US3985684A
Expired / Lapsed
US
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Heavy crude conversion
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1974-12-16
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Granted: 1976-10-12
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Expires: 1994-12-16
Abstract
Abstract This invention relates to novel catalysts, of two distinct types, useful for the catalytic hydroconversion of the 1050 DEG F.+ hydrocarbon material contained in heavy crudes and residua such that the resulting product will be suitable for further processing in conventional refinery operations allowing maximization of clean liquid products. Catalysts, which include Group VIB and Group VIII metals, preferably in admixture, and preferably including a Group IVA metal, notably germanium, having certain critical ranges of physical characteristics inclusive of large uniform pore sizes, are used for the conversion, these having been shown to possess improved catalytic activity and selectivity for the hydroconversion of the 1050 DEG F.+ materials of the heavy feeds and residua. Novel methods are described for the preparation of such catalysts, as well as for use of such catalysts. One of the catalysts, i.e., one having properties inclusive of a large number of pores in the 100-275A pore size diameter range, is particularly suitable as a first stage catalyst and the other, which has properties inclusive of a large number of pores in the 100-200A pore size diameter, is especially suitable as a second stage catalyst for use in processing the effluent of said first stage.
Inventors
- 👤 William F. Arey, Jr.
- 👤 Glen P. Hamner
- 👤 Willard H. Sawyer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 13:26
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/0009; B01J23/00; B01J23/70; B01J23/74; B01J23/76; B01J23/84; B01J23/85; B01J35/00; B01J35/40; B01J35/60; C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; B01J35/61; B01J35/615; B01J35/63; B01J35/635; B01J35/638; B01J35/64; B01J35/647; B01J35/66
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
226 words
A catalyst having enhanced selectivity suitable for the conversion and demetallization of feeds which contain large quantities of 1050° F.+ hydrocarbon materials comprising an admixture of from about 0.1 to about 10 percent of a Group IVA metal, from about 5 to about 30 percent of a Group VIB metal, and from about 1 to about 12 percent of a Group VIII metal, measured as oxides, and a porous inorganic oxide support, said catalyst, when the catalyst is of size ranging from 1/500 to about 1/50 inch average particle size diameter, having at least about 20 percent of its total pore volume of absolute diameter within the range of about 100A to about 200A; when the catalyst is of size ranging from about 1/50 inch up to 1/25 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 150A to about 250A; when the catalyst is of size ranging from about 1/25 inch to about 1/8 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 175A to about 275A, a surface area ranging at least about 200 m 2 /g to about 600 m 2 /g and a pore volume ranging from about 0.8 cc/g to about 3.0 cc/g.
Claim 2
Dependent Claim
226 words
A catalyst having enhanced selectivity suitable for the conversion and demetallization of feeds which contain large quantities of 1050° F.+ hydrocarbon materials comprising an admixture of from about 0.1 to about 10 percent of a Group IVA metal, from about 5 to about 30 percent of a Group VIB metal, and from about 1 to about 12 percent of a Group VIII metal, measured as oxides, and a porous inorganic oxide support, said catalyst, when the catalyst is of size ranging from 1/500 to about 1/50 inch average particle size diameter, having at least about 20 percent of its total pore volume of absolute diameter within the range of about 100A to about 200A; when the catalyst is of size ranging from about 1/50 inch up to 1/25 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 150A to about 250A; when the catalyst is of size ranging from about 1/25 inch to about 1/8 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 175A to about 275A, a surface area ranging at least about 200 m 2 /g to about 600 m 2 /g and a pore volume ranging from about 0.8 cc/g to about 3.0 cc/g.
Claim 3
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/500 to 1/50 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <20%
100-200A >20%
300A+ <30%
Pore Volume, cc/g 0.8-1.4
Surface Area, m.sup.2 /g
300-450.
______________________________________
Claim 4
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/500 to 1/50 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <10%
100-200A >25%
300A+ <25%
Pore Volume, cc/g 0.9-1.5
Surface Area, m.sup.2 /g
310-500.
______________________________________
Claim 5
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/500 to 1/50 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <2%
100-200A >70%
300A+ <1%
Pore Volume, cc/g 1.1-1.7
Surface Area, m.sup.2 /g
325-550.
______________________________________
Claim 6
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/50 to 1/25 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <10%
150-250A >15%
350A+ <35%
Pore Volume, cc/g 1.1-1.7
Surface Area, m.sup.2 /g
320-475.
______________________________________
Claim 7
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/50 to 1/25 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore diameters
______________________________________
0-50A <5%
150-250A >20%
350A+ <30%
Pore Volume, cc/g 1.3-1.9
Surface Area, m.sup.2 /g
340-575.
______________________________________
Claim 8
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/50 to 1/25 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <1%
150-250A >45%
350A+ <7%
Pore Volume, cc/g 1.5-2.1
Surface Area, m.sup.2 /g
360-600.
______________________________________
Claim 9
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/25 to 1/8 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <5%
175-275A >15%
350A+ <40%
Pore Volume, cc/g 1.3-1.9
Surface Area, m.sup.2 /g
340-500.
______________________________________
Claim 10
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/25 to 1/8 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore diameters
______________________________________
0-50A <4%
175-275A >20%
350A+ <35%
Pore Volume, cc/g 1.5-2.1
Surface Area, m.sup.2 /g
350-600.
______________________________________
Claim 11
Dependent Claim
48 words
The catalyst of claim 1 wherein the catalyst of particle size diameter ranging from about 1/25 to 1/8 inch particle size diameter is characterized as follows: ______________________________________
Distribution of Pore Diameters
______________________________________
0-50A <3%
175-275A >30%
350A+ <25%
Pore Volume, cc/g 1.8-2.3
Surface Area, m.sup.2 /g
370-650.
______________________________________
Claim 12
Dependent Claim
49 words
The catalyst of claim 1 wherein said catalyst comprises from about 2 to about 5 percent of a Group IVA metal, from about 15 to about 25 percent of a Group VIB metal, and from about 4 to about 8 percent of a Group VIII metal, measured as oxides.
Claim 13
Dependent Claim
12 words
The catalyst of claim 1 wherein said Group IVA metal is germanium.
Claim 14
Dependent Claim
167 words
A catalyst having enhanced selectivity for conversion, demetallization, and for Con carbon reduction of hydrocarbon feeds whcih contain substantial quantities of 1050° F.+ hydrocarbon materials comprising an admixture of from about 2 to about 5 percent of a Group IVA metal, from about 5 to about 30 percent of a Group VIB metal, and from about 1 to about 12 percent of a Group VIII metal, measured as oxides, and a porous inorganic oxide support, said catalyst including a combination of properties comprising at least about 55 percent of its total pore volume of absolute pore diameters ranging from about 100A to about 200A, less than about 10 percent of its total pore volume of absolute diameter within the range of 0 to 50A, less than 25 percent of its total pre volume of absolute diameter 300A+, a surface area ranging at least about 200 m 2 /g to about 600 m 2 /g and a pore volume ranging from about 0.6 cc/g to about 1.5 cc/g.
Claim 15
Dependent Claim
167 words
A catalyst having enhanced selectivity for conversion, demetallization, and for Con carbon reduction of hydrocarbon feeds whcih contain substantial quantities of 1050° F.+ hydrocarbon materials comprising an admixture of from about 2 to about 5 percent of a Group IVA metal, from about 5 to about 30 percent of a Group VIB metal, and from about 1 to about 12 percent of a Group VIII metal, measured as oxides, and a porous inorganic oxide support, said catalyst including a combination of properties comprising at least about 55 percent of its total pore volume of absolute pore diameters ranging from about 100A to about 200A, less than about 10 percent of its total pore volume of absolute diameter within the range of 0 to 50A, less than 25 percent of its total pre volume of absolute diameter 300A+, a surface area ranging at least about 200 m 2 /g to about 600 m 2 /g and a pore volume ranging from about 0.6 cc/g to about 1.5 cc/g.
Claim 16
Dependent Claim
100 words
The catalyst of claim 13 wherein said catalyst comprises the combination of properties wherein at least about 70 percent of the total pore volume of said catalyst is of pore diameter ranging from about 100A to about 200A, less than about 1 percent of its total pore volume is of absolute diameter within the range 0 to 50A, less than 1 percent of its total pore volume is of absolute diameter 300A+, surface area ranges at least about 250 m 2 /g to about 350 m 2 /g and pore volume ranges from about 0.9 cc/g to about 1.3 cc/g.
Claim 17
Dependent Claim
49 words
The catalyst of claim 13 wherein said catalyst comprises from about 2 to about 5 percent of a Group IVA metal, from about 15 to about 25 percent of a Group VIB metal, and from about 4 to about 8 percent of a Group VIII metal, measured as oxides.
Claim 18
Dependent Claim
12 words
The catalyst of claim 13 wherein said Group IVA metal is germanium.
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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) | 1979-10-12 | 1980-04-12 | 1980-10-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-12 | 1984-04-12 | 1984-10-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-12 | 1988-04-12 | 1988-10-12 | $7700.00 | Window Closed / Lapsed |