Pre-feasibility Report Kamnix...

Pre-feasibility Report Kamnix Biotech Survey no. 179 and 180 Village: Mahiyal, Taluka: Talod, District: Sabarkantha

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1. EXECUTIVE SUMMARY

Kamnix Biotech is a new venture for the introduction of world class biotech unit for the production of Pharma

& Food Grade Vitamins and Enzymes for the industries. The company is led by a young technocrat Ms. Niky

Upadhyay. She is a biotechnologist, who is being supported by Mr. Kamlesh Upadhyay a leading industrialist,

who is being her mentor.

Kamnix Biotech has proposed for setting up a new unit at Survey no. 179 and 180, Village: Mahiyal, Taluka:

Talod, District: Sabarkantha having total plot area of 4505 m2. No ecologically and/ or otherwise sensitive

areas fall within 25 km radius from the proposed site. State Highway 143 is the nearest highway located at

1.5 km to NW and Sabarmati River is located at 15 km to NW from the proposed site.

Products & Production Capacity:

SN Products Capacity

1 Vitamin B12 10 kg/Month


3 Vitamin C 5000 kg/Month

4 Enzymes 1000 kg/Month

TOTAL 6110 kg/Month

The proposed project has an employment potential of 50 persons. The project cost is to the tune of Rs. 3.55

Crores. Power requirement of the project is 315 KV and will be sourced from UGVCL.

The total requirement of water for the project is 22 KLD, out of which 11 KLD will be sourced from borewell

and balance 11 KLD will be recycled water from ZLD system for industrial effluent.

Flue gas emissions are form boiler of 1 TPH capacity using 50 LPH of LDO as fuel and occasionally from D.

G. Set of 250 KVA capacity using 50 LPH of HSD as fuel. Process emissions are from process vent having

scrubber as APCM and Multimill/ Micronizer having bag filter as APCM.

Project will generate hazardous wastes that will be handled and disposed as per Hazardous and Other

Wastes (Management and Transboundary Movement) Rules, 2016. Membership for common facility of

secured land fill of TSDF and incineration will be availed. Disposal by mode of co-processing will also be

envisaged. Spent solvent will be recovered in onsite solvent recovery system.


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2. INTRODUCTION OF THE PROJECT/ BACKGROUND INFORMATION

2.1 Identification of Project and Project Proponent:

Kamnix Biotech is a new venture for the introduction of world class biotech unit for the production of

Pharma & Food Grade; Vitamins and Enzymes at Survey no. 179 and 180, Village: Mahiyal, Taluka:

Talod, District: Sabarkantha having total plot area of 4505 m2.

The legal status of Kamnix Biotech is partnership firm. The company is led by a young technocrat Ms.

Niky Upadhyay. She is a biotechnologist, supported by Mr. Kamlesh Upadhyay a leading industrialist,

her mentor and Ms. Hina Upadhyay.

The proposed products fall in category 5(f)-B of the schedule, Synthetic organic chemicals industry (dyes

& dye intermediates; bulk drugs and intermediates excluding drug formulations; synthetic rubbers; basic

organic chemicals, other synthetic organic chemicals and chemical Intermediate), as per the EIA

Notification, 14th September 2006 and as amendments thereafter.

2.2 Brief Description of nature of the Project:

Kamnix Biotech is a proposed biotech unit for the production of Vitamins B12 (10 kg/Month), Vitamin B2

(100 kg/Month) & Vitamin C (5000 kg/Month) and Enzymes (1000 kg/Month). The manufacturing

process is mainly fermentation and is carried out as batch process.

2.3 Need of the Project and its importance to the country and region:

Biopharma is the largest sector contributing about 62 per cent of the total revenue followed by bio-

services (18 per cent), bio-agri (15 per cent), bio-industry (4 per cent), and bio-informatics contributing

(1 per cent).

India's biotech sector has attracted significant amount of attention over the past two decades. The

maximum benefits of biotechnology have been utilized by health care. A few developing countries like

India have scientists and technologists related to biotechnology where national strategies of

development in biotechnology is implemented. The scientific and technical manpower is shifting towards

biotechnology with the aim to produce expertise in biotechnology.


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2.4 Demand Supply Gap:

The project is envisaged to meet the demand supply gap as the demand for proposed product is steadily

increasing.

2.5 Imports v/s Indigenous Production:

Indigenous production of the proposed product is less and the project will reduce imports and enhance

indigenous production.

2.6 Export Possibility:

There is good potential of export for the proposed product and the possibility is envisaged by the project.

2.7 Domestic/ Export Market:

The project will cater to both domestic and export market.

2.8 Employment Generation (Direct and Indirect) due to Project:

Proposed project will generate the employment on levels time to tome and give priority to local persons.

Also considering this is a new project indirect employment will be generated due to development of

surrounding areas. The proposed project has a direct employment potential of 50 persons.


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3. PROJECT DESCRIPTION

3.1 Type of Project including Interlinked and Independent Projects, if any:

The project is a pharma bio-tech project. There is no interlinked project.

3.2 Location (Map showing General Location, Specific Location and Project Boundary & Project Site

Layout) with co-ordinates:

Project Site Co-ordinates: Latitude: 23.3369ON, Longitude: 72.9300OE


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Google Image:


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Plant Layout:


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3.3 Details of Alternate Sites considered and the basis of selecting the proposed site:

NA

3.4 Size and Magnitude of operation:

The proposed project is of small scale.

3.5 Project Description with process details (a schematic diagram/ flow chart showing the Project

Layout, components of the project, etc.):

Products & Production Capacity:

SN Products Capacity



3 Vitamin C 5000 kg/Month

4 Enzymes 1000 kg/Month

TOTAL 6110 kg/Month

VITAMIN B12

Process Description:

Formulation of Media: Formulation is done with Cobalt Salt along with Carbon and Nitrogen Sources.

Sterilization: The prepared media is then sterilized by using an Autoclave.

Starter Culture: Propionibacterium shermani will be the microorganism used.

Fermentation: Fermentation is done by both Anaerobic and Aerobic process.

Treatment: During this treatment precursors of pseudovitaminB12 are released free. After this, it is treated

with Cyanide solution to split the DBC and pseudo-vitamin B12. As a result, Cyanocobalamin (Vita B12) is

released free in the solution.

Recovery: Cyanocobalamin in the liquid is separated by using an adsorption column chromatography

with IRC-50 resin. The adsorbed Cyanocobalamin is then eluted out of the column using Phenolic solvent.

Powder Processing: It is sent to the Dryer which can be Tray Dryer/ VFD/Spray Dryer according to the

requirement. After drying, it is sent to the Multimill/ Micronizer. It is finally sent to the Shifter and then the

final product is stored in Storage bins and later packed.


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Material Balance:

INPUT OUTPUT

MATERIAL QTY. PRODUCT QTY. WASTE QTY.

Cobalt Chloride 0.05 Cyanocobalamin 1.00 Effluent 4540

Glucose 820.00 Emissions 5.55

Ammonium Hydroxide 49.00 RECOVERY Solid Waste 882.5

Dilute Acid 0.50 Phenolic Solvent 9.50

Cyanide Solution 5.00

Propionibacterium Shermani 9.00

Water 4545.00

Phenolic Solvent 10.00 Total 10.50 5428.05

Total Input 5438.55 Total Output 5438.55

Process Flow Chart:

STERILIZATION OF THE MEDIUM

FORMULATION OF MEDIUM

MAKING STARTER CULTURE

FERMENTATION

RECOVERY OF CYNOCOBALAMIN


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VITAMIN B2


A batch process using E. Ashbyii is analyzed. Upstream processing consists of preparation of medium

and associated continuous counter-current sterilization.

Feed components are: glucose syrup, yeast and malt extract, sunflower oil, sulfuric acid, and

concentrated salt solution at room temperature.

Fermentation is operated batch-wise with 10% inoculum ratios.

Downstream processing starts with harvesting followed by crystallization, centrifugation (decanter) and

final drying (spray dryer).

The requested purity of riboflavin is 70%. The residual 30% consists of salts and biomass.

The product is obtained as dry powder or as granulate.

Material Balance:

INPUT OUTPUT


Methionine 0.03 Riboflavin (Crystal) 1.00 Effluent 36.84

Glucose 0.35 Emission 0.59

K2HPO4 0.01 Solid Waste 0.84

Manganese Sulphate 0.01

Malt Extract 0.35

Peptone 0.35

Sunflower Oil 1.06

Yeast Extract 0.35

Sulphuric Acid 0.14

Eashbyii 0.30

Water 36.30 Total 1.00 38.27



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Process Flow Chart:

MEDIUM PREPARATION

STERILLIZATION

FINAL PRODUCT

MAIN FERMENTATION

HARVEST

PRECIPITATION/ CRYSTALLIZATION

CENTRIFUGATION/ DECANTER

DRYING/ SPRAY CRANULATION

Upstream

Downstream

Substrate, Water, CPN Source

Exhaust Inoculum Substrate, Inlet Air

Wash Water

By Products, Wastewater

By Products, Wastewater


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VITAMIN C


In the first step, sorbitol is oxidized into sorbose by fermentation.

All producers use the same micro-organism for this fermentation. Sorbitol itself is made by reducing

glucose at high temperature.

The process does not involve use of genetically modified organisms (GMOs).

Material Balance:

INPUT OUTPUT


Ascorbic Acid 150.00 Vitamin C 1.00 Effluent 160.43

Corn 150.00 Solid Waste 300.00

Glucose 0.04

Calcium Carbonate 0.03

Thioglycolic acid 0.01

Wheat 150.00

Gluconic Acid 0.15

Methionine 0.50

Tryptophan 0.50

Sorbitol 10.00

Water 0.20 Total 1.00 460.43



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Process Flow Chart:


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EMZYME


Source: Choosing a source means choosing the microorganism required for production of the specific enzyme. Optimization: Optimization means finding highest specific synthesis rate for a given amount of biomass. As, enzyme synthesis depends on primary metabolism, conditions favoring enzyme synthesis favor growth. Thus, conditions favoring growth and the relationship between growth rate and enzyme synthesis rate is determined. Fermentation: Fermentation is solid surface type. Wheat bran, whose high content of nutrients includes minerals and salts is used as media for production of amylase, protease, and lipase from Aspergillus and Mucor species, as well as for pectinase and cellulase from Aspergillus and Penicillium species. Tray Process: Substrate is spread in a thin layer in incubation rooms. After cultivation of fungi with spores, the mycelia are extracted with water or salt solution in countercurrent mode, and the concentrated enzyme solution is precipitated.

Material Balance:

INPUT OUTPUT


Bacillus Subtilis 0.13 Enzyme 1.00 Solid Waste 0.85

Soy-bean 0.50

Wheat 0.75

Aspergillus oryzae 0.13

Rhizopus Niveus 0.10

Aspergillus niger 0.25 Total 1.00 0.85



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Process Flow Chart:


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3.6 Raw Material required along with estimated quantity, likely source, marketing area of final

product/s, Mode of Transport of Raw Material and Finished Product.

Major raw material procurement is locally planned. The product market is pharma biotech market. Mode of transportation of material is mainly by road. Raw Material Consumption:

SN Raw Material for Vitamin B12 Consumption/

Month

Storage Qty. Storage Container

1 Cobalt Chloride 0.45 Kg 50 Kg HDPE Bag

2 Glucose 8181.82 Kg 150 Kg Drum

3 Ammonium Hydroxide 490.91 Kg 125 Kg Glass Bottle

4 Nitrogen 3850.00 Kg 25 Kg Drum

5 Oxygen 1150.00 Kg 50 Kg Drum

6 Propionibacterium Shermanii 86.73 Kg 50 Kg LDPE Bags

7 Phenolic Solvent 100 Kg 20 Kg Drum

8 Dilute Acid 5 Kg 50 Kg Bottle

9 Cyanide Solution 50 Kg 50 Kg Bag

SN Raw Material for Vitamin B2 Consumption/

Month


1 Methionine 2.83 Kg 150 Kg Plastic Bottle


3 K2HPO4 1.42 Kg 125 Kg LDPE Bags

4 Manganese Sulphate 1.42 Kg 25 Kg HDPE Bags

5 Malt Extract 35.38 Kg 50 Kg Linear Bags

6 Peptone 35.38 Kg 50 Kg Bottle

7 Sunflower Oil 106.13 Kg 50 Kg Drum

8 Water 3629.72 Kg 500 Kg Drum

9 Yeast Extract 35.38 Kg 25 Kg Plastic Bottle

10 Nitrogen 36062.5 Kg 25 Kg Drum

11 Oxygen 10948.11 Kg 50 Kg Drum

12 Sulphuric Acid 14.15 Kg 50 Kg Plastic Container

13 E Ashbyii (one Time) 26.75 Kg 25 Kg Plastic Container


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SN Raw Material for Vitamin C Consumption/

Month


1 Ascorbic Acid 150 Kg 250 Kg Drum

2 Corn 150 Kg 250 Kg Drum


4 Calcium Carbonate 30 Kg 10 Kg LDPE Bags

5 Thioglycolic acid 10 Kg 500 Kg Glass Bottle

6 Wheat 150 Kg 250 Kg Drum

7 Gluconic Acid 150 Kg 500 Kg Plastic Bottle

8 Methionine 500 Kg 10 Kg Plastic Bottle

9 Tryptophan 500 Kg 10 Kg Drum

10 Sorbitol 10 Kg 50 Kg HDPE Bags

SN Raw Material for Enzymes Consumption/

Month


1 Pine-apple 25 Kg 300 Kg LDPE Bags

2 Papaya 100 Kg 200 Kg LDPE Bags

3 Whole Grain 150 Kg 200 Kg Drum

4 Penicillium 25 Kg 300 Kg Plastic Container

3.7 Resource optimization/recycling and reuse envisaged in the project:

ZLD is proposed for industrial effluent (11 KLD) and recovered waster used for utility make-up and

washing consumption. Make up of scrubber is done by WTP RO reject

100 kg/month spent phenolic solvent will be generated and 95 kg/month will be recovered and will be

reused in process. Phenolic solvent recovery process is by Two Phase Batch Reaction. A steam stripping

process is proposed. This solution allows water from the steam to act as a barrier liquid between the

solvent and bio-polymer during separation, preventing the formation of a hardened plug.


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Steam Stripper and Recovery Column for Miscible System:

3.8 Availability of Water, its sources. Energy/ Power requirement and source:

The total requirement of water for the project is 22 KLD. 11 KLD will be recycled water and balance 11

KLD will be sourced from ground water through borewell.

Power requirement of the project is 315 KV and will be sourced from UGVCL. Additionally, D.G. Set of

capacity 250 KVA will be installed for power-backup.


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3.9 Quantity of Wastes to be generated (liquid and solid) and scheme for their Management/ disposal.

Water Consumption & Wastewater Generation

SN Head Consumption

Qty., KLD

Generation

Qty., KLD

1 Domestic 2.0 1.5

2 Industrial

2.1 Process 5.0 3.5

2.2 Washing 4.0 4.0

2.3 Cooling 5.0 0.5

2.4 Boiler 2.0 0.5

2.5 Plantation 1.5 --

2.6 Scrubber 0.5 0.5

2.6 RO Reject (WTP Rejects) 2.0 2.0

Total Industrial 20.0 11

Total (Industrial + Domestic) 22.0 12.5

Mode of Disposal:

Domestic Effluent: Septic Tank/ Soak Pit

Industrial Effluent: Zero Liquid Discharge consisting of ETP, RO & MEE. The recovered water

is utilized for utility make-up and washing consumption.

Air Emission:

Flue Gas Emission:

Stk. Stack Attached to Stack Height Fuel Permissible Limit

FGE-01 Boiler (1 TPH) 10 m LDO: 80 LPH PM≤150 mg/Nm3 SO2≤100 ppm NOX≤50 ppm FGE-02 D. G. Set (250 KVA) 4.5 m HSD: 50 LPH

Process Gas Emission:

Stk. Stack Attached to Stack Height APCM Permissible Limit

PGE-01 Process Vents 6 m Scrubber SO2≤40mg/Nm3

PGE-02 Multimill/ Micronizer 4 m Bag Filter PM≤150mg/Nm3


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Hazardous Waste Management:

SN Waste Category Quantity Disposal

1 Used or spent oil 5.1 0.5 MTA Sold to authorised re-refiner

2 Process Residue and wastes (Biomass)

28.1 1000 MTA Incineration at CHWIF &/or Co- processing

3 Off specification products 28.4 5 MTA Incineration at CHWIF &/or Co- processing

4 Date-expired products 28.5 5 MTA Incineration at CHWIF &/or Co- processing

5 Spent solvents 28.6 1.2

KL/Annum

Recovery onsite &/or Rule 9 authroised solvent recovery unit&/or Incineration at CHWIF &/or Co- processing

6 Empty barrels/ containers/ liners contaminated with hazardous chemicals/ wastes

33.1 100

Nos./Annum

Decontaminated Reused &/or Sold to authorised re-user/ recycler.

7 Spent ion exchange resin containing toxic metals

35.2 0.5 MTA Incineration at CHWIF

8 ETP Sludge 35.3 1 MTA Secured Landfill at TSDF.

9 Any process or distillation residue

36.1 0.05 MTA Incineration at CHWIF &/or Co- processing

10 Spent filter medium 36.2 1 MTA Incineration at CHWIF

11 Concentration or evaporation residues

37.3 5 MTA Secured Landfill at TSDF.


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3.10 Schematic representations of the feasibility drawing giving information of EIA purpose


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4. SITE ANALYSIS

4.1 Connectivity:

Plot/Survey/Khasra No. Survey no. 179 and 180

Village Mahiyal

Tehsil Talod

District Sabarkantha

State Gujarat

Nearest Railway station/airport along with

distance in kms

Talod Railway Station – 2.5 km in NE direction

Ahmedabad Railway Station – 50 km in SW direction

Sardar Vallabhbhai Patel International Airport – 43 km in

SW direction

Nearest Town, City, District Headquarters

alongwith distance in kms.

Talod Town: 2.5 km in NE direction

Himatnagar City: 30 km in in N direction

Village Panchayats, Zilla Parishad,

Municipal Corporation, Local body

(complete postal addresses with telephone

nos. to be given)

Mahiyal Gram Panchayat, Vill.: Mahiyal, Tal. Talod,

Gujarat 383215

Talod Taluka Panchayat, Talod-Dhadh Rd,

Mamlatdar Kacheri, Talod, Gujarat 383215

Sabarkantha District Panchayat,

By Pass Road, Opp, Circuit House,

Himatnagar, Gujarat 383001

4.2 Land Form, Land Use and Land ownership:

Landform is plateau. The land use for Non-Agricultural and Industrial use. Land ownership is of Partners

of Kamnix Biotech.

4.3 Topography:

The topography of the project land is flat. Mahiyal village topography is moderate ranging from 0-10%

slope.


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4.4 Existing land use pattern (agriculture, non-agriculture, forest, water bodies, (including area under

CRZ)), shortest distances from the periphery of the project to periphery of the forests, national

park, wild life sanctuary, eco sensitive areas, water bodies (distance from the HFL of the river),

CRZ.

Land Use Of Mahiyal Village Area, Ha Distribution, %

Agricultural Use 504.3 87.04

Non-Agriculture Use 31.0 5.35

Barren/ Uncultivated Use 22.2 3.83

Permanent Pasture & Grazing Use 21.9 3.78

Forest 0 0

Total 579.4 100.00

There is no forest, national park, wild life sanctuary, costal area & eco sensitive area within 25 km radius

of the project. River Sabarmati is at 15 km distance in NW direction of project.

4.5 Existing Infrastructure:

State Highway SH143 is 1.5 km in NW direction and District road is 150m in S direction of the project site.

Talod Railway Station is 2.5 km in NE direction, Ahmedabad Railway Station is 50 km in SW direction

and Sardar Vallabhbhai Patel International Airport is 43 km in SW direction from project site. For power

requirement, UGVCL Division Office is located at Talod – 382715.

There is no existing infrastructure developed within project premises.

4.6 Soil Classification:

Project falls under North West Gujarat agro climatic zone. The soil is brown to very dark grayish brown in

surface color. The depth of soil is moderate to deep about 25 to 75 cm. The predominate texture of soil

is loamy sand and silt and clay. The fertility of soil is very poor with low nitrogen, phosphorus and potash.

The order of soil is mainly Aridsol and Inseptisol. Soil type is mostly mohoram & stony.

4.7 Climate data from secondary sources:

Sabarkantha district comes under normal rainfall areas in Gujarat, having sub-tropical climate with

moderately low humidity. The main seasons prevailing in the district are (a) monsoon - mid of June to

October, (b) winter - November to February, and (c) summer – March to June. The maximum daily


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temperature during the year ranges from 31.0 °C in January to 48.5 °C in May while minimum temperature

ranges from 11.5 °C in January to 27.5°C in May. Maximum humidity ranges from 81.0% to 25.5%. The

wind speed ranges from 88.0 to 184.9 km/day, whereas evapo - transpiration ranges from 3.5 to 7.8

mm/day.

Rainfall data collected by IMD for Ahmedabad station are presented below. The observed average rainfall

for last 30 years (1982 - 2011) for Talod Taluka is 795 mm as per GSDMA.

Month - Year 2007 2008 2009 2010 2011

January 0.0 0.0 0.0 0.0 0.0

February 0.2 0.0 0.0 0.0 0.0

March 0.0 0.0 0.0 0.0 0.0

April 0.0 1.9 0.0 0.0 0.0

May 0.0 0.0 0.0 0.0 0.0

June 55.8 39.2 13.0 39.6 2.5

July 820.1 208.2 404.9 321.7 262.3

August 336.6 311.6 209.6 375.5 547.2

September 97.7 99.3 29.3 133.3 181.8

October 0.0 7.2 3.1 0.0 0.0

November 0.0 0.0 0.6 25.8 0.0

December 0.0 1.2 0.0 2.1 0.0

Total 1310 668.6 660.5 898 993.8

Average 109.2 55.72 55.04 74.83 82.82

4.8 Social Infrastructure available:

Senior Secondary School & Sub Post Office is available at Mahiyal village. Tap Water is available for

household requirement at Mahiyal village. Telephone, mobile and internet connectivity is also available.

Community Health Centre, Primary Health Centre, Maternity and Child Welfare Centre, Hospital-

Allopathic, Dispensary, Veterinary Hospital, Mobile Health Clinic & Family Welfare Centre available within

5 km.


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5. PLANNING BRIEF

5.1 Planning Concept (type of industries, facilities, transportation, etc.) Town & Country Planning/

Development authority Classification

The project is a biotech pharma industry. The manufacturing plant will consist of culture preparation,

fermentation, processing, recovery and storage area. Utility such as boiler, cooling tower, D. G. Set and

ETP will be installed. 2 nos. of entry and exist will be provided. Greenbelt around the periphery of the

premises will be developed. Internal road of 6m width will be provided round the plant. Road

transportation to the project site is available.

5.2 Population Projection

The project scale is small and employment is of 50 persons. There is no major impact on population

projection due to the project.

5.3 Land use planning (breakup along with green belt etc.)

Head Area, M2 Distribution, %

Construction 1469 32.61

Road & Parking 1236 27.44

Green Belt 1500 33.30

Open 300 6.66

Total 4505 100.00

5.4 Assessment of Infrastructure Demand (Physical & Social)

The project scale is small and employment and there is no major demand of infrastructure, the existing

infrastructure will suffice.

5.5 Amenities/Facilities

Administrative office will be provided within the premises for clerical and technical work. First aid and

medical facility will be provided as per statutory requirements.


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6. PROPOSED INFRASTRUCTURE

6.1 Industrial Area (Processing Area)

The site area for the project is adequate for the proposed project.

6.2 Residential Area (Non-Processing Area)

No residential area within project premises is proposed.

6.3 Green Belt

Out of 4505 m2 of total area, 1500 m2 (33.3%) of green belt along the periphery will be developed.

6.4 Social Infrastructure

The industry will individual and jointly contribute to the social infrastructure development of the surround

area within its capacity.

6.5 Connectivity (Traffic and Transportation Road/ Rail/ Metro/ Water ways etc.)

The project is well connected with direct road.

6.6 Drinking Water Management (Source & Supply of water)

Source of water is ground water (borewell) and adequate drinking water facility will be provided.

6.7 Sewerage System

Domestic effluent in tune of 1.5 KLD generated will be conveyed through under ground drainage and

disposed off by septic tank – soak pit arrangement.

6.8 Industrial Waste Management

Industrial waste management will be as detailed under previous section 3.8

6.9 Solid Waste Management

Solid waste management will be as detailed under previous section 3.8

6.10 Power Requirement & Supply/ Source.

Power requirement of the project is 315 KV and will be sourced from UGVCL. Additionally, D.G. Set of

capacity 250 KVA will be installed for power-backup.


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7. REHABILITATION AND RESETTLEMENT (R&R) PLAN

7.1 Policy to be adopted (central/ state) in respect of the project affected persons including home

outees, land outees and landless laborers:

Not Applicable

8. PROJECT SCHEDULE & COST ESTIMATE

8.1 Likely date of start of construction and likely date of completion (Time schedule of the project):

Construction activity will commence immediately after grant of Environmental Clearance, Consent to

Establish and other required statutory permission and will be completed in six months. The likely date of

completion will be 31/12/18.

8.2 Estimated project cost along with analysis in terms of economic viability of the project

The project cost is to the tune of Rs. 3.55 Crores. The economic viability of the project is positive

considering it to be pharma biotech project.

9. ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)

9.1 Financial and social benefits with special emphasis on the benefit to the local people including

tribal population in the area.

This project is a small step in the biotech sector of our country and will have long term financial and social

benefits. The local people will be benefited with employment, training and social development.h

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Pre-feasibility Report Kamnix...

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