Patent US3950244A successfully refreshed from Google Patents.
US3950244A
Expired / Lapsed
US
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Process for treating a solid-containing liquid hydrocarbon oil
Assignee: Gulf Research and Development Co
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Filing: 1974-06-24
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Granted: 1976-04-13
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Expires: 1994-06-24
Abstract
Abstract A process is provided for the conversion of solid-containing liquid hydrocarbon oils, and in particular for the hydrogenation of solid-containing liquid hydrocarbon oils derived from coal, oil shale and tar sands. The process comprises passing a solid-containing liquid hydrocarbon oil, together with hydrogen, through a reaction vessel that contains a plurality of reaction zones separated by porous partitions. A portion of said zones is adapted to contain a solid particulate hydrogenation catalyst which will not pass through said porous partitions. The remainder of said zones form substantially unobstructed passageways through said reaction vessel. The volumetric ratio of catalyst zones to substantially unobstructed passageways is about 10:1 to about 1:10.
Inventors
- 👤 Sun W. Chun
- 👤 Donald C. Cronauer
- 👤 Thomas W. Leslie
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 07:29
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/02; B01J8/06; C; C10; C10G; C10G1/00; C10G1/002; C10G45/00; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/0053
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
115 words
A process for the conversion of solid-containing liquid hydrocarbon oils, said solids containing in excess of about 50 weight per cent of inorganic components, which comprises introducing said solid-containing liquid hydrocarbon oils and hydrogen into a reaction vessel comprising a plurality of reaction zones separated by porous partitions, a portion of said zones containing a solid particulate hydrogenation catalyst which will not pass through said porous partitions and the remainder of said zones forming substantially unobstructed passageways through said reaction vessel and passing said liquid hydrocarbon oils and hydrogen through said unobstructed passageways and through said porous partitions into contact with said catalyst under hydrogenation conditions, whereby hydrogenation of said liquid hydrocarbon oils takes place.
Claim 2
Dependent Claim
115 words
A process for the conversion of solid-containing liquid hydrocarbon oils, said solids containing in excess of about 50 weight per cent of inorganic components, which comprises introducing said solid-containing liquid hydrocarbon oils and hydrogen into a reaction vessel comprising a plurality of reaction zones separated by porous partitions, a portion of said zones containing a solid particulate hydrogenation catalyst which will not pass through said porous partitions and the remainder of said zones forming substantially unobstructed passageways through said reaction vessel and passing said liquid hydrocarbon oils and hydrogen through said unobstructed passageways and through said porous partitions into contact with said catalyst under hydrogenation conditions, whereby hydrogenation of said liquid hydrocarbon oils takes place.
Claim 3
Dependent Claim
15 words
The process of claim 1 wherein said reaction zones are substantially elongated and vartically disposed.
Claim 4
Dependent Claim
15 words
The process of claim 1 wherein said reaction zones are substantially elongated and horizontally disposed.
Claim 5
Dependent Claim
18 words
The process of claim 1 wherein said oil has been derived from coal, oil shale or tar sands.
Claim 6
Dependent Claim
13 words
The process of claim 4 wherein said oil has been derived from coal.
Claim 7
Dependent Claim
14 words
The process of claim 4 wherein said oil has been derived from oil shale.
Claim 8
Dependent Claim
14 words
The process of claim 4 wherein said oil has been derived from tar sands.
Claim 9
Dependent Claim
35 words
A process according to claim 1 further characterized in that the ratio of the cross-sectional area of one catalyst zone to the total cross-sectional area of all catalyst zones is about 1:4 to about 1:10,000.
Claim 10
Dependent Claim
26 words
A process according to claim 1 wherein the volume proportion of substantially unobstructed passageways to catalyst is in the range of about 20:1 to about 1:10.
Claim 11
Dependent Claim
119 words
A process according to claim 1 wherein the hydrogenation catalyst comprises at least one hydrogenating component selected from the group consisting of the metals, metal sulfides and/or metal oxides of (a) a combination of about 2 to about 25 per cent by weight molybdenum and at least two iron group metals where the iron group metals are present in such amounts that the atomic ratio of each iron group metal with respect to molybdenum is less than about 0.4 and (b) a combination of about 5 to about 40 per cent by weight of nickel and tungsten where the atomic ratio of tungsten to nickel is about 1:0.1 to 5, said hydrogenating component being composited with a porous support.
Claim 12
Dependent Claim
22 words
A process according to claim 10 wherein the hydrogenating component of the catalyst is a sulfided combination of molybdenum, nickel and cobalt.
Claim 13
Dependent Claim
21 words
A process according to claim 10 wherein the hydrogenating component of the catalyst is a sulfided combination of nickel and tungsten.
Claim 14
Dependent Claim
35 words
A process according to claim 1 wherein the reaction zones are maintained at a temperature between about 500° and about 900°F. and a pressure between about 500 and about 10,000 pounds per square inch gauge.
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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) | 1979-04-13 | 1979-10-13 | 1980-04-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-04-13 | 1983-10-13 | 1984-04-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-04-13 | 1987-10-13 | 1988-04-13 | $7700.00 | Window Closed / Lapsed |