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US4152247A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon conversion with an activated multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1978-01-09
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Granted: 1979-05-01
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Expires: 1998-01-09
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Abstract

Abstract Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with a novel activated multimetallic catalytic composite comprising a combination of a catalytically effective amount of a pyrolyzed rhodium carbonyl component with a porous carrier material containing a uniform dispersion of a catalytically effective amount of a platinum group component which is maintained in the elemental metallic state. In a highly preferred embodiment, this novel catalytic composite also contains a catalytically effective amount of a halogen component. The platinum group component, pyrolyzed rhodium carbonyl component and optional halogen component are preferably present in the multimetallic catalytic composite in amounts, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % of the uniformly dispersed platinum group metal, about 0.01 to about 2 wt. % of carbonyl-derived rhodium and about 0.1 to about 3.5 wt. % of halogen. A key feature associated with the preparation of the subject catalytic composite is reaction of a rhodium carbonyl complex with a porous carrier material containing a uniform dispersion of a platinum group metal maintained in the elemental state, whereby the interaction of the rhodium moiety with the platinum group moiety is maximized due to the platinophilic (i.e. platinum-seeking) propensities of the carbon monoxide ligand used in the rhodium reagent. A specific example of the type of hydrocarbon conversion process disclosed herein 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 subject activated multimetallic catalytic composite at reforming conditions.

Inventors

  • 👤 George J. Antos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 08:39
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/40; B01J23/46; B01J23/464; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09

Claims Analysis

Total Claims: 21
Claim 1
Independent Claim 54 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion conditions with a catalytic composite comprising the pyrolyzed reaction product of a rhodium carbonyl component with a porous carrier material containing a uniform dispersion of a catalytically effective amount of a platinum group component maintained in the elemental metallic state.
Claim 2
Dependent Claim 54 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion conditions with a catalytic composite comprising the pyrolyzed reaction product of a rhodium carbonyl component with a porous carrier material containing a uniform dispersion of a catalytically effective amount of a platinum group component maintained in the elemental metallic state.
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 palladium.
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 iridium.
Claim 7
Dependent Claim 14 words
A process as defined in claim 1 wherein the platinum group component is ruthenium.
Claim 8
Dependent Claim 21 words
A process as defined in claim 1 wherein the porous carrier material contains a catalytically effective amount of a halogen component.
Claim 9
Dependent Claim 14 words
A process as defined in claim 7 wherein the halogen component is combined chloride.
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 52 words
A process as defined in claim 1 wherein the composite contains the components in amounts, calculated on an elemental metallic basis, corresponding to about 0.01 to about 2 wt. % of the uniformly dispersed platinum group metal and about 0.01 to about 2 wt. % rhodium, derived from said rhodium carbonyl component.
Claim 13
Dependent Claim 36 words
A process as defined in claim 7 wherein the halogen component is present therein in an amount sufficient to result in the composite containing, on an elemental basis, about 0.1 to about 3.5 wt. % halogen.
Claim 14
Dependent Claim 60 words
A process as defined in claim 1 wherein the composite is prepared by the steps of: (a) reacting a rhodium carbonyl compound with a porous carrier material containing a uniform dispersion of a platinum group component maintained in the elemental metallic state, and thereafter, (b) subjecting the resulting reaction product to pyrolysis conditions selected to decompose the rhodium carbonyl component.
Claim 15
Dependent Claim 24 words
A process as defined in claim 13 wherein the pyrolysis step is conducted under anhydrous conditions and in the substantial absence of free oxygen.
Claim 16
Dependent Claim 21 words
A process as defined in claim 1 wherein the porous carrier material contains a catalytically effective amount of a halogen component.
Claim 17
Dependent Claim 14 words
A process as defined in claim 15 wherein the halogen component is combined chloride.
Claim 18
Dependent Claim 28 words
A process for converting a hydrocarbon as defined in claim 1 wherein the contacting of the hydrocarbon with the catalytic composite is performed in the presence of hydrogen.
Claim 19
Dependent Claim 22 words
A process as defined in claim 1 wherein a gasoline fraction and hydrogen are contacted with said catalytic composite at reforming conditions.
Claim 20
Dependent Claim 57 words
A process as defined in claim 18 wherein the reforming conditions include a temperature of about 700° 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 hrs. -1 and a mole ratio of hydrogen to hydrocarbon of about 1:1 to about 20:1.
Claim 21
Dependent Claim 22 words
A process as defined in claim 18 wherein the reforming conditions utilized include a pressure of about 50 to about 350 psig.

References Cited (Backward Citations)

US4041092A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-04-30 1982-10-30 1983-05-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-04-30 1986-10-30 1987-05-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-04-30 1990-10-30 1991-05-01 $7700.00 Window Closed / Lapsed

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