Mathematical modeling of the process catalytic isomerization of light naphtha; Petroleum and Coal; Vol. 61, iss. 2
| Parent link: | Petroleum and Coal Vol. 61, iss. 2.— 2019.— [P. 413-417] |
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| Institution som forfatter: | |
| Andre forfattere: | , , , , , |
| Summary: | Title screen The aim of this work is to study the process of catalytic isomerization of light naphtha by the methodof mathematical modelling. The influence of temperature and feedstock flow rate on octane numberand yield of the product (branched alkanes) was studied depending on the feedstock composition. Thetemperature mode of the process was optimized depending on the composition and feedstock flowrate. Свободный доступ из сети Интернет |
| Sprog: | engelsk |
| Udgivet: |
2019
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| Fag: | |
| Online adgang: | https://www.vurup.sk/wp-content/uploads/2019/04/PC-X-2019_Chuzlov_5_rev1.pdf |
| Format: | Electronisk Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=661776 |
| Summary: | Title screen The aim of this work is to study the process of catalytic isomerization of light naphtha by the methodof mathematical modelling. The influence of temperature and feedstock flow rate on octane numberand yield of the product (branched alkanes) was studied depending on the feedstock composition. Thetemperature mode of the process was optimized depending on the composition and feedstock flowrate. Свободный доступ из сети Интернет |
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