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HomeMy WebLinkAboutDEQ-CFW_00088435DEQ-CFW 00088435 I , , , Form D: Process Information (Page 1 of 2) Facility ID# 0900009 North Carolina Department of Environment and Natural Resources Division of Air Quality 1998 Annual Air Pollutant Emissions Inventory 1. Source ID No(s): NS-7 (NS-E in Title V) 3. Process Description: "Nafion" Liquid Waste Stabilization 4. Operational Schedule: Hour per Day Day per Week 5. Start Hour of Process: Continuous 6. Percentage Annual Throughput: Dec -Feb 25 Mar -May 25 2. Permit Item No(s): (3b) Weeks per Year June -Aug 25 7. Maximum Process 8. Annual Process Rate per Hour: (ex: Throughput: gal/hr, mmcf/hr) 250 Ib/hr (ex: lb/yr, gal/yr) include units 9. Capture Efficiency (% of Process Emissions Vented Through Control Device): 100% Hours per g,760 Year Sept -Nov 25 1,552,326 lb 10. Control Device Descriptions Primary Caustic Scrubber NCD-1 (Title V NCD-Hdr1) Secondary 11. Combined Control Device Efficiency (%): 99.6% 12. ANNUAL FUEL USAGE (e.g. Coal, oil, wood, natural gas, etc.) - Use additional sheets if necessary • include units DEQ-CFW 00088436 Form 9: Process Information (Page 2 of 2) Facility ID# 0900009 Actual Emissions per Pollutant Listed for Source Described Above: Attach calculations and documentation of emission factors or other estimation methods used. i • • Source ID # NS-7 "Per Ton" Pollutant: 'Per)PM-10 SO2 IVOx VOC CO Actual Emissions: Tons/year 0.67 ***All Other HAPs/TAPs as listed in Appendix C or Appendix D (use additional sheets if necessary)*** Pa(lntant OAS Num Actin'{L13.tY ear} Caiixients Chlorine 7782-50-5 Fluorine 7782-41-4 Hydrazine 302-01-2 Hydrogen Chloride 7647-01-0 Hydrogen Fluoride 7664-39-3 2.98 Hydrogen Sulfide 7783-06-4 Lead Compounds LEADCPDS Methyl Chloroform 71-55-6 Methylene Chloride 75-09-2 Ozone 10028-15-6 Perch loroethylene 127-18-4 Phosphine 7803-51-2 Ammonia 7664-41-7 0 F-113 Information on Page 2 of Form D cannot be held confidential. DEQ-CFW 00088437 0 1998 - Waste Fluorocarbon Tanks Emissions This system includes the Waste Fluorocarbon Storage Tank (Receiver), Reactor Tank, Shipping Tank, and Catch Tank Neutralized waste mixed fluorocarbon generated in 1998 = 1,552,326 lb. Waste Fluorocarbons generated in 1998 = 315, 621 The KOH as 45 wt. % 1,131,900 lb. Water added to process for maintenance reasons 1,452 lb. Miscellaneous material shipped as RCRA waste for billing reasons, but was not RCRA waste. 103,640 lb. WASTE FLUOROCARBON STORAGE TANK (RECEIVER TANK) EMISSIONS BASIS: • Tank Volume = 1150 gallons = 153.7 cu. ft. • Control of venting tank high pressure is locked out until pressure >_ 700 kPa = 101.5 psig • Maintenance vents can be done to allow for work to be done on the system using the 0 service manifold. • Both emergency vents and maintenance vents go to Waste Gas Scrubber • Fluorocarbon liquid SPG = 1.4 Summary - maintenance vents and pressure relief device vent. HF Emissions* - assume that all vapor is HF (MW=20) and is scrubber in WGS at 99.6% efficiency. Actual emissions = 2.95 lb. HF/yr VOC emissions* — Assume vapor is Freon® 113 (MW = 187) and scrubber has no effect. Actual emissions = 1346 lb. F-133/yr = 0.67 Ton/yr 'Calculation is based on change in pressure and tank weight during the venting time frame. See attached spreadsheet. DEQ-CFW 00088438 . WASTE FLUOROCARBON REACTOR TANK EMISSIONS 11 • BASIS: • Tank Volume = 1150 gallons = 153.7 cu. ft. • Control of venting tank high pressure is locked out until pressure >_ 700 kPa = 101.5 psig • Maintenance vents can be done to allow for work to be done on the system using the service manifold. • Both emergency vents and maintenance vents go to Waste Gas Scrubber • Fluorocarbon liquid SPG = 1.4 No emissions of material from reactor are present for 1998. WASTE FLUOROCARBON SHIPPING TANK EMISSIONS Neutralizing waste fluorocarbons generates nonvolatile water soluble fluorocarbon salts. The shipping tank vents to the waste gas scrubber which would remove any acidic or water soluble component that might enter the scrubber. There are no emissions from this shipping tank for 1998. SUMMARY WASTE F/C TANK SYSTEM (NS-7) EMISSIONS B/YR BF VOCs Storage Tank Receiver 2.95 1346 Reactor Tank 0 0 Shipping Tank 10 0 DEQ-CFW 00088439 s 0 1998 Vent Emissions L�dt'cs. for F/C Waste S stem Y Date P1, kPa = P2, kPa = W1, kg = W2, kg = loss W, lb. _ VAP SPACE (ft^3), calc n1-n2 (Ibmol) = If HF, Ib. Add delta W for HF is positive change If F-113, lb. Add delta W for F113 is positive change 7-Apr-98 171 9 1235 1132 226.6 122.63 0.51 10.17 236.77 95.10 321.70 10-Apr-98 231 0 1341 1355 -30.8 119.95 0.71 14.19 132.65 28-Jun-98 880 800 3500 3362 303.6 65.53 0.13 2.68 306.28 25.10 328.70 24-Jul-98 442 395 2187 2210 -50.6 98.63 0.12 2.37 22.19 8-Au -98 332 173 2401 2430 -63.8 93.24 0.38 7.59 70.97 18-Aug-98 326 97 2198 2137 134.2 98.35 0.58 11.53 145.73 107.82 242.02 48.54 688.79 453.84 892.43 Assume constant temp = 528 R Use R = 73.98 ft^3 * kPa / Ibmol / deg R TOTAL as HF ass umin 99.6% efficiencyon scrubber, lb = 2.95 TOTAL as F-113, lb. = 1346.27 2/26/99 Emissions Calcs