Optimal design of a concentric heat exchanger for high-temperature systems using CFD simulations

Abstract Computational fluid dynamics (CFD) has been successfully used to simulate a three-dimensional concentric high temperature heat exchanger. The concentric shell with staggered fin arrays connecting serve not only as a part of the shell structure, but also as a flow-disturbing mechanism in an attempt to enhance heat transfer. This heat exchanger uses helium gas and molten salt as hot and cold streams respectively in a counter-flow mode. Flow fields and heat transfer characteristics of the two concentric channels are examined extensively. A design with an optimal performance of the heat exchanger is achieved by maximizing the effectiveness of the heat exchanger (e-NTU method) using the following parameters as optimizing variables: the width of the flow channel, the length, pitch, thickness, and angle of the fins. The number of CFD simulation are substantially reduced by Taguchi method, and the optimal configurations of the concentric high temperature heat exchanger are found with a channel width of 1 mm, a fin length of 11 mm, an angle of fin of 2.6°, and a fin thickness of 1.125 mm.

[1]  Ahmad Fakheri,et al.  Heat Exchanger Efficiency , 2007 .

[2]  Harika Sammeta,et al.  Effectiveness charts for counter flow corrugated plate heat exchanger , 2011, Simul. Model. Pract. Theory.

[3]  J. Lake,et al.  The Fourth Generation of Nuclear Power , 2000 .

[4]  Donato Aquaro,et al.  High temperature heat exchangers for power plants : Performance of advanced metallic recuperators , 2007 .

[5]  Chung-Han Tsai,et al.  Optimal structural analysis with associated passive heat removal for AP1000 shield building , 2013 .

[6]  N. Tsuzuki,et al.  Nusselt number correlations for a microchannel heat exchanger hot water supplier with S-shaped fins , 2009 .

[7]  Clayton Ray De Losier,et al.  The Parametric Study of an Innovative Offset Strip-Fin Heat Exchanger , 2007 .

[8]  T. Hung A CONCEPTUAL DESIGN OF THERMAL MODELING FOR EFFICIENTLY COOLING AN ARRAY OF HEATED , 2001 .

[9]  A. Duigou,et al.  Hydrogen production using the sulfur-iodine cycle coupled to a VHTR : An overview , 2006 .

[10]  Neil R. Ullman,et al.  Signal-to-noise ratios, performance criteria, and transformations , 1988 .

[11]  Hélio Aparecido Navarro,et al.  Effectiveness-ntu computation with a mathematical model for cross-flow heat exchangers , 2007 .

[12]  Chih-Hsiang Hsu,et al.  Heat transfer characteristics of a helical heat exchanger , 2012 .

[13]  Theoretical analysis of triple concentric-tube heat exchangers Part 1: Mathematical modelling , 1998 .

[14]  Alireza Bahadori,et al.  Simple method for estimation of effectiveness in one tube pass and one shell pass counter-flow heat exchangers , 2011 .

[15]  B. Launder,et al.  The numerical computation of turbulent flows , 1990 .

[16]  S. Subramanian CFD modeling of compact offset strip-fin high temperature heat exchanger , 2005 .

[17]  Frank P. Incropera,et al.  Fundamentals of Heat and Mass Transfer , 1981 .

[18]  T. Hung,et al.  Conjugate Heat Transfer Analysis for the Passive Enhancement of Electronic Cooling Through Geometric Modification in a Mixed Convection Domain , 1999 .

[19]  Tzu-Chen Hung,et al.  A thermodynamic analysis of high temperature gas-cooled reactors for optimal waste heat recovery and hydrogen production , 2012 .

[20]  Conjugated heat transfer in a concentric annular pipe , 1992 .

[21]  T. C. Hung,et al.  CFD modeling and thermal-hydraulic analysis for the passive decay heat removal of a sodium-cooled fast reactor , 2011 .

[22]  Makrand A. Khanwale,et al.  Investigation of flow and heat characteristics and structure identification of FLiNaK in pipe using CFD simulations , 2014 .

[23]  A. Ünal Theoretical analysis of triple concentric-tube heat exchangers Part 2: Case studies , 2001 .

[24]  B. Launder,et al.  Lectures in mathematical models of turbulence , 1972 .