SPRAY DRYER ABSORPTION PROCESS FOR FLUE GAS WITH ENTRAINED COARSE PARTICLES
    1.
    发明申请
    SPRAY DRYER ABSORPTION PROCESS FOR FLUE GAS WITH ENTRAINED COARSE PARTICLES 审中-公开
    喷雾干燥器吸收过程,用于含有粗糙颗粒的气体

    公开(公告)号:WO2010006618A1

    公开(公告)日:2010-01-21

    申请号:PCT/DK2009/050177

    申请日:2009-07-14

    Abstract: Disclosed herein is a method for reducing the amount of coarser particles from a stream of flue gas prior to treatment by a spray dryer absorption process (SDA). The method comprises the steps of directing a stream of flue gas containing entrained particles of varying sizes through a curve, thereby subjecting the particles to a centrifugal effect, collecting the particles predominately of the coarser size at a particles collecting means provided in the outer circumference of the curve, dispersing the flue gas reduced in particles of coarse particle sizes into the chamber of a spray dryer absorption apparatus, wherein the particles content of the original flue gas stream is above 20 g/Nm 3 . Also an apparatus for performing the method and a gas disperser is disclosed. The method substantially reduces the cost of the entire plant for treating flue gas having a high content of entrained coarse particles by eliminating the need for a particle pre-collector upstream the SDA.

    Abstract translation: 本文公开了一种在通过喷雾干燥器吸收过程(SDA)处理之前从烟道气流中减少较粗颗粒的量的方法。 该方法包括以下步骤:通过曲线引导含有不同大小的夹带颗粒的烟道气流,从而使颗粒进行离心效应,在设置在外围的颗粒收集装置的主颗粒收集装置 将烟道气分散在粗粒径的颗粒的喷雾干燥器吸收装置的室中,其中原始烟气流的颗粒含量高于20g / Nm 3。 还公开了一种用于执行该方法的装置和气体分散器。 该方法通过消除对SDA上游的颗粒预收集器的需要,大大降低了整个设备处理具有高夹带粗颗粒含量的烟道气的成本。

    SPRAY DRYER ABSORPTION APPARATUS WITH FLAT-BOTTOMED CHAMBER
    2.
    发明申请
    SPRAY DRYER ABSORPTION APPARATUS WITH FLAT-BOTTOMED CHAMBER 审中-公开
    喷雾干燥器吸收装置与平底室

    公开(公告)号:WO2012006996A1

    公开(公告)日:2012-01-19

    申请号:PCT/DK2010/050184

    申请日:2010-07-12

    Abstract: In the application a spray dryer absorption apparatus for treating a stream of flue gas containing acidic components is disclosed. The apparatus comprises a chamber having vertical cylindrical walls, said chamber comprises (i) an inlet for a flue gas stream containing an acidic component, (ii) an atomizer for spraying droplets of an absorbent slurry into said flue gas stream to effect a chemical reaction between the drop- lets and the acidic component of the flue gas, thereby forming a particulate reaction product, and (iii) an outlet for the treated flue gas and entrained particulate reaction product, wherein the bottom of the chamber having vertical cylindrical walls is substantially horizontal and impervious to gases.The apparatus of the invention has the advantage of a simplified geometry accounting for lower building and maintenance costs.

    Abstract translation: 在本申请中,公开了一种用于处理含有酸性组分的烟道气流的喷雾干燥器吸收装置。 该设备包括具有垂直圆柱形壁的腔室,所述腔室包括(i)用于含有酸性组分的烟道气流的入口,(ii)用于将吸收剂浆液的液滴喷射到所述烟道气流中以进行化学反应的雾化器 在烟道气和酸性组分之间,从而形成颗粒反应产物,和(iii)用于经处理的烟道气和夹带的颗粒反应产物的出口,其中具有垂直圆柱形壁的室的底部基本上 水平和不透气体。本发明的装置具有简化的几何形状的优点,从而降低建筑物和维护成本。

    SPRAY DRYER ABSORPTION PROCESS FOR FLUE GAS WITH ENTRAINED COARSE PARTICLES
    4.
    发明公开
    SPRAY DRYER ABSORPTION PROCESS FOR FLUE GAS WITH ENTRAINED COARSE PARTICLES 有权
    喷雾吸收程序粗颗粒含SMOKE

    公开(公告)号:EP2334407A1

    公开(公告)日:2011-06-22

    申请号:EP09776243.9

    申请日:2009-07-14

    Abstract: Disclosed herein is a method for reducing the amount of coarser particles from a stream of flue gas prior to treatment by a spray dryer absorption process (SDA). The method comprises the steps of directing a stream of flue gas containing entrained particles of varying sizes through a curve, thereby subjecting the particles to a centrifugal effect, collecting the particles predominately of the coarser size at a particles collecting means provided in the outer circumference of the curve, dispersing the flue gas reduced in particles of coarse particle sizes into the chamber of a spray dryer absorption apparatus, wherein the particles content of the original flue gas stream is above 20 g/Nm
    3 . Also an apparatus for performing the method and a gas disperser is disclosed. The method substantially reduces the cost of the entire plant for treating flue gas having a high content of entrained coarse particles by eliminating the need for a particle pre-collector upstream the SDA.

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