Design and Manufacturing of Heat Exchangers
Fundamentals of Related Transport Processes
Multifluid Heat Exchangers

In many applications it is necessary to involve (simultaneously) more than two fluids in a thermal interaction. Designs of such exchangers, say two fluids are in thermal contact through a third one i.e., not directly - as in a three fluid heat exchange) may be tricky. Temperature fields in such systems may be very complex and therefore the design issues challenging.

Temperature distributions within a three fluid cross-flow heat exchanger
Temperature distributions (dimensionless) within a three fluid cross-flow heat exchanger. Notice the existence of a temperature cross phenomenon that may compromise the design. (Source: Sekulic, D.P., Thermal Design Theory of Three-Fluid Heat Exchangers, Advances in Heat Transfer, Vol. 26, 1995, pp. 219-328; Baclic, B.S., Sekulic, D.P., and Gvozdenac, D.D., Performance of three-fluid single-pass crossflow heat exchanger, Heat Transfer 1982, Vol. 6 Hemisphere, Washington, DC, pp. 167-172.)
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Dimensionless temperatures of all three fluids along the respective dimensionless flow lengths
Dimensionless temperatures of all three fluids along the respective dimensionless flow lengths. Note an appearance of internal temperature crosses in parallel stream three fluid heat exchangers - an impossible event in a two-fluid heat exchanger in a parallel flow (either co-current or countercurrent). This event may lead to a design that features a significant loss of heat transfer capability. (Source: Sekulic, D.P., A compact solution of the parallelflow three-fluid heat exchanger problem, Int. J. Heat Mass Transfer Vol. 37, 1994, pp. 2183-2187.)


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Also of interest, the. . .
Brazing Research Program
References
Contact Dr. Dusan P. Sekulic, UK Center for Manufacturing, 210A CRMS Bldg., College of Engineering, University of Kentucky, Lexington, KY 40506. Phone 859-257-2972 or 859-257-6262
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Ext. 425, Fax 859-257-1071, e-mail: sekulicd@engr.uky.edu

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Last Updated: November 3, 2009