## Abstract A threeβdimensional CFD model has been developed to predict liquid phase velocities in bubble columns. An agreement was observed between the predicted and the experimental data available in the published literature. The validated CFD model has been extended for the simulation of macroβm
β¦ LIBER β¦
Mixing Time in a Short Bubble Column
β Scribed by M Ravinath; Gopal R. Kasat; Aniruddha B. Pandit
- Publisher
- John Wiley and Sons
- Year
- 2008
- Tongue
- English
- Weight
- 466 KB
- Volume
- 81
- Category
- Article
- ISSN
- 0008-4034
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
CFD Simulation of Residence Time Distrib
β
Kalekudithi Ekambara; Jyeshtharaj B. Joshi
π
Article
π
2008
π
John Wiley and Sons
π
English
β 698 KB
Liquid circulation and mixing in an incl
β
George Z. Lu; Kevin Bittorf; Brad G. Thompson; Murray R. Gray
π
Article
π
1997
π
John Wiley and Sons
π
English
β 796 KB
Axial mixing in a 15 cm diameter recipro
β
Malcolm H. I. Baird; Nadella V. Rama Rao
π
Article
π
1998
π
John Wiley and Sons
π
English
β 938 KB
Axial liquid mixing in high-pressure bub
β
G. Q. Yang; L. S. Fan
π
Article
π
2003
π
American Institute of Chemical Engineers
π
English
β 339 KB
π 1 views
Bubble dynamics investigation in a slurr
β
Chengtian Wu; Kelsey Suddard; Muthanna H. Al-dahhan
π
Article
π
2008
π
American Institute of Chemical Engineers
π
English
β 974 KB
Characterization of gas transfer and mix
β
Bjarne Rask Poulsen; Jens JΓΈrgen LΓΈnsmann Iversen
π
Article
π
1998
π
John Wiley and Sons
π
English
β 262 KB
π 1 views
Gas transfer and mixing were characterized in a 32-L bubble column reactor equipped with a commercially available rubber membrane diffuser. The performance of the membrane diffuser indicates that the slits in the membrane are best described as holes with elastic lids, acting as valves cutting off bu