Ćwiczenie nr 3
a) jednostopniowy
|
1 |
2 |
|
|
B4 |
|
B4 |
|
|
VAPOR |
VAPOR |
|
|
|
Substream: MIXED |
|
|
Mole Flow lbmol/hr |
|
|
ETHYL-01 |
555,5649 |
555,5649 |
Total Flow lbmol/hr |
555,5649 |
555,5649 |
Total Flow lb/hr |
15585,68 |
15585,68 |
Total Flow cuft/hr |
5789,849 |
42107,99 |
Temperature F |
103,73 |
103,73 |
Pressure psia |
580,1509 |
79,77076 |
Vapor Frac |
1 |
1 |
Liquid Frac |
0 |
0 |
Solid Frac |
0 |
0 |
Enthalpy Btu/lbmol |
22854,1 |
22854,1 |
Enthalpy Btu/lb |
814,6538 |
814,6538 |
Enthalpy Btu/hr |
1,27E+07 |
1,27E+07 |
Entropy Btu/lbmol-R |
-19,5538 |
-15,6136 |
Entropy Btu/lb-R |
-0,69701 |
-0,55656 |
Density lbmol/cuft |
0,095955 |
0,013194 |
Density lb/cuft |
2,691898 |
0,370136 |
Average MW |
28,05376 |
28,05376 |
Liq Vol 60F cuft/hr |
753,8736 |
753,8736 |
b)dwustopniowa
|
1 |
2 |
|
|
B4 |
|
B4 |
|
|
VAPOR |
VAPOR |
|
|
|
Substream: MIXED |
|
|
Mole Flow lbmol/hr |
|
|
ETHYL-01 |
555,5649 |
555,5649 |
Total Flow lbmol/hr |
555,5649 |
555,5649 |
Total Flow lb/hr |
15585,68 |
15585,68 |
Total Flow cuft/hr |
5789,849 |
42107,99 |
Temperature F |
103,73 |
103,73 |
Pressure psia |
580,1509 |
79,77076 |
Vapor Frac |
1 |
1 |
Liquid Frac |
0 |
0 |
Solid Frac |
0 |
0 |
Enthalpy Btu/lbmol |
22854,1 |
22854,1 |
Enthalpy Btu/lb |
814,6538 |
814,6538 |
Enthalpy Btu/hr |
1,27E+07 |
1,27E+07 |
Entropy Btu/lbmol-R |
-19,55378 |
-15,61361 |
Entropy Btu/lb-R |
-0,6970112 |
-0,5565603 |
Density lbmol/cuft |
0,0959549 |
0,0131938 |
Density lb/cuft |
2,691898 |
0,370136 |
Average MW |
28,05376 |
28,05376 |
Liq Vol 60F cuft/hr |
753,8736 |
753,8736 |
Custom steam results:
|
|
|
|
|
|
1 |
|
From |
|
B4 |
|
To |
|
|
|
Substream: MIXED |
|
|
|
Phase: |
|
Vapor |
|
Component Mole Flow |
|
|
|
ETHYL-01 |
LBMOL/HR |
555,56 |
|
Mole Flow |
LBMOL/HR |
555,56 |
|
Mass Flow |
LB/HR |
15585,68 |
|
Volume Flow |
CUFT/HR |
5789,85 |
|
Temperature |
F |
103,73 |
|
Pressure |
PSIA |
580,15 |
|
Vapor Fraction |
|
1 |
|
Liquid Fraction |
|
0 |
|
Solid Fraction |
|
0 |
|
Molar Enthalpy |
BTU/LBMOL |
22854,1 |
|
Mass Enthalpy |
BTU/LB |
814,65 |
|
Enthalpy Flow |
BTU/HR |
12696940 |
|
Molar Entropy |
BTU/LBMOL-R |
-19,55 |
|
Mass Entropy |
BTU/LB-R |
-0,7 |
|
Molar Density |
LBMOL/CUFT |
0,1 |
|
Mass Density |
LB/CUFT |
2,69 |
|
Average Molecular Weight |
|
28,05 |
|
c)trójstopniowa
Properties -> specyfication
Strumień wylotowy:
|
1 |
2 |
|
|
B4 |
|
B4 |
|
|
VAPOR |
VAPOR |
|
|
|
Substream: MIXED |
|
|
Mole Flow lbmol/hr |
|
|
ETHYL-01 |
555,5649 |
555,5649 |
Total Flow lbmol/hr |
555,5649 |
555,5649 |
Total Flow lb/hr |
15585,68 |
15585,68 |
Total Flow cuft/hr |
5789,849 |
42107,99 |
Temperature F |
103,73 |
103,73 |
Pressure psia |
580,1509 |
79,77076 |
Vapor Frac |
1 |
1 |
Liquid Frac |
0 |
0 |
Solid Frac |
0 |
0 |
Enthalpy Btu/lbmol |
22854,1 |
22854,1 |
Enthalpy Btu/lb |
814,6538 |
814,6538 |
Enthalpy Btu/hr |
1,27E+07 |
1,27E+07 |
Entropy Btu/lbmol-R |
-19,55378 |
-15,61361 |
Entropy Btu/lb-R |
-0,6970112 |
-0,5565603 |
Density lbmol/cuft |
0,0959549 |
0,0131938 |
Density lb/cuft |
2,691898 |
0,370136 |
Average MW |
28,05376 |
28,05376 |
Liq Vol 60F cuft/hr |
753,8736 |
753,8736 |
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