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Abstrakty
The results of the selective hydrogenation of dienes in the C; fraction which was distillated from the light cracking gasoline and contained about 1 wt % of dienes have been presented. Hydrogenation was performed in a liquid phase in the presence of a palladium catalyst. Optimal parameters of the process have been determined, making possible to decrease the dienes content to the level below 10 ppm wt. with a simultaneous increase of the content of reactive tertiary isoamylenes in the C5 fraction by 8 wt %.
Czasopismo
Rocznik
Tom
Strony
93--98
Opis fizyczny
Bibliogr. 7 poz., rys., tab.
Twórcy
autor
autor
- Research and Development Center of the Refining Industry in Płock, ul. Chemików 7, 09-411 Płock, Poland, tel. (024) 365-30-59, e-mail: janusz.pilarczyk@obr.pl
Bibliografia
- (1) K. Frączek, A. Dydak. Nafta-Gaz, 1996. 106 nr 5, 30.
- (2) New etherification process commercialized in Finland. Oil & Gas Journal. 1997, 44 - 45.
- (3) H. J. Muller, Ch. Herion, G. Meyer, P. Polanek, H. Laib. The SELOP- processes: BASF-technology for hydrogenations in the steamcracker downstream treatment. Petroleum and Coal. 1997, 37 (4), 34 - 43.
- (4) J. Cosyns, P. Travers. Processes for upgrading C3, C4 and C5 olefinic streams. Petroleum and Coal. 1997, 37 (4), 23 - 33.
- (5) lnquiry Materials - Hiils Selective Hydrogenation Process, http://www.uop.com/framesets/petrochemicals.html.
- (6) Inquiry Materials - NExSELECT Process, http://www.nesteengineering.com.
- (7) Inquiry Materials - Catalysts from BASF, http://www.basf.de/en/produkte/chemikalien/catalysts/ca/hydro.html.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPS3-0003-0031