US4113656A
Expired / Lapsed
US
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Hydrotreating catalyst and process utilizing the same
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1977-02-28
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Granted: 1978-09-12
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Expires: 1997-02-28
Abstract
Abstract A catalyst is provided which comprises a hydrogenation component composited with an alumina-containing support. The catalyst has a median pore radius ranging from about 70 to about 95 Angstroms and a specified pore size distribution. A preferred catalyst is cobalt-molybdenum on alumina. Also provided is a hydrotreating process utilizing said catalyst.
Inventors
- 👤 Kenneth L. Riley
- 👤 Lloyd A. Pine
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 03:15
CPC Classifications
B; B01; B01J; B01J35/00; B01J35/60; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/85; B01J35/61; B01J35/615; B01J35/63; B01J35/633; B01J35/635; B01J35/638; B01J35/64; B01J35/647; B01J35/66; B01J35/67; C; C10; C10G; C10G2300/00; C10G2300/10; C10G2300/107
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
220 words
A catalyst comprising an alumina support composited with a hydrogenation component comprising at least one Group VIB metal component selected from the group consisting of at least one elemental metal, metal oxide or metal sulfide of a Group VIB element of the Periodic Table of Elements and at least one Group VIII metal component selected from the group consisting of at least one elemental metal, metal oxide or metal sulfide of a Group VIII metal of the Periodic Table of Elements, said catalyst having a median pore radius ranging from about 70 to about 95 Angstroms, a total pore volume between 0.45 and 1.50 ml/g; less than 0.05 ml/g of said pore volume being in pores with radii greater than 100 Angstroms; at least 0.40 ml/g of said pore volume being in pores with radii in the range between said median pore radius to about 10 Angstroms above and 10 Angstroms below said median pore radius; at least 75 percent of said pore volume being in pores with radii in the range between said median pore radius to about 10 Angstroms above and 10 Angstroms below said median pore radius; less than 0.05 ml/g of said pore volume being in pores with radii below 60 Angstroms, and a total surface area ranging between 130 and 500 square meters per gram.
Claim 2
Dependent Claim
220 words
A catalyst comprising an alumina support composited with a hydrogenation component comprising at least one Group VIB metal component selected from the group consisting of at least one elemental metal, metal oxide or metal sulfide of a Group VIB element of the Periodic Table of Elements and at least one Group VIII metal component selected from the group consisting of at least one elemental metal, metal oxide or metal sulfide of a Group VIII metal of the Periodic Table of Elements, said catalyst having a median pore radius ranging from about 70 to about 95 Angstroms, a total pore volume between 0.45 and 1.50 ml/g; less than 0.05 ml/g of said pore volume being in pores with radii greater than 100 Angstroms; at least 0.40 ml/g of said pore volume being in pores with radii in the range between said median pore radius to about 10 Angstroms above and 10 Angstroms below said median pore radius; at least 75 percent of said pore volume being in pores with radii in the range between said median pore radius to about 10 Angstroms above and 10 Angstroms below said median pore radius; less than 0.05 ml/g of said pore volume being in pores with radii below 60 Angstroms, and a total surface area ranging between 130 and 500 square meters per gram.
Claim 3
Dependent Claim
81 words
The catalyst of claim 1 wherein said catalyst has the following physical characteristics: ______________________________________
Surface Area, m.sup.2 /g 130 to 500
Pore Volume, ml/g 0.45 to 1.50
Median Pore Radius, A 70 to 95
Pore Volume Distribution
PV above 100 A radius, ml/g
0 to 0.05
PV between R.sub.m + 10 A above and 10A below, ml/g
0.40 to 1.00
% PV between R.sub.m ± 10 A, %
75 to 99
PV below 60 A radius, ml/g 0 to 0.05
______________________________________
Claim 4
Dependent Claim
83 words
The catalyst of claim 1 wherein said catalyst has the following physical characteristics: ______________________________________
Surface Area, m.sup.2 /g 132 to 200
Pore Volume, ml/g 0.48 to 1.00
Median Pore Radius, A 75 to 90
Pore Volume Distribution
PV above 100 A radius, ml/g
0 to 0.04
PV between R.sub.m ± + 10 A above and 10 A below, ml/g
0.41 to 0.80
% PV between R.sub.m ± 10 A, %
80 to 98
PV below 60 A radius, ml/g 0 to 0.04
______________________________________
Claim 5
Dependent Claim
87 words
The catalyst of claim 1 wherein said catalyst has the following physical characteristics: ______________________________________
Surface Area, m.sup.2 /g 135 to 175
Pore Volume, ml/g 0.50 to 0.60
Median Pore Radius, A 78 to 86
Pore Volume Distribution
PV above 100 A radius, ml/g
0 to 0.035
PV between R.sub.m + 10 A above and 10 A below, ml/g
0.42 to 0.60
% PV between R.sub.m + 10 A above and 10 A below, %
81 to 96
PV below 60 A radius, ml/g 0 to 0.035
______________________________________
Claim 6
Dependent Claim
46 words
The catalyst of claim 1 wherein said Group VIB metal, calculated as the oxide thereof, comprises at least 8 weight percent of the total catalyst and wherein said Group VIII metal (calculated as the oxide thereof) comprises at least 2.5 weight percent of the total catalyst.
Claim 7
Dependent Claim
51 words
The catalyst of claim 1, wherein said Group VI metal, calculated as the oxide thereof, comprises from about 14 to 20 weight percent of the total catalyst and wherein said Group VIII metal, calculated as the oxide thereof, comprises from about 3.5 to about 6.5 weight percent of the total catalyst.
Claim 8
Dependent Claim
52 words
The catalyst of claim 1 wherein said Group VIB metal component is selected from the group consisting of molybdenum oxide, molybdenum sulfide, tungsten oxide, tungsten sulfide and mixtures thereof and wherein said Group VIII is selected from the group consisting of nickel oxide, cobalt oxide, nickel sulfide, cobalt sulfide and mixtures thereof.
Claim 9
Dependent Claim
14 words
The process of claim 1 wherein said alumina support contains minor amounts of silica.
Claim 10
Dependent Claim
61 words
The process of claim 1 wherein said catalyst consists essentially of a Group VIB metal component selected from the group consisting of molybdenum oxide, molybdenum sulfide, tungsten oxide, tungsten sulfide and mixtures thereof and a Group VIII metal component selected from the group consisting of nickel oxide, cobalt oxide, nickel sulfide, cobalt sulfide and mixtures thereof composited with an alumina support.
References Cited (Backward Citations)
US3814683A
Cited
US3876523A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-09-11 | 1982-03-13 | 1982-09-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-09-11 | 1986-03-13 | 1986-09-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-09-11 | 1990-03-13 | 1990-09-12 | $7700.00 | Window Closed / Lapsed |