Question 5.7 In a parallel flow heat exchanger, hot fluid enters the heat exchanger at a temperature of 150°C and a mass flow rate of 3 kg/s. The cooling medium enters the heat exchanger at a temperature of 30°C with a mass flow rate of 0.5 kg/s and Examiner's Signature Moderator's Signature Page leaves at a temperature of 70°C. The specific heat capacities of the hot and cold fluids are 1150 J/kg-K and 4180 J/kg K, respectively. The convection heat transfer coefficient on the inner and outer side of the tube is 300 W /m2.K and 800 W /m2.K, respectively. For a fouling factor of 0.0003 m2.K/W on the tube side and 0.0001 m2.K/W on the shell side, determine the overall heat transfer coefficient, the exit temperature of the hot fluid as well as the surface area of the heat exchanger.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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Question 5.7
In a parallel flow heat exchanger, hot fluid enters the heat exchanger at a
temperature of 150°C and a mass flow rate of 3 kg/s. The cooling medium enters the
heat exchanger at a temperature of 30°C with a mass flow rate of 0.5 kg/s and
Examiner's Signature
Moderator's Signature
Page
leaves at a temperature of 70°C. The specific heat capacities of the hot and cold
fluids are 1150 J/kg-K and 4180 J/kg K, respectively. The convection heat transfer
coefficient on the inner and outer side of the tube is 300 W /m2.K and 800 W /m2.K,
respectively. For a fouling factor of 0.0003 m2.K/W on the tube side and 0.0001
m2.K/W on the shell side, determine the overall heat transfer coefficient, the exit
temperature of the hot fluid as well as the surface area of the heat exchanger.
Transcribed Image Text:Question 5.7 In a parallel flow heat exchanger, hot fluid enters the heat exchanger at a temperature of 150°C and a mass flow rate of 3 kg/s. The cooling medium enters the heat exchanger at a temperature of 30°C with a mass flow rate of 0.5 kg/s and Examiner's Signature Moderator's Signature Page leaves at a temperature of 70°C. The specific heat capacities of the hot and cold fluids are 1150 J/kg-K and 4180 J/kg K, respectively. The convection heat transfer coefficient on the inner and outer side of the tube is 300 W /m2.K and 800 W /m2.K, respectively. For a fouling factor of 0.0003 m2.K/W on the tube side and 0.0001 m2.K/W on the shell side, determine the overall heat transfer coefficient, the exit temperature of the hot fluid as well as the surface area of the heat exchanger.
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