Influence of the unsteady state operations on yield and selectivity of a three phase catalytic reactor
β Scribed by L. Manna; S. Sicardi; G. Baldi; L.van Dierendonck; T. Smeets; A. Stankiewicz
- Publisher
- Elsevier Science
- Year
- 1992
- Tongue
- English
- Weight
- 462 KB
- Volume
- 47
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
β¦ Synopsis
a significative improvement of yield and selectivity can be achieved.
π SIMILAR VOLUMES
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 150Β°C and 1.6 to 10 MPa using two sizes of catalyst pellets and powdered catalys
Till now the use of two phase models for the catalytic fixed-bed reactor in the region of multiple steady states led to somewhat confusing results. A continuum of multiple steady state solutions has been obtained no matter whether the continuous two phase models proposed by Liu and Amundson or the c
It has been shown in a preceding paper that a reasonable two-phase model for the catalytic fixed-bed reactor in the region of multiple steady states should take into account beat conduction in the catalyst phase. In this paper the study of the proposed model will be continued using the example of th