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US4003955A Expired / Lapsed US ⏱️ 0.0 years remaining

Dehydrocyclization with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1976-03-08
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Granted: 1977-01-18
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Expires: 1996-03-08
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Abstract

Abstract Dehydrocyclizable hydrocarbons are converted to aromatics by contacting them at dehydrocyclization conditions with an acidic multi-metallic catalytic composite comprising a combination of catalytically effective amounts of a platinum or palladium component, a rhodium component, a nickel component, and a halogen component with a porous carrier material. In a preferred embodiment, the catalytic composite also contains a catalytically effective amount of a Group IVA metallic component. The platinum or palladium, rhodium, nickel 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 5 wt. % nickel, 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, rhodium and nickel components are in the elemental metallic state. 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

  • 👤 John C. Hayes

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 21:18
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; B; B01; B01J; B01J23/00; B01J23/70; B01J23/74; B01J23/755; B01J23/89; B01J23/8933; B01J23/8966; 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 99 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, or 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 5 wt. % nickel and about 0.1 to about 3.5 wt. % halogen; wherein the platinum or palladium, rhodium and nickel are uniformly dispersed throughout the porous carrier material; and wherein substantially all of the platinum or palladium, rhodium and nickel are present in the elemental metallic state.
Claim 2
Independent Claim 99 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, or 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 5 wt. % nickel and about 0.1 to about 3.5 wt. % halogen; wherein the platinum or palladium, rhodium and nickel are uniformly dispersed throughout the porous carrier material; and wherein substantially all of the platinum or palladium, rhodium and nickel are present 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 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 28 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° 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 0.05 to about 1 wt. % rhodium and about 0.05 to about 2 wt. % nickel 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 nickel to platinum or palladium is about 0.2:1 to about 20:1.
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 0.1:1 to about 2:1.
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 47 words
A method as defined in claim 1 wherein the catalytic composite contains, on an elemental basis, about 0.01 to about 5 wt. % Group IVA metal and wherein substantially all of the Group IVA metal is present in an oxidation state above that of the elemental metal.
Claim 23
Dependent Claim 14 words
A method as defined in claim 21 wherein the Group IVA metal is germanium.
Claim 24
Dependent Claim 14 words
A method as defined in claim 21 wherein the Group IVA metal is tin.
Claim 25
Dependent Claim 14 words
A method as defined in claim 21 wherein the Group IVA metal is lead.
Claim 26
Dependent Claim 25 words
A method as defined in claim 21 wherein the Group IVA metal is present in the catalytic composite in the form of the corresponding oxide.

References Cited (Backward Citations)

US2500146A Cited
US2911357A Cited
US3210296A Cited
US3840471A Cited
US3825487A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-01-18 1980-07-19 1981-01-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-01-18 1984-07-19 1985-01-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-01-18 1988-07-19 1989-01-18 $7700.00 Window Closed / Lapsed

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