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Yashvin Industries Chemical Expansion

The document provides a feasibility report for a proposed expansion of synthetic organic fine chemical manufacturing at an existing facility. The expansion would add 400 MT/month of production capacity for organic dyes and intermediates. It details the existing and proposed product quantities, raw materials required, process description, pollution load, hazardous waste generation, water and power requirements. The total proposed investment for the expansion is Rs. 800 lacs.

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0% found this document useful (0 votes)
236 views29 pages

Yashvin Industries Chemical Expansion

The document provides a feasibility report for a proposed expansion of synthetic organic fine chemical manufacturing at an existing facility. The expansion would add 400 MT/month of production capacity for organic dyes and intermediates. It details the existing and proposed product quantities, raw materials required, process description, pollution load, hazardous waste generation, water and power requirements. The total proposed investment for the expansion is Rs. 800 lacs.

Uploaded by

jpsingh75
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© © All Rights Reserved
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PROJECT FEASIBILTY REPORT :

1.0 EXECUTIVE SUMMARY:

M/s.Yashvin Industries is currently holding Consent to Establish for bromine recovery and bromide
based products. The consent to establish for manufacturing inorganic compounds was received vide
letter no. GPCB/NOC-VRD-5030/ID-66226/479040 dated 18/12/2018. Now M/s. Yashvin Industries
intends to add Synthetic Organic Fine Chemical Manufacturing facility to be located on their existing
plot no. 124/34, GIDC, Nandesari, Dist. Vadodara which is a chemical notified zone. The plant will
be put up on the existing plot admeasuring 2960.25 sq. mts.

The list of products are given below:

Table No. 1: LIST OF PRODUCTS:

SR. NAME OF PRODUCT QUANTITY (MT/MONTH )


NO. EXISTING PROPOSED TOTAL AFTER
PROPOSED
EXPANSION
EXISTING
1 Caesium Bromide 100 MT (Dry) ------ 100 MT (Dry)
2 500 MT 50% ------ 500 MT 50%
Calcium Bromide solution/ 250 solution/ 250 MT
MT Dry Dry
3 Potassium Bromide 100 MT (Dry) ------ 100 MT (Dry)
4 Sodium Bromide 100 MT (Dry) ------ 100 MT (Dry)
5 100 MT 80% ------ 100 MT 80%
solution/ 80 MT solution/ 80 MT
Zinc Bromide Dry Dry
6 Bromine Recovery 200 MT ------ 200 MT
7 HBr (48%) 500 ------ 500
PROPOSED
8 GROUP 1 - Leuco Dyes ------ 200 200
ODB-1 / ODB-2 / ODB RED-1/
ODB RED-2 / ODB GREEN
9 GROUP 2 - Dyes and Dye ------ 200 200
Intermediates
MMDPA / ISATIN / 4-
BROMO-N-METHYL
ANTHRAQUINONE / LEUCO
1,4-DIAMINO
ANTHRQAQUINONE / 1,4-
DIAMINO-2,3-DICHLORO
ANTHRAQUINONE / RV-FBL
/ 2,6-DIBROMO-4-METHYL
ANILINE / BUTYL BROMIDE
/ CRYSTAL VIOLET
LACTONE
Total Organic Products 400 400
The manufacturing capacity of the synthetic organic fine chemicals in the plant will be 400
MT/Month.

The raw material list is given in the table below:

Raw Material CAS No. Qty


(MT/Month)
1,4 Diamino AQ leuco 5327-72-0 188.5
1-Methyl Amino AQ 82-38-2 191.7
3 Methyl Anisole 100-84-5 147.8
4 Chloro Phenol 106-48-9 66.4
4-Dibenzylamino Phenol 103-14-0 66.4
Acetic Anhydride 108-24-7 51.6
Ammonia gas 7664-41-7 10.9
Ammonia solution (25%) 7664-41-7 744.8
Aniline 62-53-3 285.7
Bromine 7726-95-6 138.0
Bromo Methyl Anisole 27060-75-9 66.4
Butyl bromide 164365-88-2 101.5
Caustic lye 1310-73-2 816.5
Chloral hydrate 302-17-0 381.9
DCDA - Dicyandiamide 461-58-5 200.0
DEMAP- 3-Diethylaminophenol 91-68-9 72.2
Dimethyl Aniline 121-69-7 61.3
Dimethylamino Benzaldehyde 100-10-7 75.4
Diphenylamine 122-39-4 107.5
DMS - Dimethyl sulfide 75-18-3 191.5
HBr (48%) - Hydrobromic acid 10035-10-6 406.3
HCl - Hydrochloric Acid 7647-01-0 75.2
HNO3 (70%) - Nitric Acid 7697-37-2 145.7
Hydro 41.4
Hydrogen Peroxide (30%) 7722-84-1 214.2
Hydroxylamine sulfate 10039-54-0 331.4
Isonitroacetanilide 104-04-1 268.6
M Cresol 108-39-4 187.1
MAP - 4-Methoxy Acetophenone 100-06-1 35.3
Methanol 67-56-1 207.8
N- Butanol 71-36-3 121.2
NaBr (30%) 7647-15-6 281.8
NaOH 1310-73-2 141.7
ODCB- orthodichlorobenzene 95-50-1 95.0
Phenol 108-95-2 207.1
Phthalic Anhydride 85-44-9 58.8
Potassium hydroxide 1310-58-3 242.7
p-Toludiene 106-49-0 85.0
Quninizarine 81-64-1 55.3
Soda Ash 497-19-8 112.5
Sodium sulphate 7757-82-6 238.1
Sulfur 7704-34-9 8.7
sulfuric acid 7664-93-9 603.9
Sulphuryl Chloride 7791-25-5 460.0
Xylene 1330-20-7 109.0
Details of Project in brief:
Mode of Operation Batch Process
Fuel used The existing boiler has capacity 4 MT/hr. Another boiler of 4 MT/hr will
be installed. Fuel used will be Agro Waste or coal. Total consumption of
agro waste requirement will increase from 5 MT/day to 35 MT/day for
agrowaste or 15 MT/day for coal. Multi Cyclones with bag filter will be
used to control the PM
Water Requirement 191 KL/Day from GIDC Water Supply Scheme (permission taken)
Waste water Generation 150 KL/day from process which will be treated in the ETP and sent to
the CETP as per the inlet norms. (membership of CETP for additional
discharge taken). 12 KL/day domestic waste will be sent to soak pit
Treatment Method The waste water will be treated by Hydrodynamic based cavitation
treatment. This treatment methodology has been developed and provided
by the CETP authorities. This process of treatment of waste water has
been authenticated by NEERI, Nagpur.
Hazardous waste ETP sludge (2400 MT/Yr) will be disposed off in TSDF of NECL for
generation coprocessing in Cement Industries. Used oil (2 MT/Yr) will be sold off
to authorized recycler. Discarded containers / liner (24 MT/Yr) will be
sold off to authorized recycler after decontamination. Process Waste /
Distillation Residue (1000 MT/Yr) will be sent to TSDF of NECL for
Coprocessing in Cement Industries. Spent Acid (12000 MT/Yr) will be
sold to actual users with Rule 9 permission or will be sent to cement
industry. Spent Solvent (800 MT/Yr) will be sold to actual recycler with
Rule 9 permission.
Power requirement 100 KVAwill be increased to 250 KVA and will be sourced from
MGVCL
Cost of Project Rs. 800 Lacs
Table No. 3: Pollution load Summary:
Parameter For For Remarks
Existing Proposed
Plant Plant
1. Land requirement (sq.mts) 2960.25 -- Additional land is not required
2. Water requirement (KL/day) 69 191 Source is GIDC Water supply
scheme
3. Power requirement (KVA) 100 250 Will be sourced from MGVCL
4. Waste water generation 50 162 Domestic Waste water (12 KL/day)
(KL/day) will be sent to Soak pit. Industrial
waste water (150 KL/day) will be
given primary treatment to CETP
inlet norms and then will be sent to
CETP of NIA, Nandesari for its
further treatment and disposal.
5. Air pollution Control
a) Fuel Burning
i) Agro waste (MT/hr) 5 35
ii) Process Emissions, no. of 2 3 Additional scrubbers will be
scrubber installed to control HCl, SO2, Cl2
emissions
6. Hazardous Waste
a. Used /Spent oil (MT/Yr.) 1 2 Will be sold to authorized recycler or
sent to NECL
b. Discarded containers/ barrels / 5.0 24.0 Will be sold to authorized scrap
liners(MT/Yr.) dealer
c. ETP Sludge (MT/Yr.) 2000 2400 Coprocessing in cement industries
via NECL
d. Distillation residue (MT/Yr) - 800 Coprocessing in cement industries
via NECL
e. Spent Acid (MT/Yr) - 12000 Sold to actual users with Rule 9
f. Spent Solvent (MT/Yr) - 800 Sold to actual recycler with Rule 9
g. NaBr/HBr Solution(MT/Yr) - 3300 Sent toBromine recovery inside plant
h. Scrubbing solution(KL/Yr) - 600 Sent to ETP and then to CETP
2.0 INTRODUCTION:

2.1 THE PROJECT:

M/s.Yashvin Industries, located on plot ono. 124/34 GIDC, Nandesari will be established by a group
of technical entrepreneurs.The unit already poses the Consent to Establish to recover bromine and
manufacture bromine based products. The unit has already made the application under Rule 9 for
procuring Bromine containing waste water. Now the Unit intends to produce Leuco dyes and also
manufacture Dye and dye intermediates. The product details are provided in table no. 1.

2.2 PROJECT PROPONENT:

The Industry will be run a group of experienced industrialists


1) Mahesh Patel (Chemical Engineer – M.E.) – Mr. Patel has over 35 years of work experience
working in Dyes and Dye Intermediate Industries. He is also the managing Director of
Philoden Industries Pvt. Ltd.
2) Chitesh N. Panchal (B. Com.) – Mr. Panchal has over 20 years of work experience in
Chemical Industry. He is also the Director of Harsiddhi Organics Pvt. Ltd.
3) Sahil Kher (M.Sc. – Chemistry) – Mr. Kher has over 5 years work experience in chemical
industry. He is also the director of Amogh Chemicals Pvt. Ltd.
4) Narendra Patel (B.Com.) – Mr. Patel has over 35 years of work experience in accounts and
finance in various places such as GIDC, AIMS Oxygen Pvt. Ltd., Avani Lease Finance Pvt.
Ltd.
The list of Partner sare given below in Table No. 4

Table No. 4: List of Partners:


Sr.No. Name of the directors Designation Address Mobile No.
1 Chitesh N. Panchal Partner 1/1, Saurabh Park, Opp. HWP Colony, 9327741295
Channi Jakat Naka, Vadodara-390024.
2 Maheshkumar D. Patel Partner Survey No. 23,” Devashish”
Nr. Shrikunj 9375854646
Bunglow, Gotri‐Sevasi Road, Vadodara –
391101
3 Sahil S. Kher Partner D-2, Tulsidham, Thana Naka Road, Nr. 9820422369
Birmole Hospital CUF Nagar, Panvel
Raigarth, Maharashtra - 410206
4 Narendra B. Patel Partner 309, Piplagate, Sevasi, Vadodara - 391101 9924177574

2.3 NATURE OF PROJECT:

The unit will be involved in the manufacturing of Lueco Dyes and dye intermediates and is located
in the Notified Chemical Zone of GIDC, Nandesari falls under the category 5(f)b. The unit intends
to produce 400 MT/Month of chemicals.

2.4 MARKET FEASBILITY:

Yashvin Industries will be manufacturing Leuco Dyes and certain specialty intermediates. Currently,
these intermediates are being imported from China. The company intends to position itself as import
substitute for these specialty intermediates. Partners of Yashvin Industries are associated with
Philoden Industries Pvt. Ltd. and Amogh Chemicals Pvt. Ltd. Additionally, some of these products
are going to be sold and exported to multinational companies on long-term contract basis countries
like Japan, USA, Germany, Korea etc.
.
2.5 EMPLOYMENT GENERATION DUE TO PROJECT:

The project will generate employment for the local and nearby population. A total of 60 nos. of
personnel (Skilled as well as unskilled) will be employed to carry out the proposed production.

3.0 PROJECT DESCRIPTION:


3.1 TYPE OF PROJECT:
M/s.Yashvin Industries., located in the Chemical Notified Zone of GIDC, Nandesari will be
manufacturing Lueco Dyes and speciality dye intermediates. The proposed project is not interlinked
or interdependent on any other projects.

3.2 PROJECT LOCATION:

The project is located at Plot No. 124/34 in the Chemical Notified Zone of GIDC, Nandesari. The
area of the plot is 2960.25 sq mts. GIDC Nandesari is located about 17 km NW of city of Vadodara.

Table No. 5: Salient features of the site

Particulars Details
Taluka/Tehsil Vadodara
District Vadodara
Geogrophic Location 22.405385 N, 73.093587 E
Nearest city Vadodara (17 kms in the SW direction)
Nearest Town Vadodara
Nearest Highway Ahmedabad – Vadodara NH 8 Highway
Nearest Airport Vadodara
Protected Areas/Sanctuaries NA
Elevation above mean sea level 34 mts
Location of Site on GIDC Map
Landmarks in the 10 km radius circle
3.3 SITE SELECTION:

The site is located in GIDC, Nandesari. GIDC, Nandesari is a designated Chemical Zone. GIDC,
Nandesari has all the infrastructural facilities like concrete roads, well developed infrastructure
facilities required for successful running of an industry like CETP, TSDF, availability of water,
Uninterrupted power supply, common steam facility etc.

3.4 NEIGHBOURINGINDUSTRIES
The proposed site is already in the chemical Notified Zone of GIDC. Table no. 6 shows the
neighboring industries

Table no. 6Neighbouring Industries

Name of industry Direction w.r.t


Amophil Chemicals Pvt. Ltd. East
Empty Plot West
Parel Pesticide Pvt. Ltd. North
GIDC Main Road South

3.5 SIZE OF THE PROJECT:


The manufacturing capacity of the plant will be 400MT/Month. The total cost of project is expected
to be about Rs. 800 Lacs. A breakdown of the cost of project is given below in Table No. 7.

Table No. 7. Breakup of cost of Project:

Sr. No Purpose Projected Investment (Rs in Lacs)


1 Land --
2 Building 175
3 Plant and machinery 442
4 Effluent treatment plant 65
5 Fire and safety equipment 12
6 Green belt development 1.0
7 Air pollution control measures 20
8 Hazardous waste disposal 25
9 QC Lab 60
Total 800
3.6 PROCESS TECHNOLOGY:

The manufacturing process is indigenous. The unit already has operating plant manufacturing dyes
and recovery of bromine.

3.7 RAW MATERIAL:


The list of raw materials is given in table no. 8
Table 8. List of Raw Materials:

Raw Material CAS No. Qty (MT/Month)


1,4 Diamino AQ leuco 5327-72-0 188.5
1-Methyl Amino AQ 82-38-2 191.7
3 Methyl Anisole 100-84-5 147.8
4 Chloro Phenol 106-48-9 66.4
4-Dibenzylamino Phenol 103-14-0 66.4
Acetic Anhydride 108-24-7 51.6
Ammonia gas 7664-41-7 10.9
Ammonia solution (25%) 7664-41-7 744.8
Aniline 62-53-3 285.7
Bromine 7726-95-6 138.0
Bromo Methyl Anisole 27060-75-9 66.4
Butyl bromide 164365-88-2 101.5
Caustic lye 1310-73-2 816.5
Chloral hydrate 302-17-0 381.9
DCDA - Dicyandiamide 461-58-5 200.0
DEMAP- 3-Diethylaminophenol 91-68-9 72.2
Dimethyl Aniline 121-69-7 61.3
Dimethylamino Benzaldehyde 100-10-7 75.4
Diphenylamine 122-39-4 107.5
DMS - Dimethyl sulfide 75-18-3 191.5
HBr (48%) - Hydrobromic acid 10035-10-6 406.3
HCl - Hydrochloric Acid 7647-01-0 75.2
HNO3 (70%) - Nitric Acid 7697-37-2 145.7
Hydro 41.4
Hydrogen Peroxide (30%) 7722-84-1 214.2
Hydroxylamine sulfate 10039-54-0 331.4
Isonitroacetanilide 104-04-1 268.6
M Cresol 108-39-4 187.1
MAP - 4-Methoxy Acetophenone 100-06-1 35.3
Methanol 67-56-1 207.8
N- Butanol 71-36-3 121.2
NaBr (30%) 7647-15-6 281.8
NaOH 1310-73-2 141.7
ODCB- orthodichlorobenzene 95-50-1 95.0
Phenol 108-95-2 207.1
Phthalic Anhydride 85-44-9 58.8
Potassium hydroxide 1310-58-3 242.7
p-Toludiene 106-49-0 85.0
Quninizarine 81-64-1 55.3
Soda Ash 497-19-8 112.5
Sodium sulphate 7757-82-6 238.1
Sulfur 7704-34-9 8.7
sulfuric acid 7664-93-9 603.9
Sulphuryl Chloride 7791-25-5 460.0
Xylene 1330-20-7 109.0

3.8 RESOURCE OPTIMIZATION / RECYCLE & REUSE:

The addition of the raw materials will be carried out by day tanks and use of metering pumps. Only
known quantity of Raw materials will be added for the completion of the reaction. The effluent will
be treated by latest technology of hydrodynamic cavitation which has been supplied by the CETP
authorities. The footprint for this technology is very less and the area required for treatment is 1/3rd
the requirement of conventional biological systems. The recycle of waste water project will be carried
out CETP authorities. They have applied for expansion of CETP with 8 MLD of waste water to be
recycled to the industries as process water.

3.9 RESOURCE REQUIREMENT:

3.9.1 LAND:

The unit will come up in on the plot whose total area is 2960.25 Sq Mts.

3.9.2 BUILDING:

Building structures will be constructed to house the new plant, raw material and finished material
storage sheds and effluent treatment plant, hazardous waste storage yard.
3.9.3 POWER AND FUEL:

The power and fuel requirement is given in table no. 9.

Table No. 9 Fuel and power requirments

Sr. Item Capacity Fuel used Total Requirement Source


No.
Existing Proposed

1. Boiler – 2 4 MT/hr Agrowaste 5 MT/day 35 MT/day- Local


Nos. each / coal Agro waste
15 MT/day -
coal
2. Energy- 100 KVA 250 KVA MGVCL
Electricity

3.9.4 WATER:

The water will be sourced from GIDC Water supply scheme. For water consumption will be 191
KL/day. Permission to procure water has already been taken from Water Utilities Department. Total
waste water generation from the plant will be 162 KL/Day, of which 12 KL/Day will be from
domestic activities and rest 150 KL/Day from industrial activities. 150 KL/Day will be taken to ETP
plant for its treatment and further disposed to CETP of NIA. The domestic waste water will be sent
to the soak pit or CETP. The permission to dispose off 150 KL/day of waste water to CETP has been
taken.
Table No. 10: Proposed Water Consumption and Waste Water Generation details :

Water Consumption details :

Sr. No. Breakup Existing Water Proposed Water Total Water


Consumption Consumption Consumption
(KL/day) (KL/day) (KL/day)
I Domestic 10 5 15
II Industrial
a) Process 25 92 117
b) Boiler 15 7 22
c) Cooling Tower 12 13 25
d) Washing 2 5 7
III Others
Gardening 5 - 5
Total 69 122 191

Waste Water Generation Details :

Sr. Breakup Existing Waste Proposed Waste Total Waste


No. Water Water Water
Generation Generation Generation
(KL/Day) (KL/Day) (KL/Day)
I Domestic 8 4 12
II Industrial
a) Process 44 88 132
b) Cooling Tower Blowdown 2 5 7
c) Boiler Blowdown 2 2 4
(d) Washings 2 5 7
Total Industrial 50 100 150
Total 58 104 162
Water balance diagram:

3.10 EMISSIONS AND MITIGATION MEASURES:


3.10.1 PROPOSED WASTE WATER TREATMENT SCHEME:
As per the recommendation received from the CETP of Nandesari Industries Association, the unit
will install the hydrodynamic cavitation process for the treatment of the waste water.

The setup for the hydrodynamic cavitation reactor is given in the figure below: The waste water is
equalised over organic matter and flow. The pH of the waste water is raised to 10 by hydrated lime
and filtered. The waste water is then pumped through a venturi. At the suction side, chlorine is
injected to achieve hydrodynamic cavitation. This is a batch process and the system is kept under
recirculation till the COD is reached to desired limit. This is again filtered in the filter press and the
filtered waste water will be sent to the CETP.
3.10.2 GASEOUS EMISSIONS AND CONTROL:

Table No. 11. Air Emissions from Utilities:

Existing Proposed Proposed Proposed


Sources of
gaseous emissions Boiler Thermic Fluid DG Set
Boiler
heater
Capacity 4 TPH 4 TPH 2 Lac Kcal/hr 500 KVA
Fuel used Agro Waste Agrowaste/ Coal Agrowaste/ Coal HSD
Quantity of fuel 208 Kg/Hr 35 / 15 MT/day 2.2 / 1 MT/day 50 Lts/hr
Stack height 31 m 31 m 31 m 5m
Air pollution Cyclone Cyclone Cyclone Adequate Stack
control unit Separator with Separator with Separator with height
bag filter bag filter bag filter

Details of Air Pollution Control Equipments:

Cyclones followed with Bag filters will be installed as air pollution equipments to bring down the
exhaust emissions from the boilers to the permissible limits stipulated by Gujarat Pollution Control
Board. The multi clone cyclone chamber will comprise of 24 nos. of cyclonic cones. The bag filters
(150 nos.) will be of 200mm ϕ x 3000 mm length. The cleaning mechanism will comprise of Pulse
Jet type.
Table No. 12. Details of Process emissions :
Scrubber has been provided for the existing bromine recovery. Additional 2 stage scrubbers will be
provided for the process emissions.
Existing Existing Proposed Proposed Proposed
Stack attached to Bromination Bromine Reactor Reactor ETP
Reactor Recovery
Column
Gases Scrubbed HBr HBr, Cl2 NH3 HCl, SO2 Cl2
Stack height 6m 6m 12 m 12 m 12 m
No. of stages 2 2 1 2 1
Type of primary scrubber Packed Packed column Packed Packed Packed
Type of Secondary scrubber Packed Packed column -- -- --
Capacity of each scrubber 300 kg/hr 300 kg/hr 300 kg/hr 300 kg/hr 300 kg/hr
Dia of the scrubber 0.8 m 0.8 m 0.8 m 0.8 m 0.8 m
Height of Scrubber 4.5 m 4.5 m 4.5 m 4.5 m 4.5 m
Scrubbing Solution Caustic Lye Caustic Lye Water Caustic Lye Caustic Lye
Fate of the scrubbed liquid To Bromine To ETP To ETP To ETP To ETP
recovery
plant
3.10.3. DETAILS OF HAZARDOUS WASTE GENERATION AND DISPOSAL:
The details of hazardous waste generation and its disposal is given in table no. 13.

Table No. 13. Hazardous waste generation and its disposal:

Sr. Waste Waste Existing Proposed Total Mode of Disposal


No Details Category Quantity Quantity Quantity
MT/Annum MT/Annum MT/Annum
1 ETP 35.3 200 MT 2200 MT 2400 MT Collection, storage,
Sludge transportation and will
be sent for
Coprocessing in
Cement Industry
through NECL
2 Used Oil 5.1 1 MT 1 MT 2 MT Collection, storage,
transportation, disposal
by selling to registered
oil re-refiners or will
be sent for Co-
processing in Cement
Industry through
NECL
3 Liner 33.1 5 MT 17 MT 24 MT Will be used to fill up
Bags ETP sludge or sold to
authorized Scrap dealer
4 Scrubbing 35.1 -- 600 KL 600 KL Will be sent to the ETP
Solution for treatment and
disposal to CETP of
NIA
5 NaBr / -- 3300 MT 3300 MT Sent to the Bromine
HBr Recovery Plant located
Solution inside the premises
6 Process 26.1 -- 1000 MT 1000 MT Collection, storage,
waste transportation and will
residue be sent for
Coprocessing in
Cement Industry
through NECL
7 Spent 26.3 -- 12000 MT 12000 MT Storage, transport and
Acid sale to actual users
with Rule 9 permission
8 Spent 26.4 -- 800 MT 800 MT Storage, transport and
Solvent sale to recyclers
3.11 SCHEMATIC REPRESENTATION OF THE FEASIBILITY DRAWING WHICH
GIVE INFORMATION OF EIA PURPOSE:

4.0 SITE ANALYSIS:

4.1 CONNECTIVITY:

The unit is located in a Designated Chemical Zone of Gujarat Industrial Development Corporation at
Nandesari. GIDC, Nandesari is the only Chemical Estate in Gujarat where all the roads are of concrete
with paved sidings.A very good and efficient network of transport facilities exists for transport of
incoming raw material and outgoing finished goods, since the site is already located in an industrial
estate. The site is only 4 Km from the NH8 connecting Vadodara and Ahmedabad and is only 1 Km
away from Nandesari Railway station and 15 km from Vadodara railway station.
4.2 LANDUSE AND OWNERSHIP

The expansion project will come up on the existing plot of land. The land is already rented by the
promoters of the company. The total plot area is 2960.25 sq. mts.

4.5 SOIL CLASSIFICATION:

Alluvial sandy loam to sandy clay soils are found in the region.

4.6 CLIMATE DATA:

Vadodara district area, in general, being located south of Tropic of Cancer and in transition zone of
heavy rainfall areas of South Gujarat and arid areas of North Gujarat plains, have sub-tropical climate
with moderate humidity. The various season of the year are (a) monsoon - middle of June to October,
(b) winter - November to February, and (c) summer – March to June. From March onwards the
temperature starts rising till it reaches maximum, as high as 41° C in some parts of the district. January
is the coldest month of the year.

4.7 SOCIAL INFRASTRUCTURE:

The entire region including urban as well as rural area show the signs of modernization and
development. The basic parameters like education, water, medicine, post and telegraph
communication road development and power supply are available which decide the measure of this
development.

Educational facilities are available to 100% of the population. All the villages have a minimum of
one primary school. higher secondary education is available with 10 km of any village. There are
several colleges, polytechnic, industrial training schools and other employment oriented training
centres.

All the villages and towns have potable water supply and in 100% area the drinking water is supplied
through taps.
100% of the villages are connected to main commercial and industrial centres by pucca roads. There
is 100% electrification in the area.

The medical facilities are available at almost100% of the human settlements. These facilities are
available in the from of hospital,dispensary, primary health centre, family welfare centres and child
welfare centre.

5.0 PLANNING BRIEF:


5.1 PLANNING CONCEPT:
The unit is located in a Designated Chemical Zone of Gujarat Industrial Development Corporation at
Nandesari. GIDC, Nandesari is the only Chemical Estate in Gujarat where all the roads are of concrete
with paved sidings. The CETP in Nandesari, operated by Nandesari Industries Association, is the
only CETP running on advance oxidation technologies of Hydrodynamic Cavitation which has been
authenticated by NEERI, Nagpur. This CETP has received the permission to treat 12 MLD of waste
water. Now the CETP is expanding its facility from 12 MLD to 20 MLD. The TSDF facility at
GIDC, Nandesari is operated by Nandesari Environment Control Ltd., a subsidiary company of
Nandesaari Industries Association. The TSDF facilities comprises of Landfill facilities and Co-
processing permissions in Various Cement Industries.

Table No. 13: Type of Industries in Nandesari GIDC Estate:


Dye and Dye intermediates manufacturing units 32%
Pharma and Pharma Intermediate manufacturing units 23%
Synthetic Organic Chemical manufacturing Units 22%
Inorganic Chemical manufacturing Units 14%
Recovery Units 4%
Pesticide manufacturing units 3%
Engineering Units 3%
5.2 POPULATION PROJECTION:

Since the 10 Kmradius circle covers part of Vadodara and Anand, the demographic profile of both
the districts is given below:
The details of Vadodara and Anand districts are summarised in the table below:
Table No. 14: District wise Census Details

Table No15: Percentage Decadal Variation in Population for State and Districts (1901 –2011)
Percentage Decadal Variation
District State/District 1901 1911 1921 1931 1941 1951 1961 1971 1981 1991 2001
Code s -11 -21 -31 -41 -51 -61 -71 -81 -91 -01 -11

15 Anand -2.00 1.57 8.79 18.97 20.66 20.37 22.44 23.42 13.39 13.04 12.57
19 Vadodara 18.05 8.32 16.38 19.02 15.92 26.09 29.96 29.58 21.07 19.87 14.16

Table No 16: Sex-Ratio for State and Districts (1901-2011)


District Sex-ratio since (Number of females per 1000 males)
State/Districts
Code 1901 1911 1921 1931 1941 1951 1961 1971 1981 1991 2001 2011
15 Anand 897 865 872 875 896 906 890 880 905 912 910 921
19 Vadodara 914 905 904 902 899 914 906 900 915 913 919 934

5.3 LAND USE PLANNING :


Proper planning will be made for housing the different sections of the plant. The proposed layout of
the plant is given in the figure below:
5.4 ASSESSMENT OF INFRASTRUCTURE DEMAND:

There will be no impact on land resources since the proposed project is coming up in a notified
chemical zone of GIDC, Nandesari.
During the operation phase, the water requirement will be 191 KL/day. The water requirement will
be met from GIDC Water Supply Scheme. Permission for water has already been taken. The power
requirement will be 250 KVA. The demand will be met from MGVCL. The unit will provide
employment to 60 nos of skilled and unskilled workers.

5.5 AMENITIES/ FACILITIES:

The available basic amenities are as under.


a. Education facilities:
The education facility is available in each nearby Nandesari village. The school comprising
of primary and secondary school is run by Nandesari Industries Association

b. Medical facility:
The medical facility are available in the study area. Deepak Medical foundation is running
a full fledged hospital in the estate. Doctors are available round the clock. The advanced
medical treatment is available in nearby Anand and Vadodara Cities

c. Drinking water facility & power supply:


All the villages have potable water supply and in 100 % area the drinking water is supplied
through taps, wells, and tube wells.

d. Post, Telegraph and Telephone facilities:


The government has provided post and telegraph services to most of the village around.
Being a industrialized estate, facilities of Internet, courier services are also available in the
Estate
e. Transport facility:
The proposed area has a good connectivity via state road transport facility due to its
closeness to the national highway

6.0 PROPOSED INFRASTRUCTURE:

6.1 PROCESSING AREA:


For the proposed project, the processing area will cover 760 sqmts.

6.2 NON PROCESSINGAREA

The non-processing area will cover admin building, security cabin, canteen, open space which will
be 1500 sq. mts.

6.3 GREENBELT
A total of 500 sqmt will be used for developing of greenbelt

6.4 SOCIAL INFRASTRUCTURE:


The basic infrastructure facilities provides is as under:
(A) Training & Education: All the employees will be trained and educated periodically about the
hazardous nature of chemicals used in the process. Also, training will be provided for
firefighting, first aid, safe handling of hazardous chemicals.

(B) Medical facility: Pre-employment medical checkup will be undertaken at the time of
employment. In order to safe guard the health of the employees, all the employees undergo
periodic health checkup as the factory act rules.

(C) Drinking water: RO drinking water will be provided to all the employees

(D) Transportation: The unit will provide basic transportation facility for workers.

(E) Telegraph & Post: There will be provision of telephone, fax & internetfacility.

(F) Power supply: 250 KVA electric load will be sourced from MGVCL.
6.5 DRINKING WATERMANAGEMENT:
The employees will be provided with RO water for drinking.

6.6 SEWAGESYSTEM
The domestic sewage (12 KL/day) will be sent to the soak pit.

6.7 INDUSTRIAL WASTEMANAGEMENT


The waste water generated will be first treated inhouse ETP based on hydrodynamic cavitation
as per the technology supplied by the CETP authorities and will then be sent to CETP as per the
inlet norms.

6.8 SOLID WASTEMANAGEMENT


The solid hazardous waste management details are provided in Table No. 13

6.9 POWER REQUIREMENT &SUPPLY


The unit will use total 250 KVA electricity which will be sourced from MGVCL.

7.0 REHABILITATION AND RESETTLEMENT(R &R) PLAN:


The Project is located in the GIDC Estate of Nandesari and does not involve any displacement
of human population

8.0 PROJECT SCHEDULE & COST ESTIMATES


8.1 PROJECT IMPLEMENTATION S
Table No. 17 Project Implementation Schedule
Sr. Activity Required Period
No.
1. Civil work After getting CTE and EC
2. Procurement of machinery After getting EC
3. Erection & installation of machinery After receiving CTE from GPCB
4 Application for CCA 15days before commencement of Trial
5. Commercial activity After receipt of CC&A from GPCB
8.2 ESTIMATED PROJECTCOST

The Estimated cost of Project is Rs 800 Lacs.

9.0 ANALYSIS OF PROPOSAL

It is a proposed project at plot no. 124/34,GIDC, Nandesari. Dist. Vadodara. The unit intends to
manufacture specialty dyes and dye intermediates to the tune of 400 MT/Month. Agrowaste / coal
will be used as a fuel for the proposed project. The domestic waste water will be sent to soak pit and
industrial waste water will be given primary treatment before being discharged to the CETP of NIA,
Nandesari. The solid waste generated from the ETP and other residue and waste from process will be
sent to NECL, whereas recyclable waste will be sent to authorized recyclers. The local manpower
will be used as far as possible.

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