๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Pressure drop and limit deposit velocity for solid-liquid flow in pipes

โœ Scribed by Pinchas Doron; Dvora Barnea


Publisher
Elsevier Science
Year
1995
Tongue
English
Weight
740 KB
Volume
50
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

โœฆ Synopsis


Experimental data of pressure drop and flow patterns for the pipe flow of solid-liquid mixtures were obtained. Special emphasis was put on the range of low mixture flow rates, where a stationary bed is expected.


๐Ÿ“œ SIMILAR VOLUMES


A phenomenological model for pressure dr
โœ R.A. Holub; M.P. Dudukoviฤ‡; P.A. Ramachandran ๐Ÿ“‚ Article ๐Ÿ“… 1992 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 467 KB

## A phenomenological, pore-scale, hydrodynamic model is developed for representation of the uniform, two-phase, gas-liquid cocurrent flow in the low interaction regime in trickle bed reactors. The model provides improved predictions for both the pressure drop and liquid holdup using the parameters

Pressure drop and liquid holdup for two
โœ V. Specchia; G. Baldi ๐Ÿ“‚ Article ๐Ÿ“… 1977 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 844 KB

Pressure drop and hqlud holdup for two-phase concurrent downward low m packed beds were correlated for various types of packmgs by takmg mto account two hydrodynanuc regnnes a poor and a h@ gas-bqlud mteraction regnne Foammg and non-foammg systems have been consldered In the poor mteractlon regune,

Experimental Validation of a Two-Phase F
โœ Christophe Boyer; Gilles Ferschneider ๐Ÿ“‚ Article ๐Ÿ“… 2008 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 659 KB

## Abstract A new model has been developed in order to predict pressure drop and gas fraction of industrial fixed bed reactor operated in downward bubbly flow. The mechanistic approach proposed by Attou and Ferschneider (1999) has been followed. In this approach, mass and momentum balances are solv