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Plate heat exchangers, calculation methods for single- and two-phase flow
KTH, School of Industrial Engineering and Management (ITM), Energy Technology, Applied Thermodynamics and Refrigeration.ORCID iD: 0000-0002-9902-2087
KTH, School of Industrial Engineering and Management (ITM), Energy Technology, Applied Thermodynamics and Refrigeration.ORCID iD: 0000-0003-3896-2443
2005 (English)In: ICMM 2005, Proceedings of the 3rd International Conference on Microchannels and Minichannels, Pt A, 2005, p. 103-113Conference paper, Published paper (Refereed)
Abstract [en]

Plate heat exchangers were first developed about 100 years ago, but have won increasing interest during the last two decades, primarily because of the development of methods of manufacturing brazed plate heat exchangers. This type of heat exchanger offers very good heat transfer performance in single-phase flow as well as in evaporation and condensation. Part of the reason is the small hydraulic diameters, typically being less than 5 mm. Other advantages of plate heat exchangers are the extremely compact design and the efficient use of the construction material. In spite of their long use, the calculation methods for predicting heat transfer and pressure drop are not widely known. It is the purpose of this article to present such calculation methods for singe phase flow and for flow boiling and to discuss some of the specifics of this type of heat exchangers.

Place, publisher, year, edition, pages
2005. p. 103-113
National Category
Engineering and Technology
Identifiers
URN: urn:nbn:se:kth:diva-43295ISI: 000243025300012Scopus ID: 2-s2.0-27744514921ISBN: 0-7918-4185-5 (print)OAI: oai:DiVA.org:kth-43295DiVA, id: diva2:448572
Conference
3rd International Conference on Microchannels and Minichannels Location: Univ Toronto, Toronto, CANADA Date: JUN 13-15, 2005
Note
QC 20111017Available from: 2011-10-17 Created: 2011-10-14 Last updated: 2011-10-17Bibliographically approved

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Palm, Björn E.Claesson, Joachim

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