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Guard Bed Catalysts for Silicon Removal During Hydrotreating of Middle Distillates Научная публикация

Конференция III Scientific-Technological Symposium "Catalytic Hydroprocessing in Oil Refining"
16-20 апр. 2018 , Lyon
Журнал Catalysis Today
ISSN: 0920-5861 , E-ISSN: 1873-4308
Вых. Данные Год: 2019, Том: 329, Страницы: 53-62 Страниц : 10 DOI: 10.1016/j.cattod.2018.11.075
Ключевые слова Hydrotreating; Demetallization; Silicon removal; Alumina; Textural characteristics
Авторы Nadeina K.A. 1 , Kazakov M.O. 1 , Kovalskaya A.A. 1 , Danilevich V.V. 1 , Klimov O.V. 1 , Danilova I.G. 1 , Khabibulin D.F. 1 , Gerasimov E.Yu. 1 , Prosvirin I.P. 1 , Ushakov V.A. 1 , Fedotov K.V. 2 , Kondrashev D.O. 2 , Kleimenov A.V. 2 , Noskov A.S. 1
Организации
1 Boreskov Institute of Catalysis SB RAS, Pr. Lavrentieva 5, 630090, Novosibirsk, Russia
2 PJSC «Gazprom Neft», str. Pochtamtskaya, 3-5, 190000, St Petersburg, Russia

Информация о финансировании (1)

1 Министерство образования и науки Российской Федерации 14.604.21.0155 (RFMEFI60417X0155)

Реферат: The influence of textural characteristics of NiMo/Al2O3 on silicon capacity and hydrotreating activity has been investigated so as to develop guard-bed catalyst for silicon removal from middle distillates. Series of NiMo/Al2O3 catalysts with a specific surface area from 150 to 210 m2/g and an average pore diameter from 21.1 to 10.5 nm have been synthesized. The difference in textural characteristics has been achieved by variation of aging time and temperature of hydrothermal treatment of boehmites. The boehmites, supports and catalysts were studied by various physico-chemical methods: XRD, nitrogen adsorption-desorption, IR spectroscopy, UV–vis, 1H NMR, 27Al NMR, XPS, SEM, HRTEM. Catalysts were tested in hydrotreating of diesel fuel contaminated with decamethylcyclopentasiloxane as a model silicon compound. It is shown that the increase in aging time and temperature of hydrothermal treatment of initial boehmites results in the decrease of OH groups concentration per 1 g of an alumina support. The increase of the OH groups content leads to higher silicon capacity, while HDS activity of catalysts decreases. The study of catalysts surface after reaction showed that Si located on a support surface and did not cover directly active component particles. However, its location on the support near edges of active component particles could result in the decrease of HDS activity due to limited accessibility of the active sites.
Библиографическая ссылка: Nadeina K.A. , Kazakov M.O. , Kovalskaya A.A. , Danilevich V.V. , Klimov O.V. , Danilova I.G. , Khabibulin D.F. , Gerasimov E.Y. , Prosvirin I.P. , Ushakov V.A. , Fedotov K.V. , Kondrashev D.O. , Kleimenov A.V. , Noskov A.S.
Guard Bed Catalysts for Silicon Removal During Hydrotreating of Middle Distillates
Catalysis Today. 2019. V.329. P.53-62. DOI: 10.1016/j.cattod.2018.11.075 WOS Scopus РИНЦ CAPlusCA OpenAlex
Даты:
Поступила в редакцию: 20 июл. 2018 г.
Принята к публикации: 30 нояб. 2018 г.
Опубликована online: 4 дек. 2018 г.
Опубликована в печати: 1 июн. 2019 г.
Идентификаторы БД:
Web of science: WOS:000462764600007
Scopus: 2-s2.0-85057738719
РИНЦ: 38627435
Chemical Abstracts: 2018:2482616
Chemical Abstracts (print): 170:403697
OpenAlex: W2902816069
Цитирование в БД:
БД Цитирований
Scopus 22
Web of science 16
РИНЦ 25
OpenAlex 29
Альметрики: