← Back to Patent Explorer
US3909394A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalytic reforming with a catalyst containing platinum or palladium and ruthenium

Assignee: Universal Oil Products Co
•
Filing: 1974-01-18
•
Granted: 1975-09-30
•
Expires: 1994-01-18
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with a bimetallic acidic catalyst comprising a combination of catalytically effective amounts of a platinum or palladium component, a ruthenium component and a halogen component with a porous carrier material. The components are present in the bimetallic catalyst in amounts, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum or palladium, about 0.01 to about 2 wt. % ruthenium and about 0.1 to about 3.5 wt. % halogen. Moreover, the platinum or palladium component and the ruthenium component are uniformly dispersed throughout the porous carrier material and substantially all of the platinum or palladium component and the ruthenium component are present in the corresponding elemental metallic states while substantially all of the halogen component is present in the form of the combined halide. A specific example of the hydrocarbon conversion process disclosed is a process for reforming a gasoline fraction wherein the gasoline fraction and hydrogen are contacted with the disclosed bimetallic catalyst at reforming conditions. Also disclosed in a trimetallic catalyst comprising a combination of a Group IVA metallic component with the bimetallic catalyst.

Inventors

  • 👤 John C Hayes

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 03:52
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; B; B01; B01J; B01J23/00; B01J23/38; B01J23/40; B01J23/46; B01J23/462; B01J23/54; B01J23/56; B01J23/62; B01J23/622; B01J27/00; B01J27/06; B01J27/08

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 125 words
A PROCESS FOR CATALYTIC REFORMING OF A GASOLINE FRACTION TO PRODUCE A HIGH-OCTANE REFOMATE WHICH COMPRISING CONTACTING THE GASOLINE FRACTION IN THE PRESENCE OF HYDROGEN AT REFORMING CONDITIONS WITH A CATALYTIC COMPOSITE COMPRISING A POROUS CARRIER MATERIAL CONTAINING, ON AN ELEMENTAL BASIS, ABOUT 0.01 TO ABOUT 2 WT. % PLATINUM OR PALLADIUM METAL, ABOUT 0.01 TO ABOUT 2 WT. % RUTHENIUM META, AND ABOUT 0.1 O ABOUT 3.5 WT % HALOGEN, WHEREIN THE PLATINUM OR PALLADIUM METAL AND THE RUTHENIUM METAL ARE UNIFORMLY DISPERSED THROUGHOUT THE POROUS CARRIER MATERIAL WHEREIN SUBSTANTIALLY ALL OF THE PLATINUM OR PALLADIUM METAL AND THE RUTHENIUM METAL ARE PRESENT IN THE CORRESPONDING ELEMENTAL METALLIC STATES, AND WHEREIN SUBSTANTIALLY ALL OF THE HALOGEN IS PRESENT IN THE FORM OF COMBINED HALIDE.
Claim 2
Dependent Claim 125 words
A PROCESS FOR CATALYTIC REFORMING OF A GASOLINE FRACTION TO PRODUCE A HIGH-OCTANE REFOMATE WHICH COMPRISING CONTACTING THE GASOLINE FRACTION IN THE PRESENCE OF HYDROGEN AT REFORMING CONDITIONS WITH A CATALYTIC COMPOSITE COMPRISING A POROUS CARRIER MATERIAL CONTAINING, ON AN ELEMENTAL BASIS, ABOUT 0.01 TO ABOUT 2 WT. % PLATINUM OR PALLADIUM METAL, ABOUT 0.01 TO ABOUT 2 WT. % RUTHENIUM META, AND ABOUT 0.1 O ABOUT 3.5 WT % HALOGEN, WHEREIN THE PLATINUM OR PALLADIUM METAL AND THE RUTHENIUM METAL ARE UNIFORMLY DISPERSED THROUGHOUT THE POROUS CARRIER MATERIAL WHEREIN SUBSTANTIALLY ALL OF THE PLATINUM OR PALLADIUM METAL AND THE RUTHENIUM METAL ARE PRESENT IN THE CORRESPONDING ELEMENTAL METALLIC STATES, AND WHEREIN SUBSTANTIALLY ALL OF THE HALOGEN IS PRESENT IN THE FORM OF COMBINED HALIDE.
Claim 3
Dependent Claim 17 words
A process as defined in claim 1 wherein the porous carrier material is a refractory inorganic oxide.
Claim 4
Dependent Claim 14 words
A process as defined in claim 2 wherein the refractory inorganic oxide is alumina.
Claim 5
Dependent Claim 13 words
A process as defined in claim 1 wherein the halogen is combined chloride.
Claim 6
Dependent Claim 13 words
A process as defined in claim 1 wherein the halogen is combined fluoride.
Claim 7
Dependent Claim 42 words
A process as defined in claim 1 wherein the composite contains, on an elemental basis, about 0.05 to about 1 wt. % platinum or palladium, about 0.05 to about 1 wt. % ruthenium and about 0.5 to about 1.5 wt. % halogen.
Claim 8
Dependent Claim 29 words
A process as defined in claim 1 wherein the atomic ratio of ruthenium metal to platinum or palladium metal contained in the composite is about 0.1:1 to about 10:1.
Claim 9
Dependent Claim 29 words
A process as defined in claim 1 wherein the catalytic composite contains sulfur in an amount of about 0.05 to about 0.5 wt. %, calculated on an elemental basis.
Claim 10
Dependent Claim 57 words
A process as defined in claim 1 wherein the catalytic composite contains a Group IVA metallic component in an amount of about 0.01 to about 5 wt. % thereof, calculated on an elemental basis and wherein substantially all of the Group IVA metallic component is present therein in an oxidation state above that of the elemental metal.
Claim 11
Dependent Claim 15 words
A process as defined in claim 9 wherein the Group IVA metallic component is germanium.
Claim 12
Dependent Claim 15 words
A process as defined in claim 9 wherein the Group IVA metallic component is tin.
Claim 13
Dependent Claim 15 words
A process as defined in claim 9 wherein the Group IVA metallic component is lead.
Claim 14
Dependent Claim 29 words
A process as defined in claim 1 wherein the atomic ratio of ruthenium metal to platinum or palladium metal contained in the composite is about 0.25:1 to about 3:1.
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 55 words
A process as defined in claim 1 wherein the reforming conditions include a temperature of about 800* to about 1100*F., a presssure of about 0 to about 1,000 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 1 wherein the contacting is performed in a substantially water-free environment.
Claim 18
Dependent Claim 21 words
A process as defined in claim 1 wherein the reforming conditions include a pressure of about 50 to about 350 psig.

References Cited (Backward Citations)

US3173857A Cited
US3617519A Cited
US3702294A Cited
US3759841A Cited
US3775301A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-09-29 1979-03-31 1979-09-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-09-29 1983-03-31 1983-09-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-09-29 1987-03-31 1987-09-30 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag