Development of Nusselt number and friction factor correlations for the shell side of spiral-wound heat exchangers

被引:23
作者
Abolmaali, Ali Mostafazade [1 ]
Afshin, Hossein [1 ]
机构
[1] Sharif Univ Technol, Sch Mech Engn, POB 11155-9567, Tehran, Iran
关键词
Spiral-wound heat exchanger; Numerical simulation; Volume goodness factor; Multivariate correlation; Nusselt number; Friction factor; HELICALLY COILED TUBE; TRANSFER COEFFICIENTS; PRESSURE-DROP; FLOW; MODEL; PERFORMANCES; SURFACE;
D O I
10.1016/j.ijthermalsci.2019.01.038
中图分类号
O414.1 [热力学];
学科分类号
摘要
This research aims to investigate the thermo-hydraulic characteristics of flow in the shell side of spiral-wound heat exchangers with consistent shell geometry. To achieve this end, three-dimensional computational fluid dynamics is employed. Geometrical configuration of spiral-wound heat exchangers can be completely determined by knowing six primary parameters including start factor, tube outside diameter, number of tubes in the first layer, number of layers, longitudinal pitch, and radial pitch. Dividing the longitudinal and radial pitches by tube outside diameter, the six primary geometrical parameters reduce to five non-dimensional parameters. The effects of number of tubes in the first layer, number of layers, longitudinal pitch to tube outside diameter ratio, and radial pitch to tube outside diameter ratio referred to as four main non-dimensional parameters on flow and heat transfer are numerically studied by modeling 64 different geometries. The results indicate that the number of tubes in the first layer is the only parameter among four main non-dimensional parameters that does not have any influence on the flow characteristics. Based on the numerical simulation results, multivariate correlations for average Nusselt number and friction factor have been developed taking into account the three remaining main non-dimensional parameters, i.e. the number of layers, the longitudinal pitch to tube outside diameter ratio, and the radial pitch to tube outside diameter ratio. The average deviation of developed Nusselt number and friction factor correlations from numerical simulation results are 5.4% and 7.0%, respectively.
引用
收藏
页码:105 / 117
页数:13
相关论文
共 46 条
[1]   Investigation of exergy efficiency in shell and helically coiled tube heat exchangers [J].
Alimoradi, Ashkan .
CASE STUDIES IN THERMAL ENGINEERING, 2017, 10 :1-8
[2]   Prediction of heat transfer coefficients of shell and coiled tube heat exchangers using numerical method and experimental validation [J].
Alimoradi, Ashkan ;
Veysi, Farzad .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2016, 107 :196-208
[3]  
Bergman T.L., 2011, INTRO HEAT TRANSFER
[4]   Design Technology of Large-scale Spiral Wound Heat Exchanger in Refinery Industry [J].
Chen, Y. D. ;
Chen, X. D. ;
Jiang, H. F. ;
Chen, C. G. ;
Zhang, X. A. .
PRESSURE VESSEL TECHNOLOGY: PREPARING FOR THE FUTURE, 2015, 130 :286-297
[5]   Hybrid friction diffusion bonding of aluminium tube-to-tube-sheet connections in coil-wound heat exchangers [J].
Dethlefs, A. ;
Roos, A. ;
dos Santos, J. F. ;
Wimmer, G. .
MATERIALS & DESIGN, 2014, 60 :7-12
[6]   Experimental investigation on downward flow boiling heat transfer characteristics of propane in shell side of LNG spiral wound heat exchanger [J].
Ding, Chao ;
Hu, Haitao ;
Ding, Guoliang ;
Chen, Jie ;
Mi, Xiaoguang ;
Yu, Sicong ;
Li, Jianrui .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2017, 84 :13-25
[7]   A dynamic model for FLNG spiral wound heat exchanger with multiple phase-change streams based on moving boundary method [J].
Duan, Zhongdi ;
Ren, Tao ;
Ding, Guoliang ;
Chen, Jie ;
Pu, Hui .
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2016, 34 :657-669
[8]   Numerically investigated effects of different Dean number and pitch size on flow and heat transfer characteristics in a helically coil-tube heat exchanger [J].
Ferng, Y. M. ;
Lin, W. C. ;
Chieng, C. C. .
APPLIED THERMAL ENGINEERING, 2012, 36 :378-385
[9]   A review on the two-phase heat transfer characteristics in helically coiled tube heat exchangers [J].
Fsadni, Andrew Michael ;
Whitty, Justin P. M. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2016, 95 :551-565
[10]   Research on the shell-side thermal performances of heat exchangers with helical tube coils [J].
Genic, Srbislav B. ;
Jacimovic, Branislav M. ;
Jaric, Marko S. ;
Budimir, Nikola J. ;
Dobrnjac, Mirko M. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (15-16) :4295-4300