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US5560823A Expired / Lapsed US ⏱️ 0.0 years remaining

Reversible flow supercritical reactor and method for operating same

Assignee: Abitibi Price Inc
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Filing: 1994-12-21
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Granted: 1996-10-01
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Expires: 2014-12-21
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Abstract

Abstract A supercritical water oxidation reactor is described having first and second reaction zones connnected in series and through which an aqueous feed stream to be oxidized can be passed in either direction. A self-contained heat exchange fluid system allows supercritical and subcritical temperatures to be maintained in either reaction zone. When supercritical water oxidation is occuring in one reaction zone the effluent is being cooled to a subcritical temperature and used to flush the second reaction zone to remove inorganic scale.

Inventors

  • 👤 Philip Whiting

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 14:11
CPC Classifications
B; B01; B01J; B01J3/00; B01J3/008; C; C02; C02F; C02F11/00; C02F11/06; C02F11/08; C02F11/086; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/54

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 220 words
A reversible flow supercritical water oxidation reactor for oxidizing an aqueous feed stream comprising: a) a reactor for the supercritical water oxidation of organic compounds, said reactor having a first end and a second end and having first and second reaction zones therebetween connected in series through which an aqueous feed stream to be oxidized can be passed in either direction; b) a self-contained heat exchange fluid system for allowing supercritical and subcritical temperatures to be maintained alternatively in either reaction zone, wherein said heat exchange fluid system comprises a heat exchange fluid reservoir and heat exchangers defining at least three heat exchange zones between said first and second ends of said reactor; and means for directing heat exchange fluid between said heat exchange zones whereby preheating of incoming aqueous feed steam occurs alternately at either of said first and second ends of said reactor and whereby supercritical conditions occur at the one of said first and second reaction zones that is immediately downstream of said end of said reactor at which said preheating occurs and the other of said reaction zones is operated at subcritical conditions, wherein said supercritical and subcritical conditions are achieved by said means for directing heat exchange fluid and wherein said first and second reaction zones are separated by one of said heat exchange zones.
Claim 2
Dependent Claim 220 words
A reversible flow supercritical water oxidation reactor for oxidizing an aqueous feed stream comprising: a) a reactor for the supercritical water oxidation of organic compounds, said reactor having a first end and a second end and having first and second reaction zones therebetween connected in series through which an aqueous feed stream to be oxidized can be passed in either direction; b) a self-contained heat exchange fluid system for allowing supercritical and subcritical temperatures to be maintained alternatively in either reaction zone, wherein said heat exchange fluid system comprises a heat exchange fluid reservoir and heat exchangers defining at least three heat exchange zones between said first and second ends of said reactor; and means for directing heat exchange fluid between said heat exchange zones whereby preheating of incoming aqueous feed steam occurs alternately at either of said first and second ends of said reactor and whereby supercritical conditions occur at the one of said first and second reaction zones that is immediately downstream of said end of said reactor at which said preheating occurs and the other of said reaction zones is operated at subcritical conditions, wherein said supercritical and subcritical conditions are achieved by said means for directing heat exchange fluid and wherein said first and second reaction zones are separated by one of said heat exchange zones.
Claim 3
Dependent Claim 18 words
The reversible flow supercritical water oxidation reactor of claim 1 in which the reactor is a pipe reactor.
Claim 4
Dependent Claim 19 words
The reversible flow supercritical water oxidation reactor of claim 1 which the heat exchange fluid is at low pressure.
Claim 5
Dependent Claim 22 words
The reversible flow supercritical water oxidation reactor of claim 1 in which the heat exchangers are shells in contact with the reactor.

References Cited (Backward Citations)

US2665249A Cited
US2944396A Cited
US4292953A Cited
US4338199A Cited
US4543190A Cited
US4338199B1 Cited
US4822497A Cited
US5100560A Cited
US5252224A Cited

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

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