Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование
Two-component model for catalyst deactivation. / Malkovich, E. G.; Parkhomchuk, E. V.; Bazaikin, Ya V. и др.
в: Chemical Engineering Journal, Том 378, 122176, 15.12.2019.Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование
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TY - JOUR
T1 - Two-component model for catalyst deactivation
AU - Malkovich, E. G.
AU - Parkhomchuk, E. V.
AU - Bazaikin, Ya V.
AU - Lysikov, A. I.
N1 - Publisher Copyright: © 2019 Elsevier B.V.
PY - 2019/12/15
Y1 - 2019/12/15
N2 - Texture evolution of alumina hydrotreating catalyst was theoretically modeled using geometrical characteristics calculated via Monte-Carlo methods and methods of the graph theory. In the prescribed model deactivation was specified by monotonic increase of alumina grain radius, which imitated deposition of coke and metal species onto the pore surface. A novel two-component nonhomogeneous model was designed based on the diffusion of asphaltene molecules inside the cylindrical pellet according to Fick's law and deposition of the coke particles from heavy oil on the surface of the catalyst. The model resulted in non-monotonous coke distribution with a distinct maximum in the inner region of the pellet, which, nevertheless, shifts to the center at later deactivation stages due to the higher hydrogenation performance of pellet border region. Model can be applied to describe profiles of coke depositions during deactivation process for a pellet with an arbitrary boundary.
AB - Texture evolution of alumina hydrotreating catalyst was theoretically modeled using geometrical characteristics calculated via Monte-Carlo methods and methods of the graph theory. In the prescribed model deactivation was specified by monotonic increase of alumina grain radius, which imitated deposition of coke and metal species onto the pore surface. A novel two-component nonhomogeneous model was designed based on the diffusion of asphaltene molecules inside the cylindrical pellet according to Fick's law and deposition of the coke particles from heavy oil on the surface of the catalyst. The model resulted in non-monotonous coke distribution with a distinct maximum in the inner region of the pellet, which, nevertheless, shifts to the center at later deactivation stages due to the higher hydrogenation performance of pellet border region. Model can be applied to describe profiles of coke depositions during deactivation process for a pellet with an arbitrary boundary.
KW - Catalyst deactivation
KW - Fick's law
KW - Non-homogeneous model
UR - http://www.scopus.com/inward/record.url?scp=85069551312&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2019.122176
DO - 10.1016/j.cej.2019.122176
M3 - Article
AN - SCOPUS:85069551312
VL - 378
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
SN - 1385-8947
M1 - 122176
ER -
ID: 21047194