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 1300-05-030-0001 Note 1 Note 1 Note 1 Note 1 Note 1 Note 1 Stream Number 5 6 7 8 10 11 Stream Name Calomel Delivered Spent Activated Carbon Delivered Elemental Mercury Delivered Elemental Mercury from Retort Calomel Slurry to Caustic Leach Circuit Spent Activated Carbon to Retort Annual Throughput lb/yr 612,000 240,000 62,000 389,000 612,000 240,000 Slurry lb/yr 612,000 0 0 612,000 % Solids wt% 70% -- -- 70% Solids lb/yr 428,400 240,000 0 0 428,400 240,000 Hg 2Cl 2 wt% 100% 0% -- -- 100% 0% HgO wt% 0% 0% -- -- 0% 0% HgS wt% 0% 23% -- -- 0% 23% S wt% 0% 8% -- -- 0% 8% Solution lb/yr 183,600 0 0 0 183,600 0 Hg 2+ g/L 2.7 -- -- -- 2.7 -- NaOH g/L 0.0 -- -- -- 0.0 -- HCl g/L 7.8 -- -- -- 7.8 -- Cl - g/L 8.8 -- -- -- 8.8 -pH -0.2 -- -- -- -0.2 -- Elemental Mercury lb/yr 0 0 62,000 389,000 0 0 Gas (Annual Average) scfm 0 0 0 0 0 0 N2 vol% -- -- -- -- -- -- O 2 vol% -- -- -- -- -- -- Hg (v) vol% -- -- -- -- -- -- H 2O (v) vol% -- -- -- -- -- -- SO 2 vol% -- -- -- -- -- -- Notes: 1 - Maximum annual throughput
H - 340940 Precious Metals Recovery LLC Dry Hills Facility Project Stream Tables for RCRA Application Rev. C December 11, 2012 Flowsheet 1300-05-030-0002 Note 1 Note 1 Stream Number 50 51 52 55 56 57 357 358 Stream Name Caustic Soda Delivered Hydrochloric Acid Delivered TMT 15 Delivered Caustic Soda to Decomposition Tank Caustic Soda to Hydrochloric Acid to SO2 Scrubber Waste Solution Tank Compressed Air to Caustic Soda Receiving Pump Compressed Air to Hydrochloric Acid Receiving Pump Annual Throughput lb/yr 259,838 13,000 19,970 115,518 144,320 13,000 TBD TBD Slurry lb/yr 0 0 % Solids wt% -- -- Solids lb/yr 0 0 0 0 0 0 0 0 Hg2Cl2 wt% -- -- -- -- -- -- -- -- HgO wt% -- -- -- -- -- -- -- -- HgS wt% -- -- -- -- -- -- -- -- S wt% -- -- -- -- -- -- -- -- Solution lb/yr 259,838 13,000 19,970 115,518 144,320 13,000 0 0 g/L 0.0 0.0 0.0 0.0 0.0 0.0 -- -- NaOH g/L 766.2 0.0 1.3 766.2 766.2 0.0 -- -- HCl g/L 0.0 356.4 0.0 0.0 0.0 356.4 -- -- Hg 2+ Cl - g/L 0.0 346.6 0.0 0.0 0.0 346.6 -- -pH 13.7 -1.0 12.5 13.7 13.7 -1.0 -- -- Elemental Mercury lb/yr 0 0 0 0 0 0 0 0 Gas (Annual Average) scfm 0 0 0 0 0 0 TBD TBD N2 vol% -- -- -- -- -- -- 78.0% 78.0% O 2 vol% -- -- -- -- -- -- 21.0% 21.0% Hg (v) vol% -- -- -- -- -- -- 0.0% 0.0% H 2O (v) vol% -- -- -- -- -- -- 0.0% 0.0% SO2 Notes: vol% -- -- -- -- -- -- 0.0% 0.0% 1 - Compressed air requirements for equipment to be determined in detailed engineering when vendor data becomes available.
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- Page 283 and 284: APPENDIX 1-D Floor and Wall Sealant
- Page 285 and 286: C8 x 11.5 EPOXY COATING ON 2" THICK
- Page 287 and 288: 8" THICK INSULATED PRECAST CONCRETE
- Page 289 and 290: C8 x 11.5 EPOXY COATING ON 2" THICK
- 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
- Page 305 and 306: 9 LDR TREATMENT STANDARDS Waste Des
- Page 307 and 308: Drummed consolidation waste will be
- Page 309 and 310: eevaluated whenever the process tha
- Page 311 and 312: ATTACHMENT 2-A-1 Profile Instructio
- Page 313 and 314: PMR LLC 460 W. 50 North Suite 500 S
- 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
- Page 321 and 322: 7.2.3 Adjust the electrodes in the
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 1300-05-030-0002<br />
Note 1 Note 1<br />
Stream Number 50 51 52 55 56 57 357 358<br />
Stream Name<br />
Caustic<br />
Soda<br />
Delivered<br />
Hydrochloric<br />
Acid Delivered<br />
TMT 15<br />
Delivered<br />
Caustic Soda to<br />
Decomposition<br />
Tank<br />
Caustic Soda to Hydrochloric Acid to<br />
SO2 Scrubber Waste Solution Tank<br />
Compressed Air to<br />
Caustic Soda<br />
Receiving Pump<br />
Compressed Air to<br />
Hydrochloric Acid<br />
Receiving Pump<br />
Annual Throughput lb/yr 259,838 13,000 19,970 115,518 144,320 13,000 TBD TBD<br />
Slurry lb/yr 0 0<br />
% Solids wt% -- --<br />
Solids lb/yr 0 0 0 0 0 0 0 0<br />
Hg2Cl2 wt% -- -- -- -- -- -- -- --<br />
HgO wt% -- -- -- -- -- -- -- --<br />
HgS wt% -- -- -- -- -- -- -- --<br />
S wt% -- -- -- -- -- -- -- --<br />
Solution lb/yr 259,838 13,000 19,970 115,518 144,320 13,000 0 0<br />
g/L 0.0 0.0 0.0 0.0 0.0 0.0 -- --<br />
NaOH g/L 766.2 0.0 1.3 766.2 766.2 0.0 -- --<br />
HCl g/L 0.0 356.4 0.0 0.0 0.0 356.4 -- --<br />
Hg 2+<br />
Cl -<br />
g/L 0.0 346.6 0.0 0.0 0.0 346.6 -- -pH<br />
13.7 -1.0 12.5 13.7 13.7 -1.0 -- --<br />
Elemental Mercury lb/yr 0 0 0 0 0 0 0 0<br />
Gas (Annual Average) scfm 0 0 0 0 0 0 TBD TBD<br />
N2 vol% -- -- -- -- -- -- 78.0% 78.0%<br />
O 2 vol% -- -- -- -- -- -- 21.0% 21.0%<br />
Hg (v) vol% -- -- -- -- -- -- 0.0% 0.0%<br />
H 2O (v) vol% -- -- -- -- -- -- 0.0% 0.0%<br />
SO2 Notes:<br />
vol% -- -- -- -- -- -- 0.0% 0.0%<br />
1 - Compressed air requirements for equipment to be determined in detailed engineering when vendor data becomes available.
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