Precious Metals Recovery LLC RCRA Permit Application Dry Hills ...
Precious Metals Recovery LLC RCRA Permit Application Dry Hills ... Precious Metals Recovery LLC RCRA Permit Application Dry Hills ...
H - 340940 Precious Metals Recovery LLC Dry Hills Facility Project Stream Tables for RCRA Application Rev. C December 11, 2012 Flowsheet 1400-05-030-0005 Note 1 Notes 1, 2 Note 1 Notes 1, 2 Note 1 Note 3 Note 4 Notes 1, 2 Stream Number 107 167 168 258 301 302 303 305 351 452 Stream Name Hygiene Tank Off-gas - Hygiene Gas - Gas - Retort Caustic Leach Caustic Leach Area Area Circuit Tank Off-gas - Waste Solution Treatment Building Ventilation - HVAC Hygiene Off-gas to Atmosphere Dust Collector Dust to Retort Hygiene Gas to Compressed Air Dust Collector - Distribution Tank Off-gas - Waste Solution Storage Tank Annual Throughput lb/yr 6,616 -- -- -- -- -- 6,285 6,616 TBD -- Slurry lb/yr 0 0 0 0 0 0 0 0 0 0 % Solids wt% -- -- -- -- -- -- -- -- -- -- Solids lb/yr 6,616 0 0 0 0 331 6,285 6,616 0 0 Hg2Cl2 wt% 3.9% -- -- -- -- 3.9% 3.9% 3.9% -- -- HgO wt% 28.0% -- -- -- -- 28.0% 28.0% 28.0% -- -- HgS wt% 8.4% -- -- -- -- 8.4% 8.4% 8.4% -- -- S wt% 2.8% -- -- -- -- 2.8% 2.8% 2.8% -- -- Solution lb/yr 0 0 0 0 0 0 0 0 0 0 Hg 2+ g/L -- -- -- -- -- -- -- -- -- -- NaOH g/L -- -- -- -- -- -- -- -- -- -- HCl g/L -- -- -- -- -- -- -- -- -- -- Cl - g/L -- -- -- -- -- -- -- -- -- -pH -- -- -- -- -- -- -- -- -- -- Elemental Mercury lb/yr 0 0 0 0 0 0 0 0 0 0 Gas (Annual Average) scfm 2,200 150 6,000 20 2,000 10,800 0 8,200 TBD 100 N2 vol% 78.2% 74.0% 78.2% 78.1% 78.2% 78.1% -- 78.2% 78.0% 78.1% O 2 vol% 20.8% 19.7% 20.8% 20.8% 20.8% 20.7% -- 20.8% 21.0% 20.8% Hg (v) vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% -- 0.0% 0.0% 0.0% H 2O (v) vol% 1.0% 6.3% 1.0% 1.2% 1.0% 1.2% -- 1.0% 0.0% 1.2% SO 2 vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% -- 0.0% 0.0% 0.0% Notes: 1 - Assume mercury level to be at 0.1 mg/Nm 3 (OSHA level) for design purposes. 2 - Assume tank ventilation gas to have a relative humidity of 50% 3 - Design dust emission limit is 0.02 gr/dscf. Design mercury emission limit is 1.0 x 10 -5 gr/dscf. 4 - Compressed air requirements for equipment to be determined in detailed engineering when vendor data becomes available.
H - 340940 Precious Metals Recovery LLC Dry Hills Facility Project Stream Tables for RCRA Application Rev. C December 11, 2012 Flowsheet 1500-05-030-0001 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Stream Number 351 352 353 354 355 356 357 358 360 361 362 363 Stream Name Compressed Air - Dust Collector Compressed Air - Filter Press Compressed Air - Caustic Leach Circuit Pumps Compressed Air - Instrument Header Compressed Air - Retort Compressed Air - Utility Stations Compressed Air - Caustic Soda Receiving Pump Compressed Air - Hydrochloric Acid Receiving Pump Compressed Air - Waste Solution Collection Pump Compressed Air - Waste Solution Settling Tank O/F Pump Compressed Air - Waste Solution Settling Tank U/F Pump Annual Throughput lb/yr TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD Slurry lb/yr 0 0 0 0 0 0 0 0 0 0 0 0 % Solids wt% -- -- -- -- -- -- -- -- -- -- -- -- Solids lb/yr 0 0 0 0 0 0 0 0 0 0 0 0 Hg 2Cl 2 wt% -- -- -- -- -- -- -- -- -- -- -- -- HgO wt% -- -- -- -- -- -- -- -- -- -- -- -- HgS wt% -- -- -- -- -- -- -- -- -- -- -- -- S wt% -- -- -- -- -- -- -- -- -- -- -- -- Solution lb/yr 0 0 0 0 0 0 0 0 0 0 0 0 Hg 2+ g/L -- -- -- -- -- -- -- -- -- -- -- -- NaOH g/L -- -- -- -- -- -- -- -- -- -- -- -- HCl g/L -- -- -- -- -- -- -- -- -- -- -- -- g/L -- -- -- -- -- -- -- -- -- -- -- -pH -- -- -- -- -- -- -- -- -- -- -- -- Elemental Mercury lb/yr 0 0 0 0 0 0 0 0 0 0 0 0 Gas (Annual Average) scfm TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD N2 vol% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% Cl - O 2 vol% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% Hg (v) vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% H 2O (v) vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% SO2 Notes: vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 1 - Compressed air requirements for equipment to be determined in detailed engineering when vendor data becomes available. Compressed Air - Treated Water Discharge Pump
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- Page 283 and 284: APPENDIX 1-D Floor and Wall Sealant
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- Page 287 and 288: 8" THICK INSULATED PRECAST CONCRETE
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- Page 291 and 292: 2. PRODUCTS 2.1 Stonclad GS Stoncla
- Page 293 and 294: APPENDIX 2-A Waste Analysis Plan
- Page 295 and 296: WASTE ANALYSIS PLAN 1 PURPOSE AND S
- Page 297 and 298: Table 1: Analytical Methods for the
- Page 299 and 300: All wastes received will have been
- Page 301 and 302: Waste will not be accepted until th
- Page 303 and 304: Table 3: Waste Sampling Matrix Type
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- Page 309 and 310: eevaluated whenever the process tha
- Page 311 and 312: ATTACHMENT 2-A-1 Profile Instructio
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- Page 315 and 316: • Is the waste pyrophoric? a See
- Page 317 and 318: EPA's Chemical Compatibility Chart
- Page 319 and 320: 1.0 SCOPE AND APPLICATION METHOD 90
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- Page 323 and 324: METHOD 9045D SOIL AND WASTE pH 9045
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- Page 327 and 328: 10.0 REFERENCES 1. National Bureau
H - 340940<br />
<strong>Precious</strong> <strong>Metals</strong> <strong>Recovery</strong> <strong>LLC</strong><br />
<strong>Dry</strong> <strong>Hills</strong> Facility Project<br />
Stream Tables for <strong>RCRA</strong> <strong>Application</strong> Rev. C<br />
December 11, 2012<br />
Flowsheet 1500-05-030-0001<br />
Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1<br />
Stream Number 351 352 353 354 355 356 357 358 360 361 362 363<br />
Stream Name<br />
Compressed<br />
Air - Dust<br />
Collector<br />
Compressed<br />
Air - Filter<br />
Press<br />
Compressed Air<br />
- Caustic Leach<br />
Circuit Pumps<br />
Compressed<br />
Air - Instrument<br />
Header<br />
Compressed<br />
Air - Retort<br />
Compressed<br />
Air - Utility<br />
Stations<br />
Compressed<br />
Air - Caustic<br />
Soda<br />
Receiving<br />
Pump<br />
Compressed<br />
Air -<br />
Hydrochloric<br />
Acid Receiving<br />
Pump<br />
Compressed<br />
Air - Waste<br />
Solution<br />
Collection<br />
Pump<br />
Compressed<br />
Air - Waste<br />
Solution<br />
Settling Tank<br />
O/F Pump<br />
Compressed<br />
Air - Waste<br />
Solution<br />
Settling Tank<br />
U/F Pump<br />
Annual Throughput lb/yr TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD<br />
Slurry lb/yr 0 0 0 0 0 0 0 0 0 0 0 0<br />
% Solids wt% -- -- -- -- -- -- -- -- -- -- -- --<br />
Solids lb/yr 0 0 0 0 0 0 0 0 0 0 0 0<br />
Hg 2Cl 2 wt% -- -- -- -- -- -- -- -- -- -- -- --<br />
HgO wt% -- -- -- -- -- -- -- -- -- -- -- --<br />
HgS wt% -- -- -- -- -- -- -- -- -- -- -- --<br />
S wt% -- -- -- -- -- -- -- -- -- -- -- --<br />
Solution lb/yr 0 0 0 0 0 0 0 0 0 0 0 0<br />
Hg 2+<br />
g/L -- -- -- -- -- -- -- -- -- -- -- --<br />
NaOH g/L -- -- -- -- -- -- -- -- -- -- -- --<br />
HCl g/L -- -- -- -- -- -- -- -- -- -- -- --<br />
g/L -- -- -- -- -- -- -- -- -- -- -- -pH<br />
-- -- -- -- -- -- -- -- -- -- -- --<br />
Elemental Mercury lb/yr 0 0 0 0 0 0 0 0 0 0 0 0<br />
Gas (Annual Average) scfm TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD TBD<br />
N2 vol% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0% 78.0%<br />
Cl -<br />
O 2 vol% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0% 21.0%<br />
Hg (v) vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0%<br />
H 2O (v) vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0%<br />
SO2 Notes:<br />
vol% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0% 0.0%<br />
1 - Compressed air requirements for equipment to be determined in detailed engineering when vendor data becomes available.<br />
Compressed<br />
Air - Treated<br />
Water<br />
Discharge<br />
Pump
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