IPC분류정보
국가/구분 |
United States(US) Patent
등록
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국제특허분류(IPC7판) |
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출원번호 |
US-0546093
(1983-10-27)
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발명자
/ 주소 |
- Firey Joseph C. (P.O. Box 15514 Seattle WA 98115)
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인용정보 |
피인용 횟수 :
10 인용 특허 :
2 |
초록
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A cyclic velox boiler is described wherein solid carbonaceous fuels are burned in pressure vessel containers by cyclic compression and expansion with air or with air and steam as usual gas reactants. During compression air is forced deeply into the pores of the solid fuel and rapid primary burning t
A cyclic velox boiler is described wherein solid carbonaceous fuels are burned in pressure vessel containers by cyclic compression and expansion with air or with air and steam as usual gas reactants. During compression air is forced deeply into the pores of the solid fuel and rapid primary burning to carbon monoxide results due to the large internal pore area available. During expansion the primary reacted gases emerge from the pores to mix and react fully with secondary air retained outside the pores in the container. Rapid and complete burning of the char fuel can be obtained in this two step, cyclic burning process and net useful mechanical work can be obtained from an expander engine. The containers and portions of the expander are cooled with water and the resulting steam can be used to generate additional work output via a steam power cycle.
대표청구항
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The combination of a cyclic oxidation char gasifier plant comprising: at least one compressor means for compressing gases from a lower pressure to a higher pressure and each such compressor means comprising at least one stage and each such stage comprising an inlet and an outlet end; at least one ex
The combination of a cyclic oxidation char gasifier plant comprising: at least one compressor means for compressing gases from a lower pressure to a higher pressure and each such compressor means comprising at least one stage and each such stage comprising an inlet and an outlet end; at least one expander means for expanding gas from a higher pressure to a lower pressure and each such expander means comprising at least one stage and each such stage comprising an inlet end and a discharge end; at least two separate containers, each of said containers comprising pressure vessel means for containing char fuel and any gas compressed into said char fuel, each such container comprising interior surfaces on the combustion side; power means for driving said compressors and for absorbing any mechanical work done upon said expanders by said expanding gas; each such expander means comprising an expander discharge; at least one char fuel heater, said char fuel heater comprising means for heating a portion of the char fuel within each of said containing means to that temperature at which said char will react rapidly with oxygen in adjacent compressed reactant gases when said cyclic char gasifier plant is being started; at least one reactant gas supply source of gas containing appreciable oxygen gas; each such compressor whose number of stages exceeds one further comprising fixed open gas flow connections from the outlet end of each compressor stage, except one, to the inlet end of one other stage of said compressor, whereby said stages of said compressor are connected in series so that the pressure of a particular gas means, at delivery from each stage, increases as said gas mass is compressed through said series connected stages, from the inlet end to the outlet end of each stage, with the first stage in said series through which a gas mass first flows being both the lowest pressure stage and also that one stage whose inlet end does not have a fixed open gas flow connection from the outlet end of any other stage of said compressor, and with the last stage in said series through which a gas mass last flows being both the highest pressure stage and also that one stage whose outlet end does not have a fixed open gas flow connection to the supply end of any other stage of said compressor; fixed open gas flow connections from the inlet end of the lowest pressure stage of each of said compressors to at least one reactant gas supply source of gas containing appreciable oxygen gas; each such expander whose number of stages exceeds one further comprising fixed open gas flow connections from the discharge end of each expander stage, except one, to the inlet end of one other stage of said expander, whereby said stages of said expander are connected in series so that the pressure of a particular gas mass, at discharge from each stage, decreases as said gas mass is expanded through said series connected stages, from the inlet end to the discharge end of each stage, with the first stage in said series through which a gas mass first flows being both the highest pressure stage and also that one stage whose inlet end does not have a fixed open gas flow connection from the discharge end of any other stage of said expander, and with the last stage in said series through which a gas mass last flows being both the lowest pressure stage and also that one stage whose discharge end does not have a fixed open gas flow connection to the inlet end of any other stage of said expander; fixed open gas flow connections from the discharge end of the lowest pressure stage of each of said expanders to said expander discharge; changeable gas flow connections, which are openable and closeable, from each of said containers to each outlet end of each stage of each of said compressors and to each inlet end of each stage of each of said expanders; each cyclic char gasifier plant comprising a number of said containers, with changeable gas flow connections to said compressors and to said expanders, at least equal to the sum of the number of comressor stages of all compressors, and the number of expander stages of all expanders; at least one refuel mechanism, said refuel mechanism comprising; means for transferring a volume of solid materials from a supply source into said containing means when said refuel transfer means is connected to said containing means; means for connecting said refuel transfer means to said containing means for a time period for refueling and for disconnecting said refuel transfer means from said containing means at the end of said refuel time period; means for sealing said refuel means for connecting and disconnecting against gas leakage; at least one coke removal mechanism, said coke removal mechanism comprising; means for transferring a volume of non-gas materials out of said containing means; means for opening and closing said changeable gas flow connections so that each container is opened for a time period to each outlet end of each stage of each of said compressors, in a sub-sequence of time periods of open gas flow connections to compressors, said sub-sequence proceeding in time order of increasing compressor stage delivery pressure, and is opened for a time period to each inlet end of each stage of each of said expanders, in a sub-sequence of time periods of open gas flow connections to expanders, said sub-sequence proceeding in time order of decreasing expander stage inlet pressure, said sub-sequence of connections to said compressors being followed by said sub-sequence of connections to said expanders, and these together comprise one sequence of time periods of open gas flow connections, each of said containers is opened to only one stage during any one time period of said sequence of time periods, said sequence of time periods of open gas flow connections to said compressors and to said expanders is repeated for each of said containers by said means for opening and closing; means for controlling said means for opening and closing, and said means for connecting said refuel transfer means and said coke removal transfer means, so that said repeated sequences of time periods of open gas flow connections, and any time periods available only for refueling and for coke removal, are a continuous series of time periods for any one containing means, and so that the delivery end of each stage of each compressor has an open gas flow connection to one containing means, and the inlet end of each stage of each expander has an open gas flow connection to one containing means, during all time periods, whenever said plant is operating; wherein the improvement comprises adding thereto: boiler means for heating and boiling liquid water at pressure and for heating steam at pressure, and comprising a boiler feedwater inlet and a boiler steam outlet, at least one portion of said boiler means comprising at least one radiant heater means positioned on the interior surfaces of one of said containers, each such radiant heater comprising a liquid water inlet and a water outlet; a source of boiler feedwater; feedwater pumping means for pumping liquid water into said boiler means from said feedwater supply source and comprising a drive means for driving said feedwater pump and a control means for controlling the flow rate of water pumped; feedwater pump connecting means for connecting said feedwater pumping means to said boiler means and to said feedwater supply source so that liquid water is forced into said boiler liquid water inlet whenever said plant is operating; sensor and control means for sensing the quantity of char fuel within each said container when said plant is operating and operative upon said means for connecting said refuel transfer means so that, when the volume of char fuel within any one container becomes less than a minimum set value, said refuel transfer means is connected to that container by said means for connecting said refuel means, and when the volume of char fuel within any one said container exceeds a maximum set value, said refuel transfer means is disconnected from that container by said means for connecting said refuel means; whereby said cyclic oxidation char gasifier plant becomes a cyclic Velox boiler plant.
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