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US4477582A Expired / Lapsed US ⏱️ 0.0 years remaining

Reactivation of steam-deactivated catalysts

Assignee: Mobil Oil AS
•
Filing: 1983-02-04
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Granted: 1984-10-16
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Expires: 2003-02-04
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Abstract

Abstract A process is provided for reactivating a catalyst composition comprising a crystalline zeolite material having a silicon/aluminum atomic ratio of at least about 3.5, said catalyst composition having been deactivated by contact with steam. The method involves the necessary steps of contacting said steam-deactivated catalyst composition with a metal salt solution, followed by contacting said metal salt solution contacted catalyst composition with an aqueous ammonium ion-containing solution.

Inventors

  • 👤 Joseph N. Miale

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 23:28
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/90; B01J29/04; B01J29/06; B01J29/40; B01J2229/00; B01J2229/10; B01J2229/26; B01J2229/30; B01J2229/42; B01J29/65; B01J29/70

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 149 words
A process for reactivating a catalyst composition comprising a crystalline zeolite material having a silicon/aluminum atomic ratio of at least about 3.5, said catalyst composition having been contacted with steam under conditions sufficient to deactivate same by removal of aluminum from the zeolite framework, which comprises the steps of contacting said steam-deactivated catalyst composition with an aqueous metal salt solution of from about 0.05 N to about 5 N, said metal selected from the group consisting of alkali, alkaline earth and transition metals, at a temperature of from about 20° C. to about 100° C. for from about 15 minutes to about 240 minutes, and contacting said metal salt solution contacted catalyst composition with an aqueous ammonium ion solution of from about 0.05 N to about 5 N at a temperature of from about 20° C. to about 100° C. for from about 15 minutes to about 240 minutes.
Claim 2
Dependent Claim 149 words
A process for reactivating a catalyst composition comprising a crystalline zeolite material having a silicon/aluminum atomic ratio of at least about 3.5, said catalyst composition having been contacted with steam under conditions sufficient to deactivate same by removal of aluminum from the zeolite framework, which comprises the steps of contacting said steam-deactivated catalyst composition with an aqueous metal salt solution of from about 0.05 N to about 5 N, said metal selected from the group consisting of alkali, alkaline earth and transition metals, at a temperature of from about 20° C. to about 100° C. for from about 15 minutes to about 240 minutes, and contacting said metal salt solution contacted catalyst composition with an aqueous ammonium ion solution of from about 0.05 N to about 5 N at a temperature of from about 20° C. to about 100° C. for from about 15 minutes to about 240 minutes.
Claim 3
Dependent Claim 18 words
The process of claim 1 wherein said crystalline zeolite material has a silicon/aluminum atomic ratio greater than 6.
Claim 4
Dependent Claim 18 words
The process of claim 1 wherein said crystalline zeolite material has a silicon/aluminum atomic ratio greater than 25.
Claim 5
Dependent Claim 40 words
The process of claim 1 which comprises the additional step of calcining said ammonium ion solution contacted catalyst composition at a temperature of from about 200° C. to about 600° C. for from about 1 minute to about 48 hours.
Claim 6
Dependent Claim 28 words
The process of claim 4 which comprises the additional step of water washing said metal salt solution contacted catalyst composition prior to said ammonium ion solution contacting step.
Claim 7
Dependent Claim 46 words
The process of claim 1 wherein said crystalline zeolite material is selected from the group consisting of large pore structure zeolites exhibiting a Constraint Index of less than about 1 and intermediate pore structure zeolites exhibiting a Constraint Index of from about 1 to about 12.
Claim 8
Dependent Claim 35 words
The process of claim 1 wherein said crystalline zeolite material is selected from the group consisting of those having the structures of ZSM-5, ZSM-11, ZSM-5/ZSM-11 intermediate, ZSM-12, ZSM-20. ZSM-23, ZSM-35, ZSM-38, ZSM-48 and zeolite Beta.
Claim 9
Dependent Claim 19 words
The process of claim 1 wherein said catalyst composition is a composite of said zeolite material and a matrix.
Claim 10
Dependent Claim 10 words
The process of claim 8 wherein said matrix is alumina.

References Cited (Backward Citations)

US2814598A Cited
US3835030A Cited
US3493490A Cited
US3684738A Cited
US4085069A Cited
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US4375573A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-10-16 1988-04-16 1988-10-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-10-16 1992-04-16 1992-10-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-10-16 1996-04-16 1996-10-16 $7700.00 Window Closed / Lapsed

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