US4300913A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus and method for the manufacture of product gas
Assignee: NOELL-DBI ENERGIE-UND ENTSORGUNGSTECHNIK GmbH
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Filing: 1979-12-18
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Granted: 1981-11-17
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Expires: 1999-12-18
Abstract
Abstract Product gas resulting from the partial oxidation of finely divided fuel in a reactor is discharged as a stream into a tube leading downwardly into a vessel containing a water bath in which the lower end of the tube is immersed. Liquid slag produced during the partial oxidation is also discharged as a solid stream within and surrounded by the stream of product gas. The tube is cooled by circulating cooling water upwardly through an annular clearance in the tube which is discharged from the annular clearance at the upper end of the tube for gravity descent as a liquid film along the inside of the tube. The slag becomes cooled and granulated on contact with the water bath and is discharged from the vessel in granulated condition. The gas escapes from the lower open tube end, travels upwardly through the water bath to become cooled thereby, and is then discharged from the vessel in cooled condition.
Inventors
- 👤 Klaus Egert
- 👤 Wolfgang Heinrich
- 👤 Klaus Lucas
- 👤 Klaus-Otto Kuhlbrodt
- 👤 Friedrich Berger
- 👤 Peter Gohler
- 👤 Manfred Schingnitz
- 👤 Manfred Gross
- 👤 Aleksander Jegorow
- 👤 Vasilij Fedotov
- 👤 Vladimir Gavrilin
- 👤 Ernest Gudymov
- 👤 Vladimir Semenov
- 👤 Igol Achmatov
- 👤 Nikolaj Majdurov
- 👤 Evgenij Abraamov
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 09:34
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/72; C10J3/82; C10J3/84; C10J3/845; C10J3/46; C10J3/48; C10J3/52; C10J3/526; C10J3/74; C10J3/76; C10J3/78; C10K; C10K1/00; C10K1/08; C10K1/10; C10K1/101; C10J2300/00; C10J2300/18; C10J2300/1846; Y; Y10; Y10S; Y10S48/00; Y10S48/02
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
208 words
In a method of producing gas in a reactor by oxidation of finely divided fuel with concomitant formation of liquid slag, the steps of discharging from the reactor a stream of the product gas and a stream of liquid slag which travels within and is surrounded by the stream of product gas; passing the streams downwardly into a vessel through a straight central passage of a vertical doublewalled discharge tube having an annular clearance between its walls and also having a lower open end immersed in a water bath in the vessel; circulating a cooling liquid in counterflow to the streams through the annular clearance; admitting said cooling liquid at an upper end portion of the discharge tube from the annular clearance onto an inner surface of the discharge tube, for gravity descent on and along the inner surface as a liquid film which prevents local overheating or destruction of the tube; discharging the slag, which becomes cooled and granulated on entry into the water bath, from a lower part of the vessel; cooling the product gas during ascent of the same through the water bath from the lower open end of the discharge tube; and discharging the cooled product gas from an upper part of the vessel.
Claim 2
Dependent Claim
208 words
In a method of producing gas in a reactor by oxidation of finely divided fuel with concomitant formation of liquid slag, the steps of discharging from the reactor a stream of the product gas and a stream of liquid slag which travels within and is surrounded by the stream of product gas; passing the streams downwardly into a vessel through a straight central passage of a vertical doublewalled discharge tube having an annular clearance between its walls and also having a lower open end immersed in a water bath in the vessel; circulating a cooling liquid in counterflow to the streams through the annular clearance; admitting said cooling liquid at an upper end portion of the discharge tube from the annular clearance onto an inner surface of the discharge tube, for gravity descent on and along the inner surface as a liquid film which prevents local overheating or destruction of the tube; discharging the slag, which becomes cooled and granulated on entry into the water bath, from a lower part of the vessel; cooling the product gas during ascent of the same through the water bath from the lower open end of the discharge tube; and discharging the cooled product gas from an upper part of the vessel.
Claim 3
Dependent Claim
237 words
In an apparatus for producing gas by oxidation of finely divided fuel in a reactor with concomitant formation of liquid slag, a combination comprising a vessel having an upper part and a lower part for containing a water bath; a vertically oriented straight discharge tube extending downwardly from said upper part and having a lower open end immersed in the water bath, said tube also having double walls which define between themselves an annular clearance and an upper inlet for receiving a stream of product gas from the reactor and a stream of liquid slag which is within and surrounded by the gas stream so that the gas stream prevents contact between the slag and the discharge tube; means for circulating a cooling liquid through the annular clearance in counterflow to the gas and slag streams; means for admitting said cooling liquid at an upper end portion of the discharge tube from the annular clearance onto an inner surface of the discharge tube, for gravity descent on and along the inner surface as a liquid film which prevents local overheating or destruction of the tube; means for discharging from the lower part of the vessel the slag which has become cooled and granulated on entry into the water bath; and means for withdrawing from the upper part of the vessel the cooled product gas which has ascended from the lower open tube end through the water bath.
Claim 4
Dependent Claim
237 words
In an apparatus for producing gas by oxidation of finely divided fuel in a reactor with concomitant formation of liquid slag, a combination comprising a vessel having an upper part and a lower part for containing a water bath; a vertically oriented straight discharge tube extending downwardly from said upper part and having a lower open end immersed in the water bath, said tube also having double walls which define between themselves an annular clearance and an upper inlet for receiving a stream of product gas from the reactor and a stream of liquid slag which is within and surrounded by the gas stream so that the gas stream prevents contact between the slag and the discharge tube; means for circulating a cooling liquid through the annular clearance in counterflow to the gas and slag streams; means for admitting said cooling liquid at an upper end portion of the discharge tube from the annular clearance onto an inner surface of the discharge tube, for gravity descent on and along the inner surface as a liquid film which prevents local overheating or destruction of the tube; means for discharging from the lower part of the vessel the slag which has become cooled and granulated on entry into the water bath; and means for withdrawing from the upper part of the vessel the cooled product gas which has ascended from the lower open tube end through the water bath.
Claim 5
Dependent Claim
26 words
A method as defined in claim 1, wherein the flow speed of the stream of product gas in the discharge tube is between substantially 8-10 m/sec.
Claim 6
Dependent Claim
16 words
A combination as defined in claim 2, wherein said tube is arranged concentrically in said vessel.
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) | 1984-11-16 | 1985-05-18 | 1985-11-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-16 | 1989-05-18 | 1989-11-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-16 | 1993-05-18 | 1993-11-17 | $7700.00 | Window Closed / Lapsed |