Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS; Petroleum and Coal; Vol. 60, iss. 1
| Parent link: | Petroleum and Coal Vol. 60, iss. 1.— 2018.— [P. 14-23] |
|---|---|
| Autore principale: | |
| Ente Autore: | |
| Altri autori: | , |
| Riassunto: | 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. |
| Lingua: | inglese |
| Pubblicazione: |
2018
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| Soggetti: | |
| Accesso online: | https://www.vurup.sk/wp-content/uploads/2018/01/PC_6_2017_Mityanina-110cor1.pdf |
| Natura: | MixedMaterials Elettronico Capitolo di libro |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=667212 |
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| 200 | 1 | |a Simulation of industrial MTBE production in reactive distillation column using ASPEN HYSYS |f O. E. Mityanina, K. E. Sukhacheva, V. A. Kolmogorova | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: 27 tit.] | ||
| 330 | |a 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. | ||
| 461 | |t Petroleum and Coal | ||
| 463 | |t Vol. 60, iss. 1 |v [P. 14-23] |d 2018 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a reactive distillation | |
| 610 | 1 | |a MTBE | |
| 610 | 1 | |a simulation | |
| 610 | 1 | |a industrial process | |
| 610 | 1 | |a Aspen HYSYS® | |
| 700 | 1 | |a Mityanina |b O. E. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences |f 1986- |g Olga Evgenyevna |3 (RuTPU)RU\TPU\pers\32033 |9 16080 | |
| 701 | 1 | |a Sukhacheva |b K. E. |g Kristina Eduardovna | |
| 701 | 1 | |a Kolmogorova |b V. A. |g Veronika Aleksandrovna | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет |b Инженерная школа природных ресурсов |b Отделение химической инженерии |3 (RuTPU)RU\TPU\col\23513 |
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