Investigating the Process of Heavy Crude Oil Steam Cracking over Disperse Catalysts. I: Selection of Optimal Steam Cracking Conditions without Catalyst Full article
| Journal |
Catalysis in Industry
ISSN: 2070-0504 , E-ISSN: 2070-0555 |
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| Output data | Year: 2016, Volume: 8, Number: 3, Pages: 217-223 Pages count : 7 DOI: 10.1134/S207005041603003X | ||
| Tags | heavy oil, steam cracking | ||
| Authors |
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| Affiliations |
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Funding (1)
| 1 | Russian Science Foundation | 15-13-00106 |
Abstract:
The process of heavy crude oil steam cracking using semi-flow (with respect to water) and steadystate
regimes at 425°C without catalyst is investigated. It is established that in the case of a semi-flow regime,
water acts predominantly as a physical agent facilitating the distillation of hydrocarbon fractions and thus preventing their transformation into petroleum coke. A reduction in coke yield is observed for a steady-state
regime in comparison to a semi-flow regime; the introduction of water results in enhanced conversion of the
high-boiling fraction and an increased yield of light fractions in the composition of liquid products. Based on
the obtained data, it is concluded that water plays a positive role during the conversion of heavy crude oil, and
that the steam cracking process is promising for production of lighter synthetic and/or semi-synthetic oils
Cite:
Eletskii P.M.
, Mironenko O.O.
, Selishcheva S.
, Yakovlev V.A.
Investigating the Process of Heavy Crude Oil Steam Cracking over Disperse Catalysts. I: Selection of Optimal Steam Cracking Conditions without Catalyst
Catalysis in Industry. 2016. V.8. N3. P.217-223. DOI: 10.1134/S207005041603003X WOS Scopus РИНЦ OpenAlex
Investigating the Process of Heavy Crude Oil Steam Cracking over Disperse Catalysts. I: Selection of Optimal Steam Cracking Conditions without Catalyst
Catalysis in Industry. 2016. V.8. N3. P.217-223. DOI: 10.1134/S207005041603003X WOS Scopus РИНЦ OpenAlex
Original:
Елецкий П.М.
, Мироненко О.О.
, Селищева С.А.
, Яковлев В.А.
Исследование процесса каталитического парового крекинга тяжелой нефти в присутствии дисперсных катализаторов. Часть 1. Выбор оптимального режима проведения процесса парового крекинга в отсутствие катализатора
Катализ в промышленности. 2016.
Т.16. №1. С.50-56. DOI: 10.18412/1816-0387-2016-1-50-56
РИНЦ
AN
OpenAlex
Исследование процесса каталитического парового крекинга тяжелой нефти в присутствии дисперсных катализаторов. Часть 1. Выбор оптимального режима проведения процесса парового крекинга в отсутствие катализатора
Катализ в промышленности. 2016.
Т.16. №1. С.50-56. DOI: 10.18412/1816-0387-2016-1-50-56
РИНЦ
AN
OpenAlex
Dates:
| Submitted: | Nov 23, 2015 |
| Published print: | Jul 1, 2016 |
| Published online: | Oct 2, 2016 |
Identifiers:
| Web of science: | WOS:000388336000004 |
| Scopus: | 2-s2.0-84989344917 |
| Elibrary: | 27570968 |
| OpenAlex: | W2525593441 |