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Benzene Hydrogenation in the Thiophene Presence over the Sulfide Ni-Mo/γ-Al2O3 Catalyst under Periodic Operation: Kinetics and Process Modelling Full article

Conference XVII International Conference on Chemical Reactors
15-19 May 2006 , Athens-Crete
Journal Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Output data Year: 2007, Volume: 134, Number: 1-3, Pages: 100-105 Pages count : 6 DOI: 10.1016/j.cej.2007.03.048
Tags Benzene hydrogenation, Periodic operation, Sulfide catalyst, Transient kinetics
Authors Reshetnikov S.I. 1 , Ivanov E.A. 1 , Startsev A.N. 1
Affiliations
1 Boreskov Institute of Catalysis, Pr. Lavrentieva, 5, 630090 Novosibirsk, Russia

Abstract: An unsteady-state kinetic model of both benzene hydrogenation (HDA) and thiophene hydrogenolysis (HDS) on the sulfide hydrotreating catalyst Ni-Mo/Al2O3 has been developed. The model adequately describes experimental data obtained at the pressure 2 MPa, temperature 573 K and at various contact times and ratios of benzene/thiophene. The model is based on the assumption that the catalyst surface contains only one type of active sites, i.e., Ni atoms in the sulfide bimetallic species, which are responsible for both hydrogenolysis and hydrogenation reactions. On the base of the kinetic model, a theoretical analysis of the reactor performance under unsteady state conditions was carried out. The unsteady state conditions on the catalyst surface are supposed to be created by forced oscillations of thiophene concentration in the reactor inlet (periodic operation of reactor). The influence of various parameters like cycle split, length of period of forced oscillations in the reactor was investigated with respect to the conversion of the benzene. It is shown that for periodic reactor operation an average conversion was up to several times higher than a steady state value.
Cite: Reshetnikov S.I. , Ivanov E.A. , Startsev A.N.
Benzene Hydrogenation in the Thiophene Presence over the Sulfide Ni-Mo/γ-Al2O3 Catalyst under Periodic Operation: Kinetics and Process Modelling
Chemical Engineering Journal. 2007. V.134. N1-3. P.100-105. DOI: 10.1016/j.cej.2007.03.048 WOS Scopus РИНЦ ANCAN OpenAlex
Dates:
Published online: Mar 28, 2007
Published print: Nov 1, 2007
Identifiers:
Web of science: WOS:000249877600016
Scopus: 2-s2.0-34548232260
Elibrary: 13562559
Chemical Abstracts: 2007:987811
Chemical Abstracts (print): 147:504983
OpenAlex: W2017429563
Citing:
DB Citing
Web of science 14
Scopus 22
Elibrary 22
OpenAlex 12
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