Q1) A heat exchanger is to be designed to heat 32/68 mixture of ethylene glycol and water from 24 ᵒC to 55 ᵒC by a hot water stream from 79 ᵒC to 42 ᵒC. Flow rate of cold stream is 20 kg/s. Inlet pressure for both stream is 50 psi and the maximum pressure drop of 10 psi for cold stream and 8 psi for hot water are permissible. Report valid assumptions made for the design and give required justification. Estimate    Heat Transfer, Corrected LMTD,  Tube bundle diameter (Using TEMA standards and Codes) and Tube cross sectional area Heat transfer coefficient Overall heat transfer coefficient Pressure Drop (Shell side & Tube Side)

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.
Chapter9: Heat Transfer With Phase Change
Section: Chapter Questions
Problem 9.3DP
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Q1) A heat exchanger is to be designed to heat 32/68 mixture of ethylene glycol and water from 24 ᵒC to 55 ᵒC by a hot water stream from 79 ᵒC to 42 ᵒC. Flow rate of cold stream is 20 kg/s. Inlet pressure for both stream is 50 psi and the maximum pressure drop of 10 psi for cold stream and 8 psi for hot water are permissible. Report valid assumptions made for the design and give required justification. Estimate

 

  1.  Heat Transfer, Corrected LMTD,
  2.  Tube bundle diameter (Using TEMA standards and Codes) and Tube cross sectional area
  3. Heat transfer coefficient
  4. Overall heat transfer coefficient
  5. Pressure Drop (Shell side & Tube Side)
Select 1-2 counter current heat exchanger with 3/4 inch (19 mm) OD, 14 BWG (2.108
mm), 8 feet (2.44m) long tube. Triangular pitch geometry.
Transcribed Image Text:Select 1-2 counter current heat exchanger with 3/4 inch (19 mm) OD, 14 BWG (2.108 mm), 8 feet (2.44m) long tube. Triangular pitch geometry.
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