Optimization of Higher Alkanes Dehydrogenation Process under Conditions of Decreased Hydrogen Containing Gas Flow with Using Mathematical Modeling
| Parent link: | Procedia Engineering Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015.— 2015.— [P. 26–31] |
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| Körperschaft: | |
| Weitere Verfasser: | , , , , |
| Zusammenfassung: | Title screen The article proposes the way of saving catalyst resource and increasing the efficiency of higher alkanes dehydrogenation process using mathematical model method. The study has indicated, that reducing hydrogen/feedstock molar ratio results in balance shear of alkanes dehydrogenation reaction to alkenes, which is proved by the results of pilot operating of the alkenes production unit at Ltd. KINEF and by the mathematical model calculations. The results of the prediction calculation of optimum process parameters at various hydrogen/feedstock molar ratios are presented. |
| Sprache: | Englisch |
| Veröffentlicht: |
2015
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| Schlagworte: | |
| Online-Zugang: | http://earchive.tpu.ru/handle/11683/36156 http://dx.doi.org/10.1016/j.proeng.2015.07.282 |
| Format: | Elektronisch Buchkapitel |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=650247 |
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| 200 | 1 | |a Optimization of Higher Alkanes Dehydrogenation Process under Conditions of Decreased Hydrogen Containing Gas Flow with Using Mathematical Modeling |f E. D. Ivanchina [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 30-31 (26 tit.)] | ||
| 330 | |a The article proposes the way of saving catalyst resource and increasing the efficiency of higher alkanes dehydrogenation process using mathematical model method. The study has indicated, that reducing hydrogen/feedstock molar ratio results in balance shear of alkanes dehydrogenation reaction to alkenes, which is proved by the results of pilot operating of the alkenes production unit at Ltd. KINEF and by the mathematical model calculations. The results of the prediction calculation of optimum process parameters at various hydrogen/feedstock molar ratios are presented. | ||
| 461 | |t Procedia Engineering | ||
| 463 | |t Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015 |v [P. 26–31] |d 2015 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a катализаторы | |
| 610 | 1 | |a дегидрирование | |
| 610 | 1 | |a математические модели | |
| 610 | 1 | |a оптимизация | |
| 610 | 1 | |a водородсодержащие газы | |
| 701 | 1 | |a Ivanchina |b E. D. |c chemist |c Professor of Tomsk Polytechnic University, Doctor of technical sciences |f 1951-2022 |g Emilia Dmitrievna |3 (RuTPU)RU\TPU\pers\31274 |9 15452 | |
| 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 Glik |b P. A. | |
| 701 | 1 | |a Platonov |b V. V. | |
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| 856 | 4 | |u http://earchive.tpu.ru/handle/11683/36156 | |
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