Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.

Printed Circuit Heat Exchangers (PCHE's) are very efficient compact exchangers considered as recuperators in the Brayton cycle of new generation high temperature reactor designs. The heat exchangers use multiple plate layers containing tortuous micro–channels to enhance the heat transfer betwee...

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Main Author: Fourie, Jan Hendrik.
Published: North-West University 2012
Online Access:http://hdl.handle.net/10394/7622
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spelling ndltd-NWUBOLOKA1-oai-dspace.nwu.ac.za-10394-76222014-04-16T03:57:02ZThermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.Fourie, Jan Hendrik.Printed Circuit Heat Exchangers (PCHE's) are very efficient compact exchangers considered as recuperators in the Brayton cycle of new generation high temperature reactor designs. The heat exchangers use multiple plate layers containing tortuous micro–channels to enhance the heat transfer between the working fluids. Understanding the flow phenomena and its effects on heat transfer inside the channels would ultimately lead to improved exchanger designs. A numerical study was conducted on the heat transfer behaviour of fully developed laminar flow in three–dimensional serpentine channels with semi–circular and equilateral triangular cross–sections. Computational Fluid Dynamics (CFD) was used to investigate the heat transfer characteristics of various physical designs under different flow conditions. The design parameters for serpentine channels were: the bend's radius of curvature ( ), the channel diameter (d), the half–wavelength of the channel (L) and Reynolds number (Re). Results were obtained for a range of configurations (1.0 1.8, = 4.5) and flow conditions (50 400). Water was used as fluid and the uniform surface temperature boundary condition was applied to channel walls. Results showed a definite increase in heat transfer when Re was increased. Heat transfer enhancement due to fluid mixing was a maximum at the highest Reynolds number since the inertial effects dominated the viscous flow effects. However, a slight decrease in enhancement was noted as the bend radius of curvature increased, due to weaker mixing of the flow. In several test cases, secondary flow effects separate from main vortices and mixing were observed to influence the heat transfer. Future research topics are suggested to further clarify these phenomena.Thesis (M.Ing. (Nuclear Engineering))--North-West University, Potchefstroom Campus, 2011.North-West University2012-10-23T13:21:39Z2012-10-23T13:21:39Z2011Thesishttp://hdl.handle.net/10394/7622
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sources NDLTD
description Printed Circuit Heat Exchangers (PCHE's) are very efficient compact exchangers considered as recuperators in the Brayton cycle of new generation high temperature reactor designs. The heat exchangers use multiple plate layers containing tortuous micro–channels to enhance the heat transfer between the working fluids. Understanding the flow phenomena and its effects on heat transfer inside the channels would ultimately lead to improved exchanger designs. A numerical study was conducted on the heat transfer behaviour of fully developed laminar flow in three–dimensional serpentine channels with semi–circular and equilateral triangular cross–sections. Computational Fluid Dynamics (CFD) was used to investigate the heat transfer characteristics of various physical designs under different flow conditions. The design parameters for serpentine channels were: the bend's radius of curvature ( ), the channel diameter (d), the half–wavelength of the channel (L) and Reynolds number (Re). Results were obtained for a range of configurations (1.0 1.8, = 4.5) and flow conditions (50 400). Water was used as fluid and the uniform surface temperature boundary condition was applied to channel walls. Results showed a definite increase in heat transfer when Re was increased. Heat transfer enhancement due to fluid mixing was a maximum at the highest Reynolds number since the inertial effects dominated the viscous flow effects. However, a slight decrease in enhancement was noted as the bend radius of curvature increased, due to weaker mixing of the flow. In several test cases, secondary flow effects separate from main vortices and mixing were observed to influence the heat transfer. Future research topics are suggested to further clarify these phenomena. === Thesis (M.Ing. (Nuclear Engineering))--North-West University, Potchefstroom Campus, 2011.
author Fourie, Jan Hendrik.
spellingShingle Fourie, Jan Hendrik.
Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.
author_facet Fourie, Jan Hendrik.
author_sort Fourie, Jan Hendrik.
title Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.
title_short Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.
title_full Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.
title_fullStr Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.
title_full_unstemmed Thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / Fourie J.H.
title_sort thermal performance of periodic serpentine channels with semi–circular and triangular cross–sections / fourie j.h.
publisher North-West University
publishDate 2012
url http://hdl.handle.net/10394/7622
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