Monitoring of the commercial operation of reforming catalysts using a computer simulation system
| Parent link: | Catalysis in Industry: Scientific Journal Vol. 1, iss. 2.— 2009.— [P. 128-133] |
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| مؤلفون آخرون: | , , , , |
| الملخص: | Title screen A methodology of constructing nonstationary kinetic models of multicomponent catalytic processes of hydrocarbon conversion on platinum-containing catalysts was developed. Their kinetic and technological parameters in industrial catalytic reforming were estimated. The simulation system in gasoline production allows for the testing and choosing of an optimum catalyst depending on the composition of the processed hydrocarbon raw materials. The developed testing technique is based on the processing of the results of the commercial operation of platinum-containing reforming catalysts using the computer simulation system. It allows the estimation of kinetic parameters, the prediction of selectivity, and raw cycle duration after catalyst regeneration under conditions of commercial operation, taking into account the reactivity of hydrocarbons. Режим доступа: по договору с организацией-держателем ресурса |
| منشور في: |
2009
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| الموضوعات: | |
| الوصول للمادة أونلاين: | http://dx.doi.org/10.1134/S2070050409020068 |
| التنسيق: | الكتروني فصل الكتاب |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=639835 |
| الملخص: | Title screen A methodology of constructing nonstationary kinetic models of multicomponent catalytic processes of hydrocarbon conversion on platinum-containing catalysts was developed. Their kinetic and technological parameters in industrial catalytic reforming were estimated. The simulation system in gasoline production allows for the testing and choosing of an optimum catalyst depending on the composition of the processed hydrocarbon raw materials. The developed testing technique is based on the processing of the results of the commercial operation of platinum-containing reforming catalysts using the computer simulation system. It allows the estimation of kinetic parameters, the prediction of selectivity, and raw cycle duration after catalyst regeneration under conditions of commercial operation, taking into account the reactivity of hydrocarbons. Режим доступа: по договору с организацией-держателем ресурса |
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| DOI: | 10.1134/S2070050409020068 |