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    • 54. 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。
    • 55. 发明授权
    • Process and apparatus for purifying wet-processed phosphoric acid
    • 湿法磷酸净化工艺及装置
    • US4134964A
    • 1979-01-16
    • US815248
    • 1977-07-13
    • Klaus P. EhlersGero Heymer
    • Klaus P. EhlersGero Heymer
    • C01B25/237C01B25/18
    • C01B25/237
    • Process and apparatus for purifying crude wet-processed phosphoric acid containing free sulphuric acid. To this end, the wet-processed phosphoric acid is treated in a reaction zone, at a temperature of 70.degree. C to 100.degree. C, with a calcium compound and with calcium sulphate seed crystals; the sulphuric acid is precipitated in the form of calcium sulphate semihydrate with the resultant formation of a suspension; a proportion of the suspension, with the calcium sulphate semihydrate seed crystals present therein, is recycled to the reaction zone; the balance of the suspension is treated for separation of purified phosphoric acid from the accompanying precipitate; the precipitate is transformed into an aqueous suspension and the calcium sulphate semihydrate in said suspension is converted into calcium sulphate dihydrate; the aqueous phase of the suspension is separated from the solid matter therein, and the solid matter is water-washed; a proportion of the aqueous phase so separated is recycled together with a proportion of the wash water, for use in suspending and converting calcium sulphate semihydrate to dihydrate; and the balance of the aqueous phase and wash water are combined with the said purified phosphoric acid.
    • 用于净化含有游离硫酸的粗制湿法磷酸的方法和装置。 为此,湿法处理的磷酸在反应区中在70℃至100℃的温度下用钙化合物和硫酸钙晶种进行处理; 硫酸盐以硫酸钙半水合物的形式沉淀,形成悬浮液; 其中存在硫酸钙半水合物晶种的一部分悬浮液被再循环到反应区; 处理悬浮液的余量用于从所伴随的沉淀物中分离纯化的磷酸; 将沉淀物转化为水性悬浮液,并将所述悬浮液中的硫酸钙半水合物转化为硫酸钙二水合物; 悬浮液的水相与其中的固体物质分离,固体物质被水洗; 所分离的水相的一部分与一部分洗涤水一起再循环,用于将硫酸钙半水合物悬浮并转化成二水合物; 并将水相和洗涤水的余量与所述纯化的磷酸组合。
    • 56. 发明授权
    • Production of pure alkali metal phosphate solutions from wet-processed
phosphoric acids
    • 从湿法磷酸生产纯碱金属磷酸盐溶液
    • US4134962A
    • 1979-01-16
    • US771167
    • 1977-02-23
    • Klaus-Peter EhlersGero Heymer
    • Klaus-Peter EhlersGero Heymer
    • C01B25/30C01B15/16C01B25/16C01B25/26
    • C01B25/303
    • Alkali metal phosphate solutions (alkali metal oxide : P.sub.2 O.sub.5 - molar ratio greater than 1.9 : 1) of reduced vanadium and chromium contents are made from wet-processed phosphoric acids which are neutralized by means of an alkali metal hydroxide and/or carbonate. The alkali metal phosphate solutions contain less than 20 ppm of vanadium and less than 1 ppm of chromium and are made by stepwise neutralization. More specifically the acid is neutralized in a first step to an alkali metal oxide to P.sub.2 O.sub.5 - molar ratio of 1.0 : 1 to 1.8 : 1; resulting precipitate is separated and resulting solution is admixed with iron(II)salt at 60 to 90.degree. C. Next, the acid is neutralized in a second step to an alkali metal oxide to P.sub.2 O.sub.5 - molar ratio greater than 1.9 : 1, and resulting precipitate is separated again.
    • 还原的钒和铬含量的碱金属磷酸盐溶液(碱金属氧化物:P2O5 - 大于1.9:1的摩尔比)由湿法处理的磷酸制成,这些磷酸通过碱金属氢氧化物和/或碳酸盐中和。 碱金属磷酸盐溶液含有小于20ppm的钒和小于1ppm的铬,并且通过逐步中和制备。 更具体地,将酸在第一步中中和至碱金属氧化物至P2O5-摩尔比为1.0:1至1.8:1; 分离得到的沉淀物,得到的溶液与铁(II)盐在60至90℃下混合。接下来,将酸在第二步中中和至碱金属氧化物至P2O5-摩尔比大于1.9:1,得到 沉淀再次分离。