The optimization of the catalytic oxidation of sulphur dioxide in a multi-bed adiabatic reactor
β Scribed by G. Chartrand; C. M. Crowe
- Book ID
- 118282967
- Publisher
- John Wiley and Sons
- Year
- 1969
- Tongue
- English
- Weight
- 619 KB
- Volume
- 47
- Category
- Article
- ISSN
- 0008-4034
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π SIMILAR VOLUMES
general rule and a straightforward approach of the real optimal operation of a multistage adiabatic fixed-bed reactor (MAFBR) for a single reaction system, namely, the stagewise maximum conversion approach (SMCA), were derived based on the analysis of the operation of a Fauser-Montecatini type, five
Continual catalytic wet oxidation of phenol and its derivatives as a suitable chemical pretreatment before a biological treatment process was investigated. The evaluation of (i) the inΓuence of amino-, carboxy-and sulfo-phenol substituents on the course of the oxidation of hydroxyl-aromatics, (ii) t
The optimum design of an adiabatic reactor involves the choice of the size of each bed and the amount of interstage cooling between beds. These decisions can be made in an orderly way by applying the notion of dynamic programming, and in the case of a single reaction allow of a simple graphical pres