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    • 1. 发明授权
    • Decontamination of wet-processed phosphoric acid
    • 湿法磷酸的去污
    • US4200620A
    • 1980-04-29
    • US859879
    • 1977-12-12
    • Klaus-Peter EhlersWolfgang ScheibitzKlaus SchrodterGero Heymer
    • Klaus-Peter EhlersWolfgang ScheibitzKlaus SchrodterGero Heymer
    • C01B25/234C01B25/16
    • C01B25/234
    • Wet-processed phosphoric acid is decontaminated. To this end, the phosphoric acid and an organic solvent, which is partially miscible with water and capable of absorbing phosphoric acid, are contacted countercurrently with respect to one another. The resulting organic phosphoric acid solution is separated from contaminants unabsorbed by the solvent, termed primary raffinate, decontaminated phosphoric acid is recovered either in the form of free acid by re-extracting the organic phosphoric acid solution with water, or in the form of an alkali metal phosphate by reacting the organic phosphoric acid solution with an alkali, and the primary raffinate is treated countercurrently with a solvent containing a mineral acid. More specifically, the organic phosphoric acid extract, which orginates from the primary raffinate treatment and contains more than 0 up to at most 10 weight% of water, is mixed with an anhydrous solvent in a ratio by weight necessary to ensure the formation of a mixture containing more than 0 and less than 50% of water than would correspond to the saturation concentration of water in the solvent; and the mixture is contacted countercurrently with the phosphoric acid which is to be decontaminated.
    • 湿法处理的磷酸被去污。 为此,磷酸和与水部分混溶且能够吸收磷酸的有机溶剂相对于彼此逆流接触。 所得到的有机磷酸溶液与被称为初级萃余液的溶剂未被吸收的污染物分离,通过用水再次萃取有机磷酸溶液或以碱的形式将去污的磷酸以游离酸的形式回收 通过使有机磷酸溶液与碱反应,并且将主要提余液与含有无机酸的溶剂逆流处理。 更具体地说,将来自主要提余液处理并含有大于0至多10重量%的水的有机磷酸提取物与无水溶剂以确保形成混合物所需的重量比混合 含量超过溶于溶剂中的水的饱和浓度的0以上且小于50%的水; 并且将该混合物与待净化的磷酸逆流接触。
    • 6. 发明授权
    • Purification of wet-process phosphoric acid
    • 湿法磷酸的纯化
    • US4346066A
    • 1982-08-24
    • US164365
    • 1980-06-30
    • Reinhard GradlKlaus SchrodterKlaus-Peter EhlersWolfgang Scheibitz
    • Reinhard GradlKlaus SchrodterKlaus-Peter EhlersWolfgang Scheibitz
    • C01B25/234C01B25/46C01B25/16
    • C01B25/462C01B25/461
    • The invention relates to the decontamination of wet-processed phosphoric acid with the use of organic solvents in a plurality of extraction zones, of which each is comprised of a mixing zone and a separating zone, the solvent being immiscible or partially miscible with water. Resulting organic phase and the aqueous phase are contacted countercurrently with respect to one another, the organic solvent phase being dispersed in the aqueous phase. To this end, the invention provides for the aqueous phase to be admitted to the mixing zone at the onset of the extraction, and for organic phase and aqueous phase to be continuously admitted in a volume ratio of at least 2.5:1 to the respective extracting zones in an overall quantity sufficient to provide, in the mixing zones of the extraction zones, a volume ratio of organic phase to aqueous phase of at most 1:1, which is maintained therein.
    • 本发明涉及在多个提取区中使用有机溶剂对湿法磷酸进行去污,其中每一个由混合区和分离区构成,溶剂与水不混溶或部分混溶。 所得的有机相和水相相对于彼此逆流接触,有机溶剂相分散在水相中。 为此,本发明提供了在提取开始时允许进入混合区的水相,并且使有机相和水相以相对于萃取物的至少2.5:1的体积比连续进入 总量足以在萃取区的混合区中提供最多保持在其中的有机相与水相的体积比至多为1:1的区域。
    • 7. 发明授权
    • Liquid-liquid extraction apparatus
    • 液 - 液萃取仪
    • US4313826A
    • 1982-02-02
    • US164035
    • 1980-06-30
    • Reinhard GradlKlaus SchrodterKlaus-Peter Ehlers
    • Reinhard GradlKlaus SchrodterKlaus-Peter Ehlers
    • B01D11/04C01B25/46C22B3/02C22B3/26B01D17/02
    • C22B3/02B01D11/0457C01B25/462C22B3/0005Y02P10/234
    • The present invention relates to a mixer/settler-type apparatus for continuous liquid-liquid extraction. The apparatus is comprised of a separating vessel with an inclined bottom portion and an agitator-provided mixing vessel. The mixing vessel is tightly mounted to the inclined bottom portion of the separating vessel, the latter being formed with an upper outlet and a lower outlet and having a level indicator LI for determining phase boundary surface area installed therein. The lower outlet is passed through the separating vessel near its lowermost level and the upper outlet is passed therethrough near its upper end. The level indicator LI is connected to a regulator giving adjustment instructions to a structural element permitting the phase boundary surface area to be established in the separating vessel, distinctly above the upper end of the mixing vessel.
    • 本发明涉及一种用于连续液 - 液萃取的混合器/沉降器型装置。 该装置由具有倾斜底部的分离容器和具有搅拌器的混合容器组成。 混合容器紧紧地安装在分离容器的倾斜底部,后者形成有上部出口和下部出口,并具有用于确定安装在其中的相界面的水平指示器LI。 下部出口通过分离容器在其最低水平附近,并且上部出口在其上端附近通过。 电平指示器LI连接到调节器,其向结构元件施加调节指令,允许在分离容器中建立相界面表面积,明显地高于混合容器的上端。