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US4263174A Expired / Lapsed US ⏱️ 0.0 years remaining

Low coke-make FCC catalyst

Assignee: Honeywell UOP LLC
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Filing: 1979-08-29
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Granted: 1981-04-21
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Expires: 1999-08-29
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Abstract

Abstract A catalytic composite, its method of manufacture and use is disclosed. The composite comprises a zeolitic crystalline aluminosilicate dispersed in a porous inorganic oxide carrier material comprising silica, alumina or zirconium and a constituent comprising the ions of one or more rare earths with the weight ratio on a volatile free basis of the rare earth ions to the carrier material being greater than 1.0:100.0. The method of manufacture of the composite comprises mixing a catalyst powder comprising the zeolite dispersed in a porous inorganic oxide carrier material with a solution of a salt of the rare earth, separating a filter cake from the slurry by a means not involving the washing of the filter cake and calcining the filter cake. The catalytic composite may be used in a process for cracking a hydrocarbon charge stock.

Inventors

  • 👤 Hosheng Tu
  • 👤 David C. DeCoster

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 01:14
CPC Classifications
C; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/08; B01J29/084

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 131 words
A method of catalyst manufacture which comprises: (a) preparing a catalyst powder comprising a zeolite crystalline aluminosilicate dispersed in a porous carrier material consisting essentially of silica, zirconia and alumina; (b) mixing said powder with a sufficient amount of an aqueous solution of a water soluble rare earth salt to form a slurry of said catalyst powder, the stoichiometric excess concentration of said rare earth salt in the solution being sufficient to impart to the final catalyst a weight ratio on a volatile free basis of rare earth ions to said carrier material greater than 1.0:100.0; (c) filtering or centrifuging said slurry to separate therefrom a filter cake containing said catalyst powder; and; (d) calcining said filter cake without washing or drying said filter cake and recovering the resultant catalytic composite.
Claim 2
Independent Claim 131 words
A method of catalyst manufacture which comprises: (a) preparing a catalyst powder comprising a zeolite crystalline aluminosilicate dispersed in a porous carrier material consisting essentially of silica, zirconia and alumina; (b) mixing said powder with a sufficient amount of an aqueous solution of a water soluble rare earth salt to form a slurry of said catalyst powder, the stoichiometric excess concentration of said rare earth salt in the solution being sufficient to impart to the final catalyst a weight ratio on a volatile free basis of rare earth ions to said carrier material greater than 1.0:100.0; (c) filtering or centrifuging said slurry to separate therefrom a filter cake containing said catalyst powder; and; (d) calcining said filter cake without washing or drying said filter cake and recovering the resultant catalytic composite.
Claim 3
Dependent Claim 18 words
The catalytic composite of claim 1 wherein said zeolitic crystalline aluminosilicate comprises a rare earth ion exchanged Y-zeolite.
Claim 4
Dependent Claim 12 words
The catalytic composite of claim 1 wherein said rare earth comprises lanthanum.
Claim 5
Dependent Claim 17 words
The method of claim 1 wherein said zeolite crystalline aluminosilicate comprises a rare earth ion exchanged Y-zeolite.
Claim 6
Dependent Claim 11 words
The method of claim 1 wherein said rare earth comprises lanthanum.
Claim 7
Dependent Claim 14 words
The method of claim 1 wherein said rare earth salt comprises rare earth chloride.
Claim 8
Dependent Claim 42 words
The method of claim 1 wherein said calcining is effected at a temperature of from about 200° C. to about 750° C. and a calcining without washing or drying said filter cake time of from about 30 minutes to about 5 hours.
Claim 9
Dependent Claim 36 words
The method of claim 1 wherein said catalyst powder is obtained as a filter cake from an ion exchange procedure whereby sodium ions contained in the catalyst are exchanged with ammonium ions in an aqueous medium.

References Cited (Backward Citations)

US3556988A Cited
US3823092A Cited
US3930987A Cited
US4107088A Cited
US4137151A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-04-20 1984-10-20 1985-04-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-04-20 1988-10-20 1989-04-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-04-20 1992-10-20 1993-04-21 $7700.00 Window Closed / Lapsed

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