Optimal design of straight- run gasoline conversion on zeolite catalyst; Petroleum and Coal; Vol. 58, iss. 7
| Parent link: | Petroleum and Coal Vol. 58, iss. 7.— 2016.— [P. 721-725] |
|---|---|
| Autor kompanije: | |
| Daljnji autori: | , , , |
| Sažetak: | Title screen The HYSYS Aspen Plus software is used to develop a model of the reactor unit including a plug flow reactor and distillation sequence for conversion of gasoline fractions. The constructive and process variables of the key equipment were optimized stepwise with the model. The developed objective dimensionless function allows choosing optimal conditions for work in the mode of maximum yield or in the mode of maximum octane number of the product. The reactor was designed and optimal modes were found for both the reactor and fractionation unit. Свободный доступ из сети Интернет |
| Jezik: | engleski |
| Izdano: |
2016
|
| Teme: | |
| Online pristup: | http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_samborskaya_503.pdf |
| Format: | Elektronički Poglavlje knjige |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654352 |
MARC
| LEADER | 00000naa0a2200000 4500 | ||
|---|---|---|---|
| 001 | 654352 | ||
| 005 | 20250312093908.0 | ||
| 035 | |a (RuTPU)RU\TPU\network\19946 | ||
| 035 | |a RU\TPU\network\19787 | ||
| 090 | |a 654352 | ||
| 100 | |a 20170425d2016 k||y0rusy50 ba | ||
| 101 | 0 | |a eng | |
| 102 | |a SK | ||
| 135 | |a drcn ---uucaa | ||
| 181 | 0 | |a i | |
| 182 | 0 | |a b | |
| 200 | 1 | |a Optimal design of straight- run gasoline conversion on zeolite catalyst |f M. A. Samborskaya, I. A. Gryaznova, V. V. Mashina, O. A. Cherednichenko | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 724-725 (14 tit.)] | ||
| 330 | |a The HYSYS Aspen Plus software is used to develop a model of the reactor unit including a plug flow reactor and distillation sequence for conversion of gasoline fractions. The constructive and process variables of the key equipment were optimized stepwise with the model. The developed objective dimensionless function allows choosing optimal conditions for work in the mode of maximum yield or in the mode of maximum octane number of the product. The reactor was designed and optimal modes were found for both the reactor and fractionation unit. | ||
| 333 | |a Свободный доступ из сети Интернет | ||
| 461 | |t Petroleum and Coal | ||
| 463 | |t Vol. 58, iss. 7 |v [P. 721-725] |d 2016 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a zeolite-catalyst | |
| 610 | 1 | |a катализаторы | |
| 610 | 1 | |a кинетическое моделирование | |
| 610 | 1 | |a реакторы | |
| 610 | 1 | |a оптимальные режимы | |
| 701 | 1 | |a Samborskaya |b M. A. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of chemical sciences |f 1960- |g Marina Anatolievna |3 (RuTPU)RU\TPU\pers\31290 |9 15468 | |
| 701 | 1 | |a Gryaznova |b I. A. |c chemist |c assistant of Tomsk Polytechnic University |f 1989- |g Inga Andreevna |3 (RuTPU)RU\TPU\pers\35930 | |
| 701 | 1 | |a Mashina |b V. V. |g Vera Vadimovna | |
| 701 | 1 | |a Cherednichenko |b O. A. |g Olga Alekseevna | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет (ТПУ) |b Институт природных ресурсов (ИПР) |b Кафедра химической технологии топлива и химической кибернетики (ХТТ) |3 (RuTPU)RU\TPU\col\18665 |
| 801 | 2 | |a RU |b 63413507 |c 20200217 |g RCR | |
| 856 | 4 | |u http://www.vurup.sk/wp-content/uploads/dlm_uploads/2017/07/pc_7_2016_samborskaya_503.pdf | |
| 942 | |c CF | ||