Patent US4019314A successfully refreshed from Google Patents.
US4019314A
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High pressure gasification of coal using nitrogen dilution of waste gas from steam generator
Assignee: Linde GmbH
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Filing: 1976-01-27
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Granted: 1977-04-26
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Expires: 1996-01-27
Abstract
Abstract In a process for the production of a fuel gas by the pressure gasification of carbon-containing fuels with oxygen and steam, wherein the oxygen is manufactured in a low temperature air separation plant and the steam is formed in a gas-heated steam boiler, and the waste gases produced in the steam boiler are subsequently expanded in an expansion turbine, the improvement which comprises admixing the nitrogen produced during the air separation with the waste gases before the expansion of the latter.
Inventors
- 👤 Helmut Springmann
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 05:10
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/02; C10J3/06; C10J3/16; C10J3/72; C10J3/721; F; F01; F01K; F01K23/00; F01K23/02; F01K23/06; F01K23/067; F01K23/068; F02; F02C; F02C3/00; F02C3/20; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04006; F25J3/04012; F25J3/04018; F25J3/04024; F25J3/04036; F25J3/04109; F25J3/04115; F25J3/04127; F25J3/04139; F25J3/04145; F25J3/04521; F25J3/04527; F25J3/04539; F25J3/04545; F25J3/04563; F25J3/04575; F25J3/04581; F25J3/04593; F25J3/046; F25J3/04612; C10J2300/00; C10J2300/09; C10J2300/0953; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/16; C10J2300/1671; C10J2300/18; C10J2300/1807; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y02; Y02E; Y02E20/00; Y02E20/16; Y02E20/18
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
81 words
In a process for the production of a fuel gas by the pressure gasification of carbon-containing fuels with oxygen and steam, wherein the oxygen is manufactured in a low temperature air separation plant and the steam is formed in a gas-heated steam boiler, and the waste gases produced in the steam boiler are subsequently expanded in an expansion turbine, the improvement which comprises admixing the nitrogen produced during the air separation with the waste gases before the expansion of the latter.
Claim 2
Dependent Claim
81 words
In a process for the production of a fuel gas by the pressure gasification of carbon-containing fuels with oxygen and steam, wherein the oxygen is manufactured in a low temperature air separation plant and the steam is formed in a gas-heated steam boiler, and the waste gases produced in the steam boiler are subsequently expanded in an expansion turbine, the improvement which comprises admixing the nitrogen produced during the air separation with the waste gases before the expansion of the latter.
Claim 3
Dependent Claim
32 words
A process according to claim 1, wherein the expansion of the waste gases is conducted in two stages and the nitrogen is admixed to the waste gases between the two expansion stages.
Claim 4
Dependent Claim
28 words
A process according to claim 2, wherein the waste gases are expanded in the first expansion stage to the pressure of the nitrogen leaving the air separation plant.
Claim 5
Dependent Claim
31 words
A process according to claim 1, wherein mechanical energy obtained during the expansion of the admixture of waste gases and nitrogen is utilized for compressing the air required in the process.
Claim 6
Dependent Claim
25 words
A process according to claim 1, wherein a portion of the fuel gas obtained as the product is branched off for heating the steam boiler.
Claim 7
Dependent Claim
32 words
A process according to claim 1, wherein the gas required for heating the steam boiler is produced in an auxiliary gasifier charged with carbon-containing fuels and operated with compressed air and steam.
Claim 8
Dependent Claim
24 words
A process according to claim 6, characterized in that the auxiliary gasifier is operated at the upper pressure level of the air separation plant.
Claim 9
Dependent Claim
71 words
A process according to claim 6, wherein the expansion of the waste gases is conducted in two stages and the nitrogen is admixed to the waste gases between the two expansion stages, wherein the waste gases, after the first expansion, but before the admixture with the nitrogen are reheated by indirect heat exchange with the gas produced in the auxiliary gasifier, and before the latter gas is cooled in a scrubber-cooler.
Claim 10
Dependent Claim
43 words
A process according to claim 2, wherein the waste gases are expanded from 10 to 20 bars to about 5 to 10 bars in the first stage of expansion and then to about 1.2 to 5 bars in the second stage of expansion.
Claim 11
Dependent Claim
31 words
A process according to claim 1, wherein the volumetric ratio of added nitrogen to the waste gas in the mixture thereof is about 0.5 : 1 to about 5 : 1.
Claim 12
Dependent Claim
30 words
A process according to claim 1, wherein the volumetric ratio of added nitrogen to the waste gas in the mixture thereof is about 2 : 1 to 5 : 1.
Claim 13
Dependent Claim
22 words
A process according to claim 1 wherein the waste gases prior to the admixing step, are at a temperature of 800-1000° C.
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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) | 1980-04-25 | 1980-10-25 | 1981-04-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-04-25 | 1984-10-25 | 1985-04-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-04-25 | 1988-10-25 | 1989-04-26 | $7700.00 | Window Closed / Lapsed |