Hydrogenation of P-ethyl-herenal was perform\*d Honolithic reactor, segmented flcm, \*11\*\* transfer, liquid-phase reactions.
Mass transfer and selectivity in liquid-phase hydrogenation of nitro compounds in a monolithic catalyst reactor with segmented gas-liquid flow
โ Scribed by Hatziantoniou, Vasilios; Andersson, Bengt; Schoon, Nils Herman
- Book ID
- 120554184
- Publisher
- American Chemical Society
- Year
- 1986
- Weight
- 858 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0196-4305
No coin nor oath required. For personal study only.
๐ SIMILAR VOLUMES
The deactivation of a monolithic Pd/a-alumina catalyst in the selective hydrogenation of acetylene in the presence of excess ethylene has been studied. The deactivation behavior of the monolithic catalyst in the gas-phase hydrogenation was compared to that of the liquid-phase hydrogenation. It was s
## Abstract Reaction rates of selective hydrogenation of phenylacetylene (PA) and styrene were studied in a packedโbed 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
## Abstrac -The itiuence of polsonmg and mass transport on the performance of a suspended palladmm catalyst for the hquid-phase hydrogenatton of o-cresol has been mvestlgated Rate expressIons were defined for the various transport and reaction steps occunng m the three-phase slurry system and thes