pre feasibility report -...
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PRE FEASIBILITY REPORT
FOR EXPANSION IN
DYES-INTERMEDIATES MANUFACTURING UNIT
PROJECT PROPONENT:
M/s. EQUINOX IMPEXPlot No. C/42, 63+64/6, Near Fire Station,GIDC Estate, , Odhav, Ahmedabad – 382415JULY 2017
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0.0 EXECUTIVE SUMMARY
M/s Equinox Impex is a proposed expansion project located at Plot No. C/42, 63+64/6, GIDCEstate, Near Fire Station, O d h a v , Ahmedabad – 382415 in Gujarat State. M/s Equinox Impex ispromoted by Mr. Vaibhav Shah. Currently, the unit is involved in Blending the dyes with salt.Now, the project proponent intends to manufacture dyes@ 75.00 MT/Month as part of company’spolicy for backward integration.
The project falls under category ‘B’, section 5(f) of EIA notification 2006 and amendment thereof. Thesite is well connected with road and railway with the city Ahmedabad. There is no forest, national park,wildlife sanctuary, eco sensitive areas in surrounding 10 km radius. The project doesn’t fall under CRZboundaries.
1.0 INTRODUCTION OF THE PROJECT BACKGROUND INFORMATION
1.1 Identification of project and project proponent.
M/s Equinox Impex is a proposed expansion project located at Plot No. C/42, 63+64/6, GIDCEstate, Near Fire Station, Odhav, Ahmedabad – 382415 in Gujarat State. The total area for proposedexpansion project is 609.48 m2.
M/s Equinox Impex is promoted by Mr. Vaibhav Shah. The Director plans to manufacture dyes@ 75.00MT/Month.
1.2 Brief description of nature of the project.The project falls under category ‘B’, section 5 (f) of EIA notification September 2006 and amendmentsthereafter. Hence, Environment Clearance is applicable to the proposed expansion project.
1.3 Need for the project and its importance to the country and or regionThe demand for products intended to be manufacture is increasing in the country. The unit will usegood faith efforts to employ local people from the nearby villages depending upon the availability ofskilled & un-skilled man-power surrounding the project site. In operation phase, the project wouldrequire significant work force of non- technical and technical persons. Migration of highly educationand skilled experience will result in increase of literacy in the surrounding villages.
1.4 Demand-Supply GapThe gap between demand and availability of dyes is likely increase over the years. The growing demandand supply gap would require increasing emphasis to be given to the exploration and productionsector. This calls for such projects which can help in bridging the gap. Color adds to the very existenceand intrinsic value of human tribe.
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Synthetic dyes contribute heavily for the use of color. Colour has an inherent element of value additionto a wide variety of products like textiles, leather, paper, food products, cosmetics, plastics, paints, inks.
1.5 Imports. Indigenous productionRaw materials purchase from indigenous production. This helps in the economic development of thecountry to a great level. Thus, to decrease the dependency on imports, the project can work in a positivemanner.
1.6 Export PossibilityYes, we will explore an export possibility of the Dyes. In fact, Indian dyes/intermediates have large exportpotential in the world. The project proponent is already involved in export of various dyes since more than15 years and currently, intends to go for backward integration for manufacturing dyes instead of existingpractice of blending only.
1.7 Domestic/export MarketsOur products have good demand in national/international markets.
1.8 Employment Generation (Direct and Indirect) due to the projectThe proposed expansion project will give direct employment to local people based on qualification andrequirement. In addition to direct employment, indirect employment shall generate ancillary businessto some extent for the local population. In operation phase, the proposed project would requiresignificant work force of non-technical and technical persons. Migration of highly education and skilledexperience will result in increase of literacy in the surrounding villages.
2.0 PROJECT DESCRIPTION2.1 Type of project including interlinked and interdependent projects, if any.M/s Equinox Impex is a proposed expansion project located at Plot No. C/42, 63+64/6, GIDCEstate, Near Fire Station, O d h a v , Ahmedabad – 382415 in Gujarat State. The total area proposedexpansion project is 609.48 m2.
2.2 Location (map showing general location, specific location, and project boundary & project sitelayout) with coordinates.
Coordinate of the Project:
Latitudes Longitudes23° 01’27.28" N 72° 39’1.32” E
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Location of site within 500 m Radius
Location of site within 5-km Radius
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2.3 Details of alternate sites considered and the basis of selecting the proposed site, particularly theenvironmental considerations gone into should be highlighted.
No alternative site study will be carried out as proposed expansion project is located in a well-developed industrial Area of Odhav.•Proximity to Raw Material suppliers.•Site is very well connected by road and railway.• Availability of Power, Water, etc.
2.4 Size or magnitude of operation.The proposed expansion project is small scale industry and plan for manufacturing of dyes. Theproduct details are given below :
T a b l e 1 : P r o d u c t D e t a i l sSr.
No.Name of Products Existing Proposed Total
1 Blending & Mixing of S.O. Dyes withsalt
100Nos./Month
-- 100Nos./Month
2 Reactive Golden Yellow R
-- 50MT/Month
50MT/Month
3 Reactive Golden Yellow HER4 Reactive Orange W3R5 Reactive Orange 2R6 Reactive Fast Magenta7 Reactive Blue RGB8 Reactive Blue 1949 Reactive Blue ME2RL10 Reactive Blue 22211 Reactive Blue 20312 Reactive Red 19413 Reactive Red 19514 Reactive Red 19615 Reactive Red WB16 Reactive Red CD17 Reactive Black B18 Reactive Blue 5RH
-- 25MT/Month
25MT/Month
19 Reactive Yellow 16020 Reactive Red 22321 Reactive Violet 5R22 Reactive Orange H2R23 Reactive Orange 122AA
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2. 5 Project description with process details (a schematic diagram, flow chart showing theproject layout, components of the project etc. should be given)
All the dyes manufactured here are manufactured by same type of processes. The basic difference in theprocess to achieve different product is addition of raw material according to stoichiometric requirement andthe temperature at which the reaction is carried out. The typical process for manufacturing dyes is asfollows:
MANUFACTURING PROCESS
1. Diazotization:Primary Diazo chemical like (Sulfo V.S/Vinyl Sulphone/K-Acid/PCVS/Sulpho Tobias Acid, Tobias Acid, 4ADAPSA, H Acid etc) are to be diazotized in acidic medium using HCL and reducing temperature by Ice andSodium Nitrite to be added to complete diazo Diazotization. This diazo is then to be used to couple withvarious coupling components.
2. Coupler solution and Coupling:Coupler solution are to be prepared by suspending coupling components like (H-Acid/ J-Acid/MPDSA/MUA/Sodium Napthonate) are suspended in ice and desired pH is to be adjusted by usingSoda Bicarbonate into ready coupler solution. Diazo components is added and stirring is to be done uptocompletion of coupling. This procedure to be carried out once or twice as per the product.
3. Cyanuration: (Optional)Cyanuric Chloride is been used as a material for cyanuration. Cyanuration is done according to productrequirement. At 0-10 °C cooling is done with ice.
4. Condensation: (Optional)Condensation is done to cyanurated dye solution with H-Acid, Ammonia, Vinyl Sulphone etc is beencomplete by adding soda ash powder at room temperature
5. Metallization: (Optional)The ready Dye solution obtained from coupling procedure is subject to Metallization using Metal Salt likeCopper Sulphate to finish the metallization reaction.
6. FiltrationThe dye that remains by filtration is sent for Spray Dryer.
7. Spray DryingThe concentrated mass produced after all the process is transferred into spray dryer holding tank and thensprayed.
8. Strength Equilisation and StandardizationThe said obtained crude due strength into be equalisation by adding Salt and then tobe blended to obtain as per the parties standard requirement.
9. Packing & LabellingThe standard dye is to be packed and labeled as per party requirement
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Process Flow Diagram
1. Reactive Golden Yellow R:
2. Reactive Golden Yellow HER:
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3. Reactive Orange W3R:
4. Reactive Orange 2R:
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5. Reactive Fast Magenta:6.
7. Reactive Blue RGB:
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8. Reactive Blue 194:
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9. Reactive Blue ME2RL:
10. Reactive Blue 222:
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11. Reactive Blue 203:
12. Reactive Red 194:
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13. Reactive Red 195:
14. Reactive Red 196:
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15. Reactive Red WB:
16. Reactive Red CD:
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17. Reactive Black B:
18. Reactive Blue 5RH:
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19. Reactive Yellow 160:
20. Reactive Red 223:
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21. Reactive Violet 5R:
22. Reactive Orange H2R:
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23. Reactive Orange 122AA:
2.6 Raw material required along with estimated quantity, likely source, marketing area of finalproducts, Mode of transport of raw Material and Finished Product.We shall procure the raw material from domestic market by roads. Finished Product will betransported using roadways.
Table 2: List of Raw MaterialsSr.
No. Name of Products Existing Proposed(MT/Month)
Total(MT/Month)
1 Liquid S. O. Dyes 250KL/Month
-- 250KL/Month
2 Sulpho Vinyl Sulphone (Sulpho V.S.) -- 14.82 14.823 PCVS (Para Cresidine Vinyl Sulphone) -- 12.825 12.8254 Sodium Nitrite -- 9.293 9.2935 Hydrochloric Acid (HCl) – 30% -- 39.9 39.96 J - Acid -- 13.537 13.5377 Caustic Flaks -- 6.65 6.658 Sodium Bicarbonate (SBC) -- 31.5 31.59 Vinyl Sulphone (V.S.) -- 37.275 37.27510 Cyanuric Chloride -- 12.35 12.3511 H - Acid -- 22.42 22.4212 Sulpho Tobias Acid (STA) -- 17.115 17.11513 Tobias Acid -- 9.135 9.13514 Anthranilic Acid -- 7.22 7.22
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Sr.No. Name of Products Existing Proposed
(MT/Month)Total
(MT/Month)15 4 ADAPSA -- 10.83 10.83
16 MPDSA (Meta Phenylene Di Amine 4 – SulphonicAcid) -- 24.36 24.36
17 DMAVS -- 15.33 15.3318 OAVS (Ortho Anisidine Vinyl Sulphone) -- 12.635 12.63519 Picramic Acid (PA) -- 5.7 5.720 Sodium Napthonate -- 22.68 22.6821 C Acid -- 17.64 17.6422 MUA (Meta Uerido Aniline) -- 5.13 5.13
23 DASDA (4,4 Di Amino Stilbene 2,2 Disulphonic Acid) --5.7 5.7
24 Sodium Carbonate (Soda Ash) -- 7.928 7.92825 Ammonia (30%) -- 5.04 5.0426 Copper Sulfate -- 5.7 5.727 Hydrogen Peroxide -- 5.7 5.728 Sodium Chloride (Salt) -- 42 4229 2 Pyridone -- 4.2 4.230 Acetic Anhydride -- 5.985 5.98531 N.M.J. Acid -- 3.135 3.135
2.7 Resource optimization / recycling and reuse envisaged in the project, if any, should bebriefly outlined.We shall explore the reuses/recycling of effluent from the expansion project.
2.8 Availability of water its source, Energy/power requirement and source should be given.Water Source:The source of water for the proposed expansion project shall meet through GIDC Odhav. Totalwater requirement for the proposed expansion project will be 27.5 KLD. The total waste watergenerations from Industrial shall be 12.1 KLD & 0.44 KLD Domestic effluents shall be disposed throughseptic tank & Soak pit. Details of water consumption and waste water generation are given below.
Table 3: Water Balance
Sr.No.
Description
Water Consumption(KL/Day)
Waste Water Generation(KL/Day)
Existing Proposed Total Existing Proposed Total
I Domestic 0.3 0.7 1.0 0.24 0.2 0.44II Industriala. Process 0.0 18 18 0.0 5.0 5.0b. Washing 0.0 7.0 7.0 0.0 7.0 7.0c. Boiler 0.0 1.5 1.5 0.0 0.1 0.1
Total (I+II) 0.3 27.2 27.5 0.24 12.3 12.54*Domestic Waste Water will be discharged off to the septic tank / soak pit system.** The effluent generation from the proposed expansion project shall be 12.1 KL/day. The effluentwill be segregated as follows:
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High Concentrated Effluent: High concentrate process effluent @ 5.00 KL/Day will be sent to common MEE/Spray Drier for evaporation.
Low Concentrated Effluent: Low concentrated effluent from Washing and Boiler effluent @ 7.1 KL/Day willbe sent to ETP for Primary treatment and then it would be disposed off to CETP; or reject would be sent tocommon MEE /Spray Drier for evaporation.Surplus quantity of industrial effluent would be spray dried at in-house spray drier.
Electricity Requirement:Electricity shall be obtained from Torrent. Agro Waste shall be used as a fuel for Boiler; Coal andNatural Gas shall be used for Hot Air Generator. The total power & fuel requirement for theproposed expansion project are given below:
Table 3: Source of ElectricitySr. No. Source Total
1. Torrent Power 110 kW
Table 4: Fuel Requirement
Sr.No. Description Fuel Existing Proposed APCM
1. Hot Air Generator
NaturalGas -- 1000 SCM/day --
Coal -- 100 kg/hr CycloneSeparator
2. Boiler (1 TPH) AgroWaste/Briquette
s-- 50 kg/hr Cyclone
Separator
2.9 Quantity of wastes to be generated (liquid and solid) and scheme for theirManagement/disposal.
Solid & Hazardous waste generation & Management planHazardous waste generated from the process & maintenance. Empty drums and bags is hand over toauthorize vender for further recycle. The Management of Hazardous waste will be done as perHazardous Waste Management Rules 2008.
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Table5: List of Hazardous Waste
Sr.No.
Type ofWaste Category
Quantity
Mode of DisposalExisting Proposed Total
1Discarded Drum/Containers Bags
with liner33.3 4000
Nos./Month3000
Nos./Month7000
Nos./Month
Send back to rawmaterials supplier or Sold
to registered recycler
2. Used 5.1 5 Lit/Year 2 Lit/Year7
Lit/YearSold to Registered
reprocessor
3.ETP 34.30 -- 5.00
MT/Year5.00
MT/Year
Collection, Storage,Transportation, Disposal
at TSDF site.
4.Solid Waste
(Ash) - -- 4.50MT/Month 4.50 MT/Month
Sold to brickmanufacturer or cement
manufacturer
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3.0 SITE ANAYSIS3.1 Connectivity.
Site is very well connected by road and railway. Availability of water, power, etc.
3.2 Land Form, Land Use and Land OwnershipLand Form: Proposed expansion project site is within the industrial area, Odhav.Land use: Industrial
3.3 Topography (along with map).The topography map of the area shall be provided at a later stage.
3.4 Existing land use pattern (agriculture, non-agriculture, forest, (includingarea under CRZ)), shortest distances from the periphery of
water bodiesthe project to
periphery of the forests, national park, wildlife sanctuary, eco sensitive areas, water bodies (distancefrom HFL of the river),CRZ. In case of the notified industrial area, a copy of the Gazettenotification should be given. The project falls inside the notified industrial area, Odhav, Ahmedabad. There is no forest, national
park, wildlife sanctuary, eco sensitive areas in surrounding 10 Km of the plant boundary. CRZ is not applicable to the project.
3.5 Existing InfrastructureSite is very well connected by road Proximity to Raw Material suppliers
3.6 Soil ClassificationIt will be incorporated in EIA studies.
3.7 Climatic data from secondary sources.It shall be incorporated in EIA studies.
3.8 Social infrastructure available.Depending on the growth of the company the required social infrastructure will be provided.
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4.0 PLANNING BRIEF4.1 Planning Concept (type of industries, facilities, transportation etc) Town and Countryplanning/Development authority classification.
Type of Industry: Synthetic Organic Chemical Industries
5.2 PopulationProjectionWe will include in EIA Report.
5.3 Land use planning (break up along with green belt etc.)
Total Plot Area – 609.48 m2.
5.4 Assessment of Infrastructure Demand (Physical & Social)On the basis of the preliminary site visit, the infrastructure demand in the villages was assessed on the basis of needand priority. Employment would be as per prevailing norms of state government for skilled and unskilled people forthe proposed expansion project activity.
5.5 Amenities/FacilitiesProper site services such as First Aid, Canteen and Drinking Water will be provided to the workers.
5.0 PROPOSED INFRASTRUCTURE5.1 Industrial Area (Processing Area)Please refer Plant Layout as Annexure III.
5.2 Residential Area (Non Processing Area)Please refer Plant Layout as Annexure III.
5.3 Green BeltRequired greenbelt area will be provided.
5.4 Social InfrastructureDepending on the growth of the company the required social infrastructure will be provided.
5.5 Connectivity (Traffic and Transportation Road/Rail/Metro/Waterways etc)Road and railways are very close to the working site. There is no proposal to make any new kind of connectivity.
5.6 Drinking water Management (Source &Supply of water)Water requirement will meet through the GIDC
5.7 Sewerage SystemDomestic waste water will be treated into septic tank followed by soak pit.
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5.8 Industrial Waste ManagementPlease refer point no. 2.9 of pre-feasibility report for Industrial Waste Management.
Details of Effluent Treatment Plant:
The industrial effluent (7100 Liter/day) shall be treated in ETP.Finally, it would be disposed off to CETP; or reject would be sent to common MEE /Spray Drier for evaporation.Surplus quantity of industrial effluent would be spray dried at in-house spray drier.Domestic effluent would be disposed off in septic tank / soak pit .
Sr.no Name of the Unit Nos. Capacity
1 Collection cum Neutralization tank 1 5000 Litres
2 Primary Settling Tank 1 10000 liters
3 Holding tank 1 10000 liters
5 Chemical Solution Tank 3 200 Litres, each
6 Dual Media filter 1 400 mm dia
7 Treated water storage tank 1 20000 liters
Description of ETP process:
The raw effluent from the plant is collected in collection cum neutralization tank. Effluent is neutralized in this tank withlime & FeSO4 with stirring. The neutralized effluent is then pumped to the hopper bottom settling tank. Thesupernatant effluent from the settling tank is collected in a holding sump of adequate size. The effluent is then pumpedto the filter press. Then treated effluent goes to CETP.
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5.8 Industrial Waste ManagementPlease refer point no. 2.9 of pre-feasibility report for Industrial Waste Management.
Details of Effluent Treatment Plant:
The industrial effluent (7100 Liter/day) shall be treated in ETP.Finally, it would be disposed off to CETP; or reject would be sent to common MEE /Spray Drier for evaporation.Surplus quantity of industrial effluent would be spray dried at in-house spray drier.Domestic effluent would be disposed off in septic tank / soak pit .
Sr.no Name of the Unit Nos. Capacity
1 Collection cum Neutralization tank 1 5000 Litres
2 Primary Settling Tank 1 10000 liters
3 Holding tank 1 10000 liters
5 Chemical Solution Tank 3 200 Litres, each
6 Dual Media filter 1 400 mm dia
7 Treated water storage tank 1 20000 liters
Description of ETP process:
The raw effluent from the plant is collected in collection cum neutralization tank. Effluent is neutralized in this tank withlime & FeSO4 with stirring. The neutralized effluent is then pumped to the hopper bottom settling tank. Thesupernatant effluent from the settling tank is collected in a holding sump of adequate size. The effluent is then pumpedto the filter press. Then treated effluent goes to CETP.
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5.8 Industrial Waste ManagementPlease refer point no. 2.9 of pre-feasibility report for Industrial Waste Management.
Details of Effluent Treatment Plant:
The industrial effluent (7100 Liter/day) shall be treated in ETP.Finally, it would be disposed off to CETP; or reject would be sent to common MEE /Spray Drier for evaporation.Surplus quantity of industrial effluent would be spray dried at in-house spray drier.Domestic effluent would be disposed off in septic tank / soak pit .
Sr.no Name of the Unit Nos. Capacity
1 Collection cum Neutralization tank 1 5000 Litres
2 Primary Settling Tank 1 10000 liters
3 Holding tank 1 10000 liters
5 Chemical Solution Tank 3 200 Litres, each
6 Dual Media filter 1 400 mm dia
7 Treated water storage tank 1 20000 liters
Description of ETP process:
The raw effluent from the plant is collected in collection cum neutralization tank. Effluent is neutralized in this tank withlime & FeSO4 with stirring. The neutralized effluent is then pumped to the hopper bottom settling tank. Thesupernatant effluent from the settling tank is collected in a holding sump of adequate size. The effluent is then pumpedto the filter press. Then treated effluent goes to CETP.
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5.9 Solid Waste Management
Sr.No.
Type ofWaste Category
QuantityMode ofDisposalExisting Proposed Total
1 DiscardedDrum/Containers Bagswith liner 33.3
4000Nos./Month
3000Nos./Month
7000Nos./Month
Send back toraw materialssupplier or Soldto registeredrecycler
2. Used 5.1 5 Lit/Year 2 Lit/Year7
Lit/Year
Sold toRegisteredreprocessor
3. ETP 34.30 -- 5.00MT/Year
5.00MT/Year
Collection.Storage,Transportation,Disposal atTSDF site.
4. Solid Waste(Ash) - -- 4.50
MT/Month4.50
MT/Month
Sold to brickmanufacturer orcementmanufacturer
5.10 Power Requirement & Supply/Source
Sr. No. Source Total1. Torrent Power 110 kw
6.0 REHABILITATION AND RESETTLEMENT(R & R) PLAN6.1 Policy to be adopted (Central/state) in respect of the project affected persons includinghomeoustees, landoustees and land less laborers.Not Applicable because the proposed expansion project site within the GIDC Odhav, Ahmedabad.
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7.0 PROJECT SCHEDULE &COST ESTIMATES
7.1 Likely date of start of construction and likely date of completion (Time schedule for the project tobe given).We shall start construction for expansion activity after getting amendment in environmental clearanceand amendment in consent to establish. We shall start production upon making application foramendment in CCA.
7.2 Estimated Project cost along with analysis in terms of economic viability of the project.Total Project Cost for proposed expansion project activity is Rs. 1.17 Crore.
8.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)8.1 Financial and social benefits with special emphasis on the benefit to be local peopleincluding tribal population, if any, in the area.The project will be prove time by time for beneficial to the people as the company progress andexpands its activity. By CSR activity company management will committed to improve infrastructuralfacilities for the local people like Educational facilities, Medical facilities, and Transportation facilitiesetc. as well the local people especially tribal population will be taken as employers which will improvethe socio economic environment of the area.
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ANNEXURE-ICC&A COPY
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CTE-AMMENDMENT
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ANNEXURE-IIGIDC ALLOTMENT LETTER
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ANNEXURE-IIGIDC ALLOTMENT LETTER
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ANNEXURE-IIGIDC ALLOTMENT LETTER
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ANNEXURE-IIIPLANT LAYOUT
Site Plan