scholarly journals A comprehensive, mechanistic heat transfer modeling package for dispersed flow film boiling—Part 2—Implementation and assessment

2015 ◽  
Vol 291 ◽  
pp. 302-311 ◽  
Author(s):  
Michael J. Meholic ◽  
David L. Aumiller ◽  
Fan-Bill Cheung
2001 ◽  
Author(s):  
C. Frepoli ◽  
A. J. Ireland ◽  
L. E. Hochreiter ◽  
F. B. Cheung

Abstract The droplet injection experiments to be performed in a 7 × 7 rod bundle heat transfer test facility are being simulated using an advanced thermal hydraulics computer code called COBRA-TF. A current version of the code, which provides a three-dimensional, two-fluid, three-field representation of the two-phase flow, is modified to facilitate the simulation of the droplet field produced by the injection system in the test facility. The liquid phase is split into a continuous liquid field and droplet field where a separate momentum and mass equation is solved for each field, with the effects of spacer grids being properly accounted for. Pre-test analyses using the modified COBRA-TF code have been conducted for different injection conditions. Results indicate that there are specific ranges of conditions that can be simulated within the facility constraints to provide for validation of the dispersed flow film boiling models. The numerical results also show important effects of the spacer grids on the local heat transfer in the dispersed flow film boiling regime.


1983 ◽  
Vol 60 (2) ◽  
pp. 304-313 ◽  
Author(s):  
Graydon L. Yoder ◽  
David G. Morris ◽  
Charles B. Mullins ◽  
Larry J. Ott

1968 ◽  
Vol 90 (4) ◽  
pp. 399-407 ◽  
Author(s):  
R. P. Forslund ◽  
W. M. Rohsenow

New data for dispersed flow film boiling of nitrogen are presented for the following conditions: tube diameter 0.228, 0.323, and 0.462 in. ID; length 4 and 8 ft; mass velocity 70,000 to 19,000 lb/hr ft2; heat flux 0 to 2500 Btu/hr ft2; inlet condition near saturation; exit quality 35 to 315 percent. The previously presented analysis [12] is improved by accounting for droplet breakup due to vapor acceleration, modified drag coefficient on accelerating droplets, and a “Leidenfrost” heat transfer from the wall to the droplets at lower qualities. Measurements are also made to verify the existence of the substantial amount of vapor superheat in the presence of liquid droplets, as predicted by the analysis.


2013 ◽  
Vol 181 (1) ◽  
pp. 106-114 ◽  
Author(s):  
Michael J. Meholic ◽  
David L. Aumiller ◽  
Fan-Bill Cheung

Sign in / Sign up

Export Citation Format

Share Document