## Shorter Communications filters is solely in the equation for P(r. t) and in terms atfecsented in [ 11. In any event, each of the filters is an approximating the spatial variation of P. In practice, P is a much tion to the true, but unknown, exact filter. stronger function of t rather than r. so
Optimal inlet temperature trajectories for adiabatic packed reactors with catalyst decay
✍ Scribed by Juan R. González-Velasco; Miguel A. Gutiérrez-Ortiz; José A. González-Marcos; Norma Amadeo; Miguel A. Laborde; Mariano Paz
- Publisher
- Elsevier Science
- Year
- 1992
- Tongue
- English
- Weight
- 662 KB
- Volume
- 47
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
An algorithm for simulation and optimization of adiabatic fixed-bed reactors subject to catalyst deactivation is developed. It is applied to the low-temperature CO converter, the kinetic model for which is deduced from some industrial data and considering chlorine as the main cause of catalyst poisoning. Sintering is not considered due to the short range of variation of temperature in the catalyst bed. Optimal inlet temperature trajectories are determined to maximize the obtained total amount of reaction over a fixed operation time. Approximate optimal trajectories in discrete steps of temperature are proposed to be followed in industrial practice.
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📜 SIMILAR VOLUMES
Theoretical and experimental work on tubular reactors has shown that a high temperature reaction zone can be induced to move counter to the flow of reactants by conduction and/or radiation through the solid phase. This naturally occurring phenomenon represents a transient mode of operation that can