Studying the influence of the conjugate technological stages on the performance of linear benzenes synthesis unit via the mathematical model
| Parent link: | Petroleum and Coal Vol. 60, iss. 1.— 2018.— [P. 1-6] |
|---|---|
| Autor corporatiu: | |
| Altres autors: | , , , |
| Sumari: | Title screen Optimization of the operation of the chemical-technological system as a whole is possible only if the efficiency of each of the associated processes of all stages of production is increased, taking into account their interrelationship. These problems are successfully solved using the methods of mathematical modeling and computer modeling systems that take into account the volatility of the raw material composition, the change in catalyst activity and a large number of control parameters. This approach was used for benzene alkylation process and allowed us to reveal regularieties of alkylation reactor depending on the technologiscal conditions in the conjugate apparatuses. Thus, optomal HF-catalyst activity depends signifacantly both on the dehydrogenation feedstock composition and its flow rate. |
| Idioma: | anglès |
| Publicat: |
2018
|
| Matèries: | |
| Accés en línia: | https://www.vurup.sk/wp-content/uploads/2018/01/PC_6_2017_Dolganov-105.pdf |
| Format: | Electrònic Capítol de llibre |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=657665 |
MARC
| LEADER | 00000naa0a2200000 4500 | ||
|---|---|---|---|
| 001 | 657665 | ||
| 005 | 20250122175259.0 | ||
| 035 | |a (RuTPU)RU\TPU\network\24317 | ||
| 090 | |a 657665 | ||
| 100 | |a 20180305d2018 k||y0engy50 ba | ||
| 101 | 0 | |a eng | |
| 102 | |a SK | ||
| 135 | |a drcn ---uucaa | ||
| 181 | 0 | |a i | |
| 182 | 0 | |a b | |
| 200 | 1 | |a Studying the influence of the conjugate technological stages on the performance of linear benzenes synthesis unit via the mathematical model |f I. O. Dolganova, E. D. Ivanchina, E. N. Ivashkina, A. A. Borissov | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 6 (27 tit.)] | ||
| 330 | |a Optimization of the operation of the chemical-technological system as a whole is possible only if the efficiency of each of the associated processes of all stages of production is increased, taking into account their interrelationship. These problems are successfully solved using the methods of mathematical modeling and computer modeling systems that take into account the volatility of the raw material composition, the change in catalyst activity and a large number of control parameters. This approach was used for benzene alkylation process and allowed us to reveal regularieties of alkylation reactor depending on the technologiscal conditions in the conjugate apparatuses. Thus, optomal HF-catalyst activity depends signifacantly both on the dehydrogenation feedstock composition and its flow rate. | ||
| 461 | |t Petroleum and Coal | ||
| 463 | |t Vol. 60, iss. 1 |v [P. 1-6] |d 2018 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a математическое моделирование | |
| 610 | 1 | |a алкилирование | |
| 610 | 1 | |a катализаторы | |
| 610 | 1 | |a оптимальный режим | |
| 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 | |
| 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 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 Borissov |b A. A. |g Anatoli Alimpievich | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет |b Инженерная школа природных ресурсов |b Отделение химической инженерии |3 (RuTPU)RU\TPU\col\23513 |
| 801 | 2 | |a RU |b 63413507 |c 20201112 |g RCR | |
| 856 | 4 | |u https://www.vurup.sk/wp-content/uploads/2018/01/PC_6_2017_Dolganov-105.pdf | |
| 942 | |c CF | ||