Developing a method for increasing the service life of a higher paraffin dehydrogenation catalyst, based on the nonstationary kinetic model of a reactor
| Parent link: | Catalysis in Industry: Scientific Journal Vol. 4, iss. 2.— 2012.— [P. 110-120] |
|---|---|
| Otros Autores: | , , , , , |
| Sumario: | Title screen The service life of an industrial catalyst can be prolonged by improving the technological conditions of its operation. This allows us to maximally eliminate the catalyst deactivation factors. A specific feature of the catalytic dehydrogenation of hydrocarbons is its nonstationarity produced by the deactivation of catalysts. The results of modeling the industrial catalytic process of C9-C14 paraffin dehydrogenation-the key stage in the production of linear alkylbenzenes-is discussed in this paper. We consider (1) thermodynamic analysis of reactions by means of quantum chemistry, (2) estimation of the kinetic model's parameters by solving the inverse kinetic problem, (3) selection of an equation that describes the coke deactivation of a catalyst, and (4) development of a method for increasing the service life of a dehydrogenation catalyst using a nonstationary model based on the quantitative consideration of the water added to a reactor within a temperature range of 470-490°C. The higher alkane dehydrogenation flowsheet proposed on the basis of these models allows us to predict the operation of a reactor in different water supply regimes. It is shown that the service life of a catalyst grows by 20-30% on the average, if water is fed by increasing portions. Режим доступа: по договору с организацией-держателем ресурса |
| Lenguaje: | inglés |
| Publicado: |
2012
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| Materias: | |
| Acceso en línea: | http://dx.doi.org/10.1134/S2070050412020079 |
| Formato: | Electrónico Capítulo de libro |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=655694 |
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| 200 | 1 | |a Developing a method for increasing the service life of a higher paraffin dehydrogenation catalyst, based on the nonstationary kinetic model of a reactor |f E. N. Ivashkina [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [Ref.: p. 119-120 (15 tit.)] | ||
| 330 | |a The service life of an industrial catalyst can be prolonged by improving the technological conditions of its operation. This allows us to maximally eliminate the catalyst deactivation factors. A specific feature of the catalytic dehydrogenation of hydrocarbons is its nonstationarity produced by the deactivation of catalysts. The results of modeling the industrial catalytic process of C9-C14 paraffin dehydrogenation-the key stage in the production of linear alkylbenzenes-is discussed in this paper. We consider (1) thermodynamic analysis of reactions by means of quantum chemistry, (2) estimation of the kinetic model's parameters by solving the inverse kinetic problem, (3) selection of an equation that describes the coke deactivation of a catalyst, and (4) development of a method for increasing the service life of a dehydrogenation catalyst using a nonstationary model based on the quantitative consideration of the water added to a reactor within a temperature range of 470-490°C. The higher alkane dehydrogenation flowsheet proposed on the basis of these models allows us to predict the operation of a reactor in different water supply regimes. It is shown that the service life of a catalyst grows by 20-30% on the average, if water is fed by increasing portions. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Catalysis in Industry |o Scientific Journal | ||
| 463 | |t Vol. 4, iss. 2 |v [P. 110-120] |d 2012 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a ресурсоэффективность | |
| 610 | 1 | |a алканы | |
| 610 | 1 | |a катализаторы | |
| 610 | 1 | |a математическое моделирование | |
| 610 | 1 | |a методы | |
| 610 | 1 | |a квантовая химия | |
| 610 | 1 | |a дезактивация | |
| 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 Frantsina |b E. V. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences |f 1985- |g Evgeniya Vladimirovna |3 (RuTPU)RU\TPU\pers\32193 |9 16193 | |
| 701 | 1 | |a Romanovskiy |b R. V. |c Chemical Engineer |c Engineer of Tomsk Polytechnic University |f 1987- |g Rostislav Vladimirovich |3 (RuTPU)RU\TPU\pers\32191 | |
| 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 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 Kravtsov |b A. V. |c Chemical Engineer |c Consulting Professor, Doctor of Technical Sciences (DSc) |f 1938-2012 |g Anatoly Vasilyevich |3 (RuTPU)RU\TPU\pers\29428 | |
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