Kana Aroma Industries. Pre-Feasibility Report

Transcription

1 Pre-Feasibility Report

2 1. INTRODUCTION M/s. is a proposed unit to be located at Shed no. C1-41/B/1 & 2, GIDC Industrial Estate, Nandesari, Vadodara, Gujarat and proposes to manufacture Allyl Iso Thiocynate, Benzhydrol, 4-Methyl Cyclohexanol, 4- Methyl Cyclohexanone, Styrene Oxide, Phenyl Ethyl Chloride, P- Tertiary Butyl Cyclohexyl Acetate, Phenyl Ethyl Propionate, Phenyl Ethyl Butyrate, Phenyl Ethyl Iso Butyrate, Phenyl Ethyl Formate, Phenyl Ethyl Benzoate, Phenyl ethyl methyl Ether, Phenyl Ethyl Alcohol, 2- Methoxy Naphthalene, Allyl Caproate, Benzyl Alcohol, Benzyl Acetate, Amyl Salicylate, Iso Amyl Salicylate, Methyl Salicylate, Cinnamaldehyde, Hexyl Salicylate and Cetyl Chloride. The company is located on a plot measuring sq. mt. 2. COST OF PROJECT: The estimated cost of the project for the proposed expansion is estimated around Rs. 6 cr. 3. PRODUCTION CAPACITY Production capacity is prescribe below: List of Products Name Of Product Quantity (MT/Month) 01 Allyl iso thiocynate Benzhydrol methyl cyclohexanol methyl cyclohexanone Styrene oxide Phenyl ethyl chloride P- tertiary butyl cyclohexyl acetate Phenyl ethyl propionate / acetate Phenyl ethyl butyrate Phenyl ethyl iso butyrate Phenyl ethyl formate Phenyl ethyl benzoate Phenyl ethyl methyl Ether Phenyl ethyl alcohol methoxy naphthalene Allyl caproate 2.0

3 17 Benzyl alcohol Benzyl acetate Amyl salicylate Iso amyl salicylate Methyl salicylate Cinnamaldehyde Hexyl salicylate Cetyl chloride Woody Sol 9.5 TOTAL LIST OF RAW MATERIALS no. Raw material Quantity (MT/Month) Methyl cyclohexanol Acetaldehyde Acetic Acid Allyl Alcohol Allyl chloride Amyl Alcohol Benzaldehyde Benzoic Acid Benzophenone Benzyl chloride Beta naphthol Butyric Acid Caproic Acid Caustic lye Caustic Soda Cetyl Alcohol Di methyl sulphate Formic acid Hexanol Hydrogen Peroxide Iso amyl alcohol Iso Butyric Acid Methanol Para cresol Para tertiary butyl cyclohexanol PD Catalyst Phenyl Ethyl Alcohol Propionic Acid PTC PTSA 0.261

4 31. R.N. Catalyst Salicylic Acid SBC Sodium acetate Sodium carbonate Sodium thiocynate Solvent Styrene Styrene Oxide TEA Thionyl chloride BRIEF PROCESS Discussed in Form No 1 in Annexure II 6. WATER CONSUMPTION & WASTE WATER GENERATION Source of water: GIDC, Nandesasri. Source Water Consumption KL/Day I Domestic 2 II Gardening 1 II Industrial R. O. Reject 9.5 a. 1.) Process 7 2.) Boiler make up 10 b. Cooling tower make up 10 c. Washings 6 Total Industrial 42.5 Total 45.5 Total water consumption for the proposed activities will be 45.5 KLD out of which gardening & domestic water consumption will be 3 KLD and 42.5 KLD will be industrial water consumption.

5 Details of waste water generation: Source wastewater Generation KL/Day I Domestic 1.6 II Industrial (a) Process 9.5 (b) Cooling 5.0 (c) Boiler 4.0 (d) R.O reject 9.5 (e) Scrubber 2.0 III Washing 6.0 Sub Total (II+III) 36.0 Total (I+II+III) 37.6 Total waste water generation will be 37.6 KLD, out of which 1.6 KLD will be domestic effluent, which will be sent to soak pit KLD will be industrial effluent, which will be given treatment in ETP and sent to CETP Nandesari for its further treatment and disposal. 7. SOURCE OF POLLUTION Details of Air Pollution The main source of air pollution will be from stack under the Air Act, Proper stack height required for proper atmosphere dispersion. Height provided for stack is as per the pollution control norms. Air pollution is basically generated from Boiler, THF & Process vents and fugitive emissions due to raw material transfer. Boiler will be equipped with stacks of suitable height and to control process emission unit will provide scrubber followed by stack with suitable height and monitoring facility. Flue gas Emission/stack Stack attached to 1. Boiler 2. TFH (2 Lac Kcal) 3. Stack Height (m) 30 mt. Fuel Type Coal (on a dry basis) Coal (on a dry basis) Fuel consumption rate 4 MT/Day 4 MT/Day Stack Dia 0.6 m APCM Multicyclone / Bagfilter DG Set 11 mt. Diesel 15 Lit./Hr. 0.3 m N.A. Probable pollutants SO2, NOx, PM SO2, NOx, PM SO2, NOx, PM

6 Process gas Emission/stack Stack attached to Stack Height APCM Probable pollutants (m) 1. Reaction vessel 11 mt. Caustic scrubber HCL & SO2 SOURCE AND DISPOSAL OF HAZARDOUS WASTES Mainly generated from ETP. Summary of waste and ultimate disposal are summarized below: 1 Waste Details Discarded Barrels Waste Category Generation (/Year) MT/Yr. 2 Used oil KL/Yr. 3 Spent catalyst MT/Yr. 4 ETP sludge MT/Yr. 5 Distillation residue MT/Yr. Mode of Disposal and disposal to GPCB authorised recyclers. and reused within premises for lubrication purposes. and disposal to suppliers for reactivation. and disposal to TSDF and disposal to incineration ETP Sludge will be sent to TSDF, NECL, Nandesari for its disposal. 8. FUNDS FOR POLLUTION CONTROL MEASURES The management will contribute adequate funds for the pollution control measures. Necessary provision for Environmental management system will be part of practice in proposed project. Rs. 80 lacs will be used for Environment Management System. 9. MONITORING FACILITIES Air sampling will be done by outside agency and will be part of practice in future expansion projects.

7 10. CONCLUSION There will be no adverse impact on the ground water environment due to the operation of the project, as the project is located in GIDC. The air environment will have negligible effect due to the activities related to the operation of the project. The project will not contribute any adverse impact on the surrounding soil, as the pollutants emitted are of the negligible amount. Biodiversity in the surrounding area of the project will not be affected due to the operation of the project, as the pollutants emitted are of negligible amount. The project will generate direct and indirect employment.