Non-stationary mathematical model of industrial diesel fuel hydrotreating process; Petroleum and Coal; Vol. 60, iss. 1
| Parent link: | Petroleum and Coal Vol. 60, iss. 1.— 2018.— [P. 104-112] |
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| 1. autor: | |
| Korporacja: | |
| Kolejni autorzy: | |
| Streszczenie: | Title screen Catalytic hydrotreating is widely used in secondary petroleum refining industry. The main purpose of this process is to significantly lower sulfur content in the petroleum products. Currently, there is a lack of industrially applicable mathematical models of diesel hydrotreating, especially the models which take into account the reaction kinetics and catalyst deactivation. In this paper, research is focused at processing of experimental data from laboratory equipment and industrial hydrotreating unit and developing mathematical model, which adequately describe industrial data of hydrotreating industrial unit with the use of current view of chemical mechanism and catalyst deactivation. |
| Język: | angielski |
| Wydane: |
2018
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| Hasła przedmiotowe: | |
| Dostęp online: | https://www.vurup.sk/wp-content/uploads/2018/05/PC_1_2018_Belinskaya_144cor1.pdf |
| Format: | Elektroniczne Rozdział |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=658256 |
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| 200 | 1 | |a Non-stationary mathematical model of industrial diesel fuel hydrotreating process |f A. A. Tataurshchikov, N. I. Krivtsova | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 110-112 (34 tit.)] | ||
| 330 | |a Catalytic hydrotreating is widely used in secondary petroleum refining industry. The main purpose of this process is to significantly lower sulfur content in the petroleum products. Currently, there is a lack of industrially applicable mathematical models of diesel hydrotreating, especially the models which take into account the reaction kinetics and catalyst deactivation. In this paper, research is focused at processing of experimental data from laboratory equipment and industrial hydrotreating unit and developing mathematical model, which adequately describe industrial data of hydrotreating industrial unit with the use of current view of chemical mechanism and catalyst deactivation. | ||
| 461 | |t Petroleum and Coal | ||
| 463 | |t Vol. 60, iss. 1 |v [P. 104-112] |d 2018 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a математическое моделирование | |
| 610 | 1 | |a программирование | |
| 610 | 1 | |a гидроочистка | |
| 610 | 1 | |a дизельные фракции | |
| 610 | 1 | |a бензотиофены | |
| 610 | 1 | |a дибензотиофены | |
| 610 | 1 | |a константа скорости реакции | |
| 610 | 1 | |a энергия активации | |
| 610 | 1 | |a мathematical modeling | |
| 610 | 1 | |a programming | |
| 610 | 1 | |a hydrotreating process | |
| 610 | 1 | |a diesel fraction | |
| 610 | 1 | |a benzothiophene | |
| 610 | 1 | |a dibenzothiophene | |
| 610 | 1 | |a reaction rate constant | |
| 610 | 1 | |a activation energy | |
| 700 | 1 | |a Tataurshchikov |b A. A. |g Anton Andreevich | |
| 701 | 1 | |a Krivtsova |b N. I. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences |f 1983- |g Nadezhda Igorevna |3 (RuTPU)RU\TPU\pers\33903 |9 17476 | |
| 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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