2003
DOI: 10.1016/s1359-4311(02)00195-3
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Optimal design of plate heat exchangers with and without pressure drop specifications

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Cited by 72 publications
(55 citation statements)
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“…These limitations therefore constrain the optimization potential. Further optimization [58] is still possible by varying the corrugation angle [53]. In this work it was chosen to compare different cycles using identical assumptions on the plate heat exchanger geometry.…”
Section: Heat Exchanger Modelsmentioning
confidence: 99%
“…These limitations therefore constrain the optimization potential. Further optimization [58] is still possible by varying the corrugation angle [53]. In this work it was chosen to compare different cycles using identical assumptions on the plate heat exchanger geometry.…”
Section: Heat Exchanger Modelsmentioning
confidence: 99%
“…There is a great deal of research available for fluidto-fluid heat exchangers [6,7], but the information …”
Section: Previous Literaturementioning
confidence: 99%
“…The plates also come in a variety of materials; some common materials include AISI 304 and AISI 316 stainless steel [2]. by Wang to be 3.8, 0.045 and 0.09 respectively [6]. Martin also showed that head loss is related to the friction factor by Eq.…”
Section: Vertical Plate Heat Exchangermentioning
confidence: 99%
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“…The traditional design method for plate heat exchangers involves many trials in order to meet the pressure drop constraints. Proposed method by Wang and Sunden (2003) is valid for the design situations with and without pressure drop specifications. In the case of the design with pressure drop specification, only one stream can fully utilize the allowable pressure drop.…”
Section: Introductionmentioning
confidence: 99%