Published: CABEQ 30 (3) (2016) 279-290
Paper type: Original Scientific Paper
G. Maria, H. H. S. Khwayyir and D. Dinculescu
Abstract
When highly exothermic/hazardous reactions are conducted in the presence of parametric uncertainty, derivation of optimal operating policies for a chemical reactor has to
simultaneously consider several objectives of sustainability. The paper uses an original
methodology to generate the Pareto optimal solutions when reactor productivity and
safety objectives (expressed in probabilistic terms) are simultaneously considered using
the process and reactor model in a simple way, in the presence of technological constraints, uncertainty in safety boundaries, and random fluctuations in control variables.
An example is provided for the industrial fixed-bed tubular reactor used for the catalytic
hydrogenation of nitrobenzene to aniline in vapour-phase.
This work is licensed under a Creative Commons Attribution 4.0 International License
Keywords
chemical reactor failure probability, runaway boundaries, Pareto optimal policies, confidence region, catalytic reactor for aniline production