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Title: Pitch-to-diameter effect on two-phase flow across an in-line tube bundle

Journal Article · · A.I.Ch.E. Journal (American Institute of Chemical Engineers); (United States)
;  [1];  [2]
  1. Dept. of Chemical Engineering and Applied Chemistry, Univ. of Toronto, Toronto, Ontario M5S 1A4 (CA)
  2. Ontario Hydro Research Div., Ontario Hydro Toronto, Ontario (CA)

This paper reports on void fraction and friction pressure drop measurements that were made for an adiabatic, vertical two-phase flow of air-water across two horizontal, in-line, 5 {times} 20 rod bundles, one with a pitch-to-diameter ratio, P/D, of 1.3, the other 1.75. For both bundles the average void fraction showed a strong mass velocity effect and values were significantly less than those predicted by a homogeneous flow model. All void fraction data were found to be well correlated, with no P/D effect, using the dimensionless gas velocity, j*{sub g}. The two-phase friction multiplier data exhibited a strong effect of P/D and mass velocity, however, the data for both bundles could be well correlated with the Martinelli parameter for G {gt} 200 kg/m{sup 2}s. The correlations developed for void fraction and two-phase friction multiplier were successfully tested in predicting the total pressure drop in boiling freon experiments.

OSTI ID:
5540447
Journal Information:
A.I.Ch.E. Journal (American Institute of Chemical Engineers); (United States), Vol. 36:5; ISSN 0001-1541
Country of Publication:
United States
Language:
English