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https://doi.org/10.15255/CABEQ.2015.2299

Derivation of Pareto Optimal Operating Policies Based on Safety Indices for a Catalytic Multi-tubular Reactor Used for Nitrobenzene Hydrogenation

G. Maria orcid id orcid.org/0000-0003-3650-676X ; Department of Chemical and Biochemical Engineering, University POLITEHNICA of Bucharest
H. H. S. Khwayyir ; Department of Chemical and Biochemical Engineering, University POLITEHNICA of Bucharest; PhD student; leaving from Najaf Technical College Al-Furat Al-Awsat Technical University, Iraq
D. Dinculescu ; Department of Chemical and Biochemical Engineering, University POLITEHNICA of Bucharest


Puni tekst: engleski pdf 528 Kb

str. 279-290

preuzimanja: 451

citiraj


Sažetak

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.

Ključne riječi

chemical reactor failure probability; runaway boundaries; Pareto optimal policies; confidence region; catalytic reactor for aniline production

Hrčak ID:

167257

URI

https://hrcak.srce.hr/167257

Datum izdavanja:

6.10.2016.

Posjeta: 971 *