Minutes of the 37th Meeting of the Expert Appraisal Committee ...

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332(Part), 333 (Part), 334-360, 466-500, Village Hirodih, P.S. Jainagar, District Kodarma inJharkhand by M/s Jupiter Ispat Private Limited - regarding Environmental ClearanceThe project authorities and their consultant, M/s Visiontek Consultants, Bhubaneswar gave adetailed presentation on the salient features of the project and proposed environmental protectionmeasures to be undertaken as per Terms of References (TORs) awarded during the 9 th meeting of theExpert Appraisal Committee (Industry - 1) held on 7 th – 8 th April, 2010for preparation of EIA/EMP.Theproposed project is a Category B project as per the Schedule of EIA Notification 2006 and appraised bythe SEIAA/SEAC. However, due to absence of SEIAA for Jharkhand, the proposal is appraised by theExpert Appraisal Committee (Industry-1) of MoEF.M/s Jupitar Ispat Limited have proposed for setting up of Coke Oven Plant (2,37,600 TPA), Coalwashery (6,6000 TPA), slurry washery (5,28,000 TPA) and Captive Power Plant (6 MW) at VillageHirodih, P.S. Jainagar, District Kodarma, Jharkhand. Proposed plant will be set up in 40 acres and theland is acquired on lease from M/s Jupitar Spun Pipe Company Private Limited. Green belt will bedeveloped in 14.00 acres out of total 40 acres. No national park/wild life sanctuary/reserve forest islocated within 10 Km.Akto Nadi and Barakar River flow at a distance of 1.5 km and 4 km respectivelyfrom the project site. Kodarma town is at 10.5 km. Total cost of the project is Rs. 88.65 Crores. Rs. 3.6Crores and Rs. 0.29 Crores are earmarked towards capital cost and recurring cost per annum forpollution control measures.Following will be manufactured:SLManufacturing ItemsPlant CapacityTPDTPAManufacturing Technology1 Low Ash Coke 720 2,37,600 Non Recovery Coke Ovens2 Coal Washery 200 66,000 Wet media barrel separation3 Slurry Washery 1600 5,28,000 Through hydro & froth flotation4 Captive Power Plant 6 MW Through WHRB from coke ovenCoal (66,000 TPA) and slack coal (5,28,000 TPA) will be used as raw materials.MoU with BharatCoking Coal Ltd. for supply of coal is submitted. Power (6.0 MW) will be sourced initially from JSEB andfrom captive power plant at later stage. D.G. sets (500 KVA and 200 KVA) will be installed foremergency use.Coal will be burnt for manufacturinglow ash coke. After processing, coke will be takenout and air quenched. Traveling grate type circular sinter machine will be used for sintering of fines.Captive power plant (WHRB) will be installed to make use of flue gases generated from the coke oven.Ambient air quality monitoring was carried within the study area for PM 10 , SO 2 and NOx. Themaximum values of these parameters are 42.0µg/m 3 , 18.19 µg/m 3 and 22.89 µg/m 3 respectively. Theresults of the modeling study indicates that the maximum increase of GLC for the proposed project is0.046 µg/m 3 with respect to the PM 10 , 0.07 µg/m 3 with respect to the SO 2 and 0.035 µg/m 3 with respectto the NOx. The GLC predicted at all receptor locations after the proposed expansion are within theNAAQS.Particulate matter will increase due to grinding and burning process. Down draft system withtunnel and complete combustion of flue gases will be installed in coke ovens to control particulatematters. Non-recovery type of coke oven will be provided with external combustion and recuperatorsystem to recover sensible heat from outgoing flue gases before escaping from the chimney and used inpower generation through WHRB. Poly-aromatic hydrocarbon (PAH) will be burnt in the coke oven itself.Dedusting system and water sprinkler will be provided to control fugitive emissions.Total ground water requirement from bore wells and RWH will be 623 m 3 /day. Permission forground water drawl has been obtained from CGWA, New Delhi vide letter No. 21-4(85)/MER/CGWA/2011-3439, dated 19.04.2012. No liquid effluent will be generated and dischargeddue to adoption of closed loop system. Only make up water will be fed into the plant. The treatedeffluent will be used for ash conditioning, dust suppression and green belt development. Service water
will be passed through oil separator to remove oil content in the effluent. Domestic effluent will betreated in septic tank followed by soak pit. No effluent will be discharged outside the premises and Zerodischarge will be adopted. The rejects from coal washery and slurry washery will be sold to Briquetteplant/ red bricks manufacturing units and the dust from APCD will be partly reused in process and thebalance is sold to FBC units. Waste/used/spent oil and used batteries will be sold to authorized recyclers/ re-processors.Public hearing/Public consultation meeting was conducted by the Jharkhand State PollutionControl Board (JSPCB) on 23 rd October 2011. The issues raised in the public hearing meeting werew.r.t. provision of pollution control measures, employment to locals, drinking water, education, healthfacilities, tree plantation etc. and have been addressed in the EIA/EMP.After detailed deliberation, the Committee recommended the project for environmental clearancesubject to submission of revised diagram of coke oven plant and stipulation of following specificconditions along with other environmental conditions:1. Efforts shall be made to reduce RSPM levels in the ambient air and a time bound action planshall be submitted. On-line ambient air quality monitoring and continuous stack monitoringfacilities for all the stacks shall be provided.2. Stack monitoring facilities for all the major stacks and adequate air pollution control systems viz.dust catchers or cyclones, Multi stage scrubber, bag filters etc. to control particulate emissions twithin the prescribed limits from coke oven shall be provided. Carbon mono-oxide (CO) shall alsobe monitored alongwith other parameters and standards notified under E (P) Act shall befollowed. The reports shall be submitted to the Ministry’s Regional Office at the Bhubaneswar,CPCB and SPCB.3. Multi stage scrubber shall be installed to control gaseous and dust emission from the coke ovenstack. Measures shall be taken to prevent leakages from the coke oven plant.4. The prescribed emission standards for coke oven plants, as notified vide notification no. GSR 46(E) dated 3 rd February, 2006 and subsequently amended shall be complied with.5. In-plant control measures like bag filters, de-dusting and dust suppression system shall beprovided to control fugitive emissions from all the vulnerable sources. Dust extraction andsuppression system shall be provided at all the transfer points, coal handling plant and cokesorting plant of coke oven plant. Bag filters shall be provided to hoods and dust collectors to coaland coke handling to control dust emissions. Water sprinkling system shall be provided to controlsecondary fugitive dust emissions generated during screening, loading, unloading, handling andstorage of raw materials etc.6. Secondary fugitive emissions shall be controlled within the prescribed limits, regularly monitoredand records maintained. Guidelines / Code of Practice issued by the CPCB in this regard shall befollowed.7. Vehicular pollution due to transportation of raw material and finished product shall be controlled.Proper arrangements shall also be made to control dust emissions during loading and unloadingof the raw material and finished product. Efforts shall also be made to reduce impact of thetransport of the raw materials and end products on the surrounding environment includingagricultural land. All the raw materials including fly ash shall be transported in the closedcontainers only and shall not be overloaded. Vehicular emissions shall be regularly monitoredand records kept.8. Total requirement of the water shall not exceed 623 m 3 /day. All the treated wastewater shall berecycled for dust suppression and green belt development. Domestic wastewater shall be treatedin septic tank followed by soak pit and used for green belt development. Zero effluent dischargeshall be strictly followed and no wastewater shall be discharged outside the premises.
Page 1: Minutes of the 37 th Meeting of the
Page 5 and 6: ix.Electrostatic precipitator (ESP)
Page 7 and 8: No.TPA12EXISTINGSponge IronPlantInd
Page 9 and 10: 10. Slag produced in Ferro Manganes
Page 11: iv.Total water requirement shall no
Page 15 and 16: Project activityClinker ProductionC
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Page 39 and 40: The various technological advantage
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ii.iii.iv.The National Ambient Air
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viii.ix.Efforts shall be made to ma
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diagram. If surface water is used f
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There will be emissions during hand
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36. A plan for the utilization of w
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The TORs prescribed shall be valid
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25. Mass balance for the raw materi
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62. Disaster Management Plan includ
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CementProductionCaptive PowerPlanti
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38. Ambient air quality monitoring
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70. Any litigation pending against
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LIST OF PARTICIPANTS IN 37 th EAC (
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Minutes of the 37th Meeting of the Expert Appraisal Committee ...

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