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US4041092A Expired / Lapsed US ⏱️ 0.0 years remaining

Dehydrocyclization with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1976-04-23
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Granted: 1977-08-09
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Expires: 1996-04-23
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Abstract

Abstract Dehydrocyclizable hydrocarbons are converted to aromatics by contacting them at dehydrocyclization conditions with an acidic multimetallic catalytic composite comprising a combination of catalytically effective amounts of a platinum or palladium component, a rhodium component, a rhenium component, and a halogen component with a porous carrier material. The platinum or palladium, rhodium, rhenium 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 or palladium metal, about 0.01 to about 2 wt. % rhodium, about 0.01 to about 2 wt. % rhenium, and about 0.1 to about 3.5 wt. % halogen. Moreover, the catalytically active sites induced by these metallic components are uniformly dispersed throughout the porous carrier material and these metallic components are present in the catalyst in carefully controlled oxidation states such that substantially all of the platinum or palladium component is in the elemental metallic state and substantially all of the rhenium and rhodium components are in the elemental metallic state or in a state which is reducible to the elemental metallic state under dehydrocyclization conditions or in a mixture of these states. A specific example of 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 acidic multimetallic catalyst disclosed herein at dehydrocyclization conditions.

Inventors

  • 👤 George J. Antos

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 07:16
CPC Classifications
C; C07; C07C; C07C5/00; C07C5/32; C07C5/373; C07C5/393; C07C5/41; C07C5/415; C07C5/417; B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/64; B01J23/656; B01J23/6567; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 22
Claim 1
Independent Claim 133 words
A method for dehydrocyclizing a dehydrocyclizable hydrocarbon comprising contacting the hydrocarbon at dehydrocyclization conditions with an acidic catalytic composite comprising a porous carrier material containing, on an elemental basis, about 0.01 to about 2 wt. % platinum or palladium, about 0.01 to about 2 wt. % rhodium, about 0.01 to about 2 wt. % rhenium and about 0.1 to about 3.5 wt. % halogen; wherein the platinum or palladium, rhodium and rhenium are uniformly dispersed throughout the porous carrier material; wherein substantially all of the platinum or palladium is present in the elemental metallic state; and wherein substantially all of the rhenium and rhodium are present in the elemental metallic state or in a state which is reducible to the elemental metallic state under dehydrocyclization conditions or in a mixture of these states.
Claim 2
Independent Claim 133 words
A method for dehydrocyclizing a dehydrocyclizable hydrocarbon comprising contacting the hydrocarbon at dehydrocyclization conditions with an acidic catalytic composite comprising a porous carrier material containing, on an elemental basis, about 0.01 to about 2 wt. % platinum or palladium, about 0.01 to about 2 wt. % rhodium, about 0.01 to about 2 wt. % rhenium and about 0.1 to about 3.5 wt. % halogen; wherein the platinum or palladium, rhodium and rhenium are uniformly dispersed throughout the porous carrier material; wherein substantially all of the platinum or palladium is present in the elemental metallic state; and wherein substantially all of the rhenium and rhodium are present in the elemental metallic state or in a state which is reducible to the elemental metallic state under dehydrocyclization conditions or in a mixture of these states.
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 17 words
A method as defined in claim 1 wherein the porous carrier material is a refractory inorganic oxide.
Claim 5
Dependent Claim 14 words
A method as defined in claim 3 wherein the refractory inorganic oxide is alumina.
Claim 6
Dependent Claim 13 words
A method as defined in claim 1 wherein the halogen is combined chloride.
Claim 7
Dependent Claim 23 words
A method as defined in claim 1 wherein the dehydrocyclizable hydrocarbon is an aliphatic hydrocarbon containing 6 to 20 carbon atoms per molecule.
Claim 8
Dependent Claim 14 words
A method as defined in claim 6 wherein the aliphatic hydrocarbon is an olefin.
Claim 9
Dependent Claim 14 words
A method as defined in claim 6 wherein the aliphatic hydrocarbon is a paraffin.
Claim 10
Dependent Claim 22 words
A method as defined in claim 8 wherein the paraffin hydrocarbon is a paraffin containing 6 to 10 carbon atoms per molecule.
Claim 11
Dependent Claim 12 words
A method as defined in claim 8 wherein the paraffin is hexane.
Claim 12
Dependent Claim 12 words
A method as defined in claim 8 wherein the paraffin is heptane.
Claim 13
Dependent Claim 12 words
A method as defined in claim 8 wherein the paraffin is octane.
Claim 14
Dependent Claim 12 words
A method as defined in claim 8 wherein the paraffin is nonane.
Claim 15
Dependent Claim 20 words
A method as defined in claim 8 wherein the paraffin is a mixture of C 6 to C 9 paraffins.
Claim 16
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 17
Dependent Claim 50 words
A method as defined in claim 2 wherein the dehydrocyclization conditions include a temperature of 800° to about 1100° F., a pressure of 0 to 250 psig., a LHSV of 0.1 to 5 hr. - 1 , and a hydrogen to hydrocarbon mole ratio of about 0.1:1 to about 10:1.
Claim 18
Dependent Claim 51 words
A method as defined in claim 1 wherein the composite contains, on an elemental basis, about 0.05 to about 1 wt. % platinum or palladium, about 0.01 to about 1 wt. % rhodium and about 0.05 to about 1 wt. % rhenium and about 0.5 to about 1.5 wt. % halogen.
Claim 19
Dependent Claim 34 words
A method as defined in claim 1 wherein the metals content of the catalytic composite is adjusted so that the atomic ratio of rhenium to platinum or palladium is about 0.05:1 to about 10:1.
Claim 20
Dependent Claim 34 words
A method as defined in claim 1 wherein the metals content of the catalytic composite is adjusted so that the atomic ratio of rhodium to platinum or palladium is about 0.01:1 to about 20:1.
Claim 21
Dependent Claim 17 words
A method as defined in claim 1 wherein the contacting is performed in a substantially water-free environment.
Claim 22
Dependent Claim 45 words
A method as defined in claim 1 wherein the catalytic composite comprises a combination of the catalytic composite defined in claim 1 with a sulfiding reagent in an amount sufficient to incorporate about 0.01 to about 1 wt. % sulfur, calculated on an elemental basis.

References Cited (Backward Citations)

US3956103A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-08 1981-02-07 1981-08-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-08 1985-02-07 1985-08-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-08 1989-02-07 1989-08-09 $7700.00 Window Closed / Lapsed

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