Exhaust gas treating apparatus and method
    4.
    发明授权
    Exhaust gas treating apparatus and method 有权
    废气处理装置及方法

    公开(公告)号:US07939038B2

    公开(公告)日:2011-05-10

    申请号:US12602420

    申请日:2008-04-30

    IPC分类号: B01D53/56 B01D53/64 B01D53/74

    摘要: An exhaust gas treating apparatus removes nitrogen oxides and mercury in exhaust gas from a boiler using an ammonia denitration catalyst, including: an ammonium chloride powder feed unit for feeding ammonium chloride, in powder form, into a vicinity of an entrance of an economizer provided to a combustion gas flue of the boiler and/or an economizer bypass unit, the fed ammonium chloride in powder form being sublimed by a combustion gas, to thereby feed hydrogen chloride and ammonia into the flue; and an ammonium chloride liquid feed unit for feeding ammonium chloride, in liquid form, into a vicinity of the entrance of the economizer and/or the economizer bypass unit, the ammonium chloride liquid feed unit also being capable of feeding ammonium chloride, vaporization of the fed ammonium chloride in liquid form by the combustion gas also allowing hydrogen chloride and ammonia to be fed into the flue.

    摘要翻译: 废气处理装置使用氨脱硝催化剂除去来自锅炉的排气中的氮氧化物和汞,所述氨脱硝催化剂包括:用于将粉末状的氯化铵供给到供给到节能器的入口附近的氯化铵粉末供给单元, 锅炉和/或节能器旁路单元的燃烧气体烟道,粉末形式的进料氯化铵由燃烧气体升华,从而将氯化氢和氨进料到烟道中; 以及用于将液体形式的氯化铵供给到节能器和/或节能器旁路单元的入口附近的氯化铵液体进料单元,氯化铵液体进料单元也能够进料氯化铵,蒸发 通过燃烧气体以液体形式供给氯化铵,还允许将氯化氢和氨进料到烟道中。

    EXHAUST GAS TREATING APPARATUS AND METHOD
    5.
    发明申请
    EXHAUST GAS TREATING APPARATUS AND METHOD 有权
    排气处理设备及方法

    公开(公告)号:US20100183493A1

    公开(公告)日:2010-07-22

    申请号:US12602420

    申请日:2008-04-30

    IPC分类号: B01D53/56 B01D53/86

    摘要: An exhaust gas treating apparatus removes nitrogen oxides and mercury in an exhaust gas from a boiler by use of an ammonia denitration catalyst, the exhaust gas treating apparatus including: an ammonium chloride powder feed unit 101 for feeding ammonium chloride, in powder form, into any one of or both of a vicinity of an entrance of an economizer 15 provided to a combustion gas flue of the boiler and an economizer bypass unit 15a, the fed ammonium chloride in powder form being sublimed by a combustion gas, to thereby feed hydrogen chloride and ammonia into the flue 102; and an ammonium chloride liquid feed unit 110 for feeding ammonium chloride, in liquid form, into any one of or both of a vicinity of the entrance of the economizer 15 and the economizer bypass unit 15a, the ammonium chloride liquid feed unit 110 also being capable of feeding ammonium chloride, vaporization of the fed ammonium chloride in liquid form by the combustion gas also allowing hydrogen chloride and ammonia to be fed into the flue 102.

    摘要翻译: 废气处理装置通过使用氨脱硝催化剂从锅炉除去来自锅炉的废气中的氮氧化物和汞,该废气处理装置包括:将粉末状的氯化铵供给到粉末状的氯化铵粉末供给单元101 提供给锅炉的燃烧气体烟道的节能器15的入口附近的一个或两个以及经济器旁路单元15a,由燃烧气体升华的粉末形式的进料氯化铵,从而进料氯化氢和 氨进入烟道102; 以及用于将液体形式的氯化铵供给到节能器15和节能器旁路单元15a的入口附近的任意一个或两个的氯化铵液体供给单元110,氯化铵液体供给单元110也能够 进料氯化铵,通过燃烧气体将液体形式的进料氯化铵蒸发,同时还允许将氯化氢和氨进料到烟道102中。

    Flue gas denitration catalyst and preparation process thereof
    10.
    发明授权
    Flue gas denitration catalyst and preparation process thereof 有权
    烟气脱硝催化剂及其制备方法

    公开(公告)号:US07256155B2

    公开(公告)日:2007-08-14

    申请号:US10705365

    申请日:2003-11-10

    IPC分类号: B01J23/00 B01J21/00

    摘要: Provided are a flue gas denitration catalyst having high denitration activity and capable of suppressing a side reaction, that is, oxidation of SO2; and a preparation process of the catalyst. The flue gas denitration catalyst comprises TiO2, WO3 and V2O5. In the surface layer of the catalyst within 200 μm from the surface thereof, V2O5 is supported on a carrier containing TiO2 and WO3. The supported amounts of V2O5 range from 0.4 to 5 wt. % based on the weight of the surface layer and range from 0.1 to 0.9 wt. % based on the total weight of the catalyst. The V2O5 thus supported has a crystallite size of less than 10 nm as measured by X-ray diffraction. The catalyst can be available by preparing a mixture containing TiO2 and WO3 and having V2O5 supported on the surface of an extruded product of the prepared mixture by a vapor phase method. The catalyst can be also available by having V2O5 supported on a powder of the prepared mixture by a vapor phase method and having the resulting powder supported on the surface of a formed product.

    摘要翻译: 提供了具有高脱硝活性并能够抑制副反应,即SO 2氧化的烟道气脱硝催化剂。 和催化剂的制备方法。 烟道气脱硝催化剂包括TiO 2,WO 3和V 2 O 5。 在催化剂的表面200μm以内的表面层中,V 2 O 2 O 5负载在含有TiO 2和WO 2的载体上 3 。 V 2 O 5的支持量为0.4-5重量%。 %,基于表层的重量,为0.1-0.9wt。 %,基于催化剂的总重量。 如此支撑的V 2 O 5 5具有通过X射线衍射测量的小于10nm的微晶尺寸。 催化剂可以通过制备含有TiO 2和WO 3的混合物并具有V 2 O 5 O 5 在制备的混合物的挤出产物的表面上通过气相法。 催化剂也可以通过使V 2 O 2 O 5通过气相法负载在所制备的混合物的粉末上,并将所得粉末负载在表面上 成型产品。