179 |
|
|
180 |
|
|
181 |
|
|
182 |
c_tot1: cost*1.0{USdollar/yr} = column_cost + condenser_cost |
c_tot1: cost*1.0{USD/yr} = column_cost + condenser_cost |
183 |
+ reboiler_cost + water_cost + steam_cost; |
+ reboiler_cost + water_cost + steam_cost; |
184 |
|
|
185 |
|
|
196 |
Fp2 := 0.0{}; |
Fp2 := 0.0{}; |
197 |
Fm2 := 1.0{}; |
Fm2 := 1.0{}; |
198 |
|
|
199 |
M_S := 900{USdollar}; |
M_S := 900{USD}; |
200 |
|
|
201 |
Tin := 459.67{R} + 70{R}; |
Tin := 459.67{R} + 70{R}; |
202 |
Tout := 459.67{R} + 90{R}; |
Tout := 459.67{R} + 90{R}; |
203 |
Uc := 100{BTU/hr/ft^2/R}; |
Uc := 100{BTU/hr/ft^2/R}; |
204 |
CpW := 1{cal/mole/K}; |
CpW := 1{cal/mole/K}; |
205 |
Hs := 933{BTU/lbm}; |
Hs := 933{BTU/lbm}; |
206 |
Cw := 0.03{USdollar}/1000{gallon}; |
Cw := 0.03{USD}/1000{gallon}; |
207 |
Cs := 2.5{USdollar}/1000{lbm}; |
Cs := 2.5{USD}/1000{lbm}; |
208 |
Tray_height := 2.0{ft}; |
Tray_height := 2.0{ft}; |
209 |
|
|
210 |
|
|