Abstract
A universal mathematical model is derived for a reforming process in a series of three reactors with an intermediate preheated mix.
Results are presented for the modeling of reforming processes with a radial axial input of components of the reaction mix; this makes it possible to select the volume of catalyst and inlet temperature, which will ensure a product of the required quality with the reformer operating at a given output.
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References
W. L. Leffler, Petroleum Refining [Russian translation], 2nd edition, revised, Olimp-Biznes ZAO, Moscow (2004).
G. N. Maslyanskii and R. N. Shapiro, Catalytic Reforming of Gasolines: Chemistry and Technology [in Russian], Khimiya, Leningrad (1985).
B. Zharkov, “New developments in the field of catalytic gasoline reforming” Tekhnol. TÉK, No. 10 (2003).
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Translated from Khimicheskoe i Neftegazovoe Mashinostroenie, No. 10, pp. 9–11, October, 2007.
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Sharikov, Y.V., Petrov, P.A. Universal model for catalytic reforming. Chem Petrol Eng 43, 580–584 (2007). https://doi.org/10.1007/s10556-007-0103-z
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DOI: https://doi.org/10.1007/s10556-007-0103-z