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    • 3. 发明申请
    • Device and method for processing cement kiln combustion exhaust
    • 水泥窑燃烧废气处理装置及方法
    • US20090169453A1
    • 2009-07-02
    • US11794820
    • 2005-12-27
    • Shinichiro SaitoYasuhiro UchiyamaJunichi TerasakiHisashi KondoMitsuharu HagiShinyuki Masaki
    • Shinichiro SaitoYasuhiro UchiyamaJunichi TerasakiHisashi KondoMitsuharu HagiShinyuki Masaki
    • A61L9/00B01D50/00B01D53/56B01D53/62
    • B01D53/86B01D53/8625B01D53/864B01D53/8668B01D2255/10B01D2255/20707B01D2255/20723C04B7/436F27B7/2033F27D17/008Y02A50/235C04B7/364
    • A combustion exhaust gas processing device to efficiently remove harmful substances such as dust, NOx, persistent organic pollutants, a volatile organic compound and CO in cement kiln combustion exhaust gas, thereby holding down facility cost and operating cost low. The combustion exhaust gas processing device 1 comprises: a dust collector 6 collecting dust in a cement kiln combustion exhaust gas G1; a wet dust collector 7 as a catalyst-poisoning-substance stripper removing a catalyst-poisoning substance from a combustion exhaust gas G2 which passed the dust collector 6; preheaters 10 and 11 heating beforehand a combustion exhaust gas G3 which passed the wet dust collector 7; and a catalyst device 12 from which NOx, a persistent organic pollutant, etc. in the preheated combustion exhaust gas, are removed. A titanium-vanadium catalyst etc. as an oxide catalyst is used upstream of the catalyst device 12, and a platinum catalyst etc. as a noble-metal catalyst downstream of the catalyst device 12. The temperature of the combustion exhaust gas after the catalyst-poisoning substance is removed is increased up to 140° C. or more with the preheaters to prevent decline in denitration efficiency of and the decomposition efficiency of a volatile organic compound.
    • 一种燃烧废气处理装置,用于有效地去除水泥窑燃烧废气中的灰尘,NOx,持久性有机污染物,挥发性有机化合物和CO等有害物质,从而降低设备成本和运行成本。 燃烧废气处理装置1包括:集尘器6,收集水泥窑燃烧废气G1中的灰尘; 作为催化剂中毒物质汽提器的湿式集尘器7从通过集尘器6的燃烧废气G2除去催化剂中毒物质; 预热器10和11预先加热通过湿式集尘器7的燃烧废气G3; 并且除去预热的燃烧废气中的NOx,持久性有机污染物等的催化剂装置12。 在催化剂装置12的下游使用作为氧化物催化剂的钛钒催化剂等,作为贵金属催化剂的催化剂装置12的上游的铂催化剂等。催化剂装置12后面的燃烧废气的温度, 中和物质被去除时,预热器的温度升高至140℃以上,以防止脱硝效率降低,挥发性有机化合物的分解效率降低。