Three-Factor Kinetic Equation of Catalyst Deactivation
The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible dea...
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Published in | Entropy (Basel, Switzerland) Vol. 23; no. 7; p. 818 |
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Main Authors | , , , |
Format | Journal Article |
Language | English |
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Abstract | The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible deactivation (aging), respectively. The rate of the main cycle is obtained for the fresh catalyst under a quasi-steady-state assumption. The phenomena of reversible and irreversible deactivation are presented as special separate factors (hierarchical separation). In this case, the reversible deactivation factor is a function of the kinetic apparent parameters of the reversible deactivation and of those of the main cycle. The irreversible deactivation factor is a function of the apparent kinetic parameters of the main cycle, of the reversible deactivation, and of the irreversible deactivation. The conditions of such separability are found. The obtained equation is applied successfully to describe the literature data on the reversible catalyst deactivation processes in the dehydration of acetaldehyde over TiO2 anatase and in crotonaldehyde hydrogenation on supported metal catalysts. |
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AbstractList | The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible deactivation (aging), respectively. The rate of the main cycle is obtained for the fresh catalyst under a quasi-steady-state assumption. The phenomena of reversible and irreversible deactivation are presented as special separate factors (hierarchical separation). In this case, the reversible deactivation factor is a function of the kinetic apparent parameters of the reversible deactivation and of those of the main cycle. The irreversible deactivation factor is a function of the apparent kinetic parameters of the main cycle, of the reversible deactivation, and of the irreversible deactivation. The conditions of such separability are found. The obtained equation is applied successfully to describe the literature data on the reversible catalyst deactivation processes in the dehydration of acetaldehyde over TiO2 anatase and in crotonaldehyde hydrogenation on supported metal catalysts. The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible deactivation (aging), respectively. The rate of the main cycle is obtained for the fresh catalyst under a quasi-steady-state assumption. The phenomena of reversible and irreversible deactivation are presented as special separate factors (hierarchical separation). In this case, the reversible deactivation factor is a function of the kinetic apparent parameters of the reversible deactivation and of those of the main cycle. The irreversible deactivation factor is a function of the apparent kinetic parameters of the main cycle, of the reversible deactivation, and of the irreversible deactivation. The conditions of such separability are found. The obtained equation is applied successfully to describe the literature data on the reversible catalyst deactivation processes in the dehydration of acetaldehyde over T i O 2 anatase and in crotonaldehyde hydrogenation on supported metal catalysts. The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible deactivation (aging), respectively. The rate of the main cycle is obtained for the fresh catalyst under a quasi-steady-state assumption. The phenomena of reversible and irreversible deactivation are presented as special separate factors (hierarchical separation). In this case, the reversible deactivation factor is a function of the kinetic apparent parameters of the reversible deactivation and of those of the main cycle. The irreversible deactivation factor is a function of the apparent kinetic parameters of the main cycle, of the reversible deactivation, and of the irreversible deactivation. The conditions of such separability are found. The obtained equation is applied successfully to describe the literature data on the reversible catalyst deactivation processes in the dehydration of acetaldehyde over TiO2 anatase and in crotonaldehyde hydrogenation on supported metal catalysts.The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible deactivation (aging), respectively. The rate of the main cycle is obtained for the fresh catalyst under a quasi-steady-state assumption. The phenomena of reversible and irreversible deactivation are presented as special separate factors (hierarchical separation). In this case, the reversible deactivation factor is a function of the kinetic apparent parameters of the reversible deactivation and of those of the main cycle. The irreversible deactivation factor is a function of the apparent kinetic parameters of the main cycle, of the reversible deactivation, and of the irreversible deactivation. The conditions of such separability are found. The obtained equation is applied successfully to describe the literature data on the reversible catalyst deactivation processes in the dehydration of acetaldehyde over TiO2 anatase and in crotonaldehyde hydrogenation on supported metal catalysts. The three-factor kinetic equation of catalyst deactivation was obtained in terms of apparent kinetic parameters. The three factors correspond to the main cycle with a linear, detailed mechanism regarding the catalytic intermediates, a cycle of reversible deactivation, and a stage of irreversible deactivation (aging), respectively. The rate of the main cycle is obtained for the fresh catalyst under a quasi-steady-state assumption. The phenomena of reversible and irreversible deactivation are presented as special separate factors (hierarchical separation). In this case, the reversible deactivation factor is a function of the kinetic apparent parameters of the reversible deactivation and of those of the main cycle. The irreversible deactivation factor is a function of the apparent kinetic parameters of the main cycle, of the reversible deactivation, and of the irreversible deactivation. The conditions of such separability are found. The obtained equation is applied successfully to describe the literature data on the reversible catalyst deactivation processes in the dehydration of acetaldehyde over T i O 2 anatase and in crotonaldehyde hydrogenation on supported metal catalysts. |
Author | Constales, Denis Gromotka, Zoë Yablonsky, Gregory Ostrovskii, Nickolay |
AuthorAffiliation | 1 Department of Electronics and Information Systems, Ghent University, 9000 Ghent, Belgium; denis.constales@ugent.be 2 Department of Energy, Environmental & Chemical Engineering, McKelvey School of Engineering, Washington University, St. Louis, MO 63130, USA; gregoryyablonsky@gmail.com 3 Euro Gas, 24000 Subotica, Serbia; n-ostr@yandex.ru |
AuthorAffiliation_xml | – name: 1 Department of Electronics and Information Systems, Ghent University, 9000 Ghent, Belgium; denis.constales@ugent.be – name: 3 Euro Gas, 24000 Subotica, Serbia; n-ostr@yandex.ru – name: 2 Department of Energy, Environmental & Chemical Engineering, McKelvey School of Engineering, Washington University, St. Louis, MO 63130, USA; gregoryyablonsky@gmail.com |
Author_xml | – sequence: 1 givenname: Zoë orcidid: 0000-0002-5004-0575 surname: Gromotka fullname: Gromotka, Zoë – sequence: 2 givenname: Gregory surname: Yablonsky fullname: Yablonsky, Gregory – sequence: 3 givenname: Nickolay orcidid: 0000-0003-0815-0874 surname: Ostrovskii fullname: Ostrovskii, Nickolay – sequence: 4 givenname: Denis orcidid: 0000-0002-6826-6185 surname: Constales fullname: Constales, Denis |
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Cites_doi | 10.1021/i200016a011 10.1007/BF02071341 10.1016/S0926-860X(00)00843-7 10.3390/e13050966 10.1016/B978-0-12-147695-3.50009-0 10.1021/ie00075a002 10.1016/j.cej.2006.03.026 10.1016/0009-2509(68)80022-3 10.1016/S0009-2509(02)00134-3 10.1006/jcat.1999.2635 10.1016/j.ces.2009.09.005 10.1021/ie100394v 10.3390/sym12101748 10.1021/acscatal.8b03991 10.1021/ie101481y 10.1016/j.apcata.2016.07.014 10.1515/zpch-1913-8512 |
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SubjectTerms | Acetaldehyde Aging Anatase catalyst deactivation Catalysts Deactivation Dehydration kinetic equation Kinetic equations Kinetics Parameters Phase transitions Poisons reversible deactivation and aging Review separability Titanium dioxide |
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