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Experimental Investigation of Single Phase Pressure Drop in a Plate Heat Exchanger

[+] Author Affiliations
Tariq S. Khan

Petroleum Institute, Abu Dhabi, UAE

Mohammad S. Khan

Mohammad Ali Jinnah University, Islamabad, Pakistan

Zahid H. Ayub

Isotherm Inc., Arlington, TX

Paper No. AJKFluids2015-25340, pp. V01AT25A003; 8 pages
doi:10.1115/AJKFluids2015-25340
From:
  • ASME/JSME/KSME 2015 Joint Fluids Engineering Conference
  • Volume 1A: Symposia, Part 2
  • Seoul, South Korea, July 26–31, 2015
  • Conference Sponsors: Fluids Engineering Division
  • ISBN: 978-0-7918-5721-3
  • Copyright © 2015 by KSME

abstract

Pressure drop characteristics of a gasketed commercial plate heat exchanger (PHE) configured for single phase water to water flow application are presented. Isothermal pressure drop data are provided for two symmetric 30°/30°, 60°/60° and a non-symmetric 30°/60° (mixed) chevron plate configuration in the plate heat exchanger. Reynolds number was varied from 500 to 2,500. The experimental data are found to be a strong function of chevron angle and Reynolds number. Performance evaluation results show that mixed plate configuration can be a choice in optimizing the PHE design for improved performance.

Copyright © 2015 by KSME

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