RESEARCH ARTICLE

Nucleate boiling in two types of vertical narrow channels

  • Lei GUO ,
  • Shusheng ZHANG ,
  • Lin CHENG
Expand
  • Institute of Thermal Science & Technology of Shandong University, Jinan 250061, China

Received date: 10 Jun 2010

Accepted date: 02 Sep 2010

Published date: 05 Sep 2011

Copyright

2014 Higher Education Press and Springer-Verlag Berlin Heidelberg

Abstract

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.

Cite this article

Lei GUO , Shusheng ZHANG , Lin CHENG . Nucleate boiling in two types of vertical narrow channels[J]. Frontiers in Energy, 2011 , 5(3) : 250 -256 . DOI: 10.1007/s11708-010-0128-4

Acknowledgements

This program was supported by the National Basic Research Program of China (No. 2007CB206900).
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

DOI

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

DOI

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

DOI

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

DOI

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

DOI

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

DOI

12
Hahne E, Grigull U. Boiling Heat Transfer. Beijing: National Defense Industry Press, 1988

Outlines

/