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Hydrocarbon conversion with an acidic multimetallic catalytic composite

Assignee: Universal Oil Products Co
•
Filing: 1974-11-08
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Granted: 1976-06-01
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Expires: 1994-11-08
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Abstract

Abstract Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with an acidic multimetallic catalytic composite comprising a combination of catalytically effective amounts of a platinum group component, a tin component, a cobalt component and a halogen component with a porous carrier material. The platinum group component, tin component, cobalt component, and halogen component are present in the multimetallic catalyst in amounts respectively, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % tin, about 0.5 to about 5 wt. % cobalt, and about 0.1 to about 3.5 wt. % halogen. Moreover, these metallic components are uniformly dispersed throughout the porous carrier material in carefully controlled oxidation states such that substantially all of the platinum group metal is present therein in the elemental metallic state, substantially all of the cobalt component is present in the elemental metallic state or in a state which is reducible to the elemental metallic state under hydrocarbon conversion conditions, while substantially all of the tin is present therein in an oxidation state above that of the elemental metal. A specific example of the type of hydrocarbon conversion process disclosed is a process for the catalytic reforming of a low-octane gasoline fraction wherein the gasoline fraction and a hydrogen stream are contacted with the acidic multimetallic catalyst disclosed herein at reforming conditions.

Inventors

  • 👤 Ernest L. Pollitzer
  • 👤 John C. Hayes

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 09:47
CPC Classifications
C; C10; C10G; C10G47/00; C10G47/02; C10G47/10; C10G47/12; C10G47/14; B; B01; B01J; B01J23/00; B01J23/70; B01J23/89; B01J23/8913; B01J23/8933; B01J23/8966; B01J27/00; B01J27/06; B01J27/08; C07; C07C; C07C5/00; C07C5/22; C07C5/2206; C07C5/226; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; C07C2521/00; C07C2521/02; C07C2521/04; C07C2523/00; C07C2523/02; C07C2523/04; C07C2523/14; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/44; C07C2523/46; C07C2523/70; C07C2523/74; C07C2523/75; C07C2523/89; C10G2400/00; C10G2400/02

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 163 words
A process for producing a high octane reformate which comprises contacting a gasoline fraction at reforming conditions with an acidic catalytic composite comprising a porous carrier material containing, on an elemental basis, about 0.01 to about 2 wt. % platinum group metal, about 0.5 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % tin and about 0.1 to about 3.5 wt. % halogen, wherein the platinum group metal, cobalt and tin are uniformly dispersed throughout the porous carrier material, wherein the average crystallite size of the cobalt and tin is less than 100 Angstroms in maximum dimension, wherein substantially all of the platinum group metal is present in the elemental metallic state, wherein substantially all of the tin is present in an oxidation state above that of the elemental metal, and wherein substantially all of the cobalt is present in the elemental metallic state or in a state which is reducible to the elemental metallic state under reforming conditions.
Claim 2
Dependent Claim 163 words
A process for producing a high octane reformate which comprises contacting a gasoline fraction at reforming conditions with an acidic catalytic composite comprising a porous carrier material containing, on an elemental basis, about 0.01 to about 2 wt. % platinum group metal, about 0.5 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % tin and about 0.1 to about 3.5 wt. % halogen, wherein the platinum group metal, cobalt and tin are uniformly dispersed throughout the porous carrier material, wherein the average crystallite size of the cobalt and tin is less than 100 Angstroms in maximum dimension, wherein substantially all of the platinum group metal is present in the elemental metallic state, wherein substantially all of the tin is present in an oxidation state above that of the elemental metal, and wherein substantially all of the cobalt is present in the elemental metallic state or in a state which is reducible to the elemental metallic state under reforming conditions.
Claim 3
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is platinum.
Claim 4
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is iridium.
Claim 5
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is rhodium.
Claim 6
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is palladium.
Claim 7
Dependent Claim 17 words
A process as defined in claim 1 wherein the porous carrier material is a refractory inorganic oxide.
Claim 8
Dependent Claim 14 words
A process as defined in claim 6 wherein the refractory inorganic oxide is alumina.
Claim 9
Dependent Claim 13 words
A process as defined in claim 1 wherein the halogen is combined chloride.
Claim 10
Dependent Claim 27 words
A process as defined in claim 1 wherein the atomic ratio of tin to platinum group metal contained in the composite is about 0.1:1 to about 13:1.
Claim 11
Dependent Claim 27 words
A process as defined in claim 1 wherein the atomic ratio of cobalt to platinum group metal contained in the composite is about 0.8:1 to about 66:1.
Claim 12
Dependent Claim 24 words
A process as defined in claim 1 wherein substantially all of the cobalt contained in the composite is present in the elemental metallic state.
Claim 13
Dependent Claim 22 words
A process as defined in claim 1 wherein substantially all of the tin is present in the catalytic composite as tin oxide.
Claim 14
Dependent Claim 44 words
A process as defined in claim 1 wherein the composite contains about 0.05 to about 1 wt. % platinum, about 0.5 to about 2 wt. % cobalt, about 0.05 to about 1 wt. % tin and about 0.5 to about 1.5 wt. % halogen.
Claim 15
Dependent Claim 25 words
A process as defined in claim 1 wherein the contacting of the gasoline fraction with the catalytic composite is performed in the presence of hydrogen.
Claim 16
Dependent Claim 57 words
A process as defined in claim 14 wherein the reforming conditions include a temperature of about 800° to about 1100°F., a pressure of about 0 to about 1000 psig., a liquid hourly space velocity of about 0.1 to about 10 hr. - 1 and a mole ratio of hydrogen to hydrocarbon of about 1:1 to about 20:1.
Claim 17
Dependent Claim 17 words
A process as defined in claim 14 wherein the contacting is performed in a substantially water-free environment.
Claim 18
Dependent Claim 21 words
A process as defined in claim 14 wherein the reforming conditions include a pressure of about 100 to about 450 psig.
Claim 19
Dependent Claim 17 words
A process as defined in claim 14 wherein the contacting is performed in a substantially sulfur-free environment.

References Cited (Backward Citations)

US2911357A Cited
US3576766A Cited
US3830727A Cited
US3644198A Cited
US3844938A Cited
US3847794A Cited
US3775300A Cited
US3881696A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-01 1979-12-01 1980-06-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-01 1983-12-01 1984-06-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-01 1987-12-01 1988-06-01 $7700.00 Window Closed / Lapsed

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