## Abstract The use of an internal circulating fluidized bed (ICFB) is proposed for the oxidative dehydrogenation of butane. The reactor consists of two adjacent zones, separated by a wall. In the oxidizing zone the catalyst is oxidized and in the reducing zone the butane is dehydrogenated by react
Oxidative dehydrogenation of butane using membrane reactors
✍ Scribed by C. Téllez; M. Menéndez; J. Santamaría
- Publisher
- American Institute of Chemical Engineers
- Year
- 1997
- Tongue
- English
- Weight
- 829 KB
- Volume
- 43
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
📜 SIMILAR VOLUMES
Accurate simulation of fixed-bed catalytic reactors requires the computation of the effectiveness factors at each point along the length of the reactor. This requires the formulation and solution of rigorous diffusion-reaction models for the porous pellets based on the more rigorous Stefan-Maxwell e
## Abstract A membrane reactor incorporating a hollow fiber with successive parts of oxygen permeable and passivated surface segments has been developed and was used for the oxidative dehydrogenation (DH) of propane. This membrane geometry allows a controlled oxygen feeding into the reactor over it
For the oxidative dehydrogenation of methanol to formaldehyde over a Fe-Mo oxide catalyst, the performance of packed-bed membrane reactor (PBMR) was compared experimentally with that of a conventional fixed-bed reactor (FBR) under identical reaction conditions (overall species flowrates, temperature
## Abstract Propane dehydrogenation has been simulated for a composite membrane reactor and a microporous membrane reactor using plug‐flow reactor models, in which both were packed with Pt/Al~2~O~3~ catalyst in the tube‐side. The reaction kinetics employed in the analysis were obtained from experim