Preparation of FCC charge from residual fractions
AssigneeEngelhard Minerals & Chemicals Corporation
InventorDavid B. Bartholic
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AssigneeEngelhard Minerals & Chemicals Corporation
InventorDavid B. Bartholic
Estimating the term…
Residual fractions from distillation of petroleum are rendered suitable for charge to catalytic cracking by high temperature, short time contact in a decarbonizing zone with fluidizable solid particles of essentially inert character and low surface area to deposit high boiling components of the crude and metals on the fluidizable solid particles whereby Conradson Carbon values and metal content of the hydrocarbon feedstock are reduced to levels tolerable in catalytic cracking and carbon laid down on the inert fluidizable particles is burned in a burning zone separate from the decarbonizing zone. Heated inert particles are recycled at least in part to the decarbonizing zone and then to the burning zone. Additional charge of fluidizable inert solid is produced in situ in the burner on a regular or intermittent basis by spraying a slurry of a precursor of the fluidizable inert solid into the hot gases in the burner whereby the sprayed mist dries in the form of fine beads composed of inert material and the beads are cycled to the decarbonizing zone to reduce Conradson Carbon and metals content of new feedstock charge.
A process for upgrading a petroleum charge of a crude oil or a residual fraction thereof which contains high boiling components of substantial Conradson Carbon number which comprises emulsifying water in said charge as the internal phase of a water in oil emulsion, contacting the emulsion of water in said charge in a confined rising vertical column with a finely divided solid contact material consisting essentially of an inert solid material having a microactivity for catalytic cracking not substantially greater than 20 at low severity, including a temperature of at least about 900.degree. F. for a period of time less than 2 seconds and less than that which induces substantial thermal cracking of said charge, at the end of said period of time separating from said inert solid a decarbonized hydrocarbon fraction of reduced Conradson Carbon number as compared with said charge and reducing temperature of said separated fraction to a level below that at which substantial thermal cracking takes place to terminate said period of time.
In a process for preparing premium products from crude petroleum by fractionally distilling the crude petroleum to separate gasoline and distillate gas oil from a residual fraction having a substantial Conradson Carbon number and metals content and charging the distillate gas oil to catalytic cracking;
In a process for preparing premium products from crude petroleum by fractionally distilling the crude petroleum to separate gasoline and distillate gas oil from a residual fraction having a substantial Conradson Carbon number and metals contact and charging the distillate gas oil to catalytic cracking the improvement which comprises:
Dependencies are inferred from the claim text.