The residence time distribution of the gas passing through an agitated gas-liquid contactor of 0.6 m diameter was measured for various gas loads and agitator speeds, sires and heights. It was found that in the region where the agitation is effective (n > no) the residence time distribution closely r
β¦ LIBER β¦
Residence time distribution of the gas phase in a mechanically agitated gas-liquid reactor.
β Scribed by M.P.G. Thijert; M.H. Oyevaar; W.J. Kuper; K.R. Westerterp
- Publisher
- Elsevier Science
- Year
- 1992
- Tongue
- English
- Weight
- 610 KB
- Volume
- 47
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
The residence time distribution of the g
β
J. Hanhart; H. Kramers; K.R. Westerterp
π
Article
π
1963
π
Elsevier Science
π
English
β 593 KB
Interfacial areas and gas hold-ups at el
β
Ir. Martin Oyevaar; Ir. Ad Zijl; Prof. Dr. Ir. Roel Westerterp
π
Article
π
1988
π
John Wiley and Sons
π
English
β 898 KB
Role of sparger design in mechanically a
β
Prof. Vilas B. Rewatkar; Jyeshtharaj B. Joshi
π
Article
π
1991
π
John Wiley and Sons
π
English
β 661 KB
Phenomena in residence time distribution
β
Eduard Plasari; RenΓ© David; Jacques Villermaux
π
Article
π
1977
π
Elsevier Science
π
English
β 349 KB
Residence time distribution of the liqui
β
Xue-Long Yang; Jean-Paul Euzen; Gabriel Wild
π
Article
π
1990
π
Elsevier Science
π
English
β 652 KB
The authors present the first experimental investigation of the residence time distribution of the liquid in a gas-liquid upflow fixed-bed reactor with porous particles. The PDE model (plug flow with axial dispersion and exchange with well-mixed stagnant zones) represents very well the experimental
Residence time distribution in three-pha
β
Robert H. Patrick Jr.; Theresa Klindera; Lawrence L. Crynes; Ramon L. Cerro; Mar
π
Article
π
1995
π
American Institute of Chemical Engineers
π
English
β 832 KB