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    • 4. 发明授权
    • Method of separating impurities from lime and lime sludge
    • 从石灰和石灰泥中分离杂质的方法
    • US6074521A
    • 2000-06-13
    • US981642
    • 1998-01-08
    • Holgor EngdahlJouni JanttiKurt SirenJuhani Vehmaan-KreulaPasi Vanttinen
    • Holgor EngdahlJouni JanttiKurt SirenJuhani Vehmaan-KreulaPasi Vanttinen
    • C01F11/16C01F11/18D21C11/00D21C11/04
    • C01F11/16D21C11/0078D21C11/04Y02P40/44
    • A method of separating impurities from lime or the calcium carbonate or the lime sludge produced in the chemical recovery system of a pulp mill so that lime sludge or lime is dissolved in a solution containing carbonate or hydrocarbonate in order to dissolve impurities. Subsequently the lime sludge or lime is separated from the solution containing dissolved impurities. A method of causticizing green liquor containing impurities, such as silicon, in two stages. In the first stage green liquor is causticized with such an amount of lime that impurities substantially remain in the liquor. The lime produced in this stage is removed from the liquor and the rest of the lime required in the causticizing is added to this liquor, so that impurities precipitate with the lime sludge produced in the second stage and at least a portion of the lime sludge rich in impurities is discharged from the process.
    • PCT No.PCT / FI96 / 00406 Sec。 371日期1998年1月9日 102(e)1998年1月9日PCT PCT 1996年7月10日PCT公布。 出版物WO97 / 03245 日本1997年1月30日在纸浆厂的化学回收系统中分离石灰或碳酸钙或石灰污泥中的杂质的方法,使得石灰粘泥或石灰溶解在含有碳酸盐或碳酸氢盐的溶液中以便溶解杂质 。 随后将石灰渣或石灰与含溶解杂质的溶液分离。 将含有杂质(如硅)的绿液在两个阶段中苛化的方法。 在第一阶段,绿液用这样一定量的石灰碱化,使得杂质基本上留在液体中。 在该阶段中生产的石灰从液体中除去,并且将苛性碱中所需的其余石灰加入到该液体中,使得杂质与第二阶段产生的石灰粘泥沉淀,并且至少一部分富含石灰渣 杂质从工艺中排出。
    • 9. 发明授权
    • Method and apparatus for the preparation of finely divided calcium hydroxide
    • 用于制备细碎氢氧化钙的方法和装置
    • US08480018B2
    • 2013-07-09
    • US13123495
    • 2009-10-29
    • Pentti Virtanen
    • Pentti Virtanen
    • B02C13/00B02C13/20B02C21/00
    • C04B2/04B02C13/205B02C13/286B02C2013/28654C01F11/02C01F11/16C01P2004/64C04B2/08
    • Method for the preparation of finely divided calcium hydroxide, where calcium oxide is comminuted in an impact disintegrator into which in addition to the calcium hydroxide a small amount of water is led to wet the particles obtained and to bind the dust. The calcium oxide powder is led to a conveyor being in connection with the impact disintegrator and operating as a pre-quencher, to which conveyer water is added and where the material is subjected to a kneading effect. The material which is a mixture of calcium oxide and calcium hydroxide is led from the conveyor to a cistern operating as post-quencher, to which cistern the remaining portion of the total water amount required for quenching is added. The amount of water added to the impact disintegrator and to the pre-quencher is altogether 20 . . . 50% of the total amount of water required for quenching, preferably about ⅓ of the total amount of water required for quenching, and the amount of water added to the post-quencher is 80 . . . 50% of the total amount of water required for quenching, preferably about ⅔ of the total amount of water required for quenching.
    • 制备细碎氢氧化钙的方法,其中将氧化钙粉碎在冲击式粉碎机中,除了氢氧化钙之外,少量的水导致其中所得到的颗粒湿润并结合灰尘。 氧化钙粉末被引导到与冲击破碎机相连的输送机,并作为预淬火器操作,向其中加入输送机水,并且材料经受捏合作用。 作为氧化钙和氢氧化钙的混合物的材料从输送机引导到作为后淬火器操作的水箱,向其中添加用于淬火所需的总水量剩余部分。 添加到冲击粉碎机和预淬火剂中的水量总共为20。 。 。 淬火所需水量的50%,优选淬火所需水量的约1/3,并且添加到后淬火剂中的水量为80。 。 。 淬火所需水量的50%,优选淬火所需水量的2/3左右。