Water at 0.8 kg/s enters the tubes of a two-shell-pass, four-tube- pass heat exchanger at 17°C and leaves at 37°C. It cools 0.5 kg/s of air entering the shell at 250°C with U = 432 W/m²K. Determine: (a) the exit air temperature; (b) the area of the heat exchanger; and (c) the exit temperature if, after some time, the tubes become fouled with Rf = 0.0005 m²K/W. [(c) Tairout = 140.5°C]

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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Problem 3.20 please
LWO
case?
3.18 Suppose that the
shell-pass, four tube-pass exchanger with the hot fluid moving in
the tubes. (a) What would be the exit temperature in this
(b) What would be the area if we wanted the hot fluid to leave at
the same temperature as in the example? [(a) Tcout = 75.09°C]
3.19 Plot the maximum tolerable fouling resistance as a function of Unew
for a counterflow exchanger, with given inlet temperatures, if a 30%
reduction in U is the maximum that can be tolerated.
3.20 Water at 0.8 kg/s enters the tubes of a two-shell-pass, four-tube-
pass heat exchanger at 17°C and leaves at 37°C. It cools 0.5 kg/s
of air entering the shell at 250°C with U = 432 W/m²K. Determine:
(a) the exit air temperature; (b) the area of the heat exchanger; and
(c) the exit temperature if, after some time, the tubes become fouled
with Rf = 0.0005 m²K/W. [(c) Tairout = 140.5°C]
3.21 You must cool 78 kg/min of a 60%-by-mass mixture of glycerin in wa-
ter from 108°C to 50°C using cooling water available at 7°C. Design
a one-shell-pass, two-tube-pass heat exchanger if U
Which side should the water flow through? Explain any design
637 W/m²K.
decision you make and report the area, TH₂Oout, and any other
=
relevant features.
3.22 A mixture of 40%-by-weight glycerin, 60% water, enters a smooth
0.113 m I.D. tube at 30°C. The tube is kept at 50°C, and
TI boat transfer coefficient incid
3.25
3.
Transcribed Image Text:LWO case? 3.18 Suppose that the shell-pass, four tube-pass exchanger with the hot fluid moving in the tubes. (a) What would be the exit temperature in this (b) What would be the area if we wanted the hot fluid to leave at the same temperature as in the example? [(a) Tcout = 75.09°C] 3.19 Plot the maximum tolerable fouling resistance as a function of Unew for a counterflow exchanger, with given inlet temperatures, if a 30% reduction in U is the maximum that can be tolerated. 3.20 Water at 0.8 kg/s enters the tubes of a two-shell-pass, four-tube- pass heat exchanger at 17°C and leaves at 37°C. It cools 0.5 kg/s of air entering the shell at 250°C with U = 432 W/m²K. Determine: (a) the exit air temperature; (b) the area of the heat exchanger; and (c) the exit temperature if, after some time, the tubes become fouled with Rf = 0.0005 m²K/W. [(c) Tairout = 140.5°C] 3.21 You must cool 78 kg/min of a 60%-by-mass mixture of glycerin in wa- ter from 108°C to 50°C using cooling water available at 7°C. Design a one-shell-pass, two-tube-pass heat exchanger if U Which side should the water flow through? Explain any design 637 W/m²K. decision you make and report the area, TH₂Oout, and any other = relevant features. 3.22 A mixture of 40%-by-weight glycerin, 60% water, enters a smooth 0.113 m I.D. tube at 30°C. The tube is kept at 50°C, and TI boat transfer coefficient incid 3.25 3.
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