Comparative analysis of catalyst operation in the process of higher paraffins dehydrogenation at different technological modes using mathematical model
| Parent link: | Petroleum Science and Technology Vol. 36, № 20.— 2018.— [P. 1672-1682] |
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| Autor corporatiu: | |
| Altres autors: | , , , , |
| Sumari: | Title screen This paper presents the results of comparative analysis of three run cycles of platinum catalyst for higher paraffins C 9 –C 14 dehydrogenation process, performed using mathematical model. The results of model calculations were compared with the experimental data obtained at the industrial unit. It was established that deactivation of the platinum dehydrogenation cata- lyst is influenced by the technological modes of its operation, such as tem- perature, pressure, hydrogen/feedstock molar ratio and water supply. In the process of higher paraffins dehydrogenation, the phenomenon of plat- inum catalyst self-regeneration is observed. This occurs due to the action of feedstock components, in particular water and hydrogen involved in oxidation and hydrogenation of intermediate condensation products (coke structures). Model calculations showed that with a decrease in the hydro- gen/feedstock molar ratio and simultaneous increase in water supply, depending on the temperature and composition of feedstock, it is possible to slow down deactivation process and increase the catalyst service life. This fact was experimentally confirmed at industrial unit. Режим доступа: по договору с организацией-держателем ресурса |
| Idioma: | anglès |
| Publicat: |
2018
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| Matèries: | |
| Accés en línia: | https://doi.org/10.1080/10916466.2018.1504068 |
| Format: | Electrònic Capítol de llibre |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=660479 |
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| 200 | 1 | |a Comparative analysis of catalyst operation in the process of higher paraffins dehydrogenation at different technological modes using mathematical model |f E. V. Frantsina, E. D. Ivanchina, E. N. Ivashkina [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: 34 tit.] | ||
| 330 | |a This paper presents the results of comparative analysis of three run cycles of platinum catalyst for higher paraffins C 9 –C 14 dehydrogenation process, performed using mathematical model. The results of model calculations were compared with the experimental data obtained at the industrial unit. It was established that deactivation of the platinum dehydrogenation cata- lyst is influenced by the technological modes of its operation, such as tem- perature, pressure, hydrogen/feedstock molar ratio and water supply. In the process of higher paraffins dehydrogenation, the phenomenon of plat- inum catalyst self-regeneration is observed. This occurs due to the action of feedstock components, in particular water and hydrogen involved in oxidation and hydrogenation of intermediate condensation products (coke structures). Model calculations showed that with a decrease in the hydro- gen/feedstock molar ratio and simultaneous increase in water supply, depending on the temperature and composition of feedstock, it is possible to slow down deactivation process and increase the catalyst service life. This fact was experimentally confirmed at industrial unit. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Petroleum Science and Technology | ||
| 463 | |t Vol. 36, № 20 |v [P. 1672-1682] |d 2018 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a catalyst | |
| 610 | 1 | |a deactivation | |
| 610 | 1 | |a dehydrogenation | |
| 610 | 1 | |a higher paraffins | |
| 610 | 1 | |a hydrogen | |
| 610 | 1 | |a mathematical model | |
| 610 | 1 | |a molar ratio | |
| 610 | 1 | |a катализаторы | |
| 610 | 1 | |a дезактивация | |
| 610 | 1 | |a дегидрирование | |
| 610 | 1 | |a высшие парафины | |
| 610 | 1 | |a водород | |
| 610 | 1 | |a математические модели | |
| 610 | 1 | |a молярное соотношение | |
| 701 | 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 Ivanchina |b E. D. |c chemist |c Professor of Tomsk Polytechnic University, Doctor of technical sciences |f 1951- |g Emilia Dmitrievna |3 (RuTPU)RU\TPU\pers\31274 | |
| 701 | 1 | |a Ivashkina |b E. N. |c Chemical Engineer |c Professor of Tomsk Polytechnic University, Doctor of technical sciences |f 1983- |g Elena Nikolaevna |3 (RuTPU)RU\TPU\pers\31275 |9 15453 | |
| 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 Fefelova |b K. O. |g Kseniya Olegovna | |
| 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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