Kinetic model of the catalytic reforming of gasolines in moving-bed reactors

M. S. Gyngazova, A. V. Kravtsov, E. D. Ivanchina, M. V. Korolenko, D. D. Uvarkina

Research output: Contribution to journalArticle

8 Citations (Scopus)

Abstract

A mathematical model of the catalytic reforming of gasolines in a reactor with continuous catalyst regeneration is proposed. The model takes into account the motion of the catalyst, changes in its activity along the bed height, and the dependence of its activity on the circulation ratio. The kinetic parameters of the Pt-Sn catalyst are determined under operational conditions by solving the inverse kinetic problem. The composition of the reformate component as calculated by the model coincides with the experimental data within the accuracy of chromatographic analysis. The proposed model is invariant to the composition of raw materials and can be used for predictive calculations.

Original languageEnglish
Pages (from-to)374-380
Number of pages7
JournalCatalysis in Industry
Volume2
Issue number4
DOIs
Publication statusPublished - Dec 2010

Keywords

  • catalytic reforming of gasolines
  • kinetic model
  • moving-bed reactor

ASJC Scopus subject areas

  • Catalysis

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