Thermal performance investigation in a novel corrugated plate heat exchanger

被引:44
作者
Al Zahrani, Salman [1 ,2 ]
Islam, Mohammad S. [1 ]
Xu, Feng [3 ]
Saha, Suvash C. [1 ]
机构
[1] Univ Technol Sydney, Sch Mech & Mechatron Engn, Ultimo, NSW 2007, Australia
[2] Al Baha Univ, Dept Mech Engn, Al Baha, Saudi Arabia
[3] Beijing Jiaotong Univ, Sch Civil Engn, Beijing 100044, Peoples R China
关键词
Corrugated plate heat exchanger; Thermal performance; Numerical modelling; Nusselt number; PRESSURE-DROP; FLOW DISTRIBUTION; CHANNELS; SIMULATION; TUBE;
D O I
10.1016/j.ijheatmasstransfer.2019.119095
中图分类号
O414.1 [热力学];
学科分类号
摘要
Compact heat exchangers have become an essential necessity for power production and multi other purposes on a daily basis. The corrugated plate heat exchangers (CPHEs) are well-known for their high thermal performance. This study proposes a unique CPHE with a simple modification that can boost its thermal performance significantly. The overall tests have been conducted on four CPHEs for two symmetric chevron angles (beta) of 30 degrees/30 degrees and 60 degrees/60 degrees Two CPHEs belong to the newly CPHEs, and the other two belong to the well-known basic CPHE. Data are obtained for steady-state, single-phase (water-water), counter-current arrangements, and for Reynolds number (Re) ranges from 500 to 2500. Sophisticated mesh techniques have been adopted to develop the mesh for the plates and the fluids between the plates. An appropriate grid refinement test has been carried out for the accuracy of the numerical results. The results have been validated with benchmark experimental and numerical data. A realizable k - epsilon turbulence model with scalable wall treatment found to provide the most consistent and accurate prediction of the thermal performance of CPHE. The numerical results showed that the Nusselt number (Nu) and the effectiveness (epsilon) of the newly developed CPHEs are much higher than that of the basic one, which can be very useful when a heavy heat duty is required. The enhancement for Nu is up to 75% and for epsilon is up to 42%, and generally both exhibit a direct proportional relationship with Re. Based on the numerical result, a new correlation to predict Nu has been developed. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:11
相关论文
共 44 条
[1]   A thermo-hydraulic characteristics investigation in corrugated plate heat exchanger [J].
Al Zahrani, Salman ;
Islam, Mohammad S. ;
Saha, Suvash C. .
2ND INTERNATIONAL CONFERENCE ON ENERGY AND POWER (ICEP2018), 2019, 160 :597-605
[2]  
Ansys, 2009, ANSYS FLUENT 12 0 US
[3]  
Asif M, 2017, INT J HEAT TECHNOL, V35, P205, DOI 10.18280/ijht.350127
[4]   Plate heat exchanger literature survey and new heat transfer and pressure drop correlations for refrigerant evaporators [J].
Ayub, ZH .
HEAT TRANSFER ENGINEERING, 2003, 24 (05) :3-16
[5]  
BASSIOUNY MK, 1984, CHEM ENG SCI, V39, P693, DOI 10.1016/0009-2509(84)80176-1
[6]   Numerical and experimental determination of flow structure and heat transfer effects of longitudinal vortices in a channel flow [J].
Biswas, G ;
Torii, K ;
Fujii, D ;
Nishino, K .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1996, 39 (16) :3441-3451
[7]   Numerical investigation of convective heat transfer and pressure drop in wavy ducts [J].
Blomerius, H ;
Mitra, NK .
NUMERICAL HEAT TRANSFER PART A-APPLICATIONS, 2000, 37 (01) :37-54
[8]   Heat transfer in plate heat exchanger channels: Experimental validation of selected correlation equations [J].
Cieslinski, Janusz T. ;
Fiuk, Artur ;
Typinski, Krzysztof ;
Siemienczuk, Bartlomiej .
ARCHIVES OF THERMODYNAMICS, 2016, 37 (03) :19-29
[9]   Review of passive heat transfer augmentation techniques [J].
Dewan, A ;
Mahanta, P ;
Raju, KS ;
Kumar, PS .
PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART A-JOURNAL OF POWER AND ENERGY, 2004, 218 (A7) :509-527
[10]   Heat transfer and pressure drop in corrugated channels [J].
Elshafei, E. A. M. ;
Awad, M. M. ;
El-Negiry, E. ;
Ali, A. G. .
ENERGY, 2010, 35 (01) :101-110