Pre-Feasibility Report M/s. Veer Poly Chem 0
1. Introduction M/s. Veer Polychem is an existing unit located at Plot 119 & 120, Ranpur road, GIDC Dhandhuka, Dist: Ahmedabad, Gujarat. Currently, unit is producing copper sulphate with capacity of 100 MT/month. Now the unit proposes to expand its production capacity by adding pesticide products, different types of dyes & resin. 2. Cost of Project Total Cost of project is 3.0 crore out of which 0.5 crore will be used for Environment Management System. 3. Production Capacity Production capacity is prescribe below: Name of Product List of Products Quantity (MTPM) Existing Proposed Total 1. Copper Sulphate 100 0 100 2. Solvent Black 5 (Nigrosine Black SS) 3. Solvent Black 7 (Nigrosine Black Oil soluble) 4. Acid Black 2 (Nigrosine Black water soluble) 0 300 300 0 100 100 0 100 100 5. Plaster of Paris 0 220 220 6. Phenol Formaldehyde Resin 0 50 50 7. PF Moulding Powder 0 50 50 8. 2, 4-D Acid (Technical) 0 20 20 9. 2,4-D Ethyl Ester (Technical) 0 20 20 4. List of Raw Materials List of raw material is given below: Total 100 860 960 List of Raw Materials Name of Product Quantity (MT/month) Existing Proposed Total Solvent Black 5 300 MT/month 1 Aniline oil 0 153.95 153.95 2 NitroBenzene 0 152.07 152.07 M/s. Veer Poly Chem 1
3 Hydrochloric Acid 0 182.73 182.73 4 Ferrous Chloride 0 22.76 22.76 Solvent Black 7 100 MT/month 1 Solvent Black -5 Moist Material 0 158.24 158.24 2 NaOH 0 20.33 20.33 Acid Black 2 100 MT/month 1 Solvent black 5 Crude 0 91.98 91.98 2 H 2 SO 4 0 181.68 181.68 3 NaOH 0 14.12 14.12 Plaster of Paris 220 MT/month 1 Calcium Hydroxide 0 119.97 119.97 Phenol Formaldehyde Resin 50 MT/month 1 Phenol 0 26.25 26.25 2 Formaldehyde (37%) 0 27.50 27.50 3 NaOH 0 0.50 0.50 PF Moulding Powder 50 MT/month 1 P.F Resin 0 23.00 23.00 2 Hexamine 0 7.25 7.25 3 MgO 0 1.50 1.50 4 Additives 0 3.00 3.00 5 Filler 00 15.50 15.50 2, 4-D Acid (Technical) 20 MT/month 1 2,4 D Sodium salt 0 24.0 24.0 2 HCl(30%) 0 11.4 11.4 2,4-D Ethyl Ester (Technical) 20 MT/month 1 2, 4-D Acid 0 18.0 18.0 2 Sulphuric Acid 0 9.26 9.26 3 Ethyl Alcohol 0 1.2 1.2 5. Manufacturing Process Given as Annexure II in application form-1. 6. Manpower Total manpower requirement at all level of plant is 10 & additional manpower 50, so total manpower after proposed expansion will be 60. M/s. Veer Poly Chem 2
7. Water Consumption & Waste Water Generation Source Water consumption Water Consumption (KL/day) Existing Proposed addition Total I Domestic 1.5 3.5 5.0 II Greenbelt 1.0 3.0 4.0 III Industrial i) Process 1.5 54.15 55.65 ii) Washing 0 10.0 10.0 iii) Cooling 0 7.0 7.0 iv) Boiler 0 4.0 4.0 v) Scrubber 0 3.0 3.0 Total Industrial 1.5 78.15 79.65 Total (I+II+III) 4.0 84.65 88.65 Less recycle 0 0 62.4 Actual fresh water consumption 0 0 26.25 Source Wastewater Generation Wastewater Generation (KL/day) Existing Proposed addition Total I Domestic 1.0 3.0 4.0 II Greenbelt 0 0 0 III Industrial i) Process 0 51.6 51.6 ii) Washing 0 10.0 10.0 iii) Cooling 0 2.0 2.0 iv) Boiler 0 0.5 0.5 Total Industrial 0 64.1 64.1 Total (I+II) 1.0 67.1 68.1 M/s. Veer Poly Chem 3
8. Source of Pollution Details of Air Pollution Main source of air pollution will be from stack attached with Boiler & HAG. Coal/ Bio fuel (Briquette) will be used as fuel. Cyclone & bag filter will be installed as APCM. Process emission will be from stack attached to Reaction vessel of Acid black 2, where 2 stage water scrubbers will be installed as APCM. Proper stack height will be provided for proper atmospheric dispersion of pollutants. Details of stacks and APCM are given in below table. Existing Stack attached to 1. Hot Air Generator Stack Height in m Fuel Used Fuel consumption rate APC measure Pollutant 11 Wood 15 MT/month Cyclone SPM<150 mg/nm 3 SO 2 < 100 ppm NOx<50 ppm Proposed 1. Boiler (2 nos.) 21 Coal/ Bio 30 MT/month Cyclone SPM<150 mg/nm 3 (0.5 TPH) fuel & bag SO 2 < 100 ppm 2. Hot Air (Briquette) 15 MT/month filter NOx<50 ppm Generator 2. D G Set (25 kva) 3. Reaction vessel of Acid black 2 11 HSD 15 lit/hr. -- 21 -- -- 2 stage water scrubber HCl < 20 mg/nm 3 Source and disposal of waste water Source of wastewater generation is mainly from process, washing & utility. Wastewater generated from dyes and resin process will be completely recycle in close loop and w/w from pesticide products will be sent to ETP along with w/w from washing & utility. After primary treatment, it will be evaporated and recovered condensate will be reuse/recycle. Domestic effluent is disposed off into soak pit through septic tank. M/s. Veer Poly Chem 4
Source and disposal of Hazardous wastes Summary of waste and ultimate disposal are summarized below: Name of Waste Category Quantity Disposal method 1. ETP sludge & Evaporation salt 36.3 3.0 MT/month Collection, Storage, Transportation & Disposal at TSDF site 2. Used oil 5.1 25 lit/annum Collection, Storage, Transportation and disposal by selling to authorized re-refiners 3. Discarded containers/ drums Liners 33.3 250 nos./month 9. Funds for pollution control measures 0.1 T/month Collection, Storage, Transportation and disposal by selling to authorized recycler The management is quite conscious of its responsibility for maintaining clear environment adequate funds can be provided for the pollution control measures as financing part of overall expansion. Necessary provision for Environmental management system is in practice and will be part of practice in future expansion projects. 10. Monitoring facilities Air sampling will be done by outside agency and will be part of practice in future expansion projects. 11. Conclusion On the basis of information presented in the pre-feasibility report on pollution control measures and after its implementation, there will be no discharge of effluent and air emission from the plant beyond the norms specified by the Board as per the provisions of Air (Prevention and Control of Pollution) Act, 1981 and Water (Prevention and Control of Pollution) Act, 1974. M/s. Veer Poly Chem 5