Consider the steady-state counterflow heat exchanger shown below. There are separate streams of air and water, and each stream experiences no noticeable change in pressure. Stray heat transfer with the surroundings and changes in kinetic and potential energy can be ignored. For the air, the ideal gas model can be applied and Rair = 0.287 For the operating conditions provided on kg-K the figure, determine: a. The temperature of the air at the outlet of the heat exchanger, T4, in [K] b. The rate of heat transfer between the air and the water, in [kW c. The rate of entropy production for the heat exchanger, in [kW/K]

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8th Edition
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
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Chapter9: Heat Transfer With Phase Change
Section: Chapter Questions
Problem 9.32P
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Consider the steady-state counterflow heat exchanger shown below. There are separate streams of
air and water, and each stream experiences no noticeable change in pressure. Stray heat transfer
with the surroundings and changes in kinetic and potential energy can be ignored. For the air, the
ideal gas model can be applied and Rair = 0.287- For the operating conditions provided on
kg-K
the figure, determine:
a. The temperature of the air at the outlet of the heat exchanger, T4, in [K]
b. The rate of heat transfer between the air and the water, in [kW; ,
c. The rate of entropy production for the heat exchanger, in [kW/K]
kg
msteam = 12
P1 = 3 bar
X1 = 1
P2 = P1
T2 = 200
P3 = 1 bar
T3 = 1100 K
P4 = P3
T, =?
mair
kg
= 3.29
Transcribed Image Text:Consider the steady-state counterflow heat exchanger shown below. There are separate streams of air and water, and each stream experiences no noticeable change in pressure. Stray heat transfer with the surroundings and changes in kinetic and potential energy can be ignored. For the air, the ideal gas model can be applied and Rair = 0.287- For the operating conditions provided on kg-K the figure, determine: a. The temperature of the air at the outlet of the heat exchanger, T4, in [K] b. The rate of heat transfer between the air and the water, in [kW; , c. The rate of entropy production for the heat exchanger, in [kW/K] kg msteam = 12 P1 = 3 bar X1 = 1 P2 = P1 T2 = 200 P3 = 1 bar T3 = 1100 K P4 = P3 T, =? mair kg = 3.29
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