Water_Treatment_Capacities.xlsx
XLSX spreadsheet 53 KB Posted
- Solicitation number
- FA3016-18R-0020
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Water Treatment Capacity - Please ensure to view all tabs
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| File | Type | Posted |
|---|---|---|
| FA3016-18-R-0020-0001.pdf | ||
| Question_and_Answers_for_Proposal_-_Answers.pdf | ||
| SOW_Chemical_-_Approved2.pdf | ||
| FA3016-18-R-0020.pdf |
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LAK Condenser
| Attachment 2 | ||||||
| Installation | System Type | Bldg | Cooling Cpacity (Ton AC) | Condenser water flow rate (Gal/Min) | Condenser Water Make up rate (Gal/Year) | Cycles of Concentration |
| LAK | Condenser | 133 | 460 | 1380 |
1230984383C: 1230984383C:
3 GPM/ton 8,122,680.00 1230984383C: 1230984383C:
Blowdown = make up + evaporation
Assume chillers run 70% of the time.
Blowdown= Cond GPM x 60min/hr x24 hr/dayx 365 dys /year x .7 x .006 =GPM x 2207.
.006= blowdown rate coeficient for 10 deg F delta T, 5 cycles (HVAC rules of thumb book. Page 244)
Evaporation rate = .03GPM/ton x ton x 60 min/hr x 24 hr/day x 365 days/year x .7 = ton x 11037
(p. 243 HVAC rules of thumb book); assumes tower is efficient, worst case evaporation rate = worst case condenser water usage.
| 4-5 | ||||
| LAK | Condenser | 147 | 84 | 252 |
1230984383C: 1230984383C:
3 GPM/ton 1,483,272.00 1230984383C: 1230984383C:
Blowdown = make up + evaporation
Assume chillers run 70% of the time.
Blowdown= Cond GPM x 60min/hr x24 hr/dayx 365 dys /year x .7 x .006 =GPM x 2207.
.006= blowdown rate coeficient for 10 deg F delta T, 5 cycles (HVAC rules of thumb book. Page 244)
Evaporation rate = .03GPM/ton x ton x 60 min/hr x 24 hr/day x 365 days/year x .7 = ton x 11037
(p. 243 HVAC rules of thumb book); assumes tower is efficient, worst case evaporation rate = worst case condenser water usage.
| 4-5 | ||||||
| LAK | Condenser | 315 | 115 | 345 | 2,030,670.00 | 4-5 |
| LAK | Condenser | 9122 | 150 | 450 | 2,648,700.00 | 4-5 |
| LAK | Condenser | 9225 | 300 | 900 | 5,297,400.00 | 4-5 |
| LAK | Condenser | 9085 | 280 | 840 | 4,944,240.00 | 4-5 |
| LAK | Condenser | 10056 | 1000 | 3000 | 17,658,000.00 | 4-5 |
| LAK | Condenser | 9110 | 450 | 1350 | 7,946,100.00 | 4-5 |
| LAK | Condenser | 9210 | 450 | 1350 | 7,946,100.00 | 4-5 |
| LAK | Condenser | 9310 | 450 | 1350 | 7,946,100.00 | 4-5 |
| LAK | Condenser | 9410 | 450 | 1350 | 7,946,100.00 | 4-5 |
| LAK | Condenser | 7535 | 500 | 1500 | 8,829,000.00 | 4-5 |
| LAK | Condenser | 6578 (ATC 1) | 400 | 1200 | 7,063,200.00 | 4-5 |
| LAK | Condenser | 6586 (ATC 2) | 400 | 1200 | 7,063,200.00 | 4-5 |
| LAK | Condenser | 6588 (ATC 3) | 400 | 1200 | 7,063,200.00 | 4-5 |
| LAK | Condenser | 6496 (ATC 4) | 400 | 1200 | 7,063,200.00 | 4-5 |
| LAK | Condenser | 6582 (DCF 1) | 478 | 1434 | 8,440,524.00 | 4-5 |
| LAK | Condenser | 6592 (DCF 2) | 478 | 1434 | 8,440,524.00 | 4-5 |
| LAK | Condenser | 5570 | 385 | 1155 | 6,798,330.00 | 4-5 |
| LAK | Condenser | 2443 | 320 | 960 | 5,650,560.00 | 4-5 |
| LAK | Condenser | 1417 | 900 | 2700 | 15,892,200.00 | 4-5 |
| LAK | Condenser | 1385 | 280 | 840 | 4,944,240.00 | 4-5 |
| LAK | Condenser | 954 | 220 | 660 | 3,884,760.00 | 4-5 |
| LAK | Condenser | 2028 | 300 | 900 | 5,297,400.00 | 4-5 |
| LAK | Condenser | 2014 | 1000 | 3000 | 17,658,000.00 | 4-5 |
| LAK | Condenser | 2000 | 2000 | 6000 | 35,316,000.00 | 4-5 |
| LAK | Condenser | 5616 | 240 | 720 | 4,237,920.00 | 4-5 |
| LAK | Condenser | 7429 | 540 | 1620 | 9,535,320.00 | 4-5 |
| LAK | Condenser | 7355* | 600 | 1800 | 10,594,800.00 | 4-5 |
| LAK Total | 239,619,060.00 |
* Currently not in use and will not be in use in the foreseeable future
Lackland Heat Pump Loop
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| Lackland | Heat pump condenser loop | 315 | 600 |
LAK Steam
| Installation | System Type | Bldg | Output Capacity (1000 Lb Steam/Hr) | Steam Boiler Make Up Water rate Gal/yr | Cycles of Concentration |
| LAK | Steam | 150 | 1600 | 2,355,200.00 |
1230984383C: 1230984383C:
Steam make up = 4 GPM/1000 lb/hr assume boilers run 70% of the time
| Gal/yr = lb/hr x 4 GPM/1000 lb/hr x 60 min/hr x 24 hr/day x 365 days/ yr x .7 = lb/hr x 1472 | 7-9 | |||||
| LAK | Steam | 9085 | 3600 | 5,299,200.00 | 7-9 | |
| LAK | Steam | 9310 | 3600 | 5,299,200.00 | 7-9 | |
| LAK | Steam | 9410 | 3600 | 5,299,200.00 | 7-9 | |
| LAK | Steam | 7065 | 3600 | 5,299,200.00 | 7-9 | |
| LAK | Steam | 2041 | 1170 | 1,722,240.00 | 7-9 | |
| LAK | Steam | 2000 | 16000 | 23,552,000.00 | 7-9 | |
| LAK Total | 48,826,240.00 |
LAK Chilled Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| LAK | Chilled Water | 133 | 5260 |
| LAK | Chilled Water | 147 * | 1500 |
| LAK | Chilled Water | 315 | 7360 |
| LAK | Chilled Water | 9122* | 2000 |
| LAK | Chilled Water | 9225* | 2000 |
| LAK | Chilled Water | 9085* | 4800 |
| LAK | Chilled Water | 10904 | 3780 |
| LAK | Chilled Water | 10056* | 18600 |
| LAK | Chilled Water | 9110 | 4800 |
| LAK | Chilled Water | 9210 | 4800 |
| LAK | Chilled Water | 9310 | 4800 |
| LAK | Chilled Water | 9410 | 4800 |
| LAK | Chilled Water | 7535 | 3600 |
| LAK | Chilled Water | 6578 (ATC 1) | 7200 |
| LAK | Chilled Water | 6586 (ATC 2) | 7200 |
| LAK | Chilled Water | 6588 (ATC 3) | 7200 |
| LAK | Chilled Water | 6496 (ATC 4) | 7200 |
| LAK | Chilled Water | 6582 (DCF 1) | 3420 |
| LAK | Chilled Water | 6592 (DCF 2) | 3420 |
| LAK | Chilled Water | 7065 | 4800 |
| LAK | Chilled Water | 5570 | 4800 |
| LAK | Chilled Water | 2443 | 3200 |
| LAK | Chilled Water | 1417* | 4700 |
| LAK | Chilled Water | 1385 | 2100 |
| LAK | Chilled Water | 954 | 1700 |
| LAK | Chilled Water | 2041 | 1480 |
| LAK | Chilled Water | 2028* | 3060 |
| LAK | Chilled Water | 2014* | 7200 |
| LAK | Chilled Water | 2000* | 23800 |
| LAK | Chilled Water | 5616 | 1280 |
| LAK | Chilled Water | 7429* | 7300 |
| LAK | Chilled Water | 7359 | 6500 |
| 175660 |
*Suspected Leaks
LAK Hot Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| LAK | Hot water | 147 | 1500 |
| LAK | Hot water | 9122* | 2000 |
| LAK | Hot water | 9225* | 2000 |
| LAK | Hot water | 9085* | 4800 |
| LAK | Hot water | 10904 | 3780 |
| LAK | Hot water | 9110 | 4800 |
| LAK | Hot water | 9210 | 4800 |
| LAK | Hot water | 9310 | 4800 |
| LAK | Hot water | 9410 | 4800 |
| LAK | Hot water | 7535 | 3600 |
| LAK | Hot water | 6578 (ATC 1) | 7200 |
| LAK | Hot water | 6586 (ATC 2) | 7200 |
| LAK | Hot water | 6588 (ATC 3) | 7200 |
| LAK | Hot water | 6496 (ATC 4) | 7200 |
| LAK | Hot water | 6582 (DCF 1) | 3420 |
| LAK | Hot water | 6592 (DCF 2) | 3420 |
| LAK | Hot water | 7065 | 4800 |
| LAK | Hot water | 5570 | 4800 |
| LAK | Hot water | 1415 | 4700 |
| LAK | Hot water | 1385 | 2100 |
| LAK | Hot water | 954 | 1700 |
| LAK | Hot water | 2041 | 1480 |
| LAK | Hot water | 2028* | 3060 |
| LAK | Hot water | 5616 | 1280 |
| LAK | Hot water | 7429* | 7300 |
| 103740 |
FSH Condenser
| Installation | System Type | Bldg | Cooling Cpacity (Ton AC) | Condenser water flow rate (Gal/Min) | Condenser Water Make up rate (Gal/Year) | Cycles of Concentration |
| FSH | Condenser (pH control) | 1472 | 4900 | 14700 | 86,524,200.00 |
1230984383C: 1230984383C:
Blowdown = make up + evaporation
Assume chillers run 70% of the time.
Blowdown= Cond GPM x 60min/hr x24 hr/dayx 365 dys /year x .7 x .006 =GPM x 2207.
.006= blowdown rate coeficient for 10 deg F delta T, 5 cycles (HVAC rules of thumb book. Page 244)
Evaporation rate = .03GPM/ton x ton x 60 min/hr x 24 hr/day x 365 days/year x .7 = ton x 11037
(p. 243 HVAC rules of thumb book); assumes tower is efficient, worst case evaporation rate = worst case condenser water usage.
| 4-5 | ||||||
| FSH | Condenser (pH control) | 3315 | 1300 | 3900 | 22,955,400.00 | 4-5 |
| FSH | Condenser (pH control) | 1377 | 1000 | 3000 | 17,658,000.00 | 4-5 |
| FSH | Condenser (pH control) | 600 | 320 | 960 | 5,650,560.00 | 4-5 |
| FSH | Condenser (pH control) | 3260 | 1400 | 4200 | 24,721,200.00 | 4-5 |
| FSH | Condenser (non pH) | 2000 | 200 | 600 | 3,531,600.00 | 2-4 |
| FSH | Condenser (non pH) | 126 | 30 | 90 | 529,740.00 | 2-4 |
| FSH | Condenser (non pH) | 2530 | 120 | 360 | 2,118,960.00 | 2-4 |
| FSH | Condenser (non pH) | 2791 | 200 | 600 | 3,531,600.00 | 2-4 |
| FSH | Condenser (non pH) | 590 | 60 | 180 | 1,059,480.00 | 2-4 |
| FSH | Condenser (non pH) | 591 | 60 | 180 | 1,059,480.00 | 2-4 |
| FSH | Condenser (non pH) | 4196 | 140 | 420 | 2,472,120.00 | 2-4 |
| FSH | Condenser (non pH) | 2840 | 1200 | 3600 | 21,189,600.00 | 2-4 |
| FSH | Condenser (non pH) | 916 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 929 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 930 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 915 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 920 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 907 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 905 | 80 | 240 | 1,412,640.00 | 2-4 |
| FSH | Condenser (non pH) | 904 | 80 | 240 | 1,412,640.00 | 2-4 |
| Total FSH | 204,303,060.00 |
FSH Heat pump Condenser Loop
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| FSH | Heat pump condenser loop | 916 | 1600 |
| FSH | Heat pump condenser loop | 929 | 1600 |
| FSH | Heat pump condenser loop | 930 | 1600 |
| FSH | Heat pump condenser loop | 915 | 1600 |
| FSH | Heat pump condenser loop | 920 | 1600 |
| FSH | Heat pump condenser loop | 907 | 1600 |
| FSH | Heat pump condenser loop | 905 | 1600 |
| FSH | Heat pump condenser loop | 904 | 1600 |
| FSH | Heat pump condenser loop | 2000 | 3000 |
| FSH | Heat pump condenser loop | 590 | 800 |
| FSH | Heat pump condenser loop | 591 | 800 |
| FSH | Heat pump condenser loop | 1472 | 19500 |
| FSH | Heat pump condenser loop | 3315 | 26000 |
| Total | 62900 |
FSH Steam
| Installation | System Type | Bldg | Output Capacity (1000 Lb Steam/Hr) | Steam Boiler Make Up Water rate Gal/yr | Cycles of Concentration |
| FSH Steam | Steam | 3260 | 5021 | 7,390,912.00 |
1230984383C: 1230984383C:
Steam make up = 4 GPM/1000 lb/hr assume boilers run 70% of the time
Gal/yr = lb/hr x 4 GPM/1000 lb/hr x 60 min/hr x 24 hr/day x 365 days/ yr x .7 = lb/hr x 1472 7-9
FSH Chilled Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| FSH | Chilled Water | 1377 | 15000 |
| FSH | Chilled Water | 600 | 4800 |
| FSH | Chilled Water | 3260 | 21000 |
| FSH | Chilled Water | 126 | 1280 |
| FSH | Chilled Water | 2530 | 1800 |
| FSH | Chilled Water | 2791 | 3000 |
| FSH | Chilled Water | 4196 | 2100 |
| FSH | Chilled Water | 2840 | 18000 |
| FSH Total | 66980 |
FSH Hot Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| FSH | Hot water | 1472 | 46000 |
| FSH | Hot water | 600 | 4800 |
| FSH | Hot water | 3260 | 21000 |
| FSH | Hot water | 126 | 1280 |
| FSH | Hot water | 2530 | 1800 |
| FSH | Hot water | 2791 | 3000 |
| FSH | Hot water | 4196 | 2100 |
| FSH | Hot water | 2840 | 18000 |
| FSH | Hot water | 1350 | 8000 |
| FSH | Hot water | 1374 | 3500 |
| FSH | Hot water | 1375 | 3500 |
| FSH Total | 112980 |
RAN Condenser
| Installation | System Type | Bldg | Cooling Cpacity (Ton AC) | Condenser water flow rate (Gal/Min) | Condenser Water Make up rate (Gal/Year) | Cycles of Concentration |
| RAN | Condenser | 991 | 1200 | 3600 | 21,189,600.00 |
1230984383C: 1230984383C:
Blowdown = make up + evaporation
Assume chillers run 70% of the time.
Blowdown= Cond GPM x 60min/hr x24 hr/dayx 365 dys /year x .7 x .006 =GPM x 2207.
.006= blowdown rate coeficient for 10 deg F delta T, 5 cycles (HVAC rules of thumb book. Page 244)
Evaporation rate = .03GPM/ton x ton x 60 min/hr x 24 hr/day x 365 days/year x .7 = ton x 11037
(p. 243 HVAC rules of thumb book); assumes tower is efficient, worst case evaporation rate = worst case condenser water usage.
| 4-5 | ||||||
| RAN | Condenser | 395 | 1000 | 3000 | 17,658,000.00 | 4-5 |
| RAN | Condenser | 500 | 200 | 600 | 3,531,600.00 | 4-5 |
| RAN | Condenser | 738 | 1150 | 3450 | 20,306,700.00 | 4-5 |
| RAN | Condenser | 496 | 2200 | 6600 | 38,847,600.00 | 4-5 |
| RAN | Condenser | 1068 | 500 | 1500 | 8,829,000.00 | 4-5 |
RAN Total 6,250.00
RAN Steam
| Installation | System Type | Bldg | Output Capacity (1000 Lb Steam/Hr) | Steam Boiler Make Up Water rate Gal/yr | Cycles of Concentration |
| RAN Steam | Steam | 860 | 4185 | 6,160,320.00 |
1230984383C: 1230984383C:
Steam make up = 4 GPM/1000 lb/hr assume boilers run 70% of the time
Gal/yr = lb/hr x 4 GPM/1000 lb/hr x 60 min/hr x 24 hr/day x 365 days/ yr x .7 = lb/hr x 1472 7-9
RAN Chilled Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| RAN | Chilled Water | 991 | 54000 |
| RAN | Chilled Water | 395 | 42000 |
| RAN | Chilled Water | 500 | 9000 |
| RAN | Chilled Water | 738 | 48000 |
| RAN | Chilled Water | 496 | 80000 |
| RAN | Chilled Water | 1068 | 18800 |
Total RAN 251800
RAN Hot Water
| Installation | System Type | Bldg | Appx. Volume (Gal) | |
| RAN | Hot Water | 860 | 54000 | 3 |
| RAN | Hot Water | 395 | 32000 | 1.5 |
| RAN | Hot Water | 499 | 160000 | 10 |
| RAN | Hot Water | 738 | 48000 | 3 |
| RAN | Hot Water | 100 | 28000 | 2 |
| RAN | Hot Water | 112 | 12000 | 0.5 |
| RAN | Hot Water | 64 | 14000 | 0.6 |
| Total RAN | 348000 |
Camp Bullis Chilled Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| CB | Chilled Water | 6104 | 2000 |
| CB | Chilled Water | 5401 | 500 |
| CB | Chilled Water | 5405 | 500 |
| CB | Chilled Water | 5409 | 500 |
| CB | Chilled Water | 5411 | 500 |
| CB | Chilled Water | 5413 | 500 |
| CB | Chilled Water | 5420 | 500 |
| CB | Chilled Water | 5422 | 500 |
| CB | Chilled Water | 5423 | 500 |
| CB | Chilled Water | 5425 | 500 |
| CB | Chilled Water | 5428 | 500 |
Total Camp Bullis 7000
Camp Bullis Hot Water
| Installation | System Type | Bldg | Appx. Volume (Gal) |
| CB | Hot Water | 6104 | 2000 |
| CB | Hot Water | 5401 | 500 |
| CB | Hot Water | 5405 | 500 |
| CB | Hot Water | 5409 | 500 |
| CB | Hot Water | 5411 | 500 |
| CB | Hot Water | 5413 | 500 |
| CB | Hot Water | 5420 | 500 |
| CB | Hot Water | 5422 | 500 |
| CB | Hot Water | 5423 | 500 |
| CB | Hot Water | 5425 | 500 |
| CB | Hot Water | 5428 | 500 |
Total Camp Bullis 7000
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