Experimental study of the effects of key geometry parameters on shell-side vapor condensation of spiral-wound heat exchangers

被引:8
作者
Jian, Guanping [1 ]
Wang, Simin [1 ]
Sun, Lijuan [1 ]
Wen, Jian [2 ]
Tu, Jiyuan [3 ]
机构
[1] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Shanxi, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Xian 710049, Peoples R China
[3] Tsinghua Univ, Inst Nucl & New Energy Technol, Key Lab Adv Reactor Engn & Safety, Minist Educ, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Spiral wound heat exchanger; Experimental research; Vapor Condensation; Phase change; Geometry parameter; TRANSFER COEFFICIENTS; PRESSURE-DROP; FILM FLOW; OPTIMIZATION; PERFORMANCE; MODEL;
D O I
10.1016/j.applthermaleng.2019.114731
中图分类号
O414.1 [热力学];
学科分类号
摘要
The results of an experimental study of the shell-side condensation characteristics of the spiral wound heat exchanger (SWHE) are presented in this paper. Ten testing SWHEs with different structures were manufactured to investigate the effects of key geometrical parameters on the shell-side vapor condensation characteristics. The overall heat transfer performance of the SWHE reflected in the experiment was also discussed. The experimental data reveal that the geometrical parameters have obvious influences on heat transfer performance. Large tube pitch and layer pitch have positive effects on the heat transfer because of minimized surface tension effects between the shell-side tubes. Based on the experimental conditions, the heat transfer coefficient increases by an average of 43.86% when the tube pitch increases from 4 mm to 10 mm, and the average increment of the heat transfer coefficient exceeds 45% when the layer pitch increases from 0 mm to 4 mm. With the increase of the winding angle from 8 degrees to 16 degrees, the heat transfer coefficient hits a minimum at 14 degrees when the tube-side mass flow rate is over 12 m(3).h(-1) and the vapor flow rate is 280 k.gh(-1). The effects of working conditions on the heat transfer are considered as well. When the tube-side mass flow rate increases, there is a maximum in the range of 10 m(3).h(-1) to 14 m(3) .h(-1) for the overall heat transfer coefficient. The results of the experiment could be a guideline for designing and manufacturing of SWHE.
引用
收藏
页数:9
相关论文
共 30 条
[1]  
Abadzic E.E., 1973, ADV CRYOGEN ENG, V18, P42, DOI [10.1007/978-1-4684-3111-7_5, DOI 10.1007/978-1-4684-3111-7_5]
[2]   Experimental investigations on heat transfer enhancement in shell coil heat exchanger with variable baffles geometry [J].
Andrzejczyk, R. ;
Muszynski, T. ;
Gosz, M. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2018, 132 :114-126
[3]  
Barbe C., 1972, 12 JOURN HYDR
[4]   Heat transfer coefficients in falling film heaters - Streamline flow [J].
Bays, GS ;
McAdams, WH .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1937, 29 :1240-1246
[5]  
Chowdhury K., 1985, HEAT TRANSF ENG, V6, P45, DOI DOI 10.1080/01457638508939638
[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]  
Fleming R.B., 1967, ADV CRYOGEN ENG, P352
[8]  
Fredheim A.O., 1994, THESIS
[9]   Experimental study of mixed convection heat transfer in vertical helically coiled tube heat exchangers [J].
Ghorbani, N. ;
Taherian, H. ;
Gorji, M. ;
Mirgolbabaei, H. .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2010, 34 (07) :900-905
[10]   Performance evaluation of counter flow heat exchangers considering the effect of heat in leak and longitudinal conduction for low-temperature applications [J].
Gupta, P ;
Atrey, MD .
CRYOGENICS, 2000, 40 (07) :469-474