Increase of efficiency isopropylbenzene manufacturing with use of integrated mathematical models; Petroleum and Coal; Vol. 58, iss. 2
| Parent link: | Petroleum and Coal Vol. 58, iss. 2.— 2016.— [P. 155-160] |
|---|---|
| Autor corporatiu: | Национальный исследовательский Томский политехнический университет Институт природных ресурсов Кафедра химической технологии топлива и химической кибернетики |
| Altres autors: | 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 |
| Sumari: | 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 |
| Idioma: | anglès |
| Publicat: |
2016
|
| Matèries: | |
| Accés en línia: | http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_2_2016_chudinova_415.pdf |
| Format: | Electrònic Capítol de llibre |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652329 |
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