Optimization of reactant mixing in benzene alkylation technology; Petroleum and Coal; Vol. 58, iss. 7

Detalhes bibliográficos
Parent link:Petroleum and Coal
Vol. 58, iss. 7.— 2016.— [P. 736-739]
Autor Corporativo: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Outros Autores: Khlebnikova E. S. Elena Sergeevna, Yurev E. M. Egor Mikhaylovich, Ivashkina E. N. Elena Nikolaevna, Chudinova A. Alyona
Resumo:Title screen
In this paper the feasibility of mixing device reconstruction in benzene with ethylene alkylation in the presence of liquid-phase catalyst was evaluated using Comsol Multiphysics software. The hydrodynamicmodel of mixer chamber was developed and optimal options for reactants input are considered. In defined optimal variant a uniform profile of reagents concentration distribution is obtained. The mixing intensification will allow to perform alkylation more effective and reduce catalytic complex flow rate.
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Idioma:inglês
Publicado em: 2016
Assuntos:
Acesso em linha:http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_khlebnikova_506.pdf
Formato: Recurso Electrónico Capítulo de Livro
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=653531
Descrição
Resumo:Title screen
In this paper the feasibility of mixing device reconstruction in benzene with ethylene alkylation in the presence of liquid-phase catalyst was evaluated using Comsol Multiphysics software. The hydrodynamicmodel of mixer chamber was developed and optimal options for reactants input are considered. In defined optimal variant a uniform profile of reagents concentration distribution is obtained. The mixing intensification will allow to perform alkylation more effective and reduce catalytic complex flow rate.
Свободный доступ из сети Интернет