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Page 1: Result ASpen

Flowchart

Page 2: Result ASpen
Page 3: Result ASpen

MF

Parameter Somers Rubi

P low (kPa) 0.6715 0.6715

P high (kPa) 7.4606 7.4606

Conc., LiBr strong sol’n (%)

57.40 57.40

Q absorber (kW) 13.923 11.5

Q condenser (kW) 11.432 11.386

Q desorber (kW) 14.592 .89

Q evaporator (kW) 10.772 10.7720

Page 4: Result ASpen

COP (-) 0.738 12.1

MFR (kg/s) Stream 1 Stream 1A

Total 1.000 1.000

Water 0.426 0.426

KBr 0.574 0.574

Page 5: Result ASpen

State point

From ToTemperature (oC)

Pressure (kPa)

Vapor fraction (-)

Mass flow rate (kg/s)

KBr concentration (%)

1 Absorber Pump 7.36029 0.6715 0.00 1.000 57.4%

2 Pump SHX 7.36029 7.4606 0.00 1.000 57.4%

3 SHX Desorber 21.39287 7.4606 0.000.609592

57.4%

4 Desorber SHX 89.9 7.4606 0.00 1.000 94.16%

5 SHX Valve 37.07458 7.4606 0.00 1.000 94.16%

6 Valve Absorber 37.08022 0.6715 0.01 0.640443 94.16%

7 Desorber Condenser 78.4 7.4606 1.00 1.000 0.00

8 Condenser Valve 40.20039 7.4606 0.00 1.000 0.00

9 Valve Evaporator 1.300028 0.6715 0.06522 1.000 0.00

10Evaporator

Absorber 1.300028 0.6715 1.00 0.390409 0.00