Back to Search
Start Over
A comparative study of sandwich cross-flow and random catalytic packings for multiphase chemical reactors
- Source :
- Chemical Engineering Science. 54:3677-3682
- Publication Year :
- 1999
- Publisher :
- Elsevier BV, 1999.
-
Abstract
- The aim of this work was to investigate the performance of a cross-flow sandwich catalytic structure and to compare it with that of conventional random packings. The liquid-phase catalytic hydrogenation of Styrene to Ethylbenzene in n-Butanol solution was chosen as the test reaction. The intrinsic kinetics of the reaction was preliminarly investigated in a batch multiphase rotating basket reactor. The tests with the various kinds of catalytic packing were carried out in a tubular reactor (50 mm internal diameter) by recycling both the liquid and the gas phase. The results of this work show that mass transfer and hydrodynamic limiting effects in cross-flow structured packing are significantly lower than in a random bed of particles both in upflow and downflow concurrent regimes.
- Subjects :
- Work (thermodynamics)
Chromatography
Applied Mathematics
General Chemical Engineering
chemistry.chemical_element
General Chemistry
Structured packing
Chemical reactor
Ethylbenzene
Industrial and Manufacturing Engineering
Catalysis
Styrene
chemistry.chemical_compound
chemistry
Chemical engineering
Mass transfer
Palladium
Subjects
Details
- ISSN :
- 00092509
- Volume :
- 54
- Database :
- OpenAIRE
- Journal :
- Chemical Engineering Science
- Accession number :
- edsair.doi...........c02d390370ffcf2481b925aabb7ade0c