## Abstract Reaction rates of selective hydrogenation of phenylacetylene (PA) and styrene were studied in a packedβbed reactor with concurrent gas and liquid upflow. The surface reaction rates were expressed by the reaction between adsorbed PA or styrene and dissociated hydrogen atoms competing for
β¦ LIBER β¦
Mass transfer in a fixed-bed gas-liquid catalytic reactor with concurrent upflow
β Scribed by James W. Snider; Joseph J. Perona
- Publisher
- American Institute of Chemical Engineers
- Year
- 1974
- Tongue
- English
- Weight
- 598 KB
- Volume
- 20
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Selective hydrogenation and mass transfe
β
Satoshi Mochizuki; Tatsuro Matsui
π
Article
π
1976
π
American Institute of Chemical Engineers
π
English
β 528 KB
Mass transport phenomena and hydrodynami
β
Satoshi Mochizuki
π
Article
π
1978
π
American Institute of Chemical Engineers
π
English
β 349 KB
π 2 views
Gas-Liquid Mass Transfer in Fibrous Bed
β
M. Martinov; D. Hadjiev; S. D. Vlaev
π
Article
π
2009
π
John Wiley and Sons
π
English
β 212 KB
## Abstract In this work, the gasβliquid mass transfer in a labβscale fibrous bed reactor with liquid recycle was studied. The volumetric gasβliquid mass transfer coefficient, __k__~L~__a__, is determined over a range of the superficial liquid velocity (0.0042β0.0126Β m.s^β1^), gas velocity (0.006β0
Gas-Liquid mass transfer in fixed-bed re
β
J. R. Blok; C. E. Koning; A. A. H. Drinkenburg
π
Article
π
1984
π
American Institute of Chemical Engineers
π
English
β 791 KB
Identification of Flow Regimes in a Conc
β
A. V. Raghavendra Rao; R. Kishore Kumar; T. Sankarshana; A. Khan
π
Article
π
2011
π
John Wiley and Sons
π
English
β 326 KB
π 2 views
Heat Transfer in Catalytic Fixed-Bed Rea
β
M. Bauer; R. Adler
π
Article
π
2003
π
John Wiley and Sons
π
English
β 103 KB