9. The effluent from a gas compressor is cooled by contacting with water in a heat exchanger. The operating parameters for this system are given in the diagram below. water out water in ws Te = 35°C Compressor TA = 15°C P, = 104 kPa T, = 30°C m, = 35 kg/min 1 2 Heat Exchanger 3 P2 = 255 kPa T2 = 143°C P, = 255 kPa T3 = 65°C Assuming natural gas to behave as an ideal gas and negligible heat losses to the surroundings, calculate: a. power requirement for the compressor and the required cooling water mass flow rate for the heat exchanger. b. entropy production rate for the compressor and for the heat exchanger separately.
9. The effluent from a gas compressor is cooled by contacting with water in a heat exchanger. The operating parameters for this system are given in the diagram below. water out water in ws Te = 35°C Compressor TA = 15°C P, = 104 kPa T, = 30°C m, = 35 kg/min 1 2 Heat Exchanger 3 P2 = 255 kPa T2 = 143°C P, = 255 kPa T3 = 65°C Assuming natural gas to behave as an ideal gas and negligible heat losses to the surroundings, calculate: a. power requirement for the compressor and the required cooling water mass flow rate for the heat exchanger. b. entropy production rate for the compressor and for the heat exchanger separately.
Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
8th Edition
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
Publisher:Kreith, Frank; Manglik, Raj M.
Chapter7: Forced Convection Inside Tubes And Ducts
Section: Chapter Questions
Problem 7.49P
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