Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS

Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS

التفاصيل البيبلوغرافية
Parent link:Petroleum and Coal
Vol. 60, iss. 1.— 2018.— [P. 14-23]
المؤلف الرئيسي: Mityanina O. E. Olga Evgenyevna
مؤلف مشترك: Национальный исследовательский Томский политехнический университет Инженерная школа природных ресурсов Отделение химической инженерии
مؤلفون آخرون: Sukhacheva K. E. Kristina Eduardovna, Kolmogorova V. A. Veronika Aleksandrovna
الملخص: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.
اللغة:الإنجليزية
منشور في: 2018
الموضوعات:
электронный ресурс
труды учёных ТПУ
reactive distillation
MTBE
simulation
industrial process
Aspen HYSYS®
الوصول للمادة أونلاين:https://www.vurup.sk/wp-content/uploads/2018/01/PC_6_2017_Mityanina-110cor1.pdf
التنسيق: الكتروني فصل الكتاب
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=667212

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