US4336034A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the catalytic gasification of coal
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1980-03-10
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Granted: 1982-06-22
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Expires: 2000-03-10
Abstract
Abstract Carbonaceous solids are contacted in the presence of water with potassium sulfate and a calcium compound selected from the group consisting of calcium oxide, calcium hydroxide, and calcium carbonate thereby producing treated carbonaceous solids which are then gasified. The calcium compound apparently activates the relatively noncatalytic potassium sulfate thereby producing a substantial catalytic effect on the gasification reactions.
Inventors
- 👤 Robert J. Lang
- 👤 Joanne K. Pabst
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 14:34
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/482; C10J3/54; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0973; C10J2300/0983; C10J2300/0986; C10J2300/18; C10J2300/1807; C10J2300/1853; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
184 words
A process for the catalytic steam gasification of coal which comprises: (a) contacting said coal in the presence of water with potassium sulfate and a calcium compound selected from the group consisting of calcium oxide and calcium hydroxide in a contacting zone to produce a treated coal, wherein said calcium compound is present in a sufficient quantity to activate said potassium sulfate; (b) passing said treated coal from said contacting zone into a gasification zone; and (c) gasifying said treated coal with steam at a temperature between about 1200° F. and about 1400° F. in said gasification zone, wherein said potassium sulfate and said calcium compound are introduced into said contacting zone in sufficient amounts to obtain gasification rates substantially greater than the weighted average of the separate rates that would be obtained if said potassium sulfate or calcium compound were introduced alone into said contacting zone in sufficient amounts to give a cation-to-carbon atomic ratio equal to the sum of the potassium-to-carbon and calcium-to-carbon atomic ratios given by the amount of said potassium and said calcium compound actually introduced into said contacting zone.
Claim 2
Dependent Claim
184 words
A process for the catalytic steam gasification of coal which comprises: (a) contacting said coal in the presence of water with potassium sulfate and a calcium compound selected from the group consisting of calcium oxide and calcium hydroxide in a contacting zone to produce a treated coal, wherein said calcium compound is present in a sufficient quantity to activate said potassium sulfate; (b) passing said treated coal from said contacting zone into a gasification zone; and (c) gasifying said treated coal with steam at a temperature between about 1200° F. and about 1400° F. in said gasification zone, wherein said potassium sulfate and said calcium compound are introduced into said contacting zone in sufficient amounts to obtain gasification rates substantially greater than the weighted average of the separate rates that would be obtained if said potassium sulfate or calcium compound were introduced alone into said contacting zone in sufficient amounts to give a cation-to-carbon atomic ratio equal to the sum of the potassium-to-carbon and calcium-to-carbon atomic ratios given by the amount of said potassium and said calcium compound actually introduced into said contacting zone.
Claim 3
Dependent Claim
14 words
A process as defined by claim 1 wherein said calcium compound comprises calcium hydroxide.
Claim 4
Dependent Claim
30 words
A process as defined by claim 1 wherein said calcium compound is present in a sufficient quantity to yield a potassium-to-calcium atomic ratio of between about 1.33 and about 4.0.
Claim 5
Dependent Claim
38 words
A process as defined by claim 1 wherein said coal is contacted with said potassium sulfate and said calcium compound in the presence of water for a period of time between about 30 minutes and about 120 minutes.
Claim 6
Dependent Claim
15 words
A process as defined by claim 1 wherein said coal comprises a low rank coal.
Claim 7
Dependent Claim
14 words
A process as defined by claim 1 wherein said calcium compound comprises calcium oxide.
Claim 8
Dependent Claim
26 words
A process as defined by claim 3 wherein said calcium compound is present in a sufficient quantity to yield a potassium-to-calcium atomic ratio of about 2.0.
Claim 9
Dependent Claim
14 words
A process as defined by claim 1 wherein said carbonaceous solids comprise subbituminous coal.
Claim 10
Dependent Claim
13 words
A process as defined by claim 1 wherein said carbonaceous solids comprise lignite.
References Cited (Backward Citations)
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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) | 1985-06-21 | 1985-12-21 | 1986-06-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-06-21 | 1989-12-21 | 1990-06-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-06-21 | 1993-12-21 | 1994-06-22 | $7700.00 | Window Closed / Lapsed |