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Information Journal Paper

Title

MATHEMATICAL MODELING OF AN INDUSTRIAL NAPHTHA REFORMER WITH THREE ADIABATIC REACTORS IN SERIES

Pages

  97-102

Abstract

 A mathematical model for commercial naphtha catalytic reformer of Tehran refinery was developed. This model includes three sequencing fixed beds of Pt/Al2O3 catalyst at the steady state condition using detailed kinetic scheme involving 26 pseudo-components connected by a network of 47 reactions, in the range of C6 to C9 hydrocarbons. The reaction network consisted dehydrogenation, hydrogenation, ring expansion, paraffin and iso-paraffin cracking, naphthene cracking, paraffin isomerization and hydrodealkylation of aromatics. The KINETIC MODEL was fine tuned against industrial plant data using a feed characterized by PIONA (Paraffin, Iso-paraffin, Oleffin, Naphthene and Aromatics) analysis. The final outlet results of the reformer such as RON (Research Octane Number), yield and outlet reformate compositions have shown good agreement with actual conditions of Tehran Refinery reforming unit.

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  • Cite

    APA: Copy

    FAZELI, ALI, FATEMI, SHOHREH, MAHDAVIAN, MOHAMMAD, & GHAEE, A.. (2009). MATHEMATICAL MODELING OF AN INDUSTRIAL NAPHTHA REFORMER WITH THREE ADIABATIC REACTORS IN SERIES. IRANIAN JOURNAL OF CHEMISTRY AND CHEMICAL ENGINEERING (IJCCE), 28(3), 97-102. SID. https://sid.ir/paper/564456/en

    Vancouver: Copy

    FAZELI ALI, FATEMI SHOHREH, MAHDAVIAN MOHAMMAD, GHAEE A.. MATHEMATICAL MODELING OF AN INDUSTRIAL NAPHTHA REFORMER WITH THREE ADIABATIC REACTORS IN SERIES. IRANIAN JOURNAL OF CHEMISTRY AND CHEMICAL ENGINEERING (IJCCE)[Internet]. 2009;28(3):97-102. Available from: https://sid.ir/paper/564456/en

    IEEE: Copy

    ALI FAZELI, SHOHREH FATEMI, MOHAMMAD MAHDAVIAN, and A. GHAEE, “MATHEMATICAL MODELING OF AN INDUSTRIAL NAPHTHA REFORMER WITH THREE ADIABATIC REACTORS IN SERIES,” IRANIAN JOURNAL OF CHEMISTRY AND CHEMICAL ENGINEERING (IJCCE), vol. 28, no. 3, pp. 97–102, 2009, [Online]. Available: https://sid.ir/paper/564456/en

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