Development of the Mathematical Model of Diesel Fuel Catalytic Dewaxing Process Taking into Account Factors of Nonstationarity; MATEC Web of Conferences; Vol. 85 : Chemistry and Chemical Technology in XXI Century (CCT 2016)
| Parent link: | MATEC Web of Conferences Vol. 85 : Chemistry and Chemical Technology in XXI Century (CCT 2016).— 2016.— [01023, 5 p.] |
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| Κύριος συγγραφέας: | |
| Συγγραφή απο Οργανισμό/Αρχή: | |
| Άλλοι συγγραφείς: | , |
| Περίληψη: | Title screen The paper describes the results of mathematical modelling of diesel fuel catalytic dewaxing process, performed taking into account the factors of process nonstationarity driven by changes in process technological parameters, feedstock composition and catalyst deactivation. The error of hydrocarbon contents calculation via the use of the developed model does not exceed 1.6 wt.%. This makes it possible to apply the model for solution to optimization and forecasting problems occurred in catalytic systems under industrial conditions. It was shown through the model calculation that temperature in the dewaxing reactor without catalyst deactivation is lower by 19 °С than actual and catalyst deactivation degree accounts for 32 %. |
| Γλώσσα: | Αγγλικά |
| Έκδοση: |
2016
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| Θέματα: | |
| Διαθέσιμο Online: | http://dx.doi.org/10.1051/matecconf/20168501023 http://earchive.tpu.ru/handle/11683/36577 |
| Μορφή: | Ηλεκτρονική πηγή Κεφάλαιο βιβλίου |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652855 |
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| 200 | 1 | |a Development of the Mathematical Model of Diesel Fuel Catalytic Dewaxing Process Taking into Account Factors of Nonstationarity |f E. V. Frantsina, N. S. Belinskaya, N. Popova | |
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| 300 | |a Title screen | ||
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| 330 | |a The paper describes the results of mathematical modelling of diesel fuel catalytic dewaxing process, performed taking into account the factors of process nonstationarity driven by changes in process technological parameters, feedstock composition and catalyst deactivation. The error of hydrocarbon contents calculation via the use of the developed model does not exceed 1.6 wt.%. This makes it possible to apply the model for solution to optimization and forecasting problems occurred in catalytic systems under industrial conditions. It was shown through the model calculation that temperature in the dewaxing reactor without catalyst deactivation is lower by 19 °С than actual and catalyst deactivation degree accounts for 32 %. | ||
| 461 | 0 | |0 (RuTPU)RU\TPU\network\4526 |t MATEC Web of Conferences | |
| 463 | 0 | |0 (RuTPU)RU\TPU\network\17872 |t Vol. 85 : Chemistry and Chemical Technology in XXI Century (CCT 2016) |o Conference, May 17-20, 2016, Tomsk, Russia |o [proceedings] |f National Research Tomsk Polytechnic University (TPU) ; eds. A. N. Pestryakov ; E. I. Korotkova ; A. Vorobiev |v [01023, 5 p.] |d 2016 | |
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a математические модели | |
| 610 | 1 | |a дизельные топлива | |
| 610 | 1 | |a депарафинизация | |
| 610 | 1 | |a каталитическая депарафинизация | |
| 610 | 1 | |a каталитические системы | |
| 610 | 1 | |a углеводороды | |
| 610 | 1 | |a катализаторы | |
| 700 | 1 | |a Frantsina |b E. V. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences |f 1985- |g Evgeniya Vladimirovna |3 (RuTPU)RU\TPU\pers\32193 |9 16193 | |
| 701 | 1 | |a Belinskaya |b N. S. |c chemist |c Associate Professor of Tomsk Polytechnic University, Candidate of Sciences |f 1989- |g Natalia Sergeevna |3 (RuTPU)RU\TPU\pers\31267 |9 15445 | |
| 701 | 1 | |a Popova |b N. |g Natalya | |
| 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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