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    • 4. 发明授权
    • Air-fired CO2 capture ready circulating fluidized bed steam generators
    • 燃气二氧化碳捕集循环流化床蒸汽发生器
    • US08230796B2
    • 2012-07-31
    • US12392355
    • 2009-02-25
    • Herbert E. Andrus, Jr.Gregory N. LiljedahlJohn L MarionNsakala Ya Nsakala
    • Herbert E. Andrus, Jr.Gregory N. LiljedahlJohn L MarionNsakala Ya Nsakala
    • F23G5/30F23L7/00F23L15/00
    • F23C10/10F22B31/0007F23C9/00F23J15/006F23J15/06F23J2215/50F23L7/007F23L15/04F23L2900/07001F23L2900/07003F23L2900/15042Y02E20/322Y02E20/326Y02E20/344Y02E20/348
    • A combustor 110 is operative to effect therewith the combustion of fossil fuel 114′ in order to thereby both heat to a working fluid 102 and generate a flue gas 104. An air preheater 144 receives the flue gas 104 generated in the combustor 110. A blower 180 causes air 188 to flow to the air preheater 144 when operating in an air fired mode, and causes both O2 and recycled flue gas 188′ to flow when operating in the O2 firing mode. The air preheater 144 is operative to transfer heat from the flue gas 150 received thereby to the air 188 that is received when operating in an air fired mode or to both the received O2 and the recycled flue gas 188′ that is received when operating in the O2 firing mode in order to thereby effect a preheating of the air 188 or of both the O2 and recycled flue gas, 188′ depending upon the specific nature of the mode of operation thereof, and to thereby effect therewith a cooling of the flue gas received thereby. The preheated air 142 or both the preheated O2 and the recycled flue gas 142′, depending upon the specific nature of the mode of operation, is caused to flow from the air preheater 144 to the combustor 110 in order to thereby effect therewith a fluidization of the fossil fuel 114′.
    • 燃烧器110可操作以通过化石燃料114'的燃烧来实现燃烧,从而由此二者加热到工作流体102并产生烟道气体104.空气预热器144接收在燃烧器110中产生的烟道气104.鼓风机 当在空气燃烧模式下操作时,180使空气188流到空气预热器144,并且当在O 2点火模式下操作时,O 2和再循环烟道气188'都流动。 空气预热器144可操作以将热量从其接收的烟道气150转移到在空气燃烧模式下运行时接收的空气188,或者在接收的O2和被回收的废气188' O2烧制模式,从而根据其操作模式的具体特性来实现空气188或者二氧化碳和再循环烟道气188'的预热,从而使所接收到的烟气冷却 从而。 使预热的空气142或预热的氧气和再循环烟道气142'两者都取决于操作模式的具体特性,从空气预热器144流到燃烧器110,从而使其流化 化石燃料114'。
    • 5. 发明授权
    • Gas leakage reduction system
    • 气体泄漏减少系统
    • US08695514B2
    • 2014-04-15
    • US12465822
    • 2009-05-14
    • Glen D. JukkolaGregory N. LiljedahlNsakala Ya NsakalaMark Palkes
    • Glen D. JukkolaGregory N. LiljedahlNsakala Ya NsakalaMark Palkes
    • F23B70/00
    • F23C9/00F22B1/1884F22B37/42F23C2202/00Y02E20/344
    • An air infiltration abatement system (300) for a power plant (10) includes a recirculated flue gas source (175), a recirculated flue gas supply line (310) connected to the recirculated flue gas source (175) and a power plant component. The power plant component has a leakage area in fluid communication with the recirculated flue gas supply line (310). The recirculated flue gas source (175) receives a combustion flue gas (75) from an oxygen fired boiler (20) of the power plant (10), and provides the combustion flue gas (75) to the recirculated flue gas supply line (310). The recirculated flue gas supply line (310) supplies the combustion flue gas (75) as a recirculated flue gas (330) to the oxygen fired boiler (20) via the leakage area of the power plant component.
    • 用于发电厂(10)的空气渗透减排系统(300)包括再循环烟道气源(175),连接到再循环烟道气源(175)的再循环烟道气供应管线(310)和发电厂部件。 发电厂部件具有与再循环烟道气供应管线(310)流体连通的泄漏区域。 再循环烟道气源(175)接收来自发电厂(10)的氧燃锅炉(20)的燃烧烟道气(75),并将燃烧烟道气(75)提供给再循环烟道气供应管线 )。 再循环的烟气供应管线(310)经由发电厂部件的泄漏区域将作为再循环烟道气(330)的燃烧烟道气(75)供应到氧燃锅炉(20)。