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US4024052A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon conversion with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1975-11-20
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Granted: 1977-05-17
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Expires: 1995-11-20
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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 lanthanide series component, a cobalt component, and a halogen component with a porous carrier material. The platinum group component, lanthanide series 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. % lanthanide series component, about 0.05 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 catalytically available 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, or in a mixture of these states, while substantially all of the lanthanide series component 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

  • 👤 George J. Antos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 19:36
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/89; B01J23/8933; B01J23/894

Claims Analysis

Total Claims: 25
Claim 1
Independent Claim 163 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion conditions with an acidic catalytic composite consisting essentially of a porous carrier material containing, on an elemental basis, about 0.01 to about 2 wt. % platinum group metal, about 0.05 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % lanthanide series component, and about 0.1 to about 3.5 wt. % halogen, wherein the platinum group metal, catalytically available cobalt, and lanthanide series component are uniformly dispersed throughout the porous carrier material, wherein substantially all of the platinum group metal is present in the elemental metallic state, wherein substantially all of the lanthanide series component is present in an oxidation state above that of the elemental metal, and wherein substantially all of the catalytically available cobalt is present in the elemental metallic state or in a state which is reducible to the elemental metallic state under hydrocarbon conversion conditions or in a mixture of these states.
Claim 2
Dependent Claim 163 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion conditions with an acidic catalytic composite consisting essentially of a porous carrier material containing, on an elemental basis, about 0.01 to about 2 wt. % platinum group metal, about 0.05 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % lanthanide series component, and about 0.1 to about 3.5 wt. % halogen, wherein the platinum group metal, catalytically available cobalt, and lanthanide series component are uniformly dispersed throughout the porous carrier material, wherein substantially all of the platinum group metal is present in the elemental metallic state, wherein substantially all of the lanthanide series component is present in an oxidation state above that of the elemental metal, and wherein substantially all of the catalytically available cobalt is present in the elemental metallic state or in a state which is reducible to the elemental metallic state under hydrocarbon conversion conditions or in a mixture of these states.
Claim 3
Dependent Claim 54 words
A process as defined in claim 1 wherein the type of hydrocarbon conversion is catalytic reforming of a gasoline fraction to produce a high octane reformate, wherein the hydrocarbon is contained in the gasoline fraction, wherein the contacting is performed in the presence of hydrogen, and wherein the hydrocarbon conversion conditions are reforming conditions.
Claim 4
Dependent Claim 58 words
A process as defined in claim 2 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 5
Dependent Claim 17 words
A process as defined in claim 2 wherein the contacting is performed in a substantially water-free environment.
Claim 6
Dependent Claim 21 words
A process as defined in claim 2 wherein the reforming conditions include a pressure of about 100 to about 450 psig.
Claim 7
Dependent Claim 46 words
A process as defined in claim 1 wherein the composite contains about 0.05 to about 1 wt. % platinum, about 0.1 to about 2.5 wt. % cobalt, about 0.05 to about 2 wt. % lanthanide series component, and about 0.5 to about 1.5 wt. % halogen.
Claim 8
Dependent Claim 17 words
A process as defined in claim 6 wherein the contacting is performed in a substantially sulfur-free environment.
Claim 9
Dependent Claim 54 words
A process as defined in claim 6 wherein the type of hydrocarbon conversion is catalytic reforming of a gasoline fraction to produce a high octane reformate, wherein the hydrocarbon is contained in the gasoline fraction, wherein the contacting is performed in the presence of hydrogen, and wherein the hydrocarbon conversion conditions are reforming conditions.
Claim 10
Dependent Claim 17 words
A process as defined in claim 1 wherein the porous carrier material is a refractory inorganic oxide.
Claim 11
Dependent Claim 14 words
A process as defined in claim 9 wherein the refractory inorganic oxide is alumina.
Claim 12
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is platinum.
Claim 13
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is iridium.
Claim 14
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is rhodium.
Claim 15
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is palladium.
Claim 16
Dependent Claim 14 words
A process as defined in claim 1 wherein the lanthanide series component is neodymium.
Claim 17
Dependent Claim 14 words
A process as defined in claim 1 wherein the lanthanide series component is cerium.
Claim 18
Dependent Claim 14 words
A process as defined in claim 1 wherein the lanthanide series component is lanthanum.
Claim 19
Dependent Claim 13 words
A process as defined in claim 1 wherein the halogen is combined chloride.
Claim 20
Dependent Claim 29 words
A process as defined in claim 1 wherein the atomic ratio of lanthanide series component to platinum group metal contained in the composite is about 0.1:1 to about 20:1.
Claim 21
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 0.1:1 to about 66:1.
Claim 22
Dependent Claim 37 words
A process as defined in claim 1 wherein substantially all of the catalytically available cobalt contained in the composite is present in the elemental metallic state after the process is started-up and lined-out at hydrocarbon conversion conditions.
Claim 23
Dependent Claim 24 words
A process as defined in claim 1 wherein substantially all of the lanthanide series component is present in the catalytic composite as the oxide.
Claim 24
Dependent Claim 16 words
A process as defined in claim 1 wherein the catalytic composite is in a sulfur-free state.
Claim 25
Dependent Claim 24 words
A process as defined in claim 1 wherein the contacting of the hydrocarbon with the catalytic composite is performed in the presence of hydrogen.

References Cited (Backward Citations)

US2906701A Cited
US3544452A Cited
US3770616A Cited
US3780126A Cited
US3871995A Cited
US3915845A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-05-16 1980-11-15 1981-05-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-05-16 1984-11-15 1985-05-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-05-16 1988-11-15 1989-05-17 $7700.00 Window Closed / Lapsed

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