Effects of Aspect Ratio on Flow and Condensation in Rectangular Microchannels

被引:0
作者
Wu C.-X. [1 ]
Li J.-M. [1 ]
机构
[1] Key Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Energy and Power Engineering, Tsinghua University, Beijing
来源
Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities | 2018年 / 32卷 / 06期
关键词
Aspect ratio; Condensation; Gregorig effect; Injection flow; Microchannel;
D O I
10.3969/j.issn.1003-9015.2018.00.018
中图分类号
学科分类号
摘要
A transient numerical model based on volume of fluid for flow and condensation in rectangular microchannels was proposed. A separated model for vapor-liquid flow was adopted for velocity inlet considering entrance effect of velocity and liquid film thickness. The numerical mode was verified by data from literature, and condensation flow and heat transfer of R32 in three rectangular microchannels (aspect ratios of 2:3, 1:1 and 3:2) were numerically studied (annular, injection flow, bubbly flow and shrinking bubbly). The results of gas-liquid phase distribution on the channel sections and wall heat flux distribution show that with aspect ratio away from 1:1, the non-uniformity of condensate film distribution increases, which reinforces the Gregorig effect and hence enhances heat transfer. The enhanced heat transfer makes the Weber number and Capillary number of tail vapor core smaller, which leads to the injection flow further towards the inlet, and has lower occurrence frequency of the vapor slug detachment. The calculation results show that the flow and condensation process are significantly affected by the rectangular aspect ratio. Compared with square channels, strict rectangular channels are more conducive in heat transfer and can inhibit gas-liquid interface fluctuation. © 2018, Editorial Board of Journal of Chemical Engineering of Chinese Universities". All right reserved."
引用
收藏
页码:1264 / 1273
页数:9
相关论文
共 20 条
[1]  
Cheng P., Wu H.Y., Mesoscale and microscale phase-change heat transfer, Advances in Heat Transfer, 39, pp. 461-563, (2006)
[2]  
Corimnne P., Jumana B., Christian S., Et al., Analytic modeling, optimization, and realization of cooling devices in silicon technology, IEEE Transactions on Components and Packaging Technologies, 23, 4, pp. 665-672, (2000)
[3]  
Cormac E., Tara D., Mark D., Et al., Direct comparison between five different microchannels, part 1: channel manufacture and measurement, Heat Transfer Engineering, 26, 3, pp. 79-88, (2005)
[4]  
Zhang W., Xu J., Liu G., Multi-channel effect of condensation flow in a micro triple-channel condenser, International Journal of Multiphase Flow, 34, 12, pp. 1175-1184, (2008)
[5]  
Zhang W., Xu J., Thome J.R., Periodic bubble emission and appearance of an ordered bubble sequence (train) during condensation in a single microchannel, International Journal of Heat and Mass Transfer, 51, 13-14, pp. 3420-3433, (2008)
[6]  
Chen Y., Wu R., Shi M.H., Et al., Visualization study of steam condensation in triangular microchannels, International Journal of Heat and Mass Transfer, 52, 21, pp. 5122-5129, (2009)
[7]  
Wu J.F., Shi M.H., Chen Y., Et al., Visualization study of steam condensation in wide rectangular silicon microchannels, International Journal of Thermal Sciences, 49, 6, pp. 922-930, (2010)
[8]  
Fang C., David M., Wang F.M., Et al., Influence of film thickness and cross-sectional geometry on hydrophilic microchannel condensation, International Journal of Multiphase Flow, 36, 8, pp. 608-619, (2010)
[9]  
Ma X., Fan X., Lan Z., Et al., Flow patterns and transition characteristics for steam condensation in silicon microchannels, Journal of Micromechanics and Microengineering, 21, 7, (2011)
[10]  
Quan X.J., Cheng P., Wu H.Y., Transition from annular flow to plug/slug flow in condensation of steam in microchannels, International Journal of Heat and Mass Transfer, 51, 3-4, pp. 707-716, (2008)