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    • 5. 发明授权
    • LIME SLAKER
    • 石灰斯莱克
    • EP0094967B1
    • 1986-12-30
    • EP83900241
    • 1982-11-29
    • CROWN ZELLERBACH CORPORATION
    • LANE, STANLEY, C.
    • C01F11/02C04B2/08D21C11/00
    • C04B2/08C01F11/02
    • An improved lime slaker in which the lime is combined with the slaking liquor in a vertical conduit (18) which extends below the level of the liquor in the slaker vessel (10). The slaking liquor is introduced into the conduit at a high velocity tangential (26) to the interior surface of the conduit to flush the lime into the vessel. The slaker includes a vertical vent pipe (28) that extends through the bottom (14) of the vessel. In a preferred embodiment, the inlet of the vent pipe is surrounded by an entrainment separator (32). Removable covers (24, 36) permit convenient access for inspection and cleaning of the conduit and the vent pipe.
    • 一种改进的石灰消化器,其中石灰与在消化器容器(10)中液面下方延伸的垂直导管(18)中的消化液混合。 消化液以高速与导管内表面切向(26)导入导管,将石灰冲入容器中。 消化器包括延伸穿过容器底部(14)的垂直排气管(28)。 在一个优选实施例中,通气管的入口被夹带分离器(32)包围。 可移动的盖(24,36)允许方便地检查和清洁导管和通气管。
    • 8. 发明公开
    • METHOD AND APPARATUS FOR THE PREPARATION OF FINELY DIVIDED CALCIUM HYDROXIDE
    • VORRICHTUNG ZUR HERSTELLUNG VON FEIN GETEILTEM CALCUMHYDROXID
    • EP2651845A1
    • 2013-10-23
    • EP11849349.3
    • 2011-11-24
    • Fractivator OY
    • PALM, Carl-Olof
    • C04B2/02C04B2/08C01F11/02C01F11/16B02C13/22B02C13/286B02C23/18
    • C04B2/08B82Y30/00C01F11/02C01P2004/32C01P2004/64C04B2/04
    • The invention concerns a method for the preparation of finely divided calcium hydroxide, where burnt lime or calcium oxide is comminuted in an impact disintegrator (10), into which in addition to the calcium oxide part of the required amount of water led to wet the particles obtained, to bind the dust and to initiate the reaction, and the material comminuted and wetted in the impact disintegrator is led into a screw conveyor (20) being in connection with the impact disintegrator. The invention is characterized in that - the reaction is essentially completed in the screw conveyor (20) by feeding into the same the remainder of the amount of water needed for the reaction, and that - the temperature of the material in the last part of the screw conveyor is kept at a target temperature, which is essentially the vaporization temperature for water at the prevailing pressure, and the material is kept at the target temperature for a certain period of time, about 5...15 s, preferably about 10 s.
    • 本发明涉及一种制备精细分离的氢氧化钙的方法,其中将烧石灰或氧化钙在冲击式粉碎机(10)中粉碎,除了氧化钙部分所需量的水导致湿润颗粒之外, 获得,以结合灰尘并开始反应,并且在冲击式破碎机中粉碎和润湿的材料被引入与冲击分解器相连的螺旋输送机(20)。 本发明的特征在于 - 反应基本上在螺旋输送机(20)中完成,通过将反应所需的剩余量的水加入到该螺杆输送机(20)的最后部分中的温度 螺旋输送机保持在目标温度,其基本上是在主要压力下的水的蒸发温度,并将材料保持在目标温度下一段时间,约5-15秒,优选约10秒 。