## Abstract The dependency of pressure drop and liquid holdup on phase velocities, geometry of the column and packing materials as well as on the physical properties have been analyzed. Our experimental data (825 data points obtained using four liquid systems and three different particles) along wi
Flow regimes, liquid holdups and two-phase pressure drop for two-phase cocurrent downflow and upflow through packed beds: air/Newtonian and non-Newtonian liquid systems
β Scribed by I. Iliuta; F.C. Thyrion
- Publisher
- Elsevier Science
- Year
- 1997
- Tongue
- English
- Weight
- 479 KB
- Volume
- 52
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
The analysis of the hydrodynamics results of two-phase downflow and upflow through fixed beds with porous particles shows that the flow regimes, two-phase pressure drop and liquid holdups are strongly influenced by the presence of the non-Newtonian liquids. With highly viscous non-Newtonian liquids the hydrodynamic characteristics (pressure drop, dynamic and total liquid holdups) of two-phase downflow are close to those of two-phase upflow-the axial dispersion appears to be an important cause for the possible effects of the hydrodynamics on the reactor performance. ,
π SIMILAR VOLUMES
An experimental investigation was carried out to determine the effects of gas and liquid flow rates and flow consistency index on the liquid-phase axial dispersion coefficient, pressure drop and the liquid holdup for two-phase downflow and upflow in a fixed bed. Water and non-Newtonian liquids were
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,