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US3979188A Expired / Lapsed US ⏱️ 0.0 years remaining

Partial oxidation carbon removal process

Assignee: Foster Wheeler Energy Corp
•
Filing: 1974-10-25
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Granted: 1976-09-07
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Expires: 1994-10-25
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Abstract

Abstract Unreacted carbon produced during the partial oxidation of fossil fuel is removed from the reactor gaseous effluent with water, resulting in a carbon-water slurry. The carbon-water slurry is concentrated to about five to seven percent by weight of carbon mixed with fuel and injected into the reactor for the dual purposes of utilizing the carbon contained in the slurry as the feedstock for the partial oxidation process and the water as a temperature moderator for the reactor.

Inventors

  • 👤 Robert A. McCallister

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 04:29
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/485; C10J3/72; C10J3/82; C10J3/84; C10K; C10K1/00; C10K1/08; C10K1/10; C10K1/101; C10J2300/00; C10J2300/09; C10J2300/0903; C10J2300/0906; C10J2300/0913; C10J2300/0946; C10J2300/0953; C10J2300/0973; C10J2300/18; C10J2300/1807; C10J2300/1846

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 155 words
A method for the recovery of unreacted carbon produced by reaction of fossil fuel and oxygen in a partial oxidation reactor to produce an effluent stream of synthesis gas and entrained carbon comprising of the steps of: washing the effluent stream with water to remove unreacted carbon therefrom to produce a stream of clean synthesis gas and a stream of water and entrained carbon, concentrating the stream of carbon and water formed during the cleaning step into a slurry of carbon and water containing about 5 to 7 percent by weight of carbon and producing a stream of relatively clean water substantially free of carbon, introducing said slurry into a vessel, combining the slurry in said vessel with a fuel oil, mixing said fuel oil and slurry in said vessel to produce a feed stream, then pumping the feed stream through a preheater and injecting the feed stream, without vaporization, into the partial oxidation reactor.
Claim 2
Independent Claim 155 words
A method for the recovery of unreacted carbon produced by reaction of fossil fuel and oxygen in a partial oxidation reactor to produce an effluent stream of synthesis gas and entrained carbon comprising of the steps of: washing the effluent stream with water to remove unreacted carbon therefrom to produce a stream of clean synthesis gas and a stream of water and entrained carbon, concentrating the stream of carbon and water formed during the cleaning step into a slurry of carbon and water containing about 5 to 7 percent by weight of carbon and producing a stream of relatively clean water substantially free of carbon, introducing said slurry into a vessel, combining the slurry in said vessel with a fuel oil, mixing said fuel oil and slurry in said vessel to produce a feed stream, then pumping the feed stream through a preheater and injecting the feed stream, without vaporization, into the partial oxidation reactor.
Claim 3
Dependent Claim 45 words
The method as described in claim 1 further including the steps of: removing the clean water produced during the concentration step and recirculating said clean water so removed for the washing step for removing further carbon from the effluent produced by the partial oxidation reactor.
Claim 4
Dependent Claim 23 words
The method as described in claim 1 wherein the concentration of the carbon in the water is about 5 to weight percent carbon.
Claim 5
Dependent Claim 32 words
The method of claim 1 wherein the step of combining the slurry and the fuel oil stream includes the step of recirculating said slurry and fuel oil stream in a surge area.
Claim 6
Dependent Claim 23 words
The method of claim 1 wherein the step of combining the slurry and fuel oil stream includes the step of agitating the mixture.

References Cited (Backward Citations)

US3010813A Cited
US3147093A Cited
US3349029A Cited
US3615297A Cited
US3671209A Cited
US3709669A Cited
US3866411A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-09-07 1980-03-08 1980-09-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-09-07 1984-03-08 1984-09-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-09-07 1988-03-08 1988-09-07 $7700.00 Window Closed / Lapsed

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