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    • 2. 发明申请
    • METHOD OF MANUFACTURING A SOLVENT EXTRACTION SETTLER AND SOLVENT EXTRACTION SETTLER
    • 溶剂萃取装置和溶剂萃取装置的制造方法
    • WO2014001625A1
    • 2014-01-03
    • PCT/FI2013/050645
    • 2013-06-12
    • OUTOTEC OYJ
    • VAARNO, JussiSAARIO, RamiFREDRIKSSON, HenriPAJALA, Jussi
    • C22B3/02C22B3/22B01D11/04
    • B01D11/04B01D11/0446B65D90/143Y10T29/49826
    • A method of manufacturing a solvent extraction settler comprises manufacturing at the site of manufacture, such as in an engineering workshop, a plurality of self-supporting settler element modules (2, 3, 4, 5) each having exterior dimensions, strength and handling and securing means (6) conforming to shipping container standards, transporting the modules (2, 3, 4, 5) to the site of installation as normal freight by transport equipment, such as trucks, trailers and container ships, capable of handling and transporting shipping container standard compatible units, and assembling the modules (2, 3, 4, 5) into a complete settler at the site of installation. The settler comp- rises a module group (1) consisting of a plurality of self-supporting settler element modules (2, 3, 4, 5) each having exterior dimensions, strength and handling and securing means (6) conforming to ISO shipping container standards to enable ISO compatible transportability.
    • 制造溶剂萃取沉降器的方法包括在诸如工程车间的制造现场制造各自具有外部尺寸,强度和处理的多个自支撑沉降器元件模块(2,3,4,5),以及 通过符合运输集装箱标准的固定装置(6),将模块(2,3,4,5)运送到作为运输设备(如卡车,拖车和集装箱船舶)的运输现场,能够处理和运输运输 容器标准兼容单元,并将模块(2,3,4,5)组装到安装现场的完整沉淀器中。 沉降器包括由多个自支撑沉降器元件模块(2,3,4,5)组成的模块组(1),每个模块组具有外部尺寸,强度和操作以及符合ISO运输容器的固定装置(6) 标准,使ISO兼容的运输能力。
    • 8. 发明申请
    • METHOD FOR SEPARATION AND UP-CONCENTRATION OF MUTUALLY REPLACEABLE COMPONENTS
    • 分离和高浓度可替代组分的方法
    • WO2005084774A1
    • 2005-09-15
    • PCT/SK2005/000006
    • 2005-03-03
    • SISKA, Jozef
    • SISKA, Jozef
    • B01D11/04
    • B01D11/0446C02F1/26C02F2101/20C22B3/0005C22B3/165C22B3/44C22B7/006Y02P10/234
    • A separation and up-concentration of mutually replaceable components from partially miscible phases is realized by a successive contacting of a transfer phase with concentration phases containing the easiest replaceable component. After exhausting of the components to be separated and after a pre-treatment including bonding of the components from their source, the transfer phase is used again as the new input transfer phase. The transfer phase containing salts of unsaturated fatty acids and metals, transition elements, ammonium and/or amines as the components to be separated, is successively contacted with acidified water concentration solutions in order to separate and up-concentrate groups or single components. Water solution of water-soluble metals salts, transition elements, ammonium and/or amines may be used as the transfer phase the concentration phases are formed by an unsaturated fatty acid. The components are separated in the concentration phases according to their electronegativity values.
    • 通过连续接触转移相与含有最简单的可更换组分的浓缩相来实现部分混溶相的可相互替代的组分的分离和增加浓度。 在要分离的部件排气之后,并且在包括从其源的部件的粘合的预处理之后,再次使用转移相作为新的输入转移相。 含有不饱和脂肪酸和金属,过渡元素,铵和/或胺作为待分离成分的盐的转移阶段依次与酸化水浓缩溶液接触,以分离和浓缩组或单一组分。 可以使用水溶性金属盐,过渡元素,铵和/或胺的水溶液作为转移相,浓缩相由不饱和脂肪酸形成。 各组分根据其电负性值在浓度阶段分离。