Study of an aluminosilicate zeolite-containing catalyst during hydrogen-free refining of a straight-run gasoline fraction
UDC: 66.092.097:665.64
DOI: -
Authors:
MAKAROVA N.P.
1,
MELNIKOV V.B.
1
1 National University of Oil and Gas "Gubkin University", Moscow, Russia
Keywords: hydrogen-free refining of the straight-run gasoline fraction, aluminosilicate zeolite-containing catalysts, high-silica zeolites, ZSM zeolites, stable catalyst activity
Annotation:
One of the largest processes for producing high-octane additives and gasolines is catalytic reforming, which is based on the processing of straight-run gasoline in the presence of hydrogen-containing gas. Currently, in accordance with the requirements of EURO-5 and GOST 32513-2023, the catalytic reforming process is focused on producing gasoline high-octane fractions with a high content of isoparaffinic hydrocarbons, rather than aromatic ones. The authors of the article present research data on the process of the straight-run gasoline fraction refining in the absence of hydrogen-containing gas using an aluminosilicate zeolite-containing catalyst. The process of refining the straight–run gasoline fraction was studied on a standard laboratory installation with a stationary catalyst layer at a temperature of 350...500 °C, a pressure of 0,1 and 1,0 MPa and a volumetric feed rate of 1,0 hr–1.
Studies of the catalyst stable activity under the influence of multiple cycles of coking–regeneration were carried out, followed by testing in the process of hydrogen-free refining of the straight-run gasoline fraction. According to the study results, the stable activity of the catalyst and the conditions for the process of hydrogen-free refining of the straight-run gasoline fraction were determined.
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