Chenucal reactors for a smgle exothernuc reverslble reaction wlth mmlmum volume for a @ven duty are conndered m whlch the temperature IS controlled du-ectly by bypassmg cold feed around a mam feed preheater and dlstnbuting It along the length of the reactor, and rn whlch the temperature may not exce
Optimum distributed feed reactors for exothermic reversible reactions
β Scribed by D. C. Dyson; F. J. M. Horn
- Publisher
- Springer
- Year
- 1967
- Tongue
- English
- Weight
- 582 KB
- Volume
- 1
- Category
- Article
- ISSN
- 0022-3239
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Exothennic reversible reactions are industrially very significant. Previous work has looked at finding the Attainable Region for elementary kinetics and in this paper we extend the work to find optimal reactors for more complex kinetics. Using these results we show how the complexity of the kinetics
Periodic flow reversal in a packed catalytic reactor in which a reversible exothermic reaction is occurring is studied using a simplified mathematical model. Model simulations are firstly performed for a single reactor and the influence of cycle time and the use of inert sections on the ends of the
A membrane reactor with separated feed of reactants is demonstrated as a promising contactor type when dealing with heterogeneously catalysed, very fast and exothermic gas phase reactions. Due to the separation of reactants a good control of the system is obtained, because process variables can be v
Previously reported design criteria for cooled tubular reactors are based on the prevention of reactor temperature runaway and were developed for single reactions only. In this paper it is argued that such criteria should be based on the reactor selectivity, from which eventually a maximum allowable