Circumferential distribution of local heat transfer coefficient during steam stratified flow condensation in vacuum horizontal tube

被引:21
作者
Shen, Shengqiang [1 ]
Wang, Yaoxuan [1 ]
Yuan, Dayuan [1 ]
机构
[1] Dalian Univ Technol, Sch Energy & Power Engn, Key Lab Liaoning Prov Desalinat, Dalian, Peoples R China
基金
美国国家科学基金会;
关键词
Condensation; Horizontal tube; Stratified flow; Wetted angle; Desalination; INTERFACIAL MEASUREMENTS; SMOOTH; REGIME; ANGLE; R22;
D O I
10.1016/j.ijheatmasstransfer.2017.06.042
中图分类号
O414.1 [热力学];
学科分类号
摘要
An experimental system was built up to measure the wetted angle and circumferential distributions of local heat transfer coefficient during the steam stratified flow condensation in vacuum horizontal tube. The wetted angle is mainly affected by vapor quality. It decreases with vapor quality and steam mass flow rate, and increases with the steam saturation temperature. The Biberg's correlation and Rouhani's void fraction correlation are used together to predict the experimental value of wetted angle accurately. The tube wall is divided into filmwise condensation section and liquid accumulation section by the stratified interface. The local heat transfer coefficient in filmwise condensation section is significantly higher than that in liquid accumulation section. The local heat transfer coefficient increases with vapor quality and steam mass flow rate for all locations along the circumferential direction. The increase of temperature difference between steam and cooling water causes the decrease of local heat transfer coefficient in filmwise condensation section and has less effect on that in liquid accumulation section. With the change of steam saturation temperature, the heat transfer coefficients in two sections of the tube appear different variation tendencies. Based on the experimental values, new correlations for local heat transfer coefficient of steam condensation flow in stratified flow pattern are proposed. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:816 / 825
页数:10
相关论文
共 23 条
[1]  
[Anonymous], 1993, VDI WARMEATLAS VDI H
[2]   Condensation heat transfer coefficients for R22 and R407C in gravity driven flow regime within a smooth horizontal tube [J].
Aprea, C ;
Greco, A ;
Vanoli, GP .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2003, 26 (04) :393-401
[3]   An explicit approximation for the wetted angle in two-phase stratified pipe flow [J].
Biberg, D .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (06) :1221-1224
[4]  
Chato J.C., 1960, LAMINAR CONDENSATION
[5]   Condensation in smooth horizontal tubes [J].
Dobson, MK ;
Chato, JC .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1998, 120 (01) :193-213
[6]   CONDENSATION HEAT-TRANSFER IN A MIXED FLOW REGIME [J].
JASTER, H ;
KOSKY, PG .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1976, 19 (01) :95-99
[7]   Condensation heat transfer of R22 and R410A in horizontal smooth and microfin tubes [J].
Kim, MH ;
Shin, JS .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2005, 28 (06) :949-957
[8]  
Kline S.J., 1952, ASME Mechanical Engineering, V75, P3
[9]  
LOCKHART RW, 1949, CHEM ENG PROG, V45, P39
[10]  
Nusselt W., 1916, Z VEX DT ING