Modeling of Transalkylation Stage of Ethylbenzene Manufacturing with Zeolite-catalysts; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
| Источник: | Procedia Engineering Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft).— 2016.— [P. 45-50] |
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| Автор-организация: | |
| Другие авторы: | , , , |
| Примечания: | Title screen The analysis of industrial transalkylation reactor revealed regularities of catalyst activity and stability changes during its operation at change of basic technological parameters. A result of experimental data analysis, a list of possible reactions of transalkylation stage of ethylbenzene manufacturing zeolite-catalyst technology was developed. Values of Gibbs energies for change targets and adverse reactions, which were calculated with use of quantum chemistry methods, confirmed their thermodynamic probability at process conditions. The calculation results formed the basis of transalkylation process reaction network, needed to develop a mathematical model of ethylbenzene manufacturing zeolite-catalyst industrial technology. |
| Язык: | английский |
| Опубликовано: |
2016
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| Предметы: | |
| Online-ссылка: | http://dx.doi.org/10.1016/j.proeng.2016.07.622 |
| Формат: | Электронный ресурс Статья |
| Запись в KOHA: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=651758 |
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| 200 | 1 | |a Modeling of Transalkylation Stage of Ethylbenzene Manufacturing with Zeolite-catalysts |f S. A. Koshkin [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 49-50 (17 tit.)] | ||
| 330 | |a The analysis of industrial transalkylation reactor revealed regularities of catalyst activity and stability changes during its operation at change of basic technological parameters. A result of experimental data analysis, a list of possible reactions of transalkylation stage of ethylbenzene manufacturing zeolite-catalyst technology was developed. Values of Gibbs energies for change targets and adverse reactions, which were calculated with use of quantum chemistry methods, confirmed their thermodynamic probability at process conditions. The calculation results formed the basis of transalkylation process reaction network, needed to develop a mathematical model of ethylbenzene manufacturing zeolite-catalyst industrial technology. | ||
| 461 | 1 | |t Procedia Engineering | |
| 463 | 1 | |t Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft) |v [P. 45-50] |d 2016 | |
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a transalkylation | |
| 610 | 1 | |a mathematical models | |
| 610 | 1 | |a zeolite-catalyst | |
| 610 | 1 | |a трансалкилирование | |
| 610 | 1 | |a математические модели | |
| 610 | 1 | |a цеолитные катализаторы | |
| 701 | 1 | |a Koshkin |b S. A. |g Stanislav Aleksandrovich | |
| 701 | 1 | |a Ignatova |b L. S. |g Lyubov Sergeevna | |
| 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 Dolganova |b I. O. |c chemist |c Associate Scientist of Tomsk Polytechnic University, postgraduate student, candidate of technical Sciences |f 1988- |g Irena Olegovna |3 (RuTPU)RU\TPU\pers\31271 |9 15449 | |
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