Modifications of the adsorption-catalytic system for organic impurities removal; Chemical Engineering and Processing: Process Intensification; Article In Press
| Parent link: | Chemical Engineering and Processing: Process Intensification Article In Press.— 2017.— [12 p.] |
|---|---|
| Autor Corporativo: | |
| Outros autores: | , , , , , , |
| Summary: | Title screen The study was dedicated to optimization of the adsorption-catalytic process for abatement of volatile organic compounds (VOC), combining the adsorption of VOC at ambient temperature in the bed of the oxidation catalyst with the periodical regeneration of the catalyst by oxidation of adsorbed species at elevated temperature. The detailed mathematical model, accounting for occurrence of unsteady-state adsorption and oxidation reactions, heat and mass transfer process both in the catalyst bed and the catalyst pellets, was constructed. The good quality of the model was verified by bench experiments. The process simulation has confirmed the high efficiency of the new versions of the adsorption-catalytic processes: the process with the startup heater located directly inside the catalyst bed and the process with the system of parallel beds with non-simultaneous regeneration; these approaches give the way to significantly decrease the specific energy consumption and to level off the peaks of VOC outlet content and outlet gas temperature. The optimal values of process parameters were defined in the study. The developed process may be applied for VOC abatement in different waste gases, being especially advantageous in terms of energy consumption and operation flexibility in processing of lean vent gases with high flow rate. Режим доступа: по договору с организацией-держателем ресурса |
| Idioma: | inglés |
| Publicado: |
2017
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| Subjects: | |
| Acceso en liña: | https://doi.org/10.1016/j.cep.2017.04.011 |
| Formato: | Electrónico Capítulo de libro |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=654994 |
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| 200 | 1 | |a Modifications of the adsorption-catalytic system for organic impurities removal |f A. N. Zagoruiko [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: 30 tit.] | ||
| 330 | |a The study was dedicated to optimization of the adsorption-catalytic process for abatement of volatile organic compounds (VOC), combining the adsorption of VOC at ambient temperature in the bed of the oxidation catalyst with the periodical regeneration of the catalyst by oxidation of adsorbed species at elevated temperature. The detailed mathematical model, accounting for occurrence of unsteady-state adsorption and oxidation reactions, heat and mass transfer process both in the catalyst bed and the catalyst pellets, was constructed. The good quality of the model was verified by bench experiments. The process simulation has confirmed the high efficiency of the new versions of the adsorption-catalytic processes: the process with the startup heater located directly inside the catalyst bed and the process with the system of parallel beds with non-simultaneous regeneration; these approaches give the way to significantly decrease the specific energy consumption and to level off the peaks of VOC outlet content and outlet gas temperature. The optimal values of process parameters were defined in the study. The developed process may be applied for VOC abatement in different waste gases, being especially advantageous in terms of energy consumption and operation flexibility in processing of lean vent gases with high flow rate. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Chemical Engineering and Processing: Process Intensification | ||
| 463 | |t Article In Press |v [12 p.] |d 2017 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a адсорбционные системы | |
| 610 | 1 | |a каталитические системы | |
| 610 | 1 | |a летучие органические соединения | |
| 610 | 1 | |a математическое моделирование | |
| 610 | 1 | |a оптимизация процессов | |
| 610 | 1 | |a adsorption-catalytic process | |
| 610 | 1 | |a volatile organic compounds | |
| 610 | 1 | |a abatement | |
| 610 | 1 | |a mathematical modeling | |
| 610 | 1 | |a process optimization | |
| 701 | 1 | |a Zazhigalov |b S. V. |g Sergey | |
| 701 | 1 | |a Mikenin |b P. E. |g Pavel | |
| 701 | 1 | |a Pisarev |b D. A. |g Danil | |
| 701 | 1 | |a Baranov |b S. V. |g D. V. | |
| 701 | 1 | |a Lopatin |b S. A. |g Sergey | |
| 701 | 1 | |a Chumakova |b N. | |
| 701 | 1 | |a Zagoruiko |b A. N. |c Chemical Engineer |c Professor of Tomsk Polytechnic University, Doctor of technical sciences |f 1962- |g Andrey Nikolaevich |3 (RuTPU)RU\TPU\pers\33191 | |
| 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 20170613 |g RCR | |
| 856 | 4 | |u https://doi.org/10.1016/j.cep.2017.04.011 | |
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