Modeling of Transalkylation Stage of Ethylbenzene Manufacturing with Zeolite-catalysts; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)

Bibliografiske detaljer
Parent link:Procedia Engineering
Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft).— 2016.— [P. 45-50]
Institution som forfatter: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Andre forfattere: Koshkin S. A. Stanislav Aleksandrovich, Ignatova L. S. Lyubov Sergeevna, Ivashkina E. N. Elena Nikolaevna, Dolganova I. O. Irena Olegovna
Summary:Title screen
The analysis of industrial transalkylation reactor revealed regularities of catalyst activity and stability changes during its operation at change of basic technological parameters. A result of experimental data analysis, a list of possible reactions of transalkylation stage of ethylbenzene manufacturing zeolite-catalyst technology was developed. Values of Gibbs energies for change targets and adverse reactions, which were calculated with use of quantum chemistry methods, confirmed their thermodynamic probability at process conditions. The calculation results formed the basis of transalkylation process reaction network, needed to develop a mathematical model of ethylbenzene manufacturing zeolite-catalyst industrial technology.
Sprog:engelsk
Udgivet: 2016
Fag:
Online adgang:http://dx.doi.org/10.1016/j.proeng.2016.07.622
Format: xMaterials Electronisk Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=651758

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