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Hydrocarbon conversion catalyst

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1979-10-01
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Granted: 1981-08-11
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Expires: 1999-10-01
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Abstract

Abstract A hydrocarbon conversion catalyst suitable for converion of heavy hydrocarbon oils containing large amounts of metallic contaminants, such as petroleum residua, to lower boiling products comprises a porous inorganic oxide such as bulk alumina composited with an inorganic oxide gel matrix such as silica-alumina, and a crystalline aluminosilicate zeolite.

Inventors

  • 👤 Elroy M. Gladrow

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 20:58
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/08; C; C10; C10G; C10G11/00; C10G11/02; C10G11/04; C10G11/05

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 80 words
A catalyst comprising: (1) a crystalline aluminosilicate zeolite, (2) a catalytic inorganic oxide gel, and (3) a porous inorganic oxide initially having a surface area greater than about 200 square meters per gram and having at least 0.2 cubic centimeter per gram of its pore volume in pores ranging in diameter from about 90 to about 200 angstroms, said catalyst having at least 0.4 cubic centimeter per gram of its pore volume in pores greater than 90 angstroms in diameter.
Claim 2
Dependent Claim 80 words
A catalyst comprising: (1) a crystalline aluminosilicate zeolite, (2) a catalytic inorganic oxide gel, and (3) a porous inorganic oxide initially having a surface area greater than about 200 square meters per gram and having at least 0.2 cubic centimeter per gram of its pore volume in pores ranging in diameter from about 90 to about 200 angstroms, said catalyst having at least 0.4 cubic centimeter per gram of its pore volume in pores greater than 90 angstroms in diameter.
Claim 3
Dependent Claim 25 words
The catalyst of claim 1 wherein said porous inorganic oxide is selected from the group consisting of alumina, silica, titania, zirconia, magnesia and mixtures thereof.
Claim 4
Dependent Claim 12 words
The catalyst of claim 1 wherein said porous inorganic oxide is alumina.
Claim 5
Dependent Claim 12 words
The catalyst of claim 1 wherein said porous inorganic oxide is silica.
Claim 6
Dependent Claim 23 words
The catalyst of claim 1 wherein said porous inorganic oxide comprises from about 1 to about 55 weight percent of the total catalyst.
Claim 7
Dependent Claim 23 words
The catalyst of claim 1 wherein said porous inorganic oxide comprises from about 5 to about 45 weight percent of the total catalyst.
Claim 8
Dependent Claim 22 words
The catalyst of claim 1 wherein said porous inorganic oxide in itself has less catalytic activity than said inorganic oxide gel component.
Claim 9
Dependent Claim 40 words
The catalyst of claim 1 wherein said zeolite comprises from about 1 to about 40 weight percent of the total catalyst and wherein said inorganic oxide gel comprises from about 45 to about 98 weight percent of the total catalyst.
Claim 10
Dependent Claim 14 words
The catalyst of claim 1 wherein said inorganic oxide gel is a silica-containing gel.
Claim 11
Dependent Claim 15 words
The catalyst of claim 1 wherein said inorganic oxide gel is a cogel of silica-alumina.
Claim 12
Dependent Claim 15 words
The catalyst of claim 1 wherein said crystalline aluminosilicate zeolite has the structure of faujasite.
Claim 13
Dependent Claim 33 words
The catalyst of claim 1 wherein said crystalline aluminosilicate zeolite has uniform pore diameters ranging from about 6 to about 15 angstroms and wherein the silica to alumina ratio is greater than 3.
Claim 14
Dependent Claim 19 words
The catalyst of claim 1 wherein said zeolite comprises less than 10 weight percent alkali-metal, calculated as the metal.
Claim 15
Dependent Claim 28 words
The catalyst of claim 1 wherein said porous inorganic oxide has been preformed and placed in physical form such that its surface area and pore structure are stabilized.

References Cited (Backward Citations)

US2951815A Cited
US3260681A Cited
US3542670A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-10 1985-02-09 1985-08-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-10 1989-02-09 1989-08-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-10 1993-02-09 1993-08-11 $7700.00 Window Closed / Lapsed

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