7.80 Figure Pz.80 shows an insulated counterflow heat exchanger with carbon dioxide (CO2) and air flowing through the inner and outer channels, respectively. The figure provides data for operation at steady state. The heat exchanger is a component of an overall system operating in an arctic region where the average annual ambient temperature is 20°F. Heat transfer between the heat exchanger and its surroundings can be ignored, as can effects of motion and gravity. Evaluate for the heat exchanger a. the rate of exergy destruction, in Btu/s b. the exergetic efficiency given by Eq. Z27. Let To 20°F, po 1 atm Insulation Mair=1 lb/s T3 500°R 3 P3=50 lbf/in.2 T4=720°R P4=40 lbf/in.2 + Air CO2 mco=2 lb/s T-1200 R P=18 lbf/in.2 T2=1100°R P2= 14.7 lbf/in.2 FIGURE P7.80

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7.80 Figure Pz.80 shows an insulated counterflow heat exchanger with carbon dioxide (CO2) and air flowing through the
inner and outer channels, respectively. The figure provides data for operation at steady state. The heat exchanger is a
component of an overall system operating in an arctic region where the average annual ambient temperature is 20°F. Heat
transfer between the heat exchanger and its surroundings can be ignored, as can effects of motion and gravity. Evaluate for
the heat exchanger
a. the rate of exergy destruction, in Btu/s
b. the exergetic efficiency given by Eq. Z27.
Let To 20°F, po 1 atm
Insulation
Mair=1 lb/s
T3 500°R
3
P3=50 lbf/in.2
T4=720°R
P4=40 lbf/in.2 +
Air
CO2
mco=2 lb/s
T-1200 R
P=18 lbf/in.2
T2=1100°R
P2= 14.7 lbf/in.2
FIGURE P7.80
Transcribed Image Text:7.80 Figure Pz.80 shows an insulated counterflow heat exchanger with carbon dioxide (CO2) and air flowing through the inner and outer channels, respectively. The figure provides data for operation at steady state. The heat exchanger is a component of an overall system operating in an arctic region where the average annual ambient temperature is 20°F. Heat transfer between the heat exchanger and its surroundings can be ignored, as can effects of motion and gravity. Evaluate for the heat exchanger a. the rate of exergy destruction, in Btu/s b. the exergetic efficiency given by Eq. Z27. Let To 20°F, po 1 atm Insulation Mair=1 lb/s T3 500°R 3 P3=50 lbf/in.2 T4=720°R P4=40 lbf/in.2 + Air CO2 mco=2 lb/s T-1200 R P=18 lbf/in.2 T2=1100°R P2= 14.7 lbf/in.2 FIGURE P7.80
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