3
Distl Name DIST1 Property method WILS-HOC Henry's component list ID Electrolyte chemistry ID Use true species approach for electrolytes YES Free-water phase properties method STEAM-TA Water solubility method 3 Number of stages 30 Feed stage 10 Reflux ratio 0.5 Distillate to feed mole ratio 0.5 Condenser pressure [bar] 2 Reboiler pressure [bar] 2 Condenser duty [Gcal/hr] 0.0107853007 Reboiler duty [Gcal/hr] 0.0103986221 Feed stage temperature [C] 123.704071 Top stage temperature [C] 119.793572 Bottom stage temperature [C] 133.631516 Feed quality 0.0337838876 Total feed stream CO2e flow [kg/hr] 0 Total product stream CO2e flow [kg/hr] 0 Net stream CO2e production [kg/hr] 0

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DistlName DIST1Property method WILS-HOCHenry's component list IDElectrolyte chemistry IDUse true species approach for electrolytesYESFree-water phase properties method STEAM-TAWater solubility method 3Number of stages 30Feed stage 10Reflux ratio 0.5Distillate to feed mole ratio 0.5Condenser pressure [bar] 2Reboiler pressure [bar] 2Condenser duty [Gcal/hr] 0.0107853007Reboiler duty [Gcal/hr] 0.0103986221Feed stage temperature [C] 123.704071Top stage temperature [C] 119.793572Bottom stage temperature [C] 133.631516Feed quality 0.0337838876Total feed stream CO2e flow [kg/hr] 0Total product stream CO2e flow [kg/hr] 0Net stream CO2e production [kg/hr] 0

UnitOps ChartName Equipment Cost Installed CostEquipment WeightInstalled WeightDIST1 0 0 0 0

UnitOps ChartUtility Cost0