Efficiency Improvement of the Light Gasoline Fractions Isomerization by Mathematical Modeling; Procedia Engineering; Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015
| Parent link: | Procedia Engineering Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015.— 2015.— [P. 18-24] |
|---|---|
| Korporativní autor: | |
| Další autoři: | , , , |
| Shrnutí: | Title screen Optimization and forecasting of light gasoline fractions isomerization is a complex technological issue, as it includes a variety of factors and independent parameters. The most effective solution is to use the mathematical modeling method of physical and chemical laws of the process. In this paper, we propose a method of intensification of the combined fractionation and isomerization processes of pentane-hexane fraction with the aim to improve the service durability of the catalyst SI-2 on the L-35-11 / 300 production unit. The developed complex mathematical model takes into account the influence of the feedstock composition, allows for assessment of the catalyst current activity and it is also a powerful optimization tool. According to the survey results the optimizing the feedstock composition will increase the octane number of the isomerate at 1.6-2.2 points. |
| Jazyk: | angličtina |
| Vydáno: |
2015
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| Témata: | |
| On-line přístup: | http://earchive.tpu.ru/handle/11683/36135 http://dx.doi.org/10.1016/j.proeng.2015.07.305 |
| Médium: | Elektronický zdroj Kapitola |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=650572 |
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| 200 | 1 | |a Efficiency Improvement of the Light Gasoline Fractions Isomerization by Mathematical Modeling |f V. A. Chuzlov [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: р. 136-137 (17 tit.)] | ||
| 330 | |a Optimization and forecasting of light gasoline fractions isomerization is a complex technological issue, as it includes a variety of factors and independent parameters. The most effective solution is to use the mathematical modeling method of physical and chemical laws of the process. In this paper, we propose a method of intensification of the combined fractionation and isomerization processes of pentane-hexane fraction with the aim to improve the service durability of the catalyst SI-2 on the L-35-11 / 300 production unit. The developed complex mathematical model takes into account the influence of the feedstock composition, allows for assessment of the catalyst current activity and it is also a powerful optimization tool. According to the survey results the optimizing the feedstock composition will increase the octane number of the isomerate at 1.6-2.2 points. | ||
| 461 | |t Procedia Engineering | ||
| 463 | |t Vol. 113 : Oil and Gas Engineering (OGE-2015), Omsk, 25-30 April 2015 |v [P. 18-24] |d 2015 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 701 | 1 | |a Chuzlov |b V. A. |c chemist |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences |f 1991- |g Vyacheslav Alekseevich |3 (RuTPU)RU\TPU\pers\33898 |9 17471 | |
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| 701 | 1 | |a Molotov |b K. V. |g Konstantin Vladimirovich | |
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