : 30.0 m stack for proposed thermic fluid heater Stack No.3: 4.0 m (above roof level) for proposed HCl. Scrubber

Scrubber 1 No. Hcl.scrubber Man power Existing : Skilled - 5, Unskilled - 15 Total: 20

Proposed (total after expansion) : Skilled - 34 , Unskilled - 15 Total: 49

EMP cost Capital: 48.59 lakhs, Recurring: 3.84 lakhs Project Cost 2.0 Crore

Pollution Load and Mitigation Measures

The industry takes the necessary precaution to protect the environment by implementing

efficient pollution control equipments like scrubbers to control air emissions from process

& adequate stack height for boilers & DG sets as well as full-fledged ETP for treatment of

waste water. Company is having memberships of Mumbai Waste Management Ltd. -

CHWTSDF at Taloja for disposal of hazardous waste and TIMA CETP for discharge of

treated effluent. The production process equipments are so efficient and modern as such the

waste generation is very minimal.

A. Quantum of Waste Water Generated : 23.57 CMD

Existing quantity of effluent : 13.37 CMD

Total quantity of effluent (after expansion) : 23.57 CMD

Quantity of effluent to be recycled : 13.37 CMD

Quantity of effluent to be sent to CETP : 10.2 CMD

Effluent Treatment Plant

Company is having existing ETP of 20 CMD capacity comprising of primary treatment scheme in wake of proposed expansion the ETP treatment scheme will be upgraded by installing Mechanical Evaporator of 15 KL capacity.

Characteristics of effluent



Sr. No.

Parameter

Concentration

MPCB Limit

Before Treatment

After Treatment

1. pH 6.75 7.05 6-8.8

2. Oil & Grease 4.0 BDL <10

3. Total Dissolved Solids 1987.00 1901.00 <2100.00

4. COD 600.00 130.00 <250

5. BOD (3 days at 270C) 194.00 39.00 <100.00

Note: All the parameters are expressed in mg/l except pH.

B. Quantum of Waste Generated:

1. Non Hazardous waste:

Wastes such as papers/office waste from administrative buildings, metal wastes/scraps from

industrial operations.

Disposal: Papers/office waste will be disposed through local municipal waste disposal system

and metal wastes/scraps from industrial operations will be sold to recyclers.

2. Hazardous waste

Sr. No.


Total quantity (Existing)

Total quantity (Proposed)

Total Disposal


14.0 kg/A



-- 133.7 kg/day

133.7 kg/day

3 Empty bags 0.5 nos./M

2.0 nos./M

2.5 nos./M


4 Empty drums 5 nos./M

20 nos./M

25 nos./M

5 Empty carboys 7 nos./M

28 nos./M

35 nos./M

Waste Disposal:



The hazardous waste will be sent to Mumbai Waste Management - CHWTSDF at Taloja for disposal.

Air Emission Control

Sr. No

Item Utilities Existing / Proposed to be installed

1. Air Stack attached to various utilities with sufficient height

Scrubbers

Utilities Existing Proposed BoilerCapacity 1) 1 x 0.6 TPH

steam boiler 2) 1x 2 lakh kilocal./hr. - Thermic fluid heater Note: Existing steam boiler & thermic fluid heater will be sale out after expansion

1) 1x 850 kg/hr. steam boiler 2) 1x 4 lakh kilocal./hr. - Thermicfluid heater

Fuel Indonesian coal:

1507.5 kg/day Indonesian coal: 3508.9 kg/day (total fuel requirement after exapnsion)

Source of fuel

Local vendor - Gurukrupa Enterprises, Surat

Local vendor - Gurukrupa Enterprises, Surat

Stack height

Steam Boiler: Stack of 20.0 m & Multi cyclone separator followed by scrubber Thermic fluid heater: Stack of 20.0 m & Multi cyclone separator

Steam boiler: Stack of 20.0 m height & Multi cyclone separator followed by Bag filter Thermic fluid heater: Stack of 30.0 m height & Multi cyclone separator followed by Bag filter

Plant Section & Units

Height form ground level

Existing/Proposed

Process



Scrubbers: 1. HCl. Scrubber

4.0 m (above roof level)

Proposed

2. Introduction of the project/Background information

i) Identification of Project & Project Proponent

Identification of Project:

The project is for enhanced production capacity of dyes from existing 24.80 MT/M to 124.80

MT/M with addition of blending products to the tune of 40.0 MT/M.

Project Proponent:

Unilex Colours & Chemicals Ltd. An ISO 9001:2008 Certified Company is a leading

manufacturer of dyes & pigments based in India with a manufacturing range of Pigments,

Pigment preparations, Solvent Dyes and Food color.

Unilex Colours & Chemicals Ltd. has a team of highly qualified work force having vast

experience in various facets of chemical process development, process scale-up, chemical

technology & manufacturing expertise, well trained in all process & safety requirements.

Sigma Solvents provides cost effective solutions for customer’s diverse requirements.

Unilex Colours & Chemicals Ltd.’s infrastructure is designed to carry out many types of

processes in a safe manner.

Unilex Colours & Chemicals Ltd. has a successful track record in developing non-

infringing processes and scaling them up from laboratory to kilo scale to commercial scale

production. Unilex Colours & Chemicals Ltd.’s expertise enables to successfully manage

and develop a wide range of processes that conform to stringent quality and safety

guidelines.

Unilex Colours & Chemicals Ltd. quality assurance & quality control departments are

staffed with competent individuals.

Unilex Colours & Chemicals Ltd.’s long-term relationships with customers bear testimony

to our strict adherence to Intellectual Property. We leverage best practices and technology to

ensure confidentiality in our operations.

Unilex Colours & Chemicals Ltd. is committed to the health and safety of employees, the

welfare of community and environment protection. Sigma Solvents play’s a proactive role

in creating awareness, imparting training and minimizing pollution.

Sadekar EnPage 8

Figure 1: Go

Highlights o

The pr

product

The pr

expansi

plant lo

The exi

installa

The un

infrastr

ii) Brief des

iii) Employ

The current

man power

viro Engine

oogle Earth I

of the propo

roposed prod

ts is located

roject activit

ion. Since th

ocated at Plo

isting ETP o

ation of Mech

nit is locate

ructure for th

scription of

yment gener

man power

after expans

Unile

eers Pvt. Ltd

Imagery dep

osed projec

duction cap

in the Notif

ty will not

he proposed

ot No. E-10/2

of 20 CMD

hanical Evap

ed in Notif

he supply of

nature of p

ration (Direc

employed b

sion will be 4

ex Colou

.

picting Locati

MIDC In

t are:

pacity enhan

fied Tarapur

any involve

d expansion

2, no new lan

capacity wi

porator of 15

fied Tarapu

water, powe

project

ct & Indirec

by the industr

49 of which

urs And C

ion of Unilex

ndustrial Are

ncement proj

MIDC indu

e creation o

will be achi

nd is require

ith primary t

5.0 KL capa

ur MIDC in

er and transp

ct due to th

ry is 20 peop

skilled will

Chemica

x Colours An

ea

oject with ex

strial area.

of new infr

ieved within

ed.

treatment sc

city in view

ndustrial are

portation fac

e project)

ple (skilled 5

be 15 and un

als Ltd.

nd Chemicals

xisting and

astructure f

n the existin

heme will b

of the propo

ea which p

ility.

5 & unskille

nskilled will

Nov. ‐2017

s Ltd. at Tar

new (blend

for the prop

ng manufactu

be upgraded

osed expansi

provides a g

ed 15) & the

l be 34.

apur

ding)

posed

uring

with

ion.

good

total

Sadekar EnPage 9

Applicabili

The expansi

category ‘B

amendments

3. Project D

(i) Type of p

The propose

products no

(II) Locatio

layout with

Figure 2: G

viro Engine

ty for Envir

ion project o

B’, as per th

s till date.

Description

project inclu

ed expansion

interlinked

on (map show

co ordinates

Google Eart

Ta

Table 1: La

Unile

eers Pvt. Ltd

ronmental C

of Unilex Co

he “EIA No

uding interlin

n project is f

and interdep

wing genera

s).

th Imagery d

arapur MID

atitude & L

Bounda

ex Colou

.

Clearance:

olours And C

otification N

nked and inte

for enhanced

pendent proj

al location, s

depicting L

DC with bou

ongitude of

ary Corner1

2

3

urs And C

Chemicals L

No. S.O.153

erdependent

d production

ects are invo

specific loca

ocation of U

undary corn

f Boundary

Latitude &19°4872°4319°4872°4319°48

Chemica

Ltd. comes u

33 (E)” date

t projects, if

n of dyes with

olved.

tion and pro

Unilex Colou

ners of proje

Corners of

& Longitud8'0.58"N '52.93"E

8'2.54"N '53.04"E

8'2.48"N

als Ltd.

under the pro

ed 14th Sep

any.

h addition o

oject bounda

urs And Ch

ect plot

the project

e

Nov. ‐2017

oject activity

ptember 200

f new (blend

ary & project

hemicals Ltd

plot

y 5(f)

06 &

ding)

t site

d. at



72°43'54.03"E4 19°48'0.52"N

72°43'54.06"E

(iii) Details of alternate site considered and the basis of selecting the proposed site:

The proposed activity is a production capacity expansion of the existing unit located at Plot E-10/2.

The total plot area is 1275.00 sq. m. with built up area of 949.91 sq. m. whereas for the proposed

expansion no additional infrastructural developments are required hence the built up area will

remain. The production capacity enhancement will be achieved by replacing existing reactors with

reactors of high volume capacity now since there is no requirement of any new/ additional land

hence none alternative sites were considered for the proposed expansion project.

(IV) Size or Magnitude of Operation:

The project is for enhanced production capacity of dyes from existing 24.80 MT/M to 124.80

MT/M with addition of blending products to the tune of 40.0 MT/M. The detailed existing &

proposed product list along with quantities is attached as Annexure – I.

(v) Project description with process details: Process Description of Beta Blue Brief manufacturing process: IBA Process Crude CPC is ball milled to obtain activated CPC, which is further charged in reactor along with water, caustic, IBA, pH is adjusted to 10.5 to 11.0 after mixing IBA is recovered, then whole reaction mass is acidified with HCl & water pH is adjusted to 6.0 to 7.0 Reaction mass is filtered through filter press ML obtained is discharged to ETP & cake is rewashed with water and dried in SFD and packed in HDPE bags/drums.


Synthesis Scheme




Flow Chart & Material balance





Xylene Process Crude CPC is ball milled to obtain activated CPC, which is further charged in reactor along with water, caustic, gum rosin, xylene and additive, pH is adjusted to 10.5 to 11.0 after mixing xylene is recovered, then whole reaction mass is acidified with HCl & water pH is adjusted to 6.0 to 7.0 Reaction mass is filtered through filter press ML obtained is discharged to ETP & cake is rewashed with water and dried in SFD and packed in HDPE bags/drums.



Synthesis scheme





Flow char and material balance



(vi) Raw materials required The detailed raw material list is attached as Annexure – II.

Source of the Raw Material: Local

Marketing Area of the Finished Product: Local & Abroad

Mode of Transport of Raw material and Finished Products: By Road



(vii) Resource optimization/recycling and reused envisaged in the project, if, should be briefly outlined

The proposed project envisages resources optimization measures such as recycle & reuse of 60.13 CMD water after expansion.

(viii) Availability of water, its source, Energy/Power requirement

Existing water requirement: 20.5 CMD

Proposed water requirement: 72.87 CMD

Total water requirement: 93.37 CMD

Source: MIDC Power Requirement:

Existing connected load: 379 KW, Existing maximum demand: 297 kVA Proposed connected load: 77KW, Proposed additional demand: 108 kVA Total connected load (after expansion): 456 kVA, Total demand after expansion: 405 kVA Source: MSEDCL

(ix) Quantity of wastes to be generated (liquid & solid) Liquid (Effluent)

Total quantity of effluent to be generated after expansion: 23.57 CMD Total quantity of effluent to be recycled after expansion: 13.37

Total quantity of effluent to be sent to CETP after expansion: 10.2 CMD

Total quantity of water to be recycled after expansion: 60.13 CMD

Hazardous waste generation The hazardous waste generation details are as shown in the table below: Sr. No.


Total quantity

(Existing)

Total quantity

(Proposed)

Total Disposal


14.0 kg/A



-- 133.7 kg/day

133.7 kg/day

3 Empty bags 0.5 nos./M

2.0 nos./M

2.5 nos./M




4 Empty drums 5 nos./M

20 nos./M

25 nos./M

5 Empty carboys 7 nos./M

28 nos./M

35 nos./M

(x) Schematic Representation of the Feasibility Drawing of EIA

CLEAN ENVIRONMENT

PRODUCTION

ACTIVITY

RESOURCE CONSUMPTION (WATER)

POWER CONSUMPTION

WASTE GENERATION

FINISHED PRODUCTS

MARKET

ECONOMY

EMPLOYMENT

RAW MATERIAL

POLLUTION ABATEMENT



4. Site Analysis

(i) Connectivity: The project is located in Tarapur MIDC industrial area which is easily accessible

by Boisar Road which is connected to National Highway 8, the access to the project site is achieved

internal MIDC roads which are connected to Boisar Road.

Nearest Railway Station: Boisar Railway Station is approximately 3.15 km from the project

site. (Aerial distance)

Nearest Airport: Chatrapati Shivaji International (Mumbai) Airport, approximately at an

aerial distance of 79 km from the project site.

Location and Access

The industrial area is centrally located and easily accessible through all modes of transport.

Road: The entire industrial area is well connected by internal roads.

Available Road Network: Internal MIDC road (Nirlon Road) plies adjoining to the project

plot .

(ii) Land Form, Land use and Land Ownership: The Project location & the surrounding environs being located in the notified industrial area prevails industrial type of land use form.

(iii) Topography:

Since the topographic characteristics govern a greater land mass, the topography of entire district

has been taken into account as described under.

Palghar District forms a part of North Konkan Region which lies between the Sahyadri Hills in

the east and the Arabian Sea in the West. It has coastal line of about 113 km. It lies Between

18°42' and 20°20' North latitudes and 72°45' to 73°48' East longitudes in eastern part of the

state Its East-West spread is maximum at the South which is about 100 km. The North-south

length is approximately 140 km. The district is divided into three parts on the basis of its

topography.

The central portion having Sahyadri ranges and its slopes is mainly forest area

The Central Region covering mostly paddy fields and

Western part along the West coast, where horticulture, cultivation of high quality fodder



and vegetables are agricultural practices.

Hills

The Sahyadri ranges, having unbroken boundary run North South in the Eastern region of the

district. There are also spurs running laterally to the main ranges. The heights of the mountains are

maximum on the East and diminish gradually Westwards. The mountain ranges also spread

unevenly in the Central region of the district. But none of them rises higher than Sahyadris.

Rivers

The two main rivers, which join the sea on the West coast, are Vaitarna and Ulhas. The Vaitarna

river rises in the hills near Trimbak in the Nashik district and flowing Southwards takes a

Westwards turn entering Palghar district at Vihigaon in Shahapur tahsil. It is further passes across

northen boundry of Shahapur tahsil to enter Wada tahsil near Nishet village and then taking East-

West course through the middle of Wada tahsil. It enters Palghar tahsil near village Vasuri (Bk.)

and runs in North-West direction upto Manor, where-from it turns South-West and Southwards

upto village Navghar forming Vaitarns creek at the south of Palghar tahsil. The important

tributaries of Vaitarna are:-

Pinjal, which rises in the mountains in the South of Mokhada tahsil, joins it at Aleman

village in Wada tahsil

Daherja, which rises in the mountain in Jawhar tahsil, joins it at village Durvas in Palghar

tahsil

Surya, which rises in the mountains in Mokhada tahsil and taking south West and

southwards course joins it near Sakri village in Palghar tahsil.

Tansa which rises in the mountains in Shahapur Tahsil and joins it near Chirman Village in

Vasai Tahsil. The first three tributaries viz. Pinjal, Daherja and Surya join the Vaitarna from

the right and Tansa joins it from the left. The Ulhas River rises in the Bhoir pass and flows

North-West through Karjat Tahsil of Raigad District from creek at Vasai. Its important

tributaries in Palghar district are:

Bharvi which rises in the mountains in Murbad Tahsil and joins it at Apti village in

Ulhasnagar Tahsil and Bhatsa which rises in the mountains in Shahapur Tahsil and joins it

at Vadavali in Kalyan Tahsil. Kalu is an important tributary of Bhatsa River. It rises in the

mountains in Shahapur Tahsil and joins Bhatsa River near Sangoda in Kalyan Tahsil. Both



these tributaries viz. Barvi and Bhatsa join it from the right. The Vaitarna is navigable for

25 km. inside the coast and Ulhas is navigable for 40 km from Kalyan.

Soils

The soils of Palghar district can be conveniently divides into three categories.

Block Soil

Red soil in the eastern region mostly on the slopes

Brownish-black soil in the patches of the valleys mostly lying between the coastal plains

and the hilly slopes of Sahayadri.

The first type of soil, which is found in Dahanu, Palghar, Vasai and Palghar Tahsil, is fertile

and useful for horticulture, Paddy cultivation and vegetables. Whereas, the second type

which is found in Mokhada, Talasari and some parts of other tahsils on the Eastern slopes is

useful for growing coares millets like Nagli and Varai. The third type of soil found in

Bhiwandi, Kalyan and Shahapur tahsils is useful, particularly for Paddy cultivation.

(iv) Existing land use pattern

The proposed project is located in the notified industrial area which has been developed for

industrial development. The existing land use pattern in the 10 km radial distance of the project site

comprises of Industrial, human habitations/settlements, small agricultural/ crop lands land use

classes.

(v) Existing Infrastructure

Sr. No.

Description Status Existing Infrastructure

Proposed Infrastructure for

Expansion 1. Location Plot No. E-10/2, MIDC

Tarapur, Tal. & Dist. Palghar, Pin - 401506.

Proposed expansion activity will be carried out within the existing premises

2. Power demand

Existing connected load: 379 KW, Existing maximum demand: 297 kVA

Total connected load (after expansion): 456 KW, Total demand after expansion: 405 kVA

3. Water Requirement 20.5 CMD 72.87 CMD 4. ETP Capacity

20 CMD In wake of proposed expansion

Mechanical Evaporator of 15.0 KL capacity will be installed

5. Fuel Requirement Indonesian Coal: 1507.5 Indonesian Coal: 3508.9 kg/day



kg/day (Total after expansion) 6. Boiler Existing- 2 Nos.

Boiler No. 1: Steam boiler Capacity: 0.6 TPH Fuel used: Indonesian Coal Fuel Source: Local vendor - Gurukrupa Enterprises, Surat Boiler No. 2:Thermicfluid heater Capacity: 2.0 lakh kilo calorie/hr. Fuel used: Indonesian Coal Fuel Source: Local vendor - Gurukrupa Enterprises, Surat Combined fuel quantity: 1507.5 kg/day Note: Existing boiler & thermic fluid heater will be sale out after expansion Note: Existing boilers will be sold out

Proposed Boilers: 2 Nos. Boiler No. 1: Steam boiler Capacity: 850 kg/hr. Fuel used: Indonesian Coal Fuel source: Local vendor - Gurukrupa Enterprises, Surat Boiler No. 2: Thermicfluid heater Capacity: 4 lakh kilo calorie/hr. Fuel used: Indonesian Coal Fuel source: Local vendor - Gurukrupa Enterprises, Surat Combined fuel quantity: 3508.9 kg/day

The list of existing & proposed machinery & equipments - Annexure III

(vi) Soil Classification

The soils of Palghar District are broadly classified into Black Soil, Red Soil and Brownish-black

soil.

(vii) Climatic data

The climate of the district is distinctly different on the coastal plains and on the eastern slopes.

Being fully tropical, the climate on the coast, the coastal strip including Palghar, Vasai, Palghar and

Dahanu tahsils is very humid and warm. On the other hand, the climate on the eastern slopes and in

the plains at the foot of the slopes is comparatively less humid. However, variation in temperature

in the eastern region is more than that on the coastal strip. The maximum temperature lies between

28.0 to 35.2 0C and the minimum temperature lies between 16.3 to 26.5 0C.

Rainfall



The district gets assured rainfall of 2000 to 4000 mm from the South-West monsoons during the

months June to September. Generally highest rainfall is recorded in the month of July. It is

considerably more inland than on the coast. It is also less towards the North more inland than on

the coast. It is also less towards the North than towards the South.

(viii) Social Infrastructure

Hotels, Motels, sports ground, public ground, public garden, petrol pumps, school, hospital, roads,

railway station are available around the project location.

5. Planning Brief

Unilex Colours And Chemicals Ltd. is located in Notified Tarapur MIDC industrial area. The total

plot area is 1275.00 sq. m. Since this a production capacity enhancement project, existing plot &

infrastructures with modifications and realignment will be used. Additional power supply & water

requirement will be availed from MSEDCL & MIDC respectively. In the industry all necessary

safety and fire fighting equipments like Hydrant, Sprinkler, Detector System, Fire Extinguishers are

available in case of emergency.

6. Proposed Infrastructure

(i) Industrial Area: Tarapur MIDC industrial area, Dist - Palghar

(ii) Residential Area: Not applicable.

(iii) Green Belt: 3037sq. m.

(IV) Social Infrastructure and

(V) Connectivity

Road: MIDC has provided asphalt roads with varying widths; these are mainly two lane

roads and raised footpaths on either side of the roads.

Water: Water consumption of unit will be around 93.37 CMD (Existing - 20.5 CMD &

Proposed - 72.87 CMD).

Electricity: Existing connected load: 379 KW, Proposed connected load (Total after expansion): 456 KW

Streetlights: MIDC has provided street lighting facility in the area.

Telecommunication Facility / Connectivity: Fax, telex, email and Internet facilities are

available in the vicinity of project area.

(VI) Source of the Water will be MIDC. The daily water requirement will be around 93.37



CMD

(VII) Domestic Waste water will be routed to the in house aeration tank of ETP.

(VIII) The Industrial Waste will be disposed off to Mumbai Waste Management Limited -

CHWTSDF at Taloja.

(IX) The non hazardous Solid Waste generated will be mainly day to day office waste which will

be disposed off through local municipal waste disposal system.

(X) The Power Requirement will be 405 kVA which will be supplied by MSEDCL

7. Rehabilitation & Resettlement (R & R) Plan: Not Applicable

8. Project Schedule & Cost Estimates

1. The proposed schedule for approval and implementation.

Sr.

No.

Description Time Cost in

%

1. Obtaining all statutory permission with

respect to industry

22 Months 0.85 %

2. Design and Engineering Plan 2 Months 4.0 %

3. Factory Set Up 20 Months 92.15 %

4. Testing and Commissioning 6 Months 1.0 %

5. Actual Starting 26 Months 2.0 %

2. Estimated project cost along with analysis of economic viability of the project.

The estimated cost of the project is given as under in the following table.

Sr. No.

Existing (Cost in Rs.)

Proposed (Cost in Rs.)

Total (Cost in Rs.)

1 4,80,80,299.00 2,00,00,000.00 6,80,80,299.00

3. For the proposed products the new infrastructure to be constructed

The necessary required infrastructure will be erected within the premises on the existing plot.

9. Analysis of proposal (Final Recommendations)

The project will provide employment opportunities to local people and it will increase the

living standard. As the industry has the export market it will add to the net foreign exchange

earning of the country. The industry takes pride in maintaining healthy relationship with the

environment by further improvised technology of effluent treatment plant. The industry is



committed to manufacture and supply of finished products to achieve enhance customer satisfaction

by establishing and maintaining quality management system. Industry trust on employee’s strength

so management of the industry always promotes and maintains the safety conditions in and around

the workers. The regular medical checkups, safety training program’s, mock drill are being

conducted in the industry.

In view of the above points it is concluded that the project proposal will not have any

negative impact on the environment and people on the other hand will have positive impact by

improving the socio economic aspects with employment generation.



ANNEXXURE – I

(Existing & Proposed products list)

Sr. No

Product Existing (MT/M)

Proposed (MT/M)

Total (MT/M)

Group A (Manufacturing products) 1 Beta Blue 24.80 100.00 124.80 Group B (Blending products) 1 Pigment Yellow - 12,13,14,74,83,168,191 -- 40.0 40.00 2 Pigment Red -

3,4,8,112,48.2,48.3,12,53.1,57.1,146,170 --

3 Pigment Orange - 05,13,34 -- 4 Lemon Chrome -- 5 Middle Chrome -- 6 Pigment Green - 7 -- 7 Pigment Blue -- 8 Violet - 27 -- Total 24.80 140.00 164.80


ANNEXXURE – II

(Raw Material List) Sr. No.

Description Status Storage Location

Storage Capacity in

MT

Maximum Quantity of Storage at any point of

time in MT

Consumption/Month in MT

Source of Supply

Means of transportation

1 CPC Solid Shed 25.0 25.0 125.00 Local Road

2 Caustic Soda Solid Shed 3.0 3.0 4.0 Local Road

3 Gum rosin Solid Shed 4.0 4.0 4.5 Local Road

4 Xylene Liquid Shed 200.00 L 200.00 L 200.00 L Local Road

5 Isobutyl alcohol

Liquid Shed 400.00 L 400.00 L 450.00 L Local Road

6 Addictive -Pthalamide

Solid Shed 1.0 1.0 1.5 Local Road

7 Hydrochloric acid

Liquid Shed 1000.00 L 1000.00 L 10.0 Local Road

Date post:	29-Jun-2018
Category:	Documents
Upload:	phungkhanh
View:	223 times
Download:	1 times

Unilex Colours And Chemicals...

Documents