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Effect of hydro-thermal treatment on properties of aluminosilicate catalysts in cracking of petroleum fractions
Abstract 1. Hydrothermal treatment of gel during the synthesis of aluminosilicate catalysis increases catalytic activity in cracking of a kerosine-gas oil fraction by 3–7% of gasoline yeild. 2. Aluminosilicate catalysts subjected to hydro-thermal tretment produce less coke and have a higher rate of oxidative recovery, compared with an industrial cracked catalyst containing zeolite. 3. A catalyst obtained from a matrix subjected to hydro-thermal treatment and containing zeolite has a higher gasoline yield (46.4–51.0%) than AShNTs-3 spherical and zeolite-containing industrial aluminosilicate catalysts (39.0–45.4%).
Effect of hydro-thermal treatment on properties of aluminosilicate catalysts in cracking of petroleum fractions
Abstract 1. Hydrothermal treatment of gel during the synthesis of aluminosilicate catalysis increases catalytic activity in cracking of a kerosine-gas oil fraction by 3–7% of gasoline yeild. 2. Aluminosilicate catalysts subjected to hydro-thermal tretment produce less coke and have a higher rate of oxidative recovery, compared with an industrial cracked catalyst containing zeolite. 3. A catalyst obtained from a matrix subjected to hydro-thermal treatment and containing zeolite has a higher gasoline yield (46.4–51.0%) than AShNTs-3 spherical and zeolite-containing industrial aluminosilicate catalysts (39.0–45.4%).
Effect of hydro-thermal treatment on properties of aluminosilicate catalysts in cracking of petroleum fractions
Komarov, V.S. (Autor:in) / Stepanova, Ye.A. (Autor:in)
25.11.1975
9 pages
Aufsatz (Zeitschrift)
Elektronische Ressource
Englisch
Decarboxylation of petroleum acids on aluminosilicate and nanosized magnesia and titania catalysts
Springer Verlag | 2016
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