Mathematical modeling and steady states multiplicity analysis of methyl tert-butyl ether reactive distillation synthesis; Petroleum and Coal; Vol. 58, iss. 4
| Parent link: | Petroleum and Coal Vol. 58, iss. 4.— 2016.— [P. 490-498] |
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| 第一著者: | |
| 団体著者: | |
| その他の著者: | , |
| 要約: | Title screen The paper is devoted to a new approach to steady state multiplicity analysis of methyl tert-butyl ether (MTBE) production by means of reactive distillation. Reactive distillation systems are characterized by input and output multiplicities, which may cause complex and unpredictable behavior of the process. The fundamental mathematical model, which enables to reveal potential sources of nonlinearity of the process, is proposed. As the result of input multiplicity analysis, intervals of one steady state were found for vapor and reflux ratio. Output multiplicity analysis showed three possible steady states in the reactive section of the column, one of which is corresponded to the maximal product yield. The advantage of the method is the ability to find “input-output” multiplicities on every stage of the column by using control parameters of the feed, reboiler and condenser only. Свободный доступ из сети Интернет |
| 言語: | 英語 |
| 出版事項: |
2016
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| 主題: | |
| オンライン･アクセス: | http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_4_2016_mytyanina_452.pdf |
| フォーマット: | MixedMaterials 電子媒体 図書の章 |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652443 |
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| 200 | 1 | |a Mathematical modeling and steady states multiplicity analysis of methyl tert-butyl ether reactive distillation synthesis |f O. E. Mityanina, M. A. Samborskaya, A. N. Sabiev | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 497-498 (17 tit.)] | ||
| 330 | |a The paper is devoted to a new approach to steady state multiplicity analysis of methyl tert-butyl ether (MTBE) production by means of reactive distillation. Reactive distillation systems are characterized by input and output multiplicities, which may cause complex and unpredictable behavior of the process. The fundamental mathematical model, which enables to reveal potential sources of nonlinearity of the process, is proposed. As the result of input multiplicity analysis, intervals of one steady state were found for vapor and reflux ratio. Output multiplicity analysis showed three possible steady states in the reactive section of the column, one of which is corresponded to the maximal product yield. The advantage of the method is the ability to find “input-output” multiplicities on every stage of the column by using control parameters of the feed, reboiler and condenser only. | ||
| 333 | |a Свободный доступ из сети Интернет | ||
| 461 | |t Petroleum and Coal | ||
| 463 | |t Vol. 58, iss. 4 |v [P. 490-498] |d 2016 | ||
| 610 | 1 | |a электронный ресурс | |
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| 610 | 1 | |a третбутиловый спирт | |
| 610 | 1 | |a математическое моделирование | |
| 610 | 1 | |a анализ устойчивости | |
| 610 | 1 | |a стационарное состояние | |
| 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 Samborskaya |b M. A. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of chemical sciences |f 1960- |g Marina Anatolievna |3 (RuTPU)RU\TPU\pers\31290 |9 15468 | |
| 701 | 1 | |a Sabiev |b A. N. |g Ayan Nurlanovich | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет (ТПУ) |b Институт природных ресурсов (ИПР) |b Кафедра химической технологии топлива и химической кибернетики (ХТТ) |3 (RuTPU)RU\TPU\col\18665 |
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