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UDK: 66.011

2008. - V. 22. - N 1(81). - P. 83-87

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The raw material composition influence on octane number of pentane-hexane isomerization product was estimated using mathematical modeling method. Different variants of oil-processing reactors construction were viewed. On the basis of calculations for isomerization process the optimal construction was considered to be a radial reactor with the direction of raw material from the center into periphery.

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ОПТИМИЗАЦИЯ ВНУТРЕННИХ УСТРОЙСТВ РЕАКТОРА ИЗОМЕРИЗАЦИИ ПЕНТАН-ГЕКСАНОВОЙ ФРАКЦИИ

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