๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Flow Regimes, Holdup and Pressure Loss for Two-Phase Flow Through Vertical and Near Vertical Tubes

โœ Scribed by Spedding, P. L. ;Woods, G. S. ;Rahunathan, R. S. ;Watterson, J. K.


Publisher
Curtin University of Technology
Year
2008
Tongue
English
Weight
558 KB
Volume
9
Category
Article
ISSN
0969-1855

No coin nor oath required. For personal study only.

โœฆ Synopsis


Abstract

Twoโ€phase, airโ€water, coโ€current flow in a pipe, slightly inclined from the vertical at +86.5dฬ€, showed significant differences to both the corresponding vertical data and results obtained for other angles of inclination. The regime map obtained for the inclined flow was the same as that found with the vertical geometry at the higher gas rates where the annular flow regimes were present. The maps for the two geometries exhibited significant differences as the gas rate was lowered and the churn and intermittent flow patterns appeared. Two new flow regimes were discovered in the inclined flow data under these conditions, namely the slugโ€blow through slug and the slugโ€churn patterns.

The liquid holdup was, in general, greater with the inclined geometry, particularly at lower gas and liquid rates where the new types of flow patterns were in evidence. Models are presented which allow prediction of holdup with the inclined geometty for all patterns except the churn flow regime. The total pressure loss was, in general, higher for the inclined geometry. An explanation is presented based on the anisotropy of the liquid across the pipe due to the inclination from the vertical.


๐Ÿ“œ SIMILAR VOLUMES


Prediction of Pressure Loss and Holdup i
โœ Spedding, P.L. ;Cooper, R.K. ;Mcbride, W.J. ๐Ÿ“‚ Article ๐Ÿ“… 2008 ๐Ÿ› Curtin University of Technology ๐ŸŒ English โš– 246 KB ๐Ÿ‘ 1 views

## Abstract A new method is presented for calculation of twoโ€phase parameters for horizontal stratified plus roll wave pipe flow. An iterative momentum balance calculation was performed based on the actual average phase velocities and the gas liquid interfacial shape. The liquid holdup and two phas