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US4036903A Expired / Lapsed US ⏱️ 0.0 years remaining

Dehydrocyclization with an acidic multimetallic catalytic composite

Assignee: Honeywell UOP LLC
•
Filing: 1976-09-07
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Granted: 1977-07-19
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Expires: 1996-09-07
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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 bismuth component, a cobalt component, and a halogen component with a porous carrier material. The platinum group, bismuth, cobalt 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 0.05 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % bismuth, 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 group component is in the elemental metallic state, substantially all of the bismuth component is preferably in an oxidation state above that of the elemental metal, and substantially all of the catalytically available cobalt component is 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. 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 2026-11-06 06:11
CPC Classifications
C; C07; C07C; C07C5/00; C07C5/32; C07C5/373; C07C5/393; C07C5/41; C07C5/415; C07C5/417; B; B01; B01J; B01J23/00; B01J23/70; B01J23/89; B01J23/8933; B01J23/8973; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; C10G49/00; C10G49/02; C10G49/06; C07C2521/00; C07C2521/02; C07C2521/04; C07C2523/00; C07C2523/16; C07C2523/18; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/44; C07C2523/46; C07C2523/70; C07C2523/74; C07C2523/75; C07C2523/89; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52; Y10; Y10S; Y10S585/00; Y10S585/949; Y10S585/951

Claims Analysis

Total Claims: 30
Claim 1
Independent Claim 135 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 group metal, about 0.05 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % bismuth and about 0.1 to about 3.5 wt. % halogen; wherein the platinum group metal, catalytically available cobalt and bismuth 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 catalytically available cobalt is 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 135 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 group metal, about 0.05 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % bismuth and about 0.1 to about 3.5 wt. % halogen; wherein the platinum group metal, catalytically available cobalt and bismuth 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 catalytically available cobalt is 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 14 words
A method as defined in claim 1 wherein the platinum group metal is platinum.
Claim 5
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group metal is palladium.
Claim 6
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group metal is iridium.
Claim 7
Dependent Claim 14 words
A method as defined in claim 1 wherein the platinum group metal 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 13 words
A method as defined in claim 1 wherein the halogen is combined chloride.
Claim 11
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 12
Dependent Claim 14 words
A method as defined in claim 10 wherein the aliphatic hydrocarbon is an olefin.
Claim 13
Dependent Claim 14 words
A method as defined in claim 10 wherein the aliphatic hydrocarbon is a paraffin.
Claim 14
Dependent Claim 22 words
A method as defined in claim 12 wherein the paraffin hydrocarbon is a paraffin containing 6 to 10 carbon atoms per molecule.
Claim 15
Dependent Claim 12 words
A method as defined in claim 12 wherein the paraffin is hexane.
Claim 16
Dependent Claim 12 words
A method as defined in claim 12 wherein the paraffin is heptane.
Claim 17
Dependent Claim 12 words
A method as defined in claim 12 wherein the paraffin is octane.
Claim 18
Dependent Claim 12 words
A method as defined in claim 12 wherein the paraffin is nonane.
Claim 19
Dependent Claim 20 words
A method as defined in claim 12 wherein the paraffin is a mixture of C 6 to C 9 paraffins.
Claim 20
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 21
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 22
Dependent Claim 53 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 0.1 to about 2.5 wt. % cobalt and about 0.05 to about 1 wt. % bismuth and about 0.5 to about 1.5 wt. % halogen.
Claim 23
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 bismuth to platinum group metal is about 0.1:1 to about 2:1.
Claim 24
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 cobalt to platinum group metal is about 0.1:1 to about 66:1.
Claim 25
Dependent Claim 17 words
A method as defined in claim 1 wherein the contacting is performed in a substantially water-free environment.
Claim 26
Dependent Claim 17 words
A method as defined in claim 1 wherein the contacting is performed in a substantially sulfur-free environment.
Claim 27
Dependent Claim 36 words
A method as defined in claim 1 wherein substantially all of the catalytically available cobalt contained in the composite is present in the elemental metallic state after the method is started-up and lined-out at dehydrocyclization conditions.
Claim 28
Dependent Claim 29 words
A method as defined in claim 1 wherein substantially all of the bismuth is present in the catalytic composite in an oxidation state above that of the elemental metal.
Claim 29
Dependent Claim 25 words
A method as defined in claim 27 wherein substantially all of the bismuth is present in the catalytic composite as bismuth oxide or bismuth aluminate.
Claim 30
Dependent Claim 16 words
A method as defined in claim 1 wherein the catalytic composite is in a sulfur-free state.

References Cited (Backward Citations)

US3655747A Cited
US3651163A Cited
US3759823A Cited
US3878089A Cited
US3888763A Cited
US3948762A Cited
US3957624A Cited
US3939059A Cited
US3960711A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-07-18 1981-01-17 1981-07-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-07-18 1985-01-17 1985-07-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-07-18 1989-01-17 1989-07-19 $7700.00 Window Closed / Lapsed

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