The optimum position of porous insert for a double-pipe heat exchanger based on entropy generation and thermal analysis

被引:40
作者
Akbarzadeh, Mohsen [1 ,2 ,3 ]
Rashidi, Saman [4 ]
Keshmiri, Amir [5 ]
Shokri, Nima [6 ]
机构
[1] Vrije Univ Brussel, ETEC Dept, Pleinlaan 2, B-1050 Brussels, Belgium
[2] Vrije Univ Brussel, MOBI Res Grp, Pleinlaan 2, B-1050 Brussels, Belgium
[3] Flanders Make, B-3001 Heverlee, Belgium
[4] Ferdowsi Univ Mashhad, Dept Mech Engn, Mashhad 917751111, Razavi Khorasan, Iran
[5] Univ Manchester, Sch Mech Aerosp & Civil Engn MACE, Manchester M13 9PL, Lancs, England
[6] Univ Manchester, Sch Chem Engn & Analyt Sci, Manchester M13 9PL, Lancs, England
关键词
Porous insert; Double-pipe heat exchanger; Computational fluid dynamics; Heat transfer; Porous media; 2ND LAW ANALYSES; TRANSFER ENHANCEMENT; FORCED-CONVECTION; NUMERICAL DESIGN; METAL FOAM; FLUID-FLOW; PERFORMANCE; NANOFLUID; NONEQUILIBRIUM; CHANNEL;
D O I
10.1007/s10973-019-08362-x
中图分类号
O414.1 [热力学];
学科分类号
摘要
In the present paper, the first and second laws of thermodynamics are utilized to select the optimized position of porous insert to achieve maximum heat transfer and minimum pressure drop and entropy generation inside a double-pipe heat exchanger. Four different porous inserts configuration are considered in the heat exchanger, where the porous layers are placed at the core of the inner tube, wall of the inner tube, and inner or outer walls on outer tube for these cases. In addition, the effects of Darcy number and thermal conductivity of porous material on entropy generation, heat transfer enhancement and pressure drop penalty are investigated. The flow and heat transfer are modeled using Computational fluid dynamics. It was found that for outer tube of a double-pipe heat exchanger, placing the porous layer in the inner wall creates larger pressure drops. For inner tube, it is better to place the porous layer at the center, while for outer one, it is better to insert the porous layer at inner wall (interface wall) to achieve the higher values of heat transfer rate. Moreover, the thermal and viscous entropy generations are more pronounced for the cases, where the porous substrate is not located at the core of the heat exchanger.
引用
收藏
页码:411 / 426
页数:16
相关论文
共 38 条
[1]  
Akbar NS, 2016, J APPL FLUID MECH, V9, P1721
[2]   Combined effects of corrugated walls and porous inserts on performance improvement in a heat exchanger channel [J].
Akbarzadeh, Mohsen ;
Maghrebi, Mohammad Javad .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2018, 127 :266-276
[3]   Improving the performance of double-pipe heat exchangers by using porous substrates [J].
Alkam, MK ;
Al-Nimr, MA .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1999, 42 (19) :3609-3618
[4]   Second law analysis in a partly porous double pipe heat exchanger [J].
Allouache, N ;
Chikh, S .
JOURNAL OF APPLIED MECHANICS-TRANSACTIONS OF THE ASME, 2006, 73 (01) :60-65
[5]   Toward improved heat transfer performance of annular heat exchangers with water/ethylene glycol-based nanofluids containing graphene nanoplatelets [J].
Arzani, Hamed Khajeh ;
Amiri, Ahmad ;
Arzani, Hamid Khajeh ;
Bin Rozali, Shaifulazuar ;
Kazi, S. N. ;
Badarudin, A. .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2016, 126 (03) :1427-1436
[6]  
Bejan A., 1982, ENTROPY GENERATION H
[7]   Performance of tubular aluminum foam heat exchangers in multiple row bundles [J].
Chumpia, A. ;
Hooman, K. .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2019, 135 (03) :1813-1822
[8]   First and second law analyses of nanofluid forced convection in a partially-filled porous channel - The effects of local thermal non-equilibrium and internal heat sources [J].
Dickson, Craig ;
Torabi, Mohsen ;
Karimi, Nader .
APPLIED THERMAL ENGINEERING, 2016, 103 :459-480
[9]   Numerical study of conjugated heat transfer in metal foam filled double-pipe [J].
Du, Y. P. ;
Qu, Z. G. ;
Zhao, C. Y. ;
Tao, W. Q. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2010, 53 (21-22) :4899-4907
[10]   Thermal development in open-cell metal foam: An experiment with constant wall heat flux [J].
Dukhan, Nihad ;
Bagci, Ozer ;
Ozdemir, Mustafa .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2015, 85 :852-859