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Influence of Reaction Conditions and Kinetic Analysis of the Selective Hydrogenation of Oleic Acid Toward Fatty Alcohols on Ru-Sn-B/Al2O3 in the Flow Reactor Научная публикация

Журнал Applied Catalysis B: Environmental
ISSN: 0926-3373 , E-ISSN: 1873-3883
Вых. Данные Год: 2017, Том: 209, Страницы: 611-620 Страниц : 10 DOI: 10.1016/j.apcatb.2017.03.012
Ключевые слова Fatty acids, Hydrogenation, Oleyl alcohol, Ruthenium-tin catalyst, Unsaturated alcohols
Авторы Rodina V.O. 1 , Ermakov D.Yu. 1 , Saraev A.A. 1,2 , Reshetnikov S.I. 1 , Yakovlev V.A. 1,2,3
Организации
1 Boreskov Institute of Catalysis SB RAS, Lavrentieva Ave. 5, 630090, Novosibirsk, Russia
2 Novosibirsk State University, Pirogova Str. 2, 630090, Novosibirsk, Russia
3 UNICAT Ltd., Lavrentieva Ave. 5, 630090, Novosibirsk, Russia

Информация о финансировании (2)

1 Министерство образования и науки Российской Федерации
2 Российский фонд фундаментальных исследований 16-33-00682

Реферат: The hydrogenation of oleic acid (cis-9-octadecenoic acid) into oleyl alcohol (methyl-9-octadecen-1-ol) was studied in the presence of a bimetallic RuSn supported over alumina catalyst in the flow reactor. It was shown that the process should be performed at the temperature range of 280–330 °C, hydrogen pressure of 3.5-5.3 MPa and contact time less than 0.2 h in order to obtain the highest possible yield of desired products (fatty alcohols and waxes). The study by physicochemical methods (XRD, BET, TPR, XPS, TEM) revealed that modification of the catalyst with boron promotes additional simultaneous reduction of the major part of tin and ruthenium oxides, most of which are reduced below 310 °C. Crystalline RuxSny structures with variable composition, which seem to be the active component of the selective hydrogenation catalyst, were found to be formed after the reaction at temperatures higher than 300 °C. Our work demonstarted that a scheme of oleic acid transformations includes formation of waxes by recombination of carboxyl and alkanes intermediates, acid decarboxylation and hydrocracking of waxes to alkanes. Mathematic simulation methods allowed us to estimate rate constants of the process stages and the main kinetic parameters (Ea, k0).
Библиографическая ссылка: Rodina V.O. , Ermakov D.Y. , Saraev A.A. , Reshetnikov S.I. , Yakovlev V.A.
Influence of Reaction Conditions and Kinetic Analysis of the Selective Hydrogenation of Oleic Acid Toward Fatty Alcohols on Ru-Sn-B/Al2O3 in the Flow Reactor
Applied Catalysis B: Environmental. 2017. V.209. P.611-620. DOI: 10.1016/j.apcatb.2017.03.012 WOS Scopus РИНЦ CAPlusCA OpenAlex
Даты:
Поступила в редакцию: 22 дек. 2016 г.
Принята к публикации: 1 мар. 2017 г.
Опубликована online: 2 мар. 2017 г.
Опубликована в печати: 15 июл. 2017 г.
Идентификаторы БД:
Web of science: WOS:000400584900061
Scopus: 2-s2.0-85015930674
РИНЦ: 29484781
Chemical Abstracts: 2017:488772
Chemical Abstracts (print): 166:375170
OpenAlex: W2592151008
Цитирование в БД:
БД Цитирований
Web of science 32
Scopus 35
РИНЦ 31
OpenAlex 34
Альметрики: