US4272256A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for heating oxygen containing gas in conjunction with a gasification system
Assignee: Beazer East Inc
•
Filing: 1979-10-15
•
Granted: 1981-06-09
•
Expires: 1999-10-15
Abstract
Abstract A process is provided for the gasification of a carbonaceous fuel to produce a synthesis gas whereby a secondary stream of oxygen is indirectly heated from said synthesis gas and passed to the gasifier to augment the primary oxygen supply.
Inventors
- 👤 Dimitri M. Mitsak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 16:09
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/485; C10J3/72; C10J3/723; C10J3/78; C10J3/82; C10J3/84; C10J3/845; C10J3/86; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0973; C10J2300/0976; Y; Y10; Y10S; Y10S48/00; Y10S48/04
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
158 words
A process for the gasification of a carbonaceous fuel comprising: (a) feeding a mixture of primary oxygen, steam and fuel to a reaction zone to produce a synthesis gas from said mixture; (b) heating secondary oxygen indirectly from said synthesis gas wherein said step of heating said secondary oxygen includes removing heat from said synthesis gas in a first heat exchanger by heat exchange with a heat transfer gas which does not form an explosive mixture with the synthesis gas, and transferring the heat from the heat transfer gas to said secondary oxygen in a second heat exchanger and circulating the heat transfer gas between said first and second heat exchangers at a pressure which is at all times greater than the pressure of the secondary oxygen to prevent flow of secondary oxygen into the synthesis gas in the event of a leak in the second heat exchanger; and (c) feeding said secondary oxygen to said reaction zone.
Claim 2
Dependent Claim
158 words
A process for the gasification of a carbonaceous fuel comprising: (a) feeding a mixture of primary oxygen, steam and fuel to a reaction zone to produce a synthesis gas from said mixture; (b) heating secondary oxygen indirectly from said synthesis gas wherein said step of heating said secondary oxygen includes removing heat from said synthesis gas in a first heat exchanger by heat exchange with a heat transfer gas which does not form an explosive mixture with the synthesis gas, and transferring the heat from the heat transfer gas to said secondary oxygen in a second heat exchanger and circulating the heat transfer gas between said first and second heat exchangers at a pressure which is at all times greater than the pressure of the secondary oxygen to prevent flow of secondary oxygen into the synthesis gas in the event of a leak in the second heat exchanger; and (c) feeding said secondary oxygen to said reaction zone.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the heat transfer gas used to remove heat from the synthesis gas is carbon dioxide.
References Cited (Backward Citations)
US1098534A
Cited
US1799885A
Cited
GB255849A
Cited
US1913968A
Cited
US2311140A
Cited
US2699758A
Cited
US2919980A
Cited
US3818869A
Cited
US4137965A
Cited
US4044820A
Cited
US4184322A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-06-08 | 1984-12-08 | 1985-06-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-06-08 | 1988-12-08 | 1989-06-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-06-08 | 1992-12-08 | 1993-06-09 | $7700.00 | Window Closed / Lapsed |