Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS
| Parent link: | Petroleum and Coal Vol. 60, iss. 1.— 2018.— [P. 14-23] |
|---|---|
| Главный автор: | |
| Другие авторы: | , |
| Примечания: | Title screen Simulation of reactive distillation by using special engineering software is promising way to its design, research and optimization. In this work we considered the industrial-scale facility of Western Siberia, which includes a line of methyl tert-butyl ether production in a reactive distillation unit. Aspen HYSYS® was used as an instrument of simulation and further optimization studies. The calculation error of the model does not exceed 5%. Simulation of the feedstock composition changes showed that more preferable hydrocarbon fraction for the process is isobutene-isobutylene fraction. After the optimization study we obtained values of optimal reflux ratio for isobutene-isobutylene fraction to be 0.75 and for butylene-isobutylene fraction – 0.80; optimal methanol flowrate for isobutene-isobutylene fraction is 6.500 ton/h, for butylene-isobutylene fraction –6.000 ton/h. |
| Язык: | английский |
| Опубликовано: |
2018
|
| Предметы: | |
| Online-ссылка: | https://www.vurup.sk/wp-content/uploads/2018/01/PC_6_2017_Mityanina-110cor1.pdf |
| Формат: | Электронный ресурс Статья |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=667212 |