An experimental investigation of bubble growth and detachment in vertical upflow and downflow boiling

被引:242
|
作者
Thorncroft, GE
Klausner, JF [1 ]
Mei, R
机构
[1] Univ Florida, Dept Mech Engn, Gainesville, FL 32611 USA
[2] Univ Florida, Dept Aerosp Engn Mech & Engn Sci, Gainesville, FL 32611 USA
关键词
boiling; heat transfer; vapor bubble dynamics;
D O I
10.1016/S0017-9310(98)00092-1
中图分类号
O414.1 [热力学];
学科分类号
摘要
A visual study of vapor bubble growth and departure in vertical upflow and downflow forced convection boiling is presented. A vertical flow boiling facility was constructed with a transparent, electrically-heated test section in which the ebullition process could be observed. High-speed digital images of flow boiling phenomena were obtained, which were used to measure bubble growth, departure diameters, and lift-off diameters. Experiments were conducted for flow of FC-87 over a commercially-finished nichrome heating surface, with mass flux ranging from 190 to 666 kg m(-2) s(-1) and heat flux ranging from 1.3 to 14.6 kW/m(2). The flow was slightly subcooled (Delta T-sub = 1.0-5.0 degrees C), and boiling occurred at isolated nucleation sites. A major conclusion of this work is that the observed vapor bubble dynamics between upflow and downflow are significantly different. In the upflow configuration, bubbles departing the nucleation site slide along the heater wall, and typically do not lift off. In the downflow configuration, bubbles either lift off directly from the nucleation site or slide and then lift off, depending on flow and thermal conditions. The process of vapor bubble sliding appears to be responsible for enhanced energy transfer from the heating surface, as evidenced by larger heat transfer coefficients for upflow than for downflow under otherwise identical operating conditions. (C) 1998 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:3857 / 3871
页数:15
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