Hoja1123456789101112B1B3B2B4B4B5B6B1B1B2B2B3B3B4B5B5B6B6LIQUIDVAPORLIQUIDLIQUIDLIQUIDLIQUIDLIQUIDMIXEDLIQUIDLIQUIDLIQUIDLIQUIDSubstream: MIXED Mole Flow lbmol/hr WATER 157.5989132.888924.7099924.709994.09E-182.054264130.8346155.5446110.618444.92624110.61842.41E-25 AMMONIA 236.3983230.42655.9717815.9717811.60E-19230.42653.87E-075.9717814.52E-235.97178100 C2H6O-01 328.331284.947543.3835243.383524.84E-1630.184254.7635298.14720.71403277.43320.714033.30E-24 C4H11-01 590.99588.399088582.5967188.5995393.99727.24E-1018.399088196.9986196.99861.33E-3432.8331164.1655Total Flow lbmol/hr 1313.324656.662656.662262.6648393.9972262.6648393.9972656.662328.331328.331164.1655164.1655Total Flow lb/hr 84126.5320328.6363797.8922374.2641423.635351.84914976.7837351.0423658.9113692.136399.06617259.85Total Flow cuft/hr 1377.2722.66E+051075.019380.5339829.8544122.4918324.265525814.01399.9755297.5319113.9936334.0925Temperature F 77320320275.694584.69997.144448222.497211.6532270.3962179.5402218.2657546.7721Pressure psia 26.6959520.4957420.4957432.6959538.4959530.6959538.095952023.2202023.2Vapor Frac 01000000.10942860000Liquid Frac 10111110.89057141111Solid Frac 000000000000Enthalpy Btu/lbmol -1.46E+05-70896.52-1.88E+05-1.75E+05-1.79E+05-41490.88-1.18E+05-1.41E+05-1.68E+05-1.15E+05-1.37E+05-1.82E+05Enthalpy Btu/lb -2272.648-2290.122-1935.295-2051.478-1704.321-2036.342-3113.239-2477.216-2337.665-2761.802-3509.528-1733.196Enthalpy Btu/hr -1.91E+08-4.66E+07-1.23E+08-4.59E+07-7.06E+07-1.09E+07-4.66E+07-9.25E+07-5.53E+07-3.78E+07-2.25E+07-2.99E+07Entropy Btu/lbmol-R -115.1425-29.2577-152.1187-135.6247-144.4012-51.18694-62.66649-90.94798-116.3669-70.26564-66.84302-147.3486Entropy Btu/lb-R -1.797524-0.9450916-1.565734-1.592179-1.373459-2.512217-1.648579-1.59894-1.614903-1.684938-1.714831-1.401493Density lbmol/cuft 0.9535692.47E-030.61083770.69025340.47477872.1443461.2150450.02543820.82087771.1035151.440130.4913774Density lb/cuft 61.0820.076567359.3458458.7970349.9167543.6914846.18681.44692959.150946.0190456.1353351.66189Average MW 64.0561930.9575397.1548585.1818105.136920.375238.0124256.8801772.0581241.7022238.97936105.1369Liq Vol 60F cuft/hr 1458.641514.4852944.1559341.2801602.8758226.4066288.0786629.3587352.7234276.6353101.5252251.1982flashNameB1rafracGroupProperty methodUNIQ-HOCHenry's component list IDNameB2B3B5B6Electrolyte chemistry IDGroupmescladorUse true species approach for electrolytesYESProperty methodUNIQ-HOCUNIQ-HOCUNIQ-HOCUNIQ-HOCNameB4Free-water phase properties methodSTEAM-TAHenry's component list IDGroupWater solubility method3Electrolyte chemistry IDProperty methodUNIQ-HOCTemperature [C]160Use true species approach for electrolytesYESYESYESYESHenry's component list IDPressureFree-water phase properties methodSTEAM-TASTEAM-TASTEAM-TASTEAM-TAElectrolyte chemistry IDSpecified vapor fraction0.5Water solubility method3333Use true species approach for electrolytesYESSpecified heat dutyNumber of stages30383333Free-water phase properties methodSTEAM-TAEO Model componentsCondenserTOTALTOTALTOTALTOTALWater solubility method3Outlet temperature [F]320ReboilerKETTLEKETTLEKETTLEKETTLESpecified pressure [psia]20Outlet pressure [psia]20.4957Number of phases2222Temperature estimate [F]222Vapor fraction0.5Free-waterNONONONOEO Model componentsHeat duty [Btu/hr]2.12E+07Top stage pressure [psig]18165.304055.30405Outlet temperature [F]211.653Net duty [Btu/hr]2.12E+07Specified reflux ratio57.56.56Calculated outlet pressure [psia]20First liquid / total liquid1Specified bottoms rateVapor fraction0.109429Total feed stream CO2e flow [lb/hr]0Specified boilup rateFirst liquid /Total liquid1Total product stream CO2e flow [lb/hr]0Specified distillate rateTotal feed stream CO2e flow [lb/hr]0Net stream CO2e production [lb/hr]0EO Model componentsTotal product stream CO2e flow [lb/hr]0Utility CO2e production [lb/hr]0Calculated molar reflux ratio57.56.56Net stream CO2e production [lb/hr]0Total CO2e production [lb/hr]0Calculated bottoms rate [lbmol/hr]393.997393.997328.331164.165Utility usageCalculated boilup rate [lbmol/hr]2613.321002.312194.981164.27Utility costCalculated distillate rate [lbmol/hr]262.665262.665328.331164.165Utility IDCondenser / top stage temperature [F]275.6947.14445179.54218.266Condenser / top stage pressure [psia]32.695930.69592020Condenser / top stage heat duty [Btu/hr]-6.05E+07-2.71E+07-4.10E+07-2.84E+07Condenser / top stage subcooled dutyCondenser / top stage reflux rate [lbmol/hr]1313.321969.992134.15984.993Condenser / top stage free water reflux ratioReboiler pressure [psia]38.495938.095923.223.2Reboiler temperature [F]584.7222.497270.396546.772Reboiler heat duty [Btu/hr]6.74E+071.61E+074.04E+073.13E+07Total feed stream CO2e flow [lb/hr]0000Total product stream CO2e flow [lb/hr]0000Net stream CO2e production [lb/hr]0000Utility CO2e production [lb/hr]0000Total CO2e production [lb/hr]0000Condenser utility usageCondenser utility costCondenser utility IDReboiler utility usageReboiler utility costReboiler utility IDBasis for specified distillate to feed ratioMOLEMOLEMOLEMOLESpecified distillate to feed ratio0.40.40.50.5Basis for specified bottoms to feed ratioMOLEMOLEMOLEMOLESpecified bottoms to feed ratioBasis for specified boilup ratioMOLEMOLEMOLEMOLESpecified boilup ratioCalculated molar boilup ratio6.632842.543956.685257.09203Calculated mass boilup ratio6.632842.565812.264297.09203

Hoja2

Hoja3