US5560822A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus to remove inorganic scale from a supercritical water oxidation reactor
Assignee: 3500764 Canada Inc
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Filing: 1995-05-31
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Granted: 1996-10-01
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Expires: 2015-05-31
Abstract
Abstract A supercritical water oxidation reactor is alternately supplied with a feed stream and a flushing stream. The feed stream contains organic and inorganic materials. The organic materials are oxidized under supercritical conditions in the reactor and the inorganic materials precipitate out of solution under the same conditions. The flushing stream is a solution in which the inorganic material is soluble. More than one supercritical water oxidation reactor may be connected so that the feed stream is alternately supplied to each reactor. During the period when the feed stream is being supplied to a reactor the effluent from the reactor is cooled to a temperature at which inorganic precipitates are soluble and is then supplied as a flushing stream to one or more of the remaining connected supercritical water oxidation reactors.
Inventors
- 👤 Luke D. Bond
- 👤 Charles C. Mills
- 👤 Philip Whiting
- 👤 Stanley L. Koutz
- 👤 David A. Hazlebeck
- 👤 Kevin W. Downey
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 04:52
CPC Classifications
C; C02; C02F; C02F11/00; C02F11/06; C02F11/08; C02F11/086; C02F1/00; C02F1/72
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
133 words
A reactor combination for oxidizing a feed stream comprising organic compounds, inorganic compounds and water the reactor combination comprising: a) two or more connected supercritical water oxidation reactors; b) means to allow said feed stream and oxidant to be directed for oxidation in any one of said reactors; c) means to allow an effluent stream from said any one of said reactors to cool to a temperature and pressure at which inorganic precipitate formed under supercritical conditions is soluble; d) means to allow said cooled effluent stream to be directed as a flushing stream to at least one other of said two or more connected supercritical water oxidation reactors to remove inorganic precipitate therefrom, wherein each reactor has a means for alternately supplying said feed stream and said flushing stream to said reactor.
Claim 2
Dependent Claim
133 words
A reactor combination for oxidizing a feed stream comprising organic compounds, inorganic compounds and water the reactor combination comprising: a) two or more connected supercritical water oxidation reactors; b) means to allow said feed stream and oxidant to be directed for oxidation in any one of said reactors; c) means to allow an effluent stream from said any one of said reactors to cool to a temperature and pressure at which inorganic precipitate formed under supercritical conditions is soluble; d) means to allow said cooled effluent stream to be directed as a flushing stream to at least one other of said two or more connected supercritical water oxidation reactors to remove inorganic precipitate therefrom, wherein each reactor has a means for alternately supplying said feed stream and said flushing stream to said reactor.
Claim 3
Dependent Claim
37 words
The reactor combination of claim 1 further including means to allow said effluent stream to be directed as a heating stream to preheat at least one other of said two or more connected supercritical water oxidation reactors.
Claim 4
Dependent Claim
222 words
A reactor combination for oxidizing a feed stream comprising organic compounds, inorganic compounds and water, the reactor combination comprising: a) two or more connected supercritical water oxidation reactors, each of said reactors have a pair of ends for receiving and/or discharging said feed stream; b) means to allow said feed stream and oxidant to be directed for oxidation in any of one of said reactors, said means including valves located at each end of said reactors; c) means to allow an effluent stream from any one of said reactors to cool to a temperature and pressure at which inorganic precipitate formed under supercritical conditions is soluble; and d) valve means to allow said cooled effluent stream to be directed as a flushing stream to at least one other of said two or more connected supercritical water oxidation reactors operating at subcritical conditions to remove inorganic precipitate therefrom, said valve means located at each end of said reactors wherein one portion of said valve means is in the open position to allow said cooled effluent stream to be directed as said flushing stream, while another portion is in the closed position to prevent said feed stream from entering said reactors operating at subcritical conditions, wherein each reactor has a means for alternately supplying said feed stream and said flushing stream to said reactor.
Claim 5
Dependent Claim
222 words
A reactor combination for oxidizing a feed stream comprising organic compounds, inorganic compounds and water, the reactor combination comprising: a) two or more connected supercritical water oxidation reactors, each of said reactors have a pair of ends for receiving and/or discharging said feed stream; b) means to allow said feed stream and oxidant to be directed for oxidation in any of one of said reactors, said means including valves located at each end of said reactors; c) means to allow an effluent stream from any one of said reactors to cool to a temperature and pressure at which inorganic precipitate formed under supercritical conditions is soluble; and d) valve means to allow said cooled effluent stream to be directed as a flushing stream to at least one other of said two or more connected supercritical water oxidation reactors operating at subcritical conditions to remove inorganic precipitate therefrom, said valve means located at each end of said reactors wherein one portion of said valve means is in the open position to allow said cooled effluent stream to be directed as said flushing stream, while another portion is in the closed position to prevent said feed stream from entering said reactors operating at subcritical conditions, wherein each reactor has a means for alternately supplying said feed stream and said flushing stream to said reactor.
Claim 6
Dependent Claim
49 words
The reactor combination of claim 3 further including heat exchanger means and valve means to allow said effluent stream from at least one of said reactors to be directed as a heating stream to preheat at least one other of said two or more connected supercritical water oxidation reactors.
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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) | 1999-10-01 | 2000-04-01 | 2000-10-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2003-10-01 | 2004-04-01 | 2004-10-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2007-10-01 | 2008-04-01 | 2008-10-01 | $7700.00 | Window Closed / Lapsed |