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US4046672A
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Hydrocarbon conversion with an acidic multimetallic composite
Assignee: Honeywell UOP LLC
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Filing: 1976-05-20
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Granted: 1977-09-06
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Expires: 1996-05-20
Abstract
Abstract Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with an acidic multimetallic catalytic composite comprising a combination of catalytically effective amounts of a platinum group component, a tin component, a cobalt component, and a halogen component with a porous carrier material. The platinum group, tin, 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 0.01 to about 5 wt. % tin, about 0.1 to about 5 wt. % cobalt, and about 0.1 to about 3.5 wt. % halogen. Horeover, the catalytically active sites induced by these metallic components are uniformly dispersed throughout the porous carrier material and these 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 catalytically available cobalt component is in the elemental metallic state or in a state which is reducible to the elemental metallic state under hydrocarbon conversion conditions or in a mixture of these states, while substantially all of the tin component is present therein in an oxidation state above that of the elemental metal. A specific example of the type of hydrocarbon conversion process disclosed is a process for the catalytic reforming of a low-octane gasoline fraction wherein the gasoline fraction and a hydrogen stream are contacted with the acidic multimetallic catalyst disclosed herein at reforming conditions.
Inventors
- 👤 Ernest L. Pollitzer
- 👤 John C. Hayes
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 21:55
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/89; B01J23/8933; B01J23/8966; B01J27/00; B01J27/06; B01J27/08; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; C10G47/00; C10G47/02; C10G47/10; C10G47/12; C10G47/14; C07; C07C; C07C2521/00; C07C2521/02; C07C2521/04; C07C2523/00; C07C2523/02; C07C2523/04; C07C2523/14; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/44; C07C2523/46; C07C2523/70; C07C2523/74; C07C2523/75; C07C2523/89
Claims Analysis
Total Claims: 29
Claim 1
Independent Claim
175 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion 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 0.1 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % tin, and about 0.1 to about 3.5 wt. % halogen; wherein the platinum group metal, catalytically available cobalt, and tin are uniformly dispersed throughout the porous carrier material; wherein the average crystallite size of the tin and catalytically available cobalt is less than 100 Angstroms in maximum dimension; wherein substantially all of the platinum group metal is present in the elemental metallic state; wherein substantially all of the tin is present in an oxidation state above that of the elemental metal; 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 hydrocarbon conversion conditions or in a mixture of these states.
Claim 2
Dependent Claim
175 words
A process for converting a hydrocarbon which comprises contacting the hydrocarbon at hydrocarbon conversion 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 0.1 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % tin, and about 0.1 to about 3.5 wt. % halogen; wherein the platinum group metal, catalytically available cobalt, and tin are uniformly dispersed throughout the porous carrier material; wherein the average crystallite size of the tin and catalytically available cobalt is less than 100 Angstroms in maximum dimension; wherein substantially all of the platinum group metal is present in the elemental metallic state; wherein substantially all of the tin is present in an oxidation state above that of the elemental metal; 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 hydrocarbon conversion conditions or in a mixture of these states.
Claim 3
Dependent Claim
14 words
A process as defined in claim 1 wherein the platinum group metal is platinum.
Claim 4
Dependent Claim
14 words
A process as defined in claim 1 wherein the platinum group metal is iridium.
Claim 5
Dependent Claim
14 words
A process as defined in claim 1 wherein the platinum group metal is rhodium.
Claim 6
Dependent Claim
14 words
A process as defined in claim 1 wherein the platinum group metal is palladium.
Claim 7
Dependent Claim
17 words
A process as defined in claim 1 wherein the porous carrier material is a refractory inorganic oxide.
Claim 8
Dependent Claim
14 words
A process as defined in claim 6 wherein the refractory inorganic oxide is alumina.
Claim 9
Dependent Claim
16 words
A process as defined in claim 1 wherein the porous carrier material contains catalytically unavailable cobalt.
Claim 10
Dependent Claim
28 words
A process as defined in claim 8 wherein the catalytically unavailable cobalt is combined with the carrier material in the form of a refractory cobalt oxide or aluminate.
Claim 11
Dependent Claim
26 words
A process as defined in claim 1 wherein the catalytically available cobalt comprises at least about 10% of the total cobalt content of the catalytic composite.
Claim 12
Dependent Claim
13 words
A process as defined in claim 1 wherein the halogen is combined chloride.
Claim 13
Dependent Claim
27 words
A process as defined in claim 1 wherein the atomic ratio of tin to platinum group metal contained in the composite is about 0.1:1 to about 13:1.
Claim 14
Dependent Claim
27 words
A process as defined in claim 1 wherein the atomic ratio of cobalt to platinum group metal contained in the composite is about 0.15:1 to about 66:1.
Claim 15
Dependent Claim
37 words
A process 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 process is started-up and lined-out at hydrocarbon conversion conditions.
Claim 16
Dependent Claim
22 words
A process as defined in claim 1 wherein substantially all of the tin is present in the catalytic composite as tin oxide.
Claim 17
Dependent Claim
44 words
A process as defined in claim 1 wherein the composite contains about 0.05 to about 1 wt. % platinum, about 0.05 to about 2 wt. % cobalt, about 0.05 to about 2 wt. % tin, and about 0.5 to about 1.5 wt. % halogen.
Claim 18
Dependent Claim
24 words
A process as defined in claim 1 wherein the contacting of the hydrocarbon with the catalytic composite is performed in the presence of hydrogen.
Claim 19
Dependent Claim
54 words
A process as defined in claim 1 wherein the type of hydrocarbon conversion is catalytic reforming of a gasoline fraction to produce a high octane reformate, wherein the hydrocarbon is contained in the gasoline fraction, wherein the contacting is performed in the presence of hydrogen, and wherein the hydrocarbon conversion conditions are reforming conditions.
Claim 20
Dependent Claim
57 words
A process as defined in claim 18 wherein the reforming conditions include a temperature of about 800° to about 1100° F., a pressure of about 0 to about 1000 psig., a liquid hourly space velocity of about 0.1 to about 10 hr..sup. -1, and a mole ratio of hydrogen to hydrocarbon of about 1:1 to about 20:1.
Claim 21
Dependent Claim
17 words
A process as defined in claim 18 wherein the contacting is performed in a substantially water-free environment.
Claim 22
Dependent Claim
21 words
A process as defined in claim 18 wherein the reforming conditions include a pressure of about 100 to about 450 psig.
Claim 23
Dependent Claim
17 words
A process as defined in claim 18 wherein the contacting is performed in a substantially sulfur-free environment.
Claim 24
Dependent Claim
72 words
A process as defined in claim 16 wherein the type of hydrocarbon conversion is catalytic reforming of a gasoline fraction to produce a high octane reformate, wherein the hydrocarbon is contained in the gasoline fraction, wherein the contacting is performed in the presence of hydrogen, wherein the hydrocarbon conversion conditions are reforming conditions, wherein the catalytic composite is in a sulfur-free condition and wherein the contacting is performed in a sulfur-free environment.
Claim 25
Dependent Claim
160 words
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 0.1 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % tin, and about 0.1 to about 3.5 wt. % halogen; wherein the platinum group metal, catalytically available cobalt, and tin are uniformly dispersed throughout the porous carrier material; wherein the average crystallite size of the tin and catalytically available cobalt is less than 100 Angstroms in maximum dimension; wherein substantially all of the platinum group metal is present in the corresponding elemental metallic state; wherein substantially all of the tin is present in an oxidation state above that of the elemental metal; 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 hydrocarbon conversion conditions or in a mixture of these states.
Claim 26
Dependent Claim
160 words
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 0.1 to about 5 wt. % cobalt, about 0.01 to about 5 wt. % tin, and about 0.1 to about 3.5 wt. % halogen; wherein the platinum group metal, catalytically available cobalt, and tin are uniformly dispersed throughout the porous carrier material; wherein the average crystallite size of the tin and catalytically available cobalt is less than 100 Angstroms in maximum dimension; wherein substantially all of the platinum group metal is present in the corresponding elemental metallic state; wherein substantially all of the tin is present in an oxidation state above that of the elemental metal; 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 hydrocarbon conversion conditions or in a mixture of these states.
Claim 27
Dependent Claim
18 words
An acidic catalytic composite as defined in claim 24 wherein the porous carrier material contains catalytically unavailable cobalt.
Claim 28
Dependent Claim
30 words
An acidic catalytic composite as defined in claim 25 wherein the catalytically unavailable cobalt is combined with the carrier material in the form of a refractory cobalt oxide or aluminate.
Claim 29
Dependent Claim
28 words
An acidic catalytic composite as defined in claim 24 wherein the catalytically available cobalt comprises at least about 10% of the total cobalt content of the catalytic composite.
References Cited (Backward Citations)
US3960710A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-05 | 1981-03-07 | 1981-09-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-05 | 1985-03-07 | 1985-09-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-05 | 1989-03-07 | 1989-09-06 | $7700.00 | Window Closed / Lapsed |