US2687950A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Gasification of carbonaceous solids to hydrogen-rich gas and fuel gas
Assignee: Hydrocarbon Research Inc
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Filing: 1949-04-08
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Granted: 1954-08-31
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Expires: 1969-04-08
Abstract
No abstract record available.
Inventors
- 👤 John C Kalbach
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 04:13
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/463; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0933; Y; Y10; Y10S; Y10S48/00; Y10S48/04
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
189 words
A PROCESS FOR THE GASIFICATION OF A SOLID CARBONACEOUS MATERIAL CONTAINING VOLATILIZABLE CONSTITUENTS WHICH COMPRISES INTRODUCING SAID SOLID CARBONACEOUS MATERIAL INTO A CARBONIZATION ZONE INTO DIRECT CONTACT WITH HOT GASES COMPRISING CARBON MONOXIDE AND HYDROGEN AT A TEMPERATURE WITHIN THE RANGE OF FROM 1,000* F. TO 1,500* F. AND A PRESSURE WITHIN THE RANGE OF 100 TO 800 POUNDS PER SQUARE INCH GAUGE WHEREBY VOLATILIZABLE CONSTITUENTS ARE VOLATILIZED AND METHANE IS FORMED; INTRODUCING THE RESULTING CARBONACEOUS RESIDUE FROM THE CARBONIZATION ZONE INTO A GASIFICATION ZONE, REACTING SAID RESIDUE WITH A MIXTURE OF OXYGEN AND STEAM AT A TEMPERATURE WITHIN THE RANGE OF FROM 1,400* F. TO 2,100* F., TO PRODUCE CARBON MONOXIDE AND HYDROGEN AS PRINCIPAL REACTION PRODUCTS; PASSING THE RESULTING GASES FROM THE GASIFICATION ZONE TO THE CARBONIZATION ZONE AS THE SOURCE OF HOT GASES; DISCHARGING PRODUCT GASES FROM THE CARBONIZATION ZONE; SEPARATING ENTRAINED SOLIDS AND READILY LIQUEFIABLE CONSTITUENTS THEREFROM; AND SUBJECTING THE RESIDUAL GASEOUS PRODUCT COMPRISING CARBON MONOXIDE, HYDROGEN AND METHANE TO LIQUEFACTION AND FRACTIONAL DISTILLATION TO OBTAIN A METHANE-RICH FUEL GAS AND SYNTHESIS GAS COMPRISING CARBON MONOXIDE AND HYDROGEN IN SUBSTANTIAL PROPORTIONS ADAPTED FOR FISCHER-TROPSCH SYNTHESIS.
Claim 2
Dependent Claim
189 words
A PROCESS FOR THE GASIFICATION OF A SOLID CARBONACEOUS MATERIAL CONTAINING VOLATILIZABLE CONSTITUENTS WHICH COMPRISES INTRODUCING SAID SOLID CARBONACEOUS MATERIAL INTO A CARBONIZATION ZONE INTO DIRECT CONTACT WITH HOT GASES COMPRISING CARBON MONOXIDE AND HYDROGEN AT A TEMPERATURE WITHIN THE RANGE OF FROM 1,000* F. TO 1,500* F. AND A PRESSURE WITHIN THE RANGE OF 100 TO 800 POUNDS PER SQUARE INCH GAUGE WHEREBY VOLATILIZABLE CONSTITUENTS ARE VOLATILIZED AND METHANE IS FORMED; INTRODUCING THE RESULTING CARBONACEOUS RESIDUE FROM THE CARBONIZATION ZONE INTO A GASIFICATION ZONE, REACTING SAID RESIDUE WITH A MIXTURE OF OXYGEN AND STEAM AT A TEMPERATURE WITHIN THE RANGE OF FROM 1,400* F. TO 2,100* F., TO PRODUCE CARBON MONOXIDE AND HYDROGEN AS PRINCIPAL REACTION PRODUCTS; PASSING THE RESULTING GASES FROM THE GASIFICATION ZONE TO THE CARBONIZATION ZONE AS THE SOURCE OF HOT GASES; DISCHARGING PRODUCT GASES FROM THE CARBONIZATION ZONE; SEPARATING ENTRAINED SOLIDS AND READILY LIQUEFIABLE CONSTITUENTS THEREFROM; AND SUBJECTING THE RESIDUAL GASEOUS PRODUCT COMPRISING CARBON MONOXIDE, HYDROGEN AND METHANE TO LIQUEFACTION AND FRACTIONAL DISTILLATION TO OBTAIN A METHANE-RICH FUEL GAS AND SYNTHESIS GAS COMPRISING CARBON MONOXIDE AND HYDROGEN IN SUBSTANTIAL PROPORTIONS ADAPTED FOR FISCHER-TROPSCH SYNTHESIS.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1957-08-30 | 1958-03-01 | 1958-08-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1961-08-30 | 1962-03-01 | 1962-08-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1965-08-30 | 1966-03-01 | 1966-08-31 | $7700.00 | Window Closed / Lapsed |