Droplet flux measurements in two-phase, low liquid loading, horizontal pipe flow using a high-density gas

2018 ◽  
Vol 56 ◽  
pp. 472-485 ◽  
Author(s):  
Netaji R. Kesana ◽  
Roar Skartlien ◽  
Morten Langsholt ◽  
Roberto Ibarra ◽  
Murat Tutkun
2019 ◽  
Vol 70 ◽  
pp. 102967
Author(s):  
Deendarlianto ◽  
Akhmad Zidni Hudaya ◽  
Indarto ◽  
Katya Dara Ozzilenda Soegiharto

Author(s):  
J.S. Cole ◽  
G.F. Donnelly ◽  
P.L. Spedding

1987 ◽  
Vol 13 (6) ◽  
pp. 815-821 ◽  
Author(s):  
A.M. Lali ◽  
A.S. Khare ◽  
J.B. Joshi ◽  
A.C. Eapen ◽  
S.M. Rao ◽  
...  

2005 ◽  
Vol 25 (Supplement2) ◽  
pp. 289-290
Author(s):  
Junichi OHASHI ◽  
Kazumasa INABA ◽  
Yuji TASAKA ◽  
Yuichi MURAI ◽  
Yasushi TAKEDA
Keyword(s):  

AIChE Journal ◽  
1991 ◽  
Vol 37 (2) ◽  
pp. 274-276 ◽  
Author(s):  
Douglas R. Sommerville

Author(s):  
Florentina Popa ◽  
Andrey Filippov ◽  
Brent C. Houchens

One-dimensional (1D), equilibrium-based mechanistic model predictions are compared to three-dimensional (3D) transient computational fluid dynamics results for horizontal two-phase, gas-liquid pipe flow. The 3D regions of interest include both those expected to be in equilibrium conditions and those where transitions between flow regimes occur. Equilibrium simulations, such as those for stratified flow in a horizontal pipe, allow crucial validation of the equilibrium-based closure relations by means of numerical experiments. In the transitional regions, fully 3D, time-dependent numerical simulations provide a means to estimate the error in the equilibrium-based models and suggest how reasonable approximations can be made in these regions.


1997 ◽  
Vol 119 (4) ◽  
pp. 209-216 ◽  
Author(s):  
X. T. Chen ◽  
X. D. Cal ◽  
J. P. Brill

Gas-liquid stratified-wavy flow with low liquid loading is common in natural gas transmission pipelines and offshore gas pipelines. This specific case of two-phase pipe flow has been studied experimentally and theoretically in the present paper. The interfacial behavior during air-kerosene stratified-wavy flow in a 77.9-mm-dia 420-m-long pipeline was observed carefully. The gas-liquid interface usually exhibits a concave downward curved configuration. The liquid film-wetted wall fraction, liquid holdup, and pressure drop were also measured. A mechanistic “double-circle” model and a correlation for interfacial friction factor, required as a closure relationship in the model, have been developed. The new model gives significantly improved predictions for both liquid holdup and pressure drop during gas-liquid stratified-wavy flow in horizontal pipelines.


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