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US4090980A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for preparing reduced metal catalyst having metal surface area

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1977-05-06
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Granted: 1978-05-23
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Expires: 1997-05-06
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Abstract

Abstract This invention pertains to a method of stabilizing, with respect to atmospheric air, a bed containing pyrophoric reduced metal catalyst with high active metal surface area formed by reduction of a compound of said metal at an elevated temperature ranging from 200 DEG to 500 DEG C. which comprises:

Inventors

  • 👤 James L. Carter
  • 👤 Allan E. Barnett

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 01:55
CPC Classifications
B; B01; B01J; B01J33/00; B01J37/00; B01J37/12; B01J37/14; B01J23/00; B01J23/70; B01J23/74; B01J23/755; Y; Y10; Y10S; Y10S502/00; Y10S502/50

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 264 words
A process of stabilizing, with respect to atmospheric air, a bed containing pyrophoric reduced metal catalyst with high active metal surface area formed by reduction of a compound of said metal at an elevated temperature ranging from 200° C. to 500° C. which comprises; (a) continuously circulating through said bed a stream of an inert gas while maintaining a catalyst temperature of at least 300° F. (149° C.); (b) cooling the catalyst throughout the bed with said inert gas until the catalyst in said bed attains a temperature ranging from about 50° to about 100° F.; (c) decreasing the inert gas flow and progressively adding CO 2 until the CO 2 concentration in the gas stream is at least about 80%; (d) adding O 2 to the gas stream to obtain about 0.05 vol. % O 2 in the gas stream and continuing this flow until a sufficient amount of O 2 has passed through the catalyst bed to attain about 25% of a monolayer coverage of oxygen on the active metal surface; (e) increasing the O 2 concentration in the gas stream at a rate that will have passed enough O 2 through the catalyst bed to form about a monolayer on the active metal surface by the time the concentration reaches about 1 vol. % O 2 ; and (f) increasing the O 2 concentration and decreasing the CO 2 concentration until said catalyst in the bed is stabilized with respect to atmospheric air, said stabilization treatments being characterized as providing a stabilized catalyst without loss of the initial metal surface area.
Claim 2
Dependent Claim 264 words
A process of stabilizing, with respect to atmospheric air, a bed containing pyrophoric reduced metal catalyst with high active metal surface area formed by reduction of a compound of said metal at an elevated temperature ranging from 200° C. to 500° C. which comprises; (a) continuously circulating through said bed a stream of an inert gas while maintaining a catalyst temperature of at least 300° F. (149° C.); (b) cooling the catalyst throughout the bed with said inert gas until the catalyst in said bed attains a temperature ranging from about 50° to about 100° F.; (c) decreasing the inert gas flow and progressively adding CO 2 until the CO 2 concentration in the gas stream is at least about 80%; (d) adding O 2 to the gas stream to obtain about 0.05 vol. % O 2 in the gas stream and continuing this flow until a sufficient amount of O 2 has passed through the catalyst bed to attain about 25% of a monolayer coverage of oxygen on the active metal surface; (e) increasing the O 2 concentration in the gas stream at a rate that will have passed enough O 2 through the catalyst bed to form about a monolayer on the active metal surface by the time the concentration reaches about 1 vol. % O 2 ; and (f) increasing the O 2 concentration and decreasing the CO 2 concentration until said catalyst in the bed is stabilized with respect to atmospheric air, said stabilization treatments being characterized as providing a stabilized catalyst without loss of the initial metal surface area.
Claim 3
Dependent Claim 11 words
The process of claim 1 wherein the inert gas is nitrogen.
Claim 4
Dependent Claim 21 words
The process of claim 1 wherein the total gas flow is maintained constant as the various changes in flows are made.
Claim 5
Dependent Claim 12 words
The process of claim 1 wherein the O 2 gas is air.
Claim 6
Dependent Claim 21 words
The process of claim 1 wherein the CO 2 concentration in the bed in step (c) is at least about 95%.
Claim 7
Dependent Claim 13 words
The process of claim 1 wherein the catalyst is a nickel silica catalyst.
Claim 8
Dependent Claim 15 words
The process of claim 6 wherein the nickel silica catalyst has been promoted with copper.
Claim 9
Dependent Claim 18 words
The process of claim 1 wherein step (c) is carried out uniformly over about a 1 hour period.
Claim 10
Dependent Claim 19 words
The process of claim 1 wherein step (f) is carried out over about a 1 to 2 hour period.
Claim 11
Dependent Claim 254 words
A process of stabilizing, with respect to atmospheric air, a nickel silica catalyst with high active metal surface area formed by reduction of a compound of said metal at a temperature ranging from 200° to 500° C. which comprises: (a) continuously circulating through said bed an inert gas comprising nitrogen while maintaining a catalyst temperature of at least 300° F. (149° C.); (b) cooling the catalyst throughout the bed with said inert gas until said catalyst in the bed attains a temperature ranging from about 50° to about 100° F.; (c) decreasing the inert gas flow and progressively adding CO 2 until the CO 2 concentration in the gas stream is about 100%; (d) adding air to the gas stream to obtain about 0.05 vol. % O 2 in the gas stream and continuing this flow until enough O 2 has passed through the catalyst bed to effect about 25% of a monolayer coverage of the active metal surface; (e) increasing the O 2 concentration in the gas stream at a rate that will have passed enough O 2 through the catalyst bed to form about a monolayer on the active metal surface by the time the concentration reaches about 1 vol. % O 2 ; and (f) increasing the air flow and decreasing the CO 2 until the O 2 concentration reaches 20 vol. % and the catalyst is stabilized with respect to atmospheric air, said stabilization treatments being characterized as providing a stabilized catalyst without loss of the initial nickel surface area.
Claim 12
Dependent Claim 254 words
A process of stabilizing, with respect to atmospheric air, a nickel silica catalyst with high active metal surface area formed by reduction of a compound of said metal at a temperature ranging from 200° to 500° C. which comprises: (a) continuously circulating through said bed an inert gas comprising nitrogen while maintaining a catalyst temperature of at least 300° F. (149° C.); (b) cooling the catalyst throughout the bed with said inert gas until said catalyst in the bed attains a temperature ranging from about 50° to about 100° F.; (c) decreasing the inert gas flow and progressively adding CO 2 until the CO 2 concentration in the gas stream is about 100%; (d) adding air to the gas stream to obtain about 0.05 vol. % O 2 in the gas stream and continuing this flow until enough O 2 has passed through the catalyst bed to effect about 25% of a monolayer coverage of the active metal surface; (e) increasing the O 2 concentration in the gas stream at a rate that will have passed enough O 2 through the catalyst bed to form about a monolayer on the active metal surface by the time the concentration reaches about 1 vol. % O 2 ; and (f) increasing the air flow and decreasing the CO 2 until the O 2 concentration reaches 20 vol. % and the catalyst is stabilized with respect to atmospheric air, said stabilization treatments being characterized as providing a stabilized catalyst without loss of the initial nickel surface area.
Claim 13
Dependent Claim 15 words
The process of claim 10 wherein the nickel silica catalyst has been promoted with copper.
Claim 14
Dependent Claim 41 words
The process of claim 10 wherein step (e) is carried out by increasing the O 2 concentration in increments to provide enough added O 2 to form about a monolayer on the active metal when about 1% oxygen has been established.

References Cited (Backward Citations)

US1001279A Cited
US2677668A Cited
US2565347A Cited
US2750261A Cited
US3868332A Cited
US3838066A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-05-22 1981-11-21 1982-05-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-05-22 1985-11-21 1986-05-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-05-22 1989-11-21 1990-05-23 $7700.00 Window Closed / Lapsed

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