Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins; Procedia Engineering; Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft)
| Parent link: | Procedia Engineering Vol. 152 : Oil and Gas Engineering (OGE-2016), Omsk, 25-30 April 2016 (Supported by PJSC Gazprom Neft).— 2016.— [P. 81-86] |
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| Ente Autore: | |
| Altri autori: | , , , , , |
| Riassunto: | Title screen The article provides the results of applied mathematical model of sulfuric acid catalyzed alkylation of isobutane with olefins. It was shown that increasing the content of propylene in the feedstock to 2 % leads to decrease in octane number of alkylate to 0.5-1.0 points. Alkylates produced from feedstock with less isobutane mass fraction have a smaller value of octane number. Using mathematic model it was determined that the main parameter influencing the acid activity in the alkylation process is the fresh acid concentration. |
| Lingua: | inglese |
| Pubblicazione: |
2016
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| Soggetti: | |
| Accesso online: | http://dx.doi.org/10.1016/j.proeng.2016.07.632 |
| Natura: | Elettronico Capitolo di libro |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=651757 |
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| 200 | 1 | |a Mathematical Modeling Sulfuric Acid Catalyzed Alkylation of Isobutane with Olefins |f E. N. Ivashkina [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 86 (12 tit.)] | ||
| 330 | |a The article provides the results of applied mathematical model of sulfuric acid catalyzed alkylation of isobutane with olefins. It was shown that increasing the content of propylene in the feedstock to 2 % leads to decrease in octane number of alkylate to 0.5-1.0 points. Alkylates produced from feedstock with less isobutane mass fraction have a smaller value of octane number. Using mathematic model it was determined that the main parameter influencing the acid activity in the alkylation process is the fresh acid concentration. | ||
| 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. 81-86] |d 2016 | |
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a mathematical modeling | |
| 610 | 1 | |a alkylate | |
| 610 | 1 | |a optimization | |
| 610 | 1 | |a octane number | |
| 610 | 1 | |a sulfuric acid alkylation | |
| 610 | 1 | |a математическое моделирование | |
| 610 | 1 | |a оптимизация | |
| 610 | 1 | |a октановые числа | |
| 610 | 1 | |a сернокислотное алкилирование | |
| 610 | 1 | |a алкилаты | |
| 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 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 Nurmakanova |b A. E. |g Asem Eslyambekovna | |
| 701 | 1 | |a Boychenko |b S. S. |g Stanislav Sergeevich | |
| 701 | 1 | |a Ushakov |b A. S. |g Anton Sergeevich | |
| 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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