Photographic study and modeling of critical heat flux in horizontal flow boiling with inlet vapor void

被引:22
作者
Kharangate, Chirag R. [1 ]
Mudawar, Issam [1 ]
Hasan, Mohammad M. [2 ]
机构
[1] Purdue Univ, Sch Mech Engn, Boiling & Phase Flow Lab 2, W Lafayette, IN 47907 USA
[2] NASA, Glenn Res Ctr, Cleveland, OH 44135 USA
基金
美国国家航空航天局;
关键词
Flow boiling; Two-phase pressure drop; Critical heat flux (CHF); FRICTIONAL PRESSURE-DROP; RECTANGULAR CHANNEL; WATER-FLOW; CHF CORRELATIONS; EARTH GRAVITY; 2-PHASE FLOW; TUBES; MICROGRAVITY; MECHANISM; LONG;
D O I
10.1016/j.ijheatmasstransfer.2012.03.057
中图分类号
O414.1 [热力学];
学科分类号
摘要
This study explores the mechanism of flow boiling critical heat flux (CHF) in a 2.5 mm x 5 mm horizontal channel that is heated along its bottom 2.5 mm wall. Using FC-72 as working fluid, experiments were performed with mass velocities ranging from 185-1600 kg/m(2)s. A key objective of this study is to assess the influence of inlet vapor void on CHF. This influence is examined with the aid of high-speed video motion analysis of interfacial features at heat fluxes up to CHF as well as during the CHF transient. The flow is observed to enter the heated portion of the channel separated into two layers, with vapor residing above liquid. Just prior to CHF, a third vapor layer begins to develop at the leading edge of the heated wall beneath the liquid layer. Because of buoyancy effects and mixing between the three layers, the flow is less discernible in the downstream region of the heated wall, especially at high mass velocities. The observed behavior is used to construct a new separated three-layer model that facilitates the prediction of individual layer velocities and thicknesses. Combining the predictions of the new three-layer model with the interfacial lift-off CHF model provides good CHF predictions for all mass velocities, evidenced by a MAE of 11.63%. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4154 / 4168
页数:15
相关论文
共 47 条
[1]  
Akers W.W., 1958, Chem. Engr. Prog, V54, P89
[2]  
Allen W.F., 1951, Trans. ASME, V73, P257
[3]  
Baroczi C.J., 1965, 8 NAT HEAT TRANSF C
[4]   A SIMPLE 2-PHASE FRICTIONAL PRESSURE-DROP CALCULATION METHOD [J].
BEATTIE, DRH ;
WHALLEY, PB .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1982, 8 (01) :83-87
[5]  
Benjamin N.M., 1942, T ASME, V64, P657
[6]  
Bhatti MS., 1987, Handbook of SinglePhase Convective Heat Transfer
[7]  
Bottomley W.T., 1936, Trans. North East Coast Inst. Engrs. Ship Builders, V53, P65
[8]  
Bowring R. W., 1972, AEEWR789 UK AT EN AU
[9]  
Cersey C.O., 1995, INT J HEAT MASS TRAN, V38, P643
[10]  
Cersey C.O., 1995, INT J HEAT MASS TRAN, V38, P629