Non-Stationary Computer-Aided Simulation of gasoline Fraction Pyrolysis
| Parent link: | Petroleum and Coal Vol. 63, iss. 3.— 2021.— [P. 612-620] |
|---|---|
| Main Author: | |
| Corporate Author: | |
| Other Authors: | , |
| Summary: | Title screen Pyrolysis of hydrocarbons is one of the main processes in petro-chemistry due to the high demand for products derived from light alkenes such as ethene and propene. The process is performed with lackof oxygen and extreme temperatures. Thus, heavier hydrocarbons decay into lighter alkenes. Although, side reactions of these obtained alkenes polymerization with further polycondensation result in coke deposition. Therefore, crossection area of tube decreases as well as residence time. And yield of target products decreases under these conditions, i.e. the process becomes inefficient. The given paper discusses the mechanism of the pyrolysis process, presents the model itself and discusses theinfluence of main technological parameters on the process efficiency. |
| Language: | English |
| Published: |
2021
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| Subjects: | |
| Online Access: | https://www.vurup.sk/wp-content/uploads/2021/07/PC-X_Dolganova_34.pdf |
| Format: | Electronic Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=666149 |
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| 200 | 1 | |a Non-Stationary Computer-Aided Simulation of gasoline Fraction Pyrolysis |f A. A. Bunaev, I. M. Dolganov, I. O. Dolganova | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: 23 tit.] | ||
| 330 | |a Pyrolysis of hydrocarbons is one of the main processes in petro-chemistry due to the high demand for products derived from light alkenes such as ethene and propene. The process is performed with lackof oxygen and extreme temperatures. Thus, heavier hydrocarbons decay into lighter alkenes. Although, side reactions of these obtained alkenes polymerization with further polycondensation result in coke deposition. Therefore, crossection area of tube decreases as well as residence time. And yield of target products decreases under these conditions, i.e. the process becomes inefficient. The given paper discusses the mechanism of the pyrolysis process, presents the model itself and discusses theinfluence of main technological parameters on the process efficiency. | ||
| 461 | |t Petroleum and Coal | ||
| 463 | |t Vol. 63, iss. 3 |v [P. 612-620] |d 2021 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a pyrolysis | |
| 610 | 1 | |a non-stationary simulation | |
| 610 | 1 | |a coke deposition | |
| 610 | 1 | |a optimum performance | |
| 610 | 1 | |a пиролиз | |
| 610 | 1 | |a кокс | |
| 610 | 1 | |a отложения | |
| 610 | 1 | |a производительность | |
| 700 | 1 | |a Bunaev |b A. A. |c chemist |c engineer of Tomsk Polytechnic University |f 1996- |g Ayur Alekseevich |3 (RuTPU)RU\TPU\pers\47027 | |
| 701 | 1 | |a Dolganov |b I. M. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences |f 1987- |g Igor Mikhailovich |3 (RuTPU)RU\TPU\pers\32216 |9 16216 | |
| 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 | |
| 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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