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Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield. / Enikeeva, L. V.; Faskhutdinov, A. G.; Koledina, K. F. и др.

в: Reaction Kinetics, Mechanisms and Catalysis, Том 133, № 2, 08.2021, стр. 879-895.

Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование

Harvard

Enikeeva, LV, Faskhutdinov, AG, Koledina, KF, Faskhutdinova, RI & Gubaydullin, IM 2021, 'Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield', Reaction Kinetics, Mechanisms and Catalysis, Том. 133, № 2, стр. 879-895. https://doi.org/10.1007/s11144-021-02020-w

APA

Enikeeva, L. V., Faskhutdinov, A. G., Koledina, K. F., Faskhutdinova, R. I., & Gubaydullin, I. M. (2021). Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield. Reaction Kinetics, Mechanisms and Catalysis, 133(2), 879-895. https://doi.org/10.1007/s11144-021-02020-w

Vancouver

Enikeeva LV, Faskhutdinov AG, Koledina KF, Faskhutdinova RI, Gubaydullin IM. Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield. Reaction Kinetics, Mechanisms and Catalysis. 2021 авг.;133(2):879-895. doi: 10.1007/s11144-021-02020-w

Author

Enikeeva, L. V. ; Faskhutdinov, A. G. ; Koledina, K. F. и др. / Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield. в: Reaction Kinetics, Mechanisms and Catalysis. 2021 ; Том 133, № 2. стр. 879-895.

BibTeX

@article{aeb51056bcb44ee085fb1229ca37d9ea,
title = "Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield",
abstract = "The main schemes of transformations of the catalytic isomerization of the pentane-hexane fraction are considered. A mathematical model of the reactor block of the process under study has been developed, describing in detail the chemical reactions inside the reactors. The values of kinetic parameters (activation energy of stages, pre-exponential factors of the Arrhenius equation) are calculated by solving the direct and inverse problems. Based on the developed mathematical model, the problem of multi-criteria optimization of the reactor block of the process is solved. Mathematical descriptions of optimization criteria for the used model are proposed. Temperature modes of operation of the reactor block that meet the optimality criteria are presented.",
keywords = "Inverse problems of chemical kinetics, Kinetic model, Mathematical modeling, Multi-criteria optimization",
author = "Enikeeva, {L. V.} and Faskhutdinov, {A. G.} and Koledina, {K. F.} and Faskhutdinova, {R. I.} and Gubaydullin, {I. M.}",
note = "Funding Information: The reported study on numerical solution was funded by RFBR under the project numbers 19-37-60014 and 20-31-90094. The work has been also performed under the theme {\textquoteleft}Novel theoretical approaches and software for modeling complex chemical processes and compounds with tunable physicochemical properties{\textquoteright} (registration number AAAAA19-119022290011-6). Publisher Copyright: {\textcopyright} 2021, Akad{\'e}miai Kiad{\'o}, Budapest, Hungary.",
year = "2021",
month = aug,
doi = "10.1007/s11144-021-02020-w",
language = "English",
volume = "133",
pages = "879--895",
journal = "Reaction Kinetics, Mechanisms and Catalysis",
issn = "1878-5190",
publisher = "Springer Netherlands",
number = "2",

}

RIS

TY - JOUR

T1 - Modeling and optimization of the catalytic isomerization of the pentane-hexane fraction with maximization of individual high-octane components yield

AU - Enikeeva, L. V.

AU - Faskhutdinov, A. G.

AU - Koledina, K. F.

AU - Faskhutdinova, R. I.

AU - Gubaydullin, I. M.

N1 - Funding Information: The reported study on numerical solution was funded by RFBR under the project numbers 19-37-60014 and 20-31-90094. The work has been also performed under the theme ‘Novel theoretical approaches and software for modeling complex chemical processes and compounds with tunable physicochemical properties’ (registration number AAAAA19-119022290011-6). Publisher Copyright: © 2021, Akadémiai Kiadó, Budapest, Hungary.

PY - 2021/8

Y1 - 2021/8

N2 - The main schemes of transformations of the catalytic isomerization of the pentane-hexane fraction are considered. A mathematical model of the reactor block of the process under study has been developed, describing in detail the chemical reactions inside the reactors. The values of kinetic parameters (activation energy of stages, pre-exponential factors of the Arrhenius equation) are calculated by solving the direct and inverse problems. Based on the developed mathematical model, the problem of multi-criteria optimization of the reactor block of the process is solved. Mathematical descriptions of optimization criteria for the used model are proposed. Temperature modes of operation of the reactor block that meet the optimality criteria are presented.

AB - The main schemes of transformations of the catalytic isomerization of the pentane-hexane fraction are considered. A mathematical model of the reactor block of the process under study has been developed, describing in detail the chemical reactions inside the reactors. The values of kinetic parameters (activation energy of stages, pre-exponential factors of the Arrhenius equation) are calculated by solving the direct and inverse problems. Based on the developed mathematical model, the problem of multi-criteria optimization of the reactor block of the process is solved. Mathematical descriptions of optimization criteria for the used model are proposed. Temperature modes of operation of the reactor block that meet the optimality criteria are presented.

KW - Inverse problems of chemical kinetics

KW - Kinetic model

KW - Mathematical modeling

KW - Multi-criteria optimization

UR - http://www.scopus.com/inward/record.url?scp=85110728864&partnerID=8YFLogxK

U2 - 10.1007/s11144-021-02020-w

DO - 10.1007/s11144-021-02020-w

M3 - Article

AN - SCOPUS:85110728864

VL - 133

SP - 879

EP - 895

JO - Reaction Kinetics, Mechanisms and Catalysis

JF - Reaction Kinetics, Mechanisms and Catalysis

SN - 1878-5190

IS - 2

ER -

ID: 33980994