Standard

Two-component model for catalyst deactivation. / Malkovich, E. G.; Parkhomchuk, E. V.; Bazaikin, Ya V. et al.

In: Chemical Engineering Journal, Vol. 378, 122176, 15.12.2019.

Research output: Contribution to journal › Article › peer-review

Harvard

Malkovich, EG, Parkhomchuk, EV, Bazaikin, YV & Lysikov, AI 2019, 'Two-component model for catalyst deactivation', Chemical Engineering Journal, vol. 378, 122176. https://doi.org/10.1016/j.cej.2019.122176

APA

Malkovich, E. G., Parkhomchuk, E. V., Bazaikin, Y. V., & Lysikov, A. I. (2019). Two-component model for catalyst deactivation. Chemical Engineering Journal, 378, [122176]. https://doi.org/10.1016/j.cej.2019.122176

Vancouver

Malkovich EG, Parkhomchuk EV, Bazaikin YV, Lysikov AI. Two-component model for catalyst deactivation. Chemical Engineering Journal. 2019 Dec 15;378:122176. doi: 10.1016/j.cej.2019.122176

Author

Malkovich, E. G. ; Parkhomchuk, E. V. ; Bazaikin, Ya V. et al. / Two-component model for catalyst deactivation. In: Chemical Engineering Journal. 2019 ; Vol. 378.

BibTeX

@article{438b8717532047b1ae0516694c675d80,
title = "Two-component model for catalyst deactivation",
abstract = "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.",
keywords = "Catalyst deactivation, Fick's law, Non-homogeneous model",
author = "Malkovich, {E. G.} and Parkhomchuk, {E. V.} and Bazaikin, {Ya V.} and Lysikov, {A. I.}",
note = "Publisher Copyright: {\textcopyright} 2019 Elsevier B.V.",
year = "2019",
month = dec,
day = "15",
doi = "10.1016/j.cej.2019.122176",
language = "English",
volume = "378",
journal = "Chemical Engineering Journal",
issn = "1385-8947",
publisher = "Elsevier",

}

RIS

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