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US3861885A Expired / Lapsed US ⏱️ 0.0 years remaining

Carbon black fuel production

Assignee: Gas Technology Institute
•
Filing: 1973-11-05
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Granted: 1975-01-21
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Expires: 1993-11-05
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Abstract

Abstract The application discloses a method of production of nonpolluting ash free, sulfur free carbon black solid fuel from a polluting solid carbonaceous fossil fuel, such as coal or coal char. The coal is first pretreated to remove a hydrocarbon stream and the resultant devolatilized coal is gasified to produce carbon monoxide and hydrogen preferably with substantially no entrained produced carbon. The carbon monoxide and hydrogen product gases are then cooled under controlled conditions in a fluidized bed to precipitate out carbon black in a finely divided state. At least a portion of the hydrocarbon stream, preferably after sulfur removal by hydrodesulphurization, is then admixed with the carbon black product to produce a product useful as a nonpolluting ash free, sulfur free fuel for coal-fired turbines, as an additive to diesel fuel, and as a material for pipelining to areas where air pollution ordinances require a fuel with low sulfur content. The process disclosed for converting coal or coal char to a solid carbon black suitable for use as a nonpolluting fuel includes four basic steps: (a) devolatilization of the coal to produce a hydrocarbon stream; (b) production of a hot carbon oxide containing gas, rich in carbon monoxide, by partial combustion of the devolatilized coal with air, oxygen or an oxygen enriched air, at elevated temperature and pressure under catalytic conditions; (c) controlled removal of heat from the gas in a fluidized bed to promote the deposition of carbon; and (d) admixing at least a portion of the hydrocarbon stream, preferably after desulphurization, with the carbon produced. Preferably, the hot gas is enriched by intermediate clean-up to remove particulate matter and sulfur. All steps are preferably conducted at high pressures which favor formation of carbon and carbon dioxide from carbon monoxide. Preferably, substantially no carbon is formed in the first step, and the carbon deposition step is not appreciably auto-catalytic with respect to carbon deposition.

Inventors

  • 👤 Frank C Schora

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 15:08
CPC Classifications
C; C10; C10L; C10L5/00; C09; C09C; C09C1/00; C09C1/44; C09C1/48; C09C1/56; C10L1/00; C10L1/32; C10L1/322; C10L9/00; C10L9/02; C01; C01P; C01P2006/00; C01P2006/80; F; F02; F02B; F02B3/00; F02B3/06; Y; Y02; Y02A; Y02A50/00; Y02A50/20

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 13 words
A process as in claim 1 in which said oxygen-containing gas is air.
Claim 2
Dependent Claim 22 words
A process as in claim 1 in which said carbonaceous fossil fuel is coal 80% reduced in size to minus quarter mesh.
Claim 3
Dependent Claim 59 words
A process as in claim 1 in which said oxidation step includes the steps of: i. combusting a portion of said carbonaceous fossil fuel with said oxygen-containing gas to produce a combustion gas rich in CO2 and H2O, and ii. reacting said CO2 and H2O with the remainder of said solid fossil fuel to produce said carbon monoxide-rich gas.
Claim 4
Dependent Claim 13 words
A process as in claim 4 in which said oxygen-containing gas is air.
Claim 5
Dependent Claim 23 words
A process as in claim 1 which includes maintaining said coal that is oxidized with said combustion gas in a substantially fluidized condition.
Claim 6
Dependent Claim 36 words
A process as in claim 1 which includes the steps of: a. reacting residual carbon oxides in said exhaust gases with hydrogen to form carbon monoxide, and b. recycling said carbon monoxide to said fluidized bed.
Claim 7
Dependent Claim 16 words
A process as in claim 1 wherein said heat exchange surfaces are disposed in said bed.
Claim 8
Dependent Claim 26 words
A process as in claim 1 wherein said solid bed material is a catalyst capable of promoting carbon formation and promoting a water gas shift reaction.
Claim 9
Dependent Claim 33 words
A process as in claim 1 wherein said solid bed material is in the form of granules substantially spherical in shape, and range from about 100 U.S. mesh to one-quarter inch in diameter.
Claim 10
Dependent Claim 30 words
A process as in claim 9 wherein said catalyst is selected from iron, cobalt, and nickel, alloys thereof, and oxides, hydroxides and carbonates of sodium, cobalt, nickel and alloys thereof.
Claim 11
Dependent Claim 17 words
A process as in claim 11 wherein said catalyst is a mixture of iron and iron oxides.
Claim 12
Dependent Claim 11 words
A process as in claim 12 wherein said catalyst is Wustite.
Claim 13
Dependent Claim 24 words
A process as in claim 1 wherein the desulphurized hydrOcarbon is admixed with the carbon by passing the liquid to the carbon deposition zone.
Claim 14
Dependent Claim 19 words
A process as in claim 1 where the desulphurized hydrocarbon is vaporized prior to admixing with the carbon black.
Claim 15
Dependent Claim 29 words
A process as in claim 1 wherein the desulphurized hydrocarbon is admixed with the carbon in the amount of 1 to about 25 wt. % of the final product.
Claim 16
Dependent Claim 23 words
A process as in claim 1 wherein a portion of the hydrocarbon stream is passed to the oxidation step for conversion to CO.
Claim 17
Dependent Claim 15 words
A process as in claim 1 wherein the hydrocarbon stream is also subjected to cracking.

References Cited (Backward Citations)

US1693356A Cited
US1894126A Cited
US1812230A Cited
US1964744A Cited
US2631934A Cited
US2716053A Cited
US3733183A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-01-20 1978-07-22 1979-01-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-01-20 1982-07-22 1983-01-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-01-20 1986-07-22 1987-01-21 $7700.00 Window Closed / Lapsed

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