Complex modeling system for optimization of compounding process in gasoline pool to produce high-octane finished gasoline fuel
| Parent link: | Chemical Engineering Journal Vol. 277.— 2015.— [12 р.] |
|---|---|
| Autor corporatiu: | |
| Altres autors: | , , , , , |
| Sumari: | Title screen The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units. Режим доступа: по договору с организацией-держателем ресурса |
| Idioma: | anglès |
| Publicat: |
2015
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| Matèries: | |
| Accés en línia: | http://dx.doi.org/10.1016/j.cej.2015.03.014 |
| Format: | Electrònic Capítol de llibre |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=643002 |
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| 200 | 1 | |a Complex modeling system for optimization of compounding process in gasoline pool to produce high-octane finished gasoline fuel |f E. D. Ivanchina [et al.] | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 12 (20 tit.)] | ||
| 330 | |a The process of gasoline compounding is a difficult multistage industrial technology. Octane number is a numerical equivalent of gasoline detonation resistance, the main operational characteristic of trade gasoline. Prediction of octane numbers of individual hydrocarbons was performed with calculations of dissociation energy of their molecules. In this paper, a new approach is proposed for optimization and prediction of the unit operation modes for processing of multicomponent hydrocarbon mixtures, based on a complex mathematical model that considers reactivities of hydrocarbons of wide gasoline fraction in the reforming, isomerization, and compounding processes. The accuracy of calculations is confirmed with huge massive of experimental data obtained from catalytic reforming, catalytic cracking (FCC), isomerization and alkylation units. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Chemical Engineering Journal | ||
| 463 | |t Vol. 277 |v [12 р.] |d 2015 | ||
| 610 | 1 | |a электронный ресурс | |
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| 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 Kirgina |b M. V. |c Chemical Engineer |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences |f 1988- |g Mariya Vladimirovna |3 (RuTPU)RU\TPU\pers\31994 |9 16054 | |
| 701 | 1 | |a Chekantsev |b N. V. |c chemical-technologist |c Associate Professor of Tomsk Polytechnic University, Junior research, Candidate of technical sciences |f 1985- |g Nikita Vitalievich |3 (RuTPU)RU\TPU\pers\33870 | |
| 701 | 1 | |a Sakhnevich |b B.V. | |
| 701 | 1 | |a Sviridova |b E. V. |c specialist in the field of chemical technology, petrochemistry and biotechnology |c engineer of Tomsk Polytechnic University |f 1994- |g Elizaveta Vitaljevna |3 (RuTPU)RU\TPU\pers\46149 | |
| 701 | 1 | |a Romanovskiy |b R. V. |c Chemical-technologist |c Engineer of Tomsk Polytechnic University |f 1987- |g Rostislav Vladimirovich |3 (RuTPU)RU\TPU\pers\32191 | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет |c (2009- ) |9 26305 |
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