unilex colours and chemicals...
TRANSCRIPT
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
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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
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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:
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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
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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.
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
Waste Disposal:
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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
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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.
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72°43'54.03"E4 19°48'0.52"N
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(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.
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Synthesis Scheme
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Flow Chart & Material balance
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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.
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Synthesis scheme
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Flow char and material balance
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(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
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(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.
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
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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
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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
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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
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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
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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
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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
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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
Unilex Colours And Chemicals Ltd. Nov. ‐2017
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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.
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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
Unilex Colours And Chemicals Ltd. Nov. ‐2017
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