Studying the Steam Cracking of Heavy Oil over Iron- and Molybdenum-Containing Dispersed Catalysts in a Flow-Type Reactor

被引:8
|
作者
Kukushkin R.G. [1 ,2 ]
Eletskii P.M. [1 ]
Zaikina O.O. [1 ,2 ]
Sosnin G.A. [1 ,2 ]
Bulavchenko O.A. [1 ,2 ]
Yakovlev V.A. [1 ,2 ]
机构
[1] Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, Novosibirsk
[2] Novosibirsk State University, Novosibirsk
关键词
catalytic steam cracking; dispersed catalysts; oxidative cracking; steam reforming; upgrading of heavy oil feedstocks;
D O I
10.1134/S2070050418040104
中图分类号
学科分类号
摘要
Abstract: Results are presented from studying the steam cracking of heavy oil at a temperature of 425°C and a pressure of 2.0 MPa over dispersed iron and molybdenum based catalysts in a slurry reactor. The catalysts are synthesized through the decomposition of water-soluble precursors of metal salts in situ. The yield of upgraded oil (the sum of liquid products) is found to grow with steam cracking, in comparison to thermal cracking (80 and 77%, respectively). The use of dispersed monometallic (iron- or molybdenum-containing) catalysts and a bimetallic catalyst for the catalytic steam cracking (CSC) of heavy oil increases the yield of SOPs. In addition, the yield of light fractions (Т b < 350°C) in the CSC process is found to grow in comparison to steam and thermal cracking, and the viscosity and density of products falls, relative to the initial feedstock. © 2018, Pleiades Publishing, Ltd.
引用
收藏
页码:344 / 352
页数:8
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