초록 ▼

An aromatic gasoline component is prepared in a multi-step petroleum refining process starting with a heavy carbometallic petroleum fraction which is catalytically cracked to yield a light catalytic cycle oil which, in turn, is mildly hydrogenated to produce a partially saturated bicyclic hydrocarbo

An aromatic gasoline component is prepared in a multi-step petroleum refining process starting with a heavy carbometallic petroleum fraction which is catalytically cracked to yield a light catalytic cycle oil which, in turn, is mildly hydrogenated to produce a partially saturated bicyclic hydrocarbon fraction which itself is catalytically cracked to yield a monoaromatic hydrocarbon fraction from which is recovered a gasoline product. The bicyclic hydrocarbons are converted to monoaromatics by selective partial saturation and ring scission.

대표청구항 ▼

A process for the production of high octane gasoline component comprising the sequential steps of: A. Cracking carbometallic petroleum oil characterized by a Conradson Carbon content of at least 1.0 wt% and a metals content of at least 4 ppm Nickel Equivalents by weight in a riser cracking zone at c

A process for the production of high octane gasoline component comprising the sequential steps of: A. Cracking carbometallic petroleum oil characterized by a Conradson Carbon content of at least 1.0 wt% and a metals content of at least 4 ppm Nickel Equivalents by weight in a riser cracking zone at cracking conditions in the presence of fluid cracking catalyst, B. recovering by distillation a light cycle oil fraction boiling in the range of about 216°C. to about 332°C. (about 430°F. to about 630°F.) and containing from about 10 vol. % to about 60 vol. % dual ring unsaturated aromatic hydrocarbons, C. contacting said fraction in the mixed phase in a saturation hydrogenation zone with a nickel-containing hydrogenation catalyst at selective conditions of temperature, pressure, space velocity and hydrogen circulation rate whereby at least 20-80 wt. % of the unsaturated aromatic hydrocarbons add hydrogen molecules to one of the rings to produce a partially saturated bicyclic hydrocarbon fraction, D. subjecting said partially saturated bicyclic hydrocarbon fraction to fluid catalytic cracking in a riser cracking zone at cracking conditions in the presence of with a zeolite fluid cracking catalyst and a metals passivator and in the absence of added hydrogen whereby rate of dehydrogenation is slowed sufficiently so that one ring of the bicyclic hydrocarbon rings cracks yielding monoaromatic hydrocarbons and, E. recovering from said monoaromatic hydrocarbons a gasoline component product characterized by an average octane of at least 91 and a monoaromatic hydrocarbon content in the range of 35 to 55 vol. %.