a significative improvement of yield and selectivity can be achieved.
On the experimental study and scale-up of three-phase catalytic reactors: Hydrogenation of glucose on nickel catalyst
โ Scribed by F. Turek; R.K. Chakrabarti; R. Lange; R. Geike; W. Flock
- Publisher
- Elsevier Science
- Year
- 1983
- Tongue
- English
- Weight
- 616 KB
- Volume
- 38
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
โฆ Synopsis
Measurements of reaction kinetics and pore diffusion were made in four different types of laboratory scale reactors_ 'lbe liquid-phase hydrogenation of glucose to sorbit on a nickel-silica catalyst was studied at 80 to 150ยฐC and 1.6 to 10 MPa using two sizes of catalyst pellets and powdered catalysts. The experimental results were computed with the help of a heterogeneous model by employing the kinetic parameters. The objective was to show the applicability of the reaction kinetics and the effective diiusivities under other operating conditions.
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