| Autor: | A. A. Romanov, S. Sh. Gershuni, A. A. Nikitin, M. I. Belkin, S. B. Yukhtin, S. V. Rumyantsev, E. A. Esipko |
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| Rok vydání: | 2003 |
| Předmět: |
Hydrocyclone
General Chemical Engineering technology industry and agriculture Energy Engineering and Power Technology Separator (oil production) General Chemistry Alkylation equipment and supplies complex mixtures law.invention chemistry.chemical_compound Fuel Technology chemistry Chemical engineering law Isobutane Octane rating Organic chemistry Gasoline Distillation Octane |
| Zdroj: | Chemistry and Technology of Fuels and Oils. 39:15-19 |
| ISSN: | 0009-3092 |
| DOI: | 10.1023/a:1023280901701 |
| Popis: | Experience in operating a sulfuric–acid alkylation jet reactor of new design — with no mixers and heat–exchange bank and a process scheme that includes this reactor, a hydrocyclone, three–phase separator, and circulating centrifugal pumps are described. An additional quantity of feedstock is added to the jet reactor operating in tandem with a cascade reactor without addition of circulating isobutane. The concentration of high–octane components in the products of the reaction, i.e., the alkylate production volume, increases. The results of operating the jet reactor in incorporation of propylene feedstock from the cascade reactor to “butylene” alkylate are reported. The additional volume of “propylene” alkylate is up to 1/3 of the total output of the unit, distillation is improved, and the Motor Octane Number decreases insignificantly — by a maximum of 0.5 points. |
| Databáze: | OpenAIRE |
| Externí odkaz: |
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