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

Olga E. Mityanina, Kristina E. Sukhacheva, Veronika A. Kolmogorova

Результат исследований: Материалы для журналаСтатья

Выдержка

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 оригиналаАнглийский
Страницы (с-по)14-23
Число страниц10
ЖурналPetroleum and Coal
Том60
Номер выпуска1
СостояниеОпубликовано - 1 янв 2018

Отпечаток

Distillation columns
Distillation
Feedstocks
Ethers
Software engineering
Methanol
Hydrocarbons
Chemical analysis

ASJC Scopus subject areas

  • Energy(all)

Цитировать

Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS. / Mityanina, Olga E.; Sukhacheva, Kristina E.; Kolmogorova, Veronika A.

В: Petroleum and Coal, Том 60, № 1, 01.01.2018, стр. 14-23.

Результат исследований: Материалы для журналаСтатья

Mityanina, Olga E. ; Sukhacheva, Kristina E. ; Kolmogorova, Veronika A. / Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS. В: Petroleum and Coal. 2018 ; Том 60, № 1. стр. 14-23.
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