1. 400,000 Ibm/hr of 270°F water is to be heated to 370°F by condensing saturated 390°F steam. (The steam does not sub cool upon condensing). Your job is to design the heat exchanger. The following parameters represent constraint your design. number of tube passes 4 tube fluid water being heated number of shell pass 1 shell fluid steam being cooled 700 BTU /hr – ft² – °F 1 in U (based on outside tube area) tube outside diameter tube wall thickness 1/16 in bulk tube fluid velocity 5 ft/s (a) How many tubes are required per pass? (b) How many tubes are required total? (c) Allowing 3 ft for headers and flanges, how long should the exchanger be?

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.
Chapter10: Heat Exchangers
Section: Chapter Questions
Problem 10.6P: Mot water is used to heat air in a double-pipe heat exchanger as shown in the following sketch. If...
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1. 400,000 Ibm/hr of 270°F water is to be heated to 370°F by condensing saturated
390°F steam. (The steam does not sub cool upon condensing). Your job is to design
the heat exchanger. The following parameters represent constraint your design.
number of tube passes
4
tube fluid
water being heated
number of shell pass
shell fluid
steam being cooled
U (based on outside tube area)
700 BTU/hr – ft² – °F
1 in
tube outside diameter
tube wall thickness
1/16 in
bulk tube fluid velocity
5 ft/s
(a) How many tubes are required per pass?
(b) How many tubes are required total?
(c) Allowing 3 ft for headers and flanges, how long should the exchanger be?
Transcribed Image Text:1. 400,000 Ibm/hr of 270°F water is to be heated to 370°F by condensing saturated 390°F steam. (The steam does not sub cool upon condensing). Your job is to design the heat exchanger. The following parameters represent constraint your design. number of tube passes 4 tube fluid water being heated number of shell pass shell fluid steam being cooled U (based on outside tube area) 700 BTU/hr – ft² – °F 1 in tube outside diameter tube wall thickness 1/16 in bulk tube fluid velocity 5 ft/s (a) How many tubes are required per pass? (b) How many tubes are required total? (c) Allowing 3 ft for headers and flanges, how long should the exchanger be?
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