𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Kinetics and fixed-bed reactor modeling of butane oxidation to maleic anhydride

✍ Scribed by Ramesh K. Sharma; David L. Cresswell; Esmond J. Newson


Publisher
American Institute of Chemical Engineers
Year
1991
Tongue
English
Weight
763 KB
Volume
37
Category
Article
ISSN
0001-1541

No coin nor oath required. For personal study only.


πŸ“œ SIMILAR VOLUMES


Oxidation of Benzene to Maleic Anhydride
✍ C. Uraz; S. Atalay πŸ“‚ Article πŸ“… 2007 πŸ› John Wiley and Sons 🌐 English βš– 480 KB πŸ‘ 3 views

## Abstract In this project, the selective oxidation of benzene to maleic anhydride (MAN) was studied. Gas phase catalytic oxidation of benzene was carried out in a laboratory scale fluidized bed reactor on six different types of catalysts, which have different compositions. Effects of temperature,

Transient kinetics of n-Butane oxidation
✍ Xiao-Feng Huang; Cheng-Yue Li; Biao-Hua Chen; P. L. Silveston πŸ“‚ Article πŸ“… 2002 πŸ› American Institute of Chemical Engineers 🌐 English βš– 303 KB πŸ‘ 2 views

## Abstract Transient reaction kinetics is usually needed to model the reactor system operated under unsteady‐state mode to improve the performance of the catalyst packed in such a reactor system and to match operating conditions of different reaction steps in this system. The transient reaction ki

Dynamic modelling of a gas phase catalyt
✍ Knud Waede Hansen; Sten Bay JΓΈrgensen πŸ“‚ Article πŸ“… 1976 πŸ› Elsevier Science 🌐 English βš– 737 KB

A lange scale Bxed bed pilot reactor for performing dynamic experiments is described. The reactor system is especially designed to suppress secondary dispersion effects not characteristic for the packed bed itself. As a model reaction the reaction between oxygen (~1%) and hydrogen on a platinum cat

Computer Simulation of the Performance o
✍ G. Emig; A. May; P. Scheidel πŸ“‚ Article πŸ“… 2002 πŸ› John Wiley and Sons 🌐 English βš– 264 KB πŸ‘ 2 views

A reactor model for a downer-regenerator circulating fluidized-bed (CFB) during the partial oxidation of n-butane to maleic anhydride is presented. Upflow reactors (risers) suffer from severe solids back mixing and gas-solids-separation, in comparison down flow reactors exhibit a more uniform gas-so