Kinetic model of the catalytic reforming of gasolines in moving-bed reactors; Catalysis in Industry; Vol. 2, iss. 4
| Parent link: | Catalysis in Industry: Scientific Journal Vol. 2, iss. 4.— 2010.— [P. 374-380] |
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| Andre forfattere: | , , , , |
| Summary: | Title screen A mathematical model of the catalytic reforming of gasolines in a reactor with continuous catalyst regeneration is proposed. The model takes into account the motion of the catalyst, changes in its activity along the bed height, and the dependence of its activity on the circulation ratio. The kinetic parameters of the Pt-Sn catalyst are determined under operational conditions by solving the inverse kinetic problem. The composition of the reformate component as calculated by the model coincides with the experimental data within the accuracy of chromatographic analysis. The proposed model is invariant to the composition of raw materials and can be used for predictive calculations. Режим доступа: по договору с организацией-держателем ресурса |
| Sprog: | engelsk |
| Udgivet: |
2010
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| Fag: | |
| Online adgang: | http://dx.doi.org/10.1134/S2070050410040124 |
| Format: | Electronisk Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=655719 |
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| 200 | 1 | |a Kinetic model of the catalytic reforming of gasolines in moving-bed reactors |f M. S. Gyngazova [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [Ref.: p. 380 (15 tit.)] | ||
| 330 | |a A mathematical model of the catalytic reforming of gasolines in a reactor with continuous catalyst regeneration is proposed. The model takes into account the motion of the catalyst, changes in its activity along the bed height, and the dependence of its activity on the circulation ratio. The kinetic parameters of the Pt-Sn catalyst are determined under operational conditions by solving the inverse kinetic problem. The composition of the reformate component as calculated by the model coincides with the experimental data within the accuracy of chromatographic analysis. The proposed model is invariant to the composition of raw materials and can be used for predictive calculations. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Catalysis in Industry |o Scientific Journal | ||
| 463 | |t Vol. 2, iss. 4 |v [P. 374-380] |d 2010 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a каталитический риформинг | |
| 610 | 1 | |a бензины | |
| 610 | 1 | |a модели | |
| 610 | 1 | |a реакторы | |
| 701 | 1 | |a Gyngazova |b M. S. |c Chemical Engineer |c Engineer of Tomsk Polytechnic University, Candidate of technical sciences |f 1985- |g Mariya Sergeevna |3 (RuTPU)RU\TPU\pers\31995 | |
| 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 | |
| 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 Korolenko |b M. V. |c chemist |c Postgraduate of Tomsk Polytechnic University |f 1986- |g Mikhail Vladimirovich |3 (RuTPU)RU\TPU\pers\32186 | |
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| 856 | 4 | |u http://dx.doi.org/10.1134/S2070050410040124 | |
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