| Spark Gap | 13.62 | Absporption Chilling | x2 | |||||||
| $/kWh | 0.08 | Required Steam Flow Rate (lbm/hr) | 2945.1 | 5890.2 | ||||||
| $/Therm | 0.983 | COP | 1.17 | |||||||
| BTU/Therm | 100000 | Required Steam Pressure (psig) | 115 | 230 | ||||||
| Required Steam Enthalpy (BTU/lbm) | 1192.65 | 2385.3 | ||||||||
| $/1,000,000BTU Electricity | 23.45 | Required Steam (BTU/hr) | 3512474 | 7024947 | ||||||
| $/1,000,000BTU Propane | 9.83 | Capacity (Tons) | 300 | 600 | ||||||
| Density of Propane (lbm/ft3) | 0.11855 | |||||||||
| Domestic Water Heating | ||||||||||
| Maximum Hot Water Temp (oF) | 140 | |||||||||
| LHV Annual Consumption (lbm/yr) | 18910892 | Water Inlet Temp (oF) | 55 | |||||||
| HHV Annual Consumption (lbm/yr) | 17398757 | Recovery (gph) | 121 | |||||||
| HHV Annual Cost ($/yr) | 1442681 | Storage Capacity (gal) | 200 | |||||||
| LHV Annual Cost ($/yr) | 1568065 | |||||||||
| HRSG | ||||||||||
| Exhaust Ref. Temp (oF) | 350 | |||||||||
| Exhaust Enthalpy (BTU/hr) | 19200000 | |||||||||
| Exhaust Temp (oF) | 833 | |||||||||
| Exhaust Dew Point Temp (oF) | 98 | |||||||||
| Unfired Steam Output (lbm/hr) | 17900 | |||||||||
| Steam Pressure (psig) | 125 | |||||||||
| Pinch Point Temp (oF) | 30 | |||||||||