Increase of efficiency isopropylbenzene manufacturing with use of integrated mathematical models

Bibliographic Details
Parent link:Petroleum and Coal
Vol. 58, iss. 2.— 2016.— [P. 155-160]
Corporate Author: Национальный исследовательский Томский политехнический университет Институт природных ресурсов Кафедра химической технологии топлива и химической кибернетики
Other Authors: Chudinova A. A. Alyona Anatoljevna, Buchatskaya N. I. Nadezhda, Podgorniy V. V. Vladimir, Gavrikov А. А. Aleksey Alekseevich, Ivashkina E. N. Elena Nikolaevna, Dolganova I. O. Irena Olegovna
Summary:Title screen
A mathematical model of isopropyl benzene obtaining reactor process on chloroaluminum catalyst was developed. With use of HYSYS software a computer model of benzene with propylene alkylation technological scheme was created. Integration of computer models allowed carrying out calculations to determine technological modes of production, allowing to obtain a marketable product of higher quality. It was shown that increasing of isopropylbenzene concentration in commercial product to 99.9% by weight can be achieved by implementing of sequence separation in distillation columns due to redistribution of ethylbenzene and n-butyl benzene loads.
Свободный доступ из сети Интернет
Language:English
Published: 2016
Subjects:
Online Access:http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_2_2016_chudinova_415.pdf
Format: Electronic Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652329