Abstract
A 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-stage ammonia synthesis reactor. The SMCA can be implemented in reactors which have ageing catalysts and maldistributed gas. The SMCA has been applied efficiently to industrial SO 2 oxidation and NH 3 synthesis plants. Suggestions on the design of a new MAFBR are made.
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