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US4295959A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon dehydrocyclization with an attentuated superactive multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1980-10-20
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Granted: 1981-10-20
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Expires: 2000-10-20
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Abstract

Abstract Dehydrocyclizable hydrocarbons are converted to aromatics by contacting them at hydrocarbon dehydrocyclization conditions with an attenuated superactive acidic multimetallic catalytic composite comprising a combination of a catalytically effective amount of a pyrolyzed rhenium carbonyl component with a porous carrier material containing catalytically effective amounts of a halogen component, a silver component and a uniform dispersion a catalytically effective amount of a platinum group component which is maintained in the elemental metallic state. The platinum group, pyrolyzed rhenium carbonyl, silver 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 0.01 to about 5 wt. % rhenium, about 0.01 to about 5 wt. % silver and about 0.1 to about 3.5 wt. % halogen. A specific example of a dehydrocyclization method disclosed herein is a method for converting a feed mixture of n-hexane and n-heptane to a product mixture of benzene and toluene which involves contacting the feed mixture and a hydrogen stream with the attenuated superactive acidic multimetallic catalyst disclosed herein at hydrocarbon dehydrocyclization conditions.

Inventors

  • 👤 George J. Antos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 03:42
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/66; B01J23/68; B01J23/688; C; C07; C07C; C07C5/00; C07C5/32; C07C5/373; C07C5/393; C07C5/41; C07C5/415; C07C5/417; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 26
Claim 1
Independent Claim 70 words
A method for dehydrocyclizing a dehydrocyclizable hydrocarbon comprising contacting the hydrocarbon at hydrocarbon dehydrocyclization conditions with an acidic catalytic composite comprising a combination of a catalytically effective amount of a pyrolyzed rhenium carbonyl component with a porous carrier material containing catalytically effective amounts of a halogen component, a silver component and a uniform dispersion of a catalytically effective amount of a platinum group component maintained in the elemental metallic state.
Claim 2
Independent Claim 70 words
A method for dehydrocyclizing a dehydrocyclizable hydrocarbon comprising contacting the hydrocarbon at hydrocarbon dehydrocyclization conditions with an acidic catalytic composite comprising a combination of a catalytically effective amount of a pyrolyzed rhenium carbonyl component with a porous carrier material containing catalytically effective amounts of a halogen component, a silver component and a uniform dispersion of a catalytically effective amount of a platinum group component maintained in the elemental metallic state.
Claim 3
Dependent Claim 21 words
A method as defined in claim 1 wherein the dehydrocyclizable hydrocarbon is admixed with hydrogen when it contacts the catalytic composite.
Claim 4
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group component is platinum.
Claim 5
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group component is iridium.
Claim 6
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group component is palladium.
Claim 7
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group component is rhodium.
Claim 8
Dependent Claim 17 words
A method as defined in claim 1 wherein the porous carrier material is a refractory inorganic oxide.
Claim 9
Dependent Claim 14 words
A method as defined in claim 7 wherein the refractory inorganic oxide is alumina.
Claim 10
Dependent Claim 12 words
A method as defined in claim 1 wherein the halogen is chlorine.
Claim 11
Dependent Claim 59 words
A method as defined in claim 1 wherein the acidic catalytic composite contains the components in amounts, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % rhenium, about 0.01 to about 5 wt. % silver and about 0.01 to about 3.5 wt. % halogen.
Claim 12
Dependent Claim 21 words
A method as defined in claim 1 wherein substantially all of the silver component is present in the elemental metallic state.
Claim 13
Dependent Claim 49 words
A method as defined in claim 1 wherein the metals contents of the composite are adjusted so that the atomic ratio of silver to platinum group metal is about 0.01:1 to about 10:1 and the atomic ratio of rhenium to platinum group metal is about 0.1:1 to about 10:1.
Claim 14
Dependent Claim 22 words
A method as defined in claim 1 wherein the dehydrocyclizable hydrocarbon is an aliphatic hydrocarbon containing 6 to 20 atoms per molecule.
Claim 15
Dependent Claim 14 words
A method as defined in claim 13 wherein the aliphatic hydrocarbon is an olefin.
Claim 16
Dependent Claim 14 words
A method as defined in claim 13 wherein the aliphatic hydrocarbon is a paraffin.
Claim 17
Dependent Claim 22 words
A method as defined in claim 15 wherein the paraffin hydrocarbon is a paraffin containing 6 to 10 carbon atoms per molecule.
Claim 18
Dependent Claim 12 words
A method as defined in claim 15 wherein the paraffin is hexane.
Claim 19
Dependent Claim 12 words
A method as defined in claim 15 wherein the paraffin is heptane.
Claim 20
Dependent Claim 12 words
A method as defined in claim 15 wherein the paraffin is octane.
Claim 21
Dependent Claim 12 words
A method as defined in claim 15 wherein the paraffin is nonane.
Claim 22
Dependent Claim 20 words
A method as defined in claim 15 wherein the paraffin is a mixture of C 6 to C 9 paraffins.
Claim 23
Dependent Claim 29 words
A method as defined in claim 1 wherein the dehydrocyclizable hydrocarbon is contained in a naphtha fraction boiling in the range of about 140° F. to about 400° F.
Claim 24
Dependent Claim 54 words
A method as defined in claim 2 wherein the dehydrocyclization conditions include a temperature of about 800° to about 1100° F., a pressure of about 0 to about 250 psig., a LSHV of about 0.1 to about 5 hr. -1 , and a hydrogen to hydrocarbon mole ratio of about 0.1:1 to about 10:1.
Claim 25
Dependent Claim 52 words
A method as defined in claim 1 wherein the acidic catalytic composite contains, on an elemental basis, about 0.05 to about 1 wt. % platinum group metal, about 0.05 to about 1 wt. % rhenium, about 0.01 to about 1 wt. % silver and about 0.5 to about 1.5 wt. % halogen.
Claim 26
Dependent Claim 17 words
A method as defined in claim 1 wherein the contacting is performed in a substantially water-free environment.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-10-19 1985-04-20 1985-10-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-10-19 1989-04-20 1989-10-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-10-19 1993-04-20 1993-10-20 $7700.00 Window Closed / Lapsed

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