Nucleate boiling in two types of vertical narrow channels
Lei GUO, Shusheng ZHANG, Lin CHENG
Nucleate boiling in two types of vertical narrow channels
To explore the mechanism of boiling bubble dynamics in narrow channels, we investigate 2-mm wide I- and Z-shaped channels. The influence of wall contact angle on bubble generation and growth is studied using numerical simulation. The relationships between different channel shapes and the pressure drop are also examined, taking into account the effects of gravity, surface tension, and wall adhesion. The wall contact angle imposes considerable influence over the morphology of bubbles. The smaller the wall contact angle, the rounder the bubbles, and the less time the bubbles take to depart from the wall. Otherwise, the bubbles experience more difficulty in departure. Variations in the contact angle also affect the heat transfer coefficient. The greater the wall contact angle, the larger the bubble-covered area. Therefore, wall thermal resistance increases, bubble nucleation is suppressed, and the heat transfer coefficient is lowered. The role of surface tension in boiling heat transfer is considerably more important than that of gravity in narrow channels. The generation of bubbles dramatically disturbs the boundary layer, and the bubble bottom micro-layer can enhance heat transfer. The heat transfer coefficient of Z-shaped channels is larger than that of the I-shaped type, and the pressure drop of the former is clearly higher.
nucleate boiling / narrow channel / numerical simulation / bubble dynamics
[1] |
Klausner J F, Mei R, Bernhard D M, Zeng L Z. Vapor bubble departure in forced convection boiling. International Journal of Heat and Mass Transfer, 1993, 36(3): 651–662
CrossRef
Google scholar
|
[2] |
Wambsganss M W, France D M, Jendrzejczyk J A, Tran T N. Boiling heat transfer in a small diameter tube. ASME Journal of Heat Transfer, 1992, 115(4): 963–972
CrossRef
Google scholar
|
[3] |
Bowers M B, Mudawar I. High flux boiling in low flow rate, low pressure drop mini-channel and micro-channel heat sinks. International Journal of Heat and Mass Transfer, 1994, 37(2): 321–332
CrossRef
Google scholar
|
[4] |
De J, Xin D M. Heat transfer performance of ethanol three-dimensional inner micro-fin heat pipe. Journal of Chongqing University, 2003, 26(4): 39–41
|
[5] |
Mishima K, Hibiki T. Some characteristics of air-water two-phase flow in small diameter vertical tubes. International Journal of Multiphase Flow, 1996, 22(4): 703–712
CrossRef
Google scholar
|
[6] |
Chen E F, Li Y Z, Wang S M. Numerical simulation of subcooled boiling water in vertical concentric ammulus under low pressure. Journal of Xi’an Jiaotong University, 2008, 42(7): 855–859
|
[7] |
Chen D Q, Pan L M, Yuan D W, Deng J W, Wang X J. Experimental study on bubble growth in vertical narrow channel. Nuclear Power Engineering, 2008, 29(5): 52–55
|
[8] |
Talebi S, Abbasi F, Davilu H. A 2D numerical simulation of sub-cooled flow boiling at low-pressure and low-flow rates. Nuclear Engineering and Design, 2009, 239(1): 140–146
CrossRef
Google scholar
|
[9] |
Tang C Y. The relationship between surface tension and temperature of water. Journal of Anqing Normal University, 2000, 6(1): 73–74
|
[10] |
Lin R T. Boiling Heat Transfer. Beijing: Science Press, 1988
|
[11] |
Guo L, Zhang S S, Chen Y Q, Cheng L. Numerical simulation of boiling heat transfer of water in vertical rectangular mini-channels. Applied Mechanics and Materials, 2010, 29-32: 61–67
CrossRef
Google scholar
|
[12] |
Hahne E, Grigull U. Boiling Heat Transfer. Beijing: National Defense Industry Press, 1988
|
/
〈 | 〉 |