

Studies of Steam Cracking of Heavy Oil in the Presence of Iron- and Molybdenum-Containing Disperse Catalysts in a Flow Type Reactor
https://doi.org/10.18412/1816-0387-2018-3-54-63
Abstract
Steam cracking of heavy oil was studied at 425 °C and 2.0 MPa in the presence of disperse catalysts based on iron and molybdenum in a slurry reactor. The catalysts were prepared via in situ decomposition of water soluble precursors of the metal salts. In the steam cracking, the yield of a total of liquid products increased against that in thermal cracking (80 and 77 wt %, respectively). The use of disperse monometal catalysts (iron- and molybdenum-containing), as well as the bimetal catalyst for catalytic steam cracking (CSC) of heavy oil resulted in an increase in the total of liquid products yield up to 85–92 wt %. In addition, CSC provided a higher yield of light fractions (Tboil <350 °C) than steam and thermal cracking processes, as well as a decrease in viscosity and density in comparison to those of the raw feedstock.
About the Authors
R. G. KukushkinRussian Federation
P. M. Eletskiy
Russian Federation
O. O. Zaikina
Russian Federation
G. A. Sosnin
Russian Federation
O. A. Bulavchenko
Russian Federation
V. A. Yakovlev
Russian Federation
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Review
For citations:
Kukushkin R.G., Eletskiy P.M., Zaikina O.O., Sosnin G.A., Bulavchenko O.A., Yakovlev V.A. Studies of Steam Cracking of Heavy Oil in the Presence of Iron- and Molybdenum-Containing Disperse Catalysts in a Flow Type Reactor. Kataliz v promyshlennosti. 2018;18(3):54-63. (In Russ.) https://doi.org/10.18412/1816-0387-2018-3-54-63