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US4087352A Expired / Lapsed US ⏱️ 0.0 years remaining

Dehydrocyclization with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
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Filing: 1977-01-10
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Granted: 1978-05-02
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Expires: 1997-01-10
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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 group component, a Group IVA metallic component, a lanthanide series component, and a halogen component with a porous carrier material. The platinum group, Group IVA metallic and halogen components are present in the multimetallic catalyst in amounts respectively, calculated as wt. % of finished caralyst and on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % Group IVA metal, and about 0.1 to about 3.5 wt. % halogen. The lanthanide series component is present in an amount corresponding to an atomic ratio of lanthanide series metal to platinum group metal of about 0.1:1 to about 1.25:1. 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 platnium group component is in the elemental metallic state and substantially all of the Group IVA metallic component and lanthanide series component are present in an oxidation state above that of the corresponding elemental metal. A specific example of dehydrocyclization method disclosed herein is a method for converting a feed mixture of n-hexane and n-heptane to a produce 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 2026-11-06 09:16
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/63; B01J23/62; B01J23/622; C; C07; C07C; C07C5/00; C07C5/32; C07C5/373; C07C5/393; C07C5/41; C07C5/415; C07C5/417; 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: 33
Claim 1
Independent Claim 157 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, calculated on a wt. % of finished composite and on an elemental basis, about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % Group IVA metal, about 0.1 to about 3.5 wt. % halogen, and a lanthanide series component in an amount sufficient to result in an atomic ratio of lanthanide series metal to platinum group metal of about 0.1:1 to about 1.25:1; wherein the platinum group metal, Group IVA metal and lanthanide series component are uniformly dispersed throughout the porous carrier material; wherein substantially all of the platinum group metal is present in the elemental metallic state; and wherein substantially all of the Group IVA metal and the lanthanide series component are present in an oxidation state above that of the corresponding elemental metal.
Claim 2
Independent Claim 157 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, calculated on a wt. % of finished composite and on an elemental basis, about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % Group IVA metal, about 0.1 to about 3.5 wt. % halogen, and a lanthanide series component in an amount sufficient to result in an atomic ratio of lanthanide series metal to platinum group metal of about 0.1:1 to about 1.25:1; wherein the platinum group metal, Group IVA metal and lanthanide series component are uniformly dispersed throughout the porous carrier material; wherein substantially all of the platinum group metal is present in the elemental metallic state; and wherein substantially all of the Group IVA metal and the lanthanide series component are present in an oxidation state above that of the corresponding elemental metal.
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 14 words
A method as defined in claim 1 wherein the platinum group metal is platinum.
Claim 8
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group metal is iridium.
Claim 9
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group metal is palladium.
Claim 10
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group metal is rhodium.
Claim 11
Dependent Claim 14 words
A method as defined in claim 1 wherein the lanthanide series component is neodymium.
Claim 12
Dependent Claim 14 words
A method as defined in claim 1 wherein the lanthanide series component is cerium.
Claim 13
Dependent Claim 14 words
A method as defined in claim 1 wherein the lanthanide series component is lanthanum.
Claim 14
Dependent Claim 14 words
A method as defined in claim 1 wherein the Group IVA metal is germanium.
Claim 15
Dependent Claim 14 words
A method as defined in claim 1 wherein the Group IVA metal is tin.
Claim 16
Dependent Claim 14 words
A method as defined in claim 1 wherein the Group IVA metal is lead.
Claim 17
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 18
Dependent Claim 14 words
A method as defined in claim 16 wherein the aliphatic hydrocarbon is an olefin.
Claim 19
Dependent Claim 14 words
A method as defined in claim 16 wherein the aliphatic hydrocarbon is a paraffin.
Claim 20
Dependent Claim 22 words
A method as defined in claim 18 wherein the paraffin hydrocarbon is a paraffin containing 6 to 10 carbon atoms per molecule.
Claim 21
Dependent Claim 12 words
A method as defined in claim 18 wherein the paraffin is hexane.
Claim 22
Dependent Claim 12 words
A method as defined in claim 18 wherein the paraffin is heptane.
Claim 23
Dependent Claim 12 words
A method as defined in claim 18 wherein the paraffin is octane.
Claim 24
Dependent Claim 12 words
A method as defined in claim 18 wherein the paraffin is nonane.
Claim 25
Dependent Claim 20 words
A method as defined in claim 18 wherein the paraffin is a mixture of C 6 to C 9 paraffins.
Claim 26
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 27
Dependent Claim 49 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 28
Dependent Claim 61 words
A method as defined in claim 1 wherein the composite contains, on an elemental basis, about 0.05 to about 1 wt. % platinum group metal, about 0.05 to about 2 wt. % Group IVA metal, about 0.5 to about 1.5 wt. % halogen and an atomic ratio of lanthanide series metal to platinum group metal of about 0.4:1 to about 1:1.
Claim 29
Dependent Claim 36 words
A method as defined in claim 1 wherein the metals content of the catalytic composite is adjusted so that the atomic ratio of Group IVA metal to platinum group metal is about 0.05:1 to about 10:1.
Claim 30
Dependent Claim 28 words
A method as defined in claim 1 wherein substantially all of the Group IVA metal is present in the catalytic composite in the form of the corresponding oxide.
Claim 31
Dependent Claim 28 words
A method as defined in claim 1 wherein substantially all of the lanthanide series component is present in the catalytic composite in the form of the corresponding oxide.
Claim 32
Dependent Claim 17 words
A method as defined in claim 1 wherein the contacting is performed in a substantially water-free environment.
Claim 33
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 0.05 to about 0.5 wt. % sulfur, calculated on an elemental basis.

References Cited (Backward Citations)

US3915845A Cited
US4003826A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-05-01 1981-10-31 1982-05-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-05-01 1985-10-31 1986-05-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-05-01 1989-10-31 1990-05-02 $7700.00 Window Closed / Lapsed

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