US3988238A
Expired / Lapsed
US
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Process for recovering upgraded products from coal
Assignee: BP Corp North America Inc
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Filing: 1974-07-01
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Granted: 1976-10-26
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Expires: 1994-07-01
Abstract
Abstract A process for recovering and upgrading products from solid coal by contacting the coal with a dense-water-containing fluid at a temperature in the range of from about 600° F. to about 900° F. in the absence of externally supplied hydrogen or other reducing gas and in the presence of a sulfur-resistant catalyst.
Inventors
- 👤 John D. McCollum
- 👤 Leonard M. Quick
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 08:47
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/08; C10G1/083; Y; Y10; Y10S; Y10S208/00; Y10S208/952
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
235 words
A process for recovering upgraded products from coal solids, comprising contacting the coal solids with a water-containing fluid, to thereby produce gases, liquids, and upgraded solids from the coal solids, under super-atmospheric pressure, at a temperature in the range of from about 600° F. to about 900° F. in the absence of externally supplied hydrogen or other reducing gas, and in the presence of an externally supplied, sulfur-resistant catalyst, selected from the group consisting of at least one basic metal carbonate, basic metal hydroxide, transition metal oxide, oxide-forming transition metal salt, and combinations thereof, wherein said catalyst is present in a catalytically effective amount, wherein the transition metal in the oxide and salt is selected from the group consisting of a transition metal of Group IVB, VB, VIB, and VIIB of the Periodic Chart and the metal in the basic metal carbonate and hydroxide is selected from the group consisting of alkali metals, and wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.10 gram per milliliter and serves as an effective solvent for the liquids and gases produced from the coal solids; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for such liquids and gases and to thereby form separate phases.
Claim 2
Dependent Claim
235 words
A process for recovering upgraded products from coal solids, comprising contacting the coal solids with a water-containing fluid, to thereby produce gases, liquids, and upgraded solids from the coal solids, under super-atmospheric pressure, at a temperature in the range of from about 600° F. to about 900° F. in the absence of externally supplied hydrogen or other reducing gas, and in the presence of an externally supplied, sulfur-resistant catalyst, selected from the group consisting of at least one basic metal carbonate, basic metal hydroxide, transition metal oxide, oxide-forming transition metal salt, and combinations thereof, wherein said catalyst is present in a catalytically effective amount, wherein the transition metal in the oxide and salt is selected from the group consisting of a transition metal of Group IVB, VB, VIB, and VIIB of the Periodic Chart and the metal in the basic metal carbonate and hydroxide is selected from the group consisting of alkali metals, and wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.10 gram per milliliter and serves as an effective solvent for the liquids and gases produced from the coal solids; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for such liquids and gases and to thereby form separate phases.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the density of water in the water-containing fluid is at least 0.15 gram per milliliter.
Claim 4
Dependent Claim
21 words
The processs of claim 2 wherein the density of water in the water-containing fluid is at least 0.2 gram per milliliter.
Claim 5
Dependent Claim
13 words
The process of claim 1 wherein the temperature is at least 705° F.
Claim 6
Dependent Claim
31 words
The process of claim 1 wherein the coal solids and water-containing fluid are contacted for a period of time in the range of from about 1 minute to about 6 hours.
Claim 7
Dependent Claim
31 words
The process of claim 5 wherein the coal solids and water-containing fluid are contacted for a period of time in the range of from about 5 minutes to about 3 hours.
Claim 8
Dependent Claim
31 words
The process of claim 6 wherein the coal solids and water-containing fluid are contacted for a period of time in the range of from about 10 minutes to about 1 hour.
Claim 9
Dependent Claim
27 words
The process of claim 1 wherein the weight ratio of coal solids-to-water in the water-containing fluid is in the range of from about 3:2 to about 1:10.
Claim 10
Dependent Claim
27 words
The process of claim 8 wherein the weight ratio of coal solids-to-water in the water-containing fluid is in the range of from about 1:1 to about 1:3.
Claim 11
Dependent Claim
12 words
The process of claim 1 wherein the water-containing fluid is substantialaly water.
Claim 12
Dependent Claim
11 words
The process of claim 1 wherein the water-containing fluid is water.
Claim 13
Dependent Claim
18 words
The process of claim 1 wherein the coal solids have a maximum particle size of one-half inch diameter.
Claim 14
Dependent Claim
18 words
The process of claim 12 wherein the coal solids have a maximum particle size of one-quarter inch diameter.
Claim 15
Dependent Claim
17 words
The process of claim 13 wherein the coal solids have a maximum particle size of 8 mesh.
Claim 16
Dependent Claim
39 words
The process of claim 1 wherein the water-containing fluid contains an organic material selected from the group consisting of biphenyl, pyridine, a highly saturated oil, an aromatic oil, a partly hydrogenated aromatic oil, and a mono- or polyhydric compound.
Claim 17
Dependent Claim
31 words
The process of claim 15 wherein the water-containing fluid contains an organic material selected from the group consisting of biphenyl, pyridine, a highly saturated oil, and a mono- or polyhydric compound.
Claim 18
Dependent Claim
14 words
The process of claim 16 wherein the water-containing fluid contains a highly saturated oil.
Claim 19
Dependent Claim
32 words
The process of claim 1 wherein the transition metal in the oxide and salt is selected from the group consisting of vanadium, chromium, manganese, titanium, molybdenum, zirconium, niobium, tantalum, rhenium, and tungsten.
Claim 20
Dependent Claim
27 words
The process of claim 18 wherein the transition metal in the oxide and salt is selected from the group consisting of chromium, manganese, titanium, tantalum, and tungsten.
Claim 21
Dependent Claim
25 words
The process of claim 1 wherein the metal in the basic metal carbonate and hydroxide is selected from the group consisting of sodium and potassium.
Claim 22
Dependent Claim
41 words
The process of claim 1 wherein the catalyst is present in a catalytically effective amount which is equivalent to a concentration level in the water in the water-containing fluid in the range of from about 0.01 to about 3.0 weight percent.
Claim 23
Dependent Claim
41 words
The process of claim 21 wherein the catalyst is present in a catalytically effective amount which is equivalent to a concentration level in the water in the water-containing fluid in the range of from about 0.10 to about 0.50 weight percent.
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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) | 1979-10-26 | 1980-04-26 | 1980-10-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-26 | 1984-04-26 | 1984-10-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-26 | 1988-04-26 | 1988-10-26 | $7700.00 | Window Closed / Lapsed |