Experimental and Numerical Analysis of Two-Phase Flows in Plunge Pools

2020 ◽  
Vol 146 (6) ◽  
pp. 04020044 ◽  
Author(s):  
J. M. Carrillo ◽  
L. G. Castillo ◽  
F. Marco ◽  
J. T. García
1989 ◽  
Vol 203 ◽  
pp. 475-515 ◽  
Author(s):  
R. Ishii ◽  
Y. Umeda ◽  
M. Yuhi

This paper is concerned with a numerical analysis of axisymmetric gas-particle two-phase flows. Underexpanded supersonic free-jet flows and supersonic flows around a truncated cylinder of gas-particle mixtures are solved numerically on the super computer Fujitsu VP-400. The gas phase is treated as a continuum medium, and the particle phase is treated partly as a discrete one. The particle cloud is divided into a large number of small clouds. In each cloud, the particles are approximated to have the same velocity and temperature. The particle flow field is obtained by following these individual clouds separately in the whole computational domain. In estimating the momentum and heat transfer rates from the particle phase to the gas phase, the contributions from these clouds are averaged over some volume whose characteristic length is small compared with the characteristic length of the flow field but large compared with that of the clouds. The results so obtained reveal that the flow characteristics of the gas-particle mixtures are widely different from those of the dust-free gas at many points.


Author(s):  
Rajeshwar Sripada ◽  
Vasudeva Rao Veeredhi ◽  
Siva Subrahmanyam Mendu

Abstract Critical heat flux (CHF) and premature tube burnout are the common failure modes observed in steam water two-phase flows. Unlike the vertically upward two-phase flows, the vertically downward two-phase flows pose significant challenges including two-phase flow instabilities and premature tube burnout arising due to competing behavior between the buoyancy effects on vapor bubble and momentum and gravitational force acting on the liquid. Experimental investigations were conducted previously to understand the CHF at atmospheric pressures. There were very limited number of numerical analysis conducted in vertically downward flows using commercially available software and at such low-pressure conditions. In the current investigations, numerical simulations were carried with commercially available computational fluid dynamics software Fluent for vertically downward two-phase flows up to pressures of 5 bar. The magnitude of CHF from numerical investigations was compared with the experimental results conducted in house up to 5 bar and including the sub-cooling effects. The numerical results tend to agree with the experimental data at lower flow rates and at all pressures considered, but tend to deviate significantly at higher flow rates and at all pressures. Finally, A CHF correlation is proposed as a function of mass flux, inlet temperature and pressure. The proposed CHF correlations fits in with an average deviation of 16% and a standard deviation of 21%.


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