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Catalytic Steam Cracking of Heavy Crude Oil with Molybdenum and Nickel Nanodispersed Catalysts Full article

Journal Catalysis in Industry
ISSN: 2070-0504 , E-ISSN: 2070-0555
Output data Year: 2017, Volume: 9, Number: 3, Pages: 221-229 Pages count : 9 DOI: 10.1134/S2070050417030084
Tags catalytic steam cracking, dispersed catalyst, heavy crude oil, molybdenum, nickel
Authors Mironenko O.O. 1 , Sosnin G.A. 1,2 , Eletskii P.M. 1 , Gulyaeva Yu.K. 1 , Bulavchenko O.A. 1,2 , Stonkus O.A. 1,2 , Rodina V.O. 1 , Yakovlev V.A. 1
Affiliations
1 Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk, 630090 Russia
2 Novosibirsk State University, Novosibirsk, 630090 Russia

Funding (1)

1 Russian Science Foundation 15-13-00106

Abstract: The catalytic steam cracking (CSC) of heavy crude oil with high amount of sulfur (4.3 wt %) and high-boiling fractions (>500°C) is studied using Mo and Ni nanodispersed catalysts under static conditions (in an autoclave) at 425°C. Experiments on thermal cracking, steam cracking, and catalytic cracking without water are performed to compare and identify the features of CSC. The relationship between the composition and properties of liquid and gaseous products and process conditions, the type of catalyst, and water is studied. Using Ni catalyst in CSC raises the H: C ratio (1.69) in liquid products, compared to other types of cracking, but also increases the yield of coke and gaseous products, so the yield of liquid products falls. When Mo catalyst is used in CSC, low-viscosity semi-synthetic oil with a higher H: C ratio (1.70) and the lowest amount of sulfur in liquid products (2.8 wt %) is produced. XRF and HRTEM studies of the catalyst-containing solid residue (coke) show that under CSC conditions, nickel is present in the form of well-crystallized nanoparticles of Ni9S8 15–40 nm in size, while molybdenum exists in two phases: MoO2 and MoS2, the ratio between which depends on the conditions of the transformation of heavy crude oil. The findings indicate that CSC is a promising process for improving heavy crude oil.
Cite: Mironenko O.O. , Sosnin G.A. , Eletskii P.M. , Gulyaeva Y.K. , Bulavchenko O.A. , Stonkus O.A. , Rodina V.O. , Yakovlev V.A.
Catalytic Steam Cracking of Heavy Crude Oil with Molybdenum and Nickel Nanodispersed Catalysts
Catalysis in Industry. 2017. V.9. N3. P.221-229. DOI: 10.1134/S2070050417030084 WOS Scopus РИНЦ OpenAlex
Original: Мироненко О.О. , Соснин Г.А. , Елецкий П.М. , Гуляева Ю.К. , Булавченко О.А. , Стонкус О.А. , Родина В.О. , Яковлев В.А.
Каталитический паровой крекинг тяжелой нефти в присутствии молибден- и никельсодержащих нанодисперсных катализаторов
Катализ в промышленности. 2017. Т.17. №2. С.127-136. DOI: 10.18412/1816-0387-2017-2-127-136 РИНЦ AN OpenAlex
Dates:
Submitted: Dec 7, 2016
Published print: Jul 1, 2017
Published online: Sep 21, 2017
Identifiers:
Web of science: WOS:000423241700006
Scopus: 2-s2.0-85029764813
Elibrary: 31063603
OpenAlex: W2754647345
Citing:
DB Citing
Web of science 13
Scopus 14
Elibrary 11
OpenAlex 18
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