[특허]Process for in-situ passivation of partially-dried coal

River Basin Energy, Inc.

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특허 상세정보

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Process for in-situ passivation of partially-dried coal

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	C10L-005/00
미국특허분류(USC)	044/626; 044/620
출원번호	UP-0316508 (2005-12-22)
등록번호	US-7695535 (2010-05-20)
발명자 / 주소	Dunlop, Donald D.
출원인 / 주소	River Basin Energy, Inc.
대리인 / 주소	Sheridan Ross P.C.
인용정보	피인용 횟수 : 7 인용 특허 : 111

초록
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Thus, a novel process for producing a passivated coal material has been disclosed, comprising the steps of (a) drying a coal material by heating said coal material in the presence of a first gas comprised of less than about five volume percent of oxygen until said coal material has a moisture content of from above about 1 to about 20 weight percent, thereby producing a partially dried coal material, wherein said coal material is selected from the group consisting of lignitic coal, sub-bituminous coal, bituminous coal, coal char, and mixtures thereof; (b) heating said partially dried coal material to a temperature of from about 100 to about 600 degrees Fahrenheit, thereby producing a heated partially dried coal material; (c) charging said heated partially dried coal material to a fluidized bed reactor; (d) feeding a second gas with an oxygen content of from about 6 to about 15 volume percent into said fluidized bed reactor; (e) contacting said heated partially dried coal material with said second gas while maintaining said heated partially dried coal material at a temperature of from about 450 to about 650 degrees Fahrenheit; and, thereafter, (f) removing water from said heated partially dried coal material until no more than about 1 weight percent of water remains in said heated partially dried coal material.

대표
청구항
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I claim: 1. A process for producing a passivated coal material, comprising the steps of: (a) drying a coal material by heating said coal material in the presence of a first gas comprised of less than about five volume percent of oxygen until said coal material has a moisture content of from above about 1 to about 20 weight percent, thereby producing a partially dried coal material, wherein said coal material is selected from the group consisting of lignitic coal, sub-bituminous coal, bituminous coal, coal char, and mixtures thereof; (b) heating said partially dried coal material to a temperature of from about 100 to about 600 degrees Fahrenheit, thereby producing a heated partially dried coal material; (c) charging said heated partially dried coal material to a fluidized bed reactor; (d) feeding a second gas with an oxygen content of from about 6 to about 15 volume percent into said fluidized bed reactor; (e) contacting said heated partially dried coal material with said second gas while maintaining said heated partially dried coal material at a temperature of from about 450 to about 650 degrees Fahrenheit; and, thereafter, (f) removing water from said heated partially dried coal material until no more than about 1 weight percent of water remains in said heated partially dried coal material. 2. The process for producing a passivated coal material as recited in claim 1, further comprising the step of simultaneously feeding said second gas into said fluidized bed reactor and maintaining said fluidized bed at a density of from about 20 to about 50 pounds per cubic foot while removing water from said fluidized bed reactor. 3. The process for producing a passivated coal material as recited in claim 1, wherein said second gas comprises from about 7 to about 10 volume percent oxygen. 4. The process for producing a passivated coal material as recited in claim 3, wherein said second gas comprises air. 5. The process for producing a passivated coal material as recited in claim 1, further comprising the step of heating said second gas prior to the time it is fed into said fluidized bed reactor. 6. The process for producing a passivated coal material as recited in claim 5, wherein said process further comprises the steps of combining said heated second gas with a third gas comprising from about 7 to about 10 volume percent oxygen and feeding said combined heated second gas and third gas into said fluidized bed reactor. 7. The process for producing a passivated coal material as recited in claim 6, wherein said third gas comprises recycled gas from said fluidized bed reactor. 8. The process for producing a passivated coal material as recited in claim 1, wherein said temperature in said fluidized bed reactor is from about 550 to about 600 degrees Fahrenheit. 9. The process for producing a passivated coal material as recited in claim 1, wherein said heated partially dried coal material is charged to the fluidized bed reactor at a rate of from about 0.01 to about 4000 pounds per hour. 10. The process for producing a passivated coal material as recited in claim 1, wherein said heated partially dried coal material is contacted with said second gas for about one to about fifteen minutes. 11. The process for producing a passivated coal material as recited in claim 10, wherein said heated partially dried coal material is contacted with said second gas for about four to about ten minutes. 12. The process for producing a passivated coal material as recited in claim 1, wherein said water is removed from said coal material until no more than from about 0.01 to about 1.0 weight percent of water remains in said coal material. 13. The process for producing a passivated coal material as recited in claim 1, wherein said second gas is fed into said fluidized bed reactor at a velocity of from about 3 to about 12.2 feet per second. 14. The process for producing a passivated coal material as recited in claim 6, wherein said second gas and said third gas are fed into said fluidized bed reactor at a velocity of from about 3 to about 12.2 feet per second. 15. The process for producing a passivated coal material as recited in claim 1, wherein said heated partially dried coal material is charged to the fluidized bed reactor at a rate of from about 100 to about 400 pounds per hour. 16. A process for producing a passivated coal material, comprising the steps of: (a) drying a coal material by heating said coal material in the presence of a first gas comprised of less than about five volume percent of oxygen until said coal material has a moisture content of from above about 1 to about 20 weight percent, thereby producing a partially dried coal material, wherein said coal material is selected from the group consisting of lignitic coal, sub-bituminous coal, bituminous coal, coal char, and mixtures thereof, and wherein said coal material has a residual oxygen demand of about 10 to about 30; (b) heating said partially dried coal material to a temperature of from about 100 to about 600 degrees Fahrenheit, thereby producing a heated partially dried coal material; (c) charging said heated partially dried coal material to a fluidized bed reactor; (d) heating a second gas with an oxygen content of from about 6 to about 15 volume percent via a heat exchanger; (e) combining said heated second gas with a third gas with an oxygen content of from about 7 to about 10 volume percent and feeding said combined heated second gas and said third gases into said fluidized bed reactor; (f) maintaining said fluidized bed at a density of from about 20 to about 50 pounds per cubic foot while removing water from said fluidized bed reactor; (g) contacting said heated partially dried coal material with said second gas while maintaining said heated partially dried coal material at a temperature of from about 550 to about 650 degrees Fahrenheit; and, thereafter, (h) removing water from said heated partially dried coal material until no more than about 1 weight percent of water remains in said heated partially dried coal material. 17. The process for producing a passivated coal material as recited in claim 16, wherein said second gas is fed into said fluidized bed reactor at a velocity of from about 3 to about 12.2 feet per second. 18. The process for producing a passivated coal material as recited in claim 16, wherein said heated partially dried coal material is charged to said fluidized bed reactor at a rate of from about 0.01 to about 400 pounds per hour. 19. A process for producing a passivated coal material, comprising the steps of: (a) drying a coal material by pyrolysis by heating said coal material in the presence of a first gas comprised of less than about five volume percent of oxygen until said coal material has a moisture content of from above about 1 to about 20 weight percent, thereby producing a partially dried coal material, wherein said coal material is selected from the group consisting of lignitic coal, sub-bituminous coal, bituminous coal, coal char, and mixtures thereof, and wherein said coal material has a residual oxygen demand of about 10 to about 30; (b) heating said partially dried coal material to a temperature of from about 100 to about 600 degrees Fahrenheit, thereby producing a heated partially dried coal material; (c) charging said heated partially dried coal material to a fluidized bed reactor at a rate of from about 0.01 to about 4000 pounds per hour; (d) heating a second gas with an oxygen content of from about 6 to about 15 volume percent via a heat exchanger; (e) combining said heated second gas with a third gas with an oxygen content of from about 7 to about 10 volume percent and feeding said combined heated second gas and said third gases into said fluidized bed reactor at a velocity of from about 3 to about 12.2 feet per second; (f) maintaining said fluidized bed at a density of from about 20 to about 50 pounds per cubic foot while removing water from said fluidized bed reactor; (g) contacting said heated partially dried coal material with said second gas while maintaining said heated partially dried coal material at a temperature of from about 550 to about 650 degrees Fahrenheit; and, thereafter, (h) removing water from said heated partially dried coal material for a period of from about one to about fifteen minutes until no more than about one weight percent of water remains in said heated partially dried coal material. 20. The process for producing a passivated coal material as recited in claim 19, wherein water is removed from said heated partially dried coal material for a period of from about four to about five minutes until no more than about 0.5 weight percent of water remains in said heated partially dried coal material.

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Process for in-situ passivation of partially-dried coal

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Process for in-situ passivation of partially-dried coal

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