Q1. A long thin-walled double-pipe heat exchanger with tube and shell diameters of 2 cm and 4 cm, respectively, is used to condense refrigerant-134a by water at 20 °C. The refrigerant flows through the tube, with a convection heat transfer coefficient of hi = 4000 W/m²-K. A l-mm-thick layer of limestone (k = 1.2 W/m·K) forms on the outer surface of the inner tube. Water flows through the shell at a rate of 0.4 kg/s. Determine the overall heat transfer coefficient U of this heat exchanger with and without the fouling factor, and the error in U introduced by neglecting the fouling factor. Comment the fouling effect on this heat exchanger.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
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A long thin-walled double-pipe heat exchanger with tube and shell diameters of 2 cm and 4 cm, respectively, is used to condense refrigerant-134a by water at 20 C. The refrigerant flows through the tube, with a convection heat transfer coefficient of hi = 4000 W/m2 K.
A 1-mm-thick layer of limestone (k = 1.2 W/mK) forms on the outer surface of the inner tube. Water flows through the shell at a rate of 0.4 kg/s. Determine the overall heat transfer coefficient U of this heat exchanger with and without the fouling factor, and the error in U introduced by neglecting the fouling factor. Comment the fouling effect on this heat exchanger.

Q1. A long thin-walled double-pipe heat exchanger with tube and shell diameters of 2 cm and
4 cm, respectively, is used to condense refrigerant-134a by water at 20 °C. The refrigerant
flows through the tube, with a convection heat transfer coefficient of hi = 4000 W/m²-K.
A l-mm-thick layer of limestone (k = 1.2 W/m·K) forms on the outer surface of the inner
tube. Water flows through the shell at a rate of 0.4 kg/s. Determine the overall heat
transfer coefficient U of this heat exchanger with and without the fouling factor, and the
error in U introduced by neglecting the fouling factor. Comment the fouling effect on this
heat exchanger.
Transcribed Image Text:Q1. A long thin-walled double-pipe heat exchanger with tube and shell diameters of 2 cm and 4 cm, respectively, is used to condense refrigerant-134a by water at 20 °C. The refrigerant flows through the tube, with a convection heat transfer coefficient of hi = 4000 W/m²-K. A l-mm-thick layer of limestone (k = 1.2 W/m·K) forms on the outer surface of the inner tube. Water flows through the shell at a rate of 0.4 kg/s. Determine the overall heat transfer coefficient U of this heat exchanger with and without the fouling factor, and the error in U introduced by neglecting the fouling factor. Comment the fouling effect on this heat exchanger.
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