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US3928177A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon conversion with a multimetallic catalytic composite

Assignee: Universal Oil Products Co
•
Filing: 1974-02-14
•
Granted: 1975-12-23
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Expires: 1994-02-14
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Abstract

Abstract Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with a trimetallic acidic catalytic composite comprising a combination of catalytically effective amounts of a platinum group component, a Group IVA metallic component, a Group VIB transition metal component and a halogen component with a porous carrier material. The platinum group component, Group IVA metallic component, and halogen component are present in the trimetallic 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. % Group IVA metal and about 0.1 to about 3.5 wt. % halogen. The Group VIB component is present in an amount of about 0.01 to about 3 wt. % and the atomic ratio of Group VIB metal to platinum group metal is about 0.05:1 to about 4:1. 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 while substantially all of the Group IVA metallic component and of the Group VIB component are present therein in oxidation states above that of the corresponding 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 hydrogen stream are contacted with the novel trimetallic catalyst disclosed herein at reforming conditions.

Inventors

  • 👤 John C Hayes

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 21:22
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/22; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/64; B01J23/652; B01J23/6527; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; C07; C07C; C07C2523/00; C07C2523/02; C07C2523/04; C07C2523/14; C07C2523/16; C07C2523/24; C07C2523/30; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/54; C07C2523/56; C07C2523/64; C07C2523/652

Claims Analysis

Total Claims: 25
Claim 1
Independent Claim 170 words
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
Claim 2
Dependent Claim 170 words
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
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 palladium.
Claim 5
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group metal is iridium.
Claim 6
Dependent Claim 14 words
A process as defined in claim 1 wherein the halogen component is combined chloride.
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 Group IVA metal is germanium.
Claim 10
Dependent Claim 14 words
A process as defined in claim 1 wherein the Group IVA metal is tin.
Claim 11
Dependent Claim 15 words
A process as defined in claim 1 wherein the Group VIB transition metal is tungsten.
Claim 12
Dependent Claim 15 words
A process as defined in claim 1 wherein the Group VIB transition metal is molybdenum.
Claim 13
Dependent Claim 15 words
A process as defined in claim 1 wherein the Group VIB transition metal is chromium.
Claim 14
Dependent Claim 24 words
A process as defined in claim 1 wherein the Group IVA metal to platinum group metal atomic ratio is about 0.05:1 to about 10:
Claim 15
Dependent Claim 25 words
A process as defined in claim 1 wherein the catalytic composite contains about 0.05 to about 0.5 wt. % sulfur, calculated on an elemental basis.
Claim 16
Dependent Claim 28 words
A process as defined in claim 1 wherein substantially all of the Group IVA metal is present in the catalytic composite as the corresponding Group IVA metal oxide.
Claim 17
Dependent Claim 29 words
A process as defined in claim 1 wherein substantially all of the Group VIB transition metal is present in the catalytic composite as the corresponding Group VIB metal oxide.
Claim 18
Dependent Claim 52 words
A process as defined in claim 1 wherein the catalytic composite contains about 0.05 to about 1 wt. % platinum group metal, about 0.05 to about 2 wt. % Group IVA metal, about 0.05 to about 1 wt. % Group VIB transition metal and about 0.5 to about 1.5 wt. % halogen.
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 53 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 56 words
A process as defined in claim 19 wherein the reforming conditions include a temperature of about 800* to 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 50 to about 350 psig.
Claim 24
Dependent Claim 167 words
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
Claim 25
Dependent Claim 167 words
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

References Cited (Backward Citations)

US3827973A Cited
US3827988A Cited
US3827971A Cited
US3827972A Cited
US3781221A Cited
US3806446A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-12-22 1979-06-23 1979-12-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-12-22 1983-06-23 1983-12-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-12-22 1987-06-23 1987-12-23 $7700.00 Window Closed / Lapsed

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