Study on the two-phase critical flow through a small bottom break in a pressurized horizontal pipe

2008 ◽  
Vol 313 (1-2) ◽  
pp. 7-15 ◽  
Author(s):  
Moon-Sun Chung
2007 ◽  
Author(s):  
Wenhong Liu ◽  
Liejin Guo ◽  
Ximin Zhang ◽  
Kai Lin ◽  
Long Yang ◽  
...  

Author(s):  
L. Wenhong ◽  
G. Liejin ◽  
Z. Ximin ◽  
L. Kai ◽  
Y. Long ◽  
...  

2008 ◽  
Author(s):  
Moon-Sun Chung ◽  
Sung-Jae Lee

Two-phase critical flows through some breaks of pressurized pipe systems are calculated by an improved critical flow model. These phenomena have many difficulties in predicting the two-phase critical flow rates at the break points mainly due to the inaccuracies of the critical flow model. Further, the case of critical flow through the small bottom break of horizontal pipe, the accuracy of a quality prediction model is also important as well as the critical flow model itself. In this study, an improved critical flow model is introduced which is based on a new sound speed criterion derived from the hyperbolic two-fluid model for non-equilibrium flow and this model is implemented to a system analysis code. Following to the vertically upward flows with quality variation and Marviken tests as benchmark problems, the small bottom break of a pressurized horizontal pipe is calculated and discussed in some details. The assessment results on the critical flow test through a small bottom break in a horizontal pipe show the importance of the accuracy of the critical flow model as well as that of the quality prediction model to reduce the relative errors.


2014 ◽  
Vol 501 ◽  
pp. 012015 ◽  
Author(s):  
L P M Colombo ◽  
M Guilizzoni ◽  
G M Sotgia ◽  
S Bortolotti ◽  
L Pavan

1971 ◽  
Vol 93 (2) ◽  
pp. 179-187 ◽  
Author(s):  
Robert E. Henry ◽  
Hans K. Fauske

The critical flow of one-component, two-phase mixtures through convergent nozzles is investigated and discussed including considerations of the interphase heat, mass, and momentum transfer rates. Based on the experimental results of previous investigators, credible assumptions are made to approximate these interphase processes which lead to a transcendental expression for the critical pressure ratio as a function of the stagnation pressure and quality. A solution to this expression also yields a prediction for the critical flow rate. Based on the experimental results of single-phase compressible flow through orifices and short tubes, the two-phase model is extended to include such geometries. The models are compared with steam-water, cryogenic, and alkali-metal experimental data.


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