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US4148715A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon conversion with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1978-03-13
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Granted: 1979-04-10
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Expires: 1998-03-13
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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 nickel component, and a halogen component with a porous carrier material. The platinum group, lanthanide series, nickel, and halogen components are present in the multimetallic catalyst in amounts respctively, 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 metal, 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 metal 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 lanthanide series component is present in an oxidation state above that of the elemental metal. A specific example of the type of hydrocarbn 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 multimetllic catalyst disclosed herein at reforming conditions.

Inventors

  • 👤 George J. Antos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 11:32
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/89; B01J23/8933; B01J23/8966; B01J23/894; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09

Claims Analysis

Total Claims: 25
Claim 1
Independent Claim 152 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 0.01 to about 5 wt.% lanthanide series metal, and about 0.1 to about 3.5 wt.% halogen; wherein the platinum group metal, catalytically available nickel, and lanthanide series metal are uniformly dispersed throughout the porous carrier material; wherein substantially all of the lanthanide series metal is present in a positive oxidation state; wherein substantially all of the platinum group metal is present in the elemental metallic state; and wherein substantially all of the catalytically available nickel 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 152 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 0.01 to about 5 wt.% lanthanide series metal, and about 0.1 to about 3.5 wt.% halogen; wherein the platinum group metal, catalytically available nickel, and lanthanide series metal are uniformly dispersed throughout the porous carrier material; wherein substantially all of the lanthanide series metal is present in a positive oxidation state; wherein substantially all of the platinum group metal is present in the elemental metallic state; and wherein substantially all of the catalytically available nickel 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 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 14 words
A process as defined in claim 1 wherein the lanthanide series component is neodymium.
Claim 11
Dependent Claim 14 words
A process as defined in claim 1 wherein the lanthanide series component is cerium.
Claim 12
Dependent Claim 14 words
A process as defined in claim 1 wherein the lanthanide series component is lanthanum.
Claim 13
Dependent Claim 29 words
A process as defined in claim 1 wherein the atomic ratio of lanthanide series metal to platinum group metal contained in the composite is about 0.1:1 to about 20:1.
Claim 14
Dependent Claim 27 words
A process as defined in claim 1 wherein the atomic ratio of nickel to platinum group metal contained in the composite is about 0.1:1 to about 66:1.
Claim 15
Dependent Claim 37 words
A process as defined in claim 1 wherein substantially all of the catalytically available nickel 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 16
Dependent Claim 27 words
A process as defined in claim 1 wherein substantially all of the lanthanide series metal is present in the composite in the form of the corresponding oxide.
Claim 17
Dependent Claim 46 words
A process as defined in claim 1 wherein the composite contains, on an elemental basis, about 0.05 to about 1 wt.% platinum, about 0.1 to about 2.5 wt.% nickel, about 0.05 to about 2 wt.% lanthanide series metal, and about 0.5 to about 1.5 wt.% halogen.
Claim 18
Dependent Claim 16 words
A process as defined in claim 1 wherein the catalytic composite is in a sulfur-free state.
Claim 19
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 20
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 21
Dependent Claim 58 words
A process as defined in claim 19 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 22
Dependent Claim 17 words
A process as defined in claim 19 wherein the contacting is performed in a substantially water-free environment.
Claim 23
Dependent Claim 21 words
A process as defined in claim 19 wherein the reforming conditions include a pressure of about 100 to about 450 psig.
Claim 24
Dependent Claim 17 words
A process as defined in claim 19 wherein the contacting is performed in a substantially sulfur-free environment.
Claim 25
Dependent Claim 54 words
A process as defined in claim 16 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.

References Cited (Backward Citations)

US3436335A Cited
US4024052A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-04-09 1982-10-09 1983-04-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-04-09 1986-10-09 1987-04-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-04-09 1990-10-09 1991-04-10 $7700.00 Window Closed / Lapsed

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