Patent US4014821A successfully refreshed from Google Patents.
US4014821A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heavy crude conversion catalyst
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1974-12-16
•
Granted: 1977-03-29
•
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 materials 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 selectively 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 the 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
- 👤 Glen P. Hamner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 22:43
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J23/74; B01J35/00; B01J35/60; B01J37/00; B01J37/0009; C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; B01J35/61; B01J35/615; B01J35/63; B01J35/638; B01J35/64; B01J35/647; B01J35/66; B01J35/67
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
248 words
A catalyst having enhanced selectively suitable for the conversion and demetallization of feeds which contain large quantities of 1050° F.+ hydrocarbon materials comprising a composite of from about 5 to about 50 percent of a Group VIB metal, or compound thereof thermally decomposable to an oxide, or from about 1 to about 12 percent of a Group VIII metal, or compound thereof thermally decomposable to an oxide, or a composite which comprises an admixture of said Group VIB and Group VIII metals, or compounds thereof thermally decomposable to oxides, measured as oxides, and a porous inorganic oxide support, said catalyst comprising, when the catalyst is of size ranging 1/500 to 1/50 inch average particle size diameter, 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; surface areas ranging at least about 200 m 2 /g to about 600 m 2 /g and pore volumes ranging from about 0.8 cc/g to about 3.0 cc/g.
Claim 2
Dependent Claim
248 words
A catalyst having enhanced selectively suitable for the conversion and demetallization of feeds which contain large quantities of 1050° F.+ hydrocarbon materials comprising a composite of from about 5 to about 50 percent of a Group VIB metal, or compound thereof thermally decomposable to an oxide, or from about 1 to about 12 percent of a Group VIII metal, or compound thereof thermally decomposable to an oxide, or a composite which comprises an admixture of said Group VIB and Group VIII metals, or compounds thereof thermally decomposable to oxides, measured as oxides, and a porous inorganic oxide support, said catalyst comprising, when the catalyst is of size ranging 1/500 to 1/50 inch average particle size diameter, 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; surface areas ranging at least about 200 m 2 /g to about 600 m 2 /g and pore volumes ranging from about 0.8 cc/g to about 3.0 cc/g.
Claim 3
Dependent Claim
47 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
47 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
47 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
47 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
47 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
47 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
47 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
47 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
47 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
56 words
The catalyst of claim 1 wherein said catalyst comprises from about 15 to about 25 percent of a Group VIB metal, or compound thereof, and from about 4 to about 8 percent of a Group VIII metal, or compound thereof, or admixture of said Group VIB and Group VIII metals, or compounds thereof, measured as oxides.
References Cited (Backward Citations)
US2486361A
Cited
US3661805A
Cited
US3654133A
Cited
US3873470A
Cited
US3798156A
Cited
US3867281A
Cited
US3746660A
Cited
US3746661A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-03-28 | 1980-09-27 | 1981-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-03-28 | 1984-09-27 | 1985-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-03-28 | 1988-09-27 | 1989-03-29 | $7700.00 | Window Closed / Lapsed |