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US4179360A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon conversion with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1978-07-27
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Granted: 1979-12-18
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Expires: 1998-07-27
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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 nickel component, a uranium component, and a halogen component with a porous carrier material. The platinum group, uranium, nickel, and halogen components 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 0.1 to about 10 wt. % uranium, about 0.05 to about 5 wt. % nickel, 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 component is present therein in the elemental metallic state, substantially all of the catalytically available nickel 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 uranium component is present 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

  • 👤 John F. Flagg
  • 👤 George J. Antos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 18:19
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 153 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion 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 0.05 to about 5 wt.% nickel, about 0.1 to about 10 wt.% uranium, and about 0.1 to about 3.5 wt.% halogen; wherein the platinum group, catalytically available nickel, and uranium components are uniformly dispersed throughout the porous carrier material; wherein substantially all of the platinum group component is present in the elemental metallic state; wherein substantially all of the uranium component is present in an oxidation state above that of the elemental metal; and wherein substantially all of the catalytically available nickel 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.
Claim 2
Dependent Claim 153 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion 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 0.05 to about 5 wt.% nickel, about 0.1 to about 10 wt.% uranium, and about 0.1 to about 3.5 wt.% halogen; wherein the platinum group, catalytically available nickel, and uranium components are uniformly dispersed throughout the porous carrier material; wherein substantially all of the platinum group component is present in the elemental metallic state; wherein substantially all of the uranium component is present in an oxidation state above that of the elemental metal; and wherein substantially all of the catalytically available nickel 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.
Claim 3
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group component is platinum.
Claim 4
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group component is iridium.
Claim 5
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group component is rhodium.
Claim 6
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group component 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 14 words
A process as defined in claim 1 wherein the halogen component is combined chloride.
Claim 10
Dependent Claim 48 words
A process as defined in claim 1 wherein the atomic ratio of uranium to platinum group metal contained in the composite is about 0.1:1 to about 80:1 and wherein the atomic ratio of nickel to platinum group metal contained in the composite is about 0.1:1 to about 66:1.
Claim 11
Dependent Claim 38 words
A process as defined in claim 1 wherein substantially all of the catalytically available nickel component 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 12
Dependent Claim 35 words
A process as defined in claim 1 wherein substantially all of the uranium component is present in the catalytic composite in the form of uranium oxide or uranium oxyhalide or uranium aluminate or mixtures thereof.
Claim 13
Dependent Claim 44 words
A process as defined in claim 1 wherein the composite contains about 0.05 to about 1 wt.% platinum group metal, about 0.1 to about 2.5 wt.% nickel, about 0.25 to about 5 wt. % uranium, and about 0.5 to about 1.5 wt. % halogen.
Claim 14
Dependent Claim 17 words
A process as defined in claim 1 wherein the catalytic composite is in substantially a sulfur-free state.
Claim 15
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.
Claim 16
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 17
Dependent Claim 58 words
A process as defined in claim 15 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 18
Dependent Claim 17 words
A process as defined in claim 15 wherein the contacting is performed in a substantially water-free environment.
Claim 19
Dependent Claim 21 words
A process as defined in claim 15 wherein the reforming conditions include a pressure of about 100 to about 450 psig.
Claim 20
Dependent Claim 17 words
A process as defined in claim 15 wherein the contacting is performed in a substantially sulfur-free environment.

References Cited (Backward Citations)

US3929624A Cited
US3788977A Cited
US3846282A Cited
US3939060A Cited
US3956107A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-12-17 1983-06-18 1983-12-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-12-17 1987-06-18 1987-12-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-12-17 1991-06-18 1991-12-18 $7700.00 Window Closed / Lapsed

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