Catalyst for the conversion of hydrocarbons

Claim 2

A hydrocarbon conversion catalyst comprising a platinum component, a non-acidic potassium form L-zeolite, and an amorphous silica binder, where the catalyst is prepared by the steps of: (a) commingling the non-acidic potassium form L-zeolite with amorpous silica powder; (b) adding an aqueous solution of potassium hydroxide to the L-zeolite and silica powder and mixing to form an extrudable dough; (c) extruding the dough to form extrudates that are non-acidic as a result of the incorporated potassium hydroxide; (d) calcining the extrudates at temperatures exceeding 26° C. without prior wasing or low-temperature drying of the extrudates or without subjecting the extrudates to any treatment that would neutralize or reduce the basicity of the extrudates or would result in a loss of potassium cations; (e) contacting the calcined extrudate with a solution comprising a platinum component and a potassium component; and, (f) subjecting the resultant extrudate of step (e) to an oxidation treatment and subsequently to a reduction treatment.

Claim 3

The catalyst of claim 1 further characterized in that it comprises from about 25 to 90 wt. % non-acidic potassium form L-zeolite.

Claim 4

The catalyst of claim 1 further characterized in that it comprises from about 0.01 to about 5.0 wt. % platinum.

Claim 5

The catalyst of claim 1 further characterized in that the platinum component is added to the catalyst by a competitive ion exchange procedure using a solution of tetra-amine platinum chloride and a potassium compound or mixture of potassium compounds.

Claim 6

A dehydrocyclization catalyst composition useful for the conversion of C 6 to C 8 hydrocarbons which comprises 0.01 to 5 wt. % platinum, 20 to 90 wt. % non-acidic potassium form L-zeolite, and 80 to 10 wt. % silica binder where the catalyst is prepared by the steps of: (a) commingling non-acidic potassium form L-zeolite with solid precipitated powdered silica in a dry weight ratio of L-zeolite to silica of at least 1:4; (b) adding an aqueous solution of potassium hydroxide to the L-zeolite and silica in an amount of from about 0.1 to about 1.2 pounds potassium hydroxide per 100 pounds dry solids to form an extrudable dough; (c) extruding the dough to form cylindrical extrudates; (d) calcining the extrudates at a temperature of at least 454° C. without performing any prior steps to neutralize the basicity imparted to the extrudates by the potassium hydroxide solution; (e) contacting the calined extrudate with a solution comprising tetra-amine platinum chloride and potassium chloride; and, (f) oxidizing the resultant extrudate from step (e) in oxygen-containing gas at a temperature of at least 316° C. followed by contacting the oxidized extrudate in a reducing atmosphere at a temperature of at least 90° C.

Claim 7

A dehydrocyclization catalyst composition useful for the conversion of C 6 to C 8 hydrocarbons which comprises 0.01 to 5 wt. % platinum, 20 to 90 wt. % non-acidic potassium form L-zeolite, and 80 to 10 wt. % silica binder where the catalyst is prepared by the steps of: (a) commingling non-acidic potassium form L-zeolite with solid precipitated powdered silica in a dry weight ratio of L-zeolite to silica of at least 1:4; (b) adding an aqueous solution of potassium hydroxide to the L-zeolite and silica in an amount of from about 0.1 to about 1.2 pounds potassium hydroxide per 100 pounds dry solids to form an extrudable dough; (c) extruding the dough to form cylindrical extrudates; (d) calcining the extrudates at a temperature of at least 454° C. without performing any prior steps to neutralize the basicity imparted to the extrudates by the potassium hydroxide solution; (e) contacting the calined extrudate with a solution comprising tetra-amine platinum chloride and potassium chloride; and, (f) oxidizing the resultant extrudate from step (e) in oxygen-containing gas at a temperature of at least 316° C. followed by contacting the oxidized extrudate in a reducing atmosphere at a temperature of at least 90° C.