Experimental investigation of CHF during countercurrent flow in transient boiling systems

Authors
Citation
Yt. Kang, Experimental investigation of CHF during countercurrent flow in transient boiling systems, HEAT TR ENG, 20(4), 1999, pp. 27-37
Citations number
13
Categorie Soggetti
Chemical Engineering
Journal title
HEAT TRANSFER ENGINEERING
ISSN journal
01457632 → ACNP
Volume
20
Issue
4
Year of publication
1999
Pages
27 - 37
Database
ISI
SICI code
0145-7632(199910/12)20:4<27:EIOCDC>2.0.ZU;2-Q
Abstract
The objectives of this study are to investigate the effects of the power tr ansient on critical heat flux (CHF), and to develop CHF and maximum heat fl ux (MHF) correlations in transient boiling systems with a countercurrent fl ow between the liquid and vapor flow: The test section consists of narrow: vertical, rectangular channels between parallel plates. Rate of change of w all temperature at the CHF point, (dT(w)/dt)(CHF), and a nondimensional tra nsient parameter, tau(o) = (L-2/alpha(f) T-sat)/(dT(w)/dt)/(CHF) are introd uced to evaluate the effects of power transients on CHF and MHF, Experiment al ranges were 738.0-1,968.0 kg/m(2)s for mass flux, 7.0-17.5 degrees C for inlet subcooling, and 3.0-8.0 mm for channel gap distance. The system pres sure was kept constant at 1.0 aim. The experimental results show that CHF a nd MHF values increase with an increasing rate of change of wall temperatur e, and the increasing rate of CHF is higher in a wider channel gap distance . CHF and MNF increase linearly with increasing mass flux at the top of the test section, and the linearity decreases at the bottom of the test sectio n, The effect of the inlet subcooling is significant at the top of the test section, therefore the test location closest to liquid inlet has a higher CHF value than the location immediately below it, It,was also found that th e wider the channel gap distance, the higher was the CHF value obtained for a given rate of change of wall temperature. New CHF and MHF correlations a re developed for countercurrent flow in transient boiling systems. The CHF and MHF correlations are in good agreement with the experimental data withi n +/-25% error bands, respectively.