Zeolite catalysis
AssigneeMobil Oil Corporation
InventorsPochen Chu, William E. Garwood, Albert B. Schwartz
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Abstract
A surface-inactive shape selective metallosilicate catalyst, useful for the conversion of lower molecular weight olefins to liquid hydrocarbons such as gasoline, distillate, and high viscosity lube oils, is prepared by a process comprising forming a silica shell on a metallosilicate core by crystallizing silica in the presence of fluoride ion onto the surface of the core.
Claims10
A process for preparing hydrocarbons boiling in the gasoline and/or distillate range by contacting a feedstock comprising lower molecular weight olefins in a reaction zone under conditions of elevated temperature and pressure with a shape selective crystalline aluminosilicate catalyst, comprising:
- reducing the non-shape selective surface-cracking and/or surface isomerization activity of the aluminosilicate catalyst by a process comprising:
- preparing an aqueous solution comprising colloidal silica, optionally an organic directing agent, and a source of hydroxide ions;
- mixing the aqueous solution with an aqueous dispersion of shape-selective crystalline aluminosilicate to form a homogeneous mixture which is subsequently heated;
- adding an aqueous solution comprising a source of fluoride ions to the homogeneous mixture to form a reactive composition;
- heating the reactive composition at a temperature to effectively form a surface-deactivated catalyst comprising a crystalline fluoride-containing silica outer shell on an aluminosilicate;
- withdrawing the surface-deactivated catalyst from the reactive composition for washing, drying, and calcining of the catalyst;
- and
- removing the catalyst to the reaction zone for contact with the olefin feedstock.
A process for preparing a high viscosity index lube oil from a feedstock comprising lower molecular weight olefins comprising:
- contacting the feedstock at reaction conditions in a reaction zone with a catalyst comprising an inner portion and an outer portion disposed as a porous shell around the inner portion, the inner portion comprising a medium pore shape-selective crystalline acidic metallosilicate, and the outer portion comprising a fluoride-containing crystalline silica shell substantially free of acid sites;
- and
- withdrawing from the reaction zone a hydrocarbon liquid comprising a high viscosity index lube oil and higher boiling hydrocarbons.
A process for the shape-selective conversion of hydrocarbons comprising;
- contacting the hydrocarbons at reaction conditions with a catalyst comprising an inner portion and an outer portion disposed as a porous shell around the inner portion, the inner portion comprising a shape-selective tetrahedrally coordinated crystalline acidic metallosilicate, and the outer portion comprising a fluoride-containing crystalline silica shell substantially free of acid sites.
Dependencies are inferred from the claim text.