Counterflow heat exchanger with core and plenums at both ends

dc.contributor.author

Bejan, A

dc.contributor.author

Alalaimi, M

dc.contributor.author

Lorente, S

dc.contributor.author

Sabau, AS

dc.contributor.author

Klett, JW

dc.date.accessioned

2017-02-09T18:52:52Z

dc.date.available

2017-02-09T18:52:52Z

dc.date.issued

2016-08-01

dc.description.abstract

This paper illustrates the morphing of flow architecture toward greater performance in a counterflow heat exchanger. The architecture consists of two plenums with a core of counterflow channels between them. Each stream enters one plenum and then flows in a channel that travels the core and crosses the second plenum. The volume of the heat exchanger is fixed while the volume fraction occupied by each plenum is variable. Performance is driven by two objectives, simultaneously: low flow resistance and low thermal resistance. The analytical and numerical results show that the overall flow resistance is the lowest when the core is absent, and each plenum occupies half of the available volume and is oriented in counterflow with the other plenum. In this configuration, the thermal resistance also reaches its lowest value. These conclusions hold for fully developed laminar flow and turbulent flow through the core. The curve for effectiveness vs number of heat transfer units (Ntu) is steeper (when Ntu < 1) than the classical curves for counterflow and crossflow.

dc.identifier.issn

0017-9310

dc.identifier.uri

https://hdl.handle.net/10161/13609

dc.publisher

Elsevier BV

dc.relation.ispartof

International Journal of Heat and Mass Transfer

dc.relation.isversionof

10.1016/j.ijheatmasstransfer.2016.03.117

dc.title

Counterflow heat exchanger with core and plenums at both ends

dc.type

Journal article

pubs.begin-page

622

pubs.end-page

629

pubs.organisational-group

Duke

pubs.organisational-group

Mechanical Engineering and Materials Science

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Pratt School of Engineering

pubs.publication-status

Published

pubs.volume

99

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