## 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
β¦ LIBER β¦
Pressure drop in gas-liquid downflow through packed beds
β Scribed by P. S. T. Sai; Y. B. G. Varma
- Publisher
- American Institute of Chemical Engineers
- Year
- 1987
- Tongue
- English
- Weight
- 672 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Prediction of two-phase pressure drop an
β
Ponnan Ettiyappan Jagadeesh Babu; Appusamy Arunagiri; Thanapalan Murugesan
π
Article
π
2005
π
Wiley (John Wiley & Sons)
π
English
β 230 KB
π 1 views
A model for pressure drop in two-phase g
β
V. G. Rao; A. A. H. Drinkenburg
π
Article
π
1985
π
American Institute of Chemical Engineers
π
English
β 800 KB
Lateral thermal dispersion in gas-liquid
β
K. Grosser; R. G. Carbonell; A. Cavero; A. E. SΓ‘ez
π
Article
π
1996
π
American Institute of Chemical Engineers
π
English
β 685 KB
Solid-liquid mass transfer in packed bed
β
V. G. Rao; A. A. H. Drinkenburg
π
Article
π
1985
π
American Institute of Chemical Engineers
π
English
β 951 KB
Two-phase pressure drop in cocurrent dow
β
L. D. Clements; P. C. Schmidt
π
Article
π
1980
π
American Institute of Chemical Engineers
π
English
β 364 KB
π 2 views
Influence of liquid viscosity and bed po
β
Ahamed Khan; Asad Ali Khan; Y. B. G. Varma
π
Article
π
2002
π
John Wiley and Sons
π
English
β 177 KB
π 1 views
## Abstract It was observed in the experimental investigations that the concurrent upflow of airβMonoethanol amine system through the packed bed gave higher pressure drop in bubble flow regime than the airβwater system. But when the flow regime changed to spray flow, airβwater system showed higher