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    • 11. 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。
    • 12. 发明授权
    • Production of pure alkali metal phosphate solutions from wet-processed
phosphoric acid
    • 从湿法磷酸生产纯碱金属磷酸盐溶液
    • US4100261A
    • 1978-07-11
    • US640772
    • 1975-12-15
    • Klaus-Peter EhlersSiegfried LischkaSiegfried Burkhardt
    • Klaus-Peter EhlersSiegfried LischkaSiegfried Burkhardt
    • C01B25/30C01B15/16C01B25/26
    • C01B25/303
    • Production of pure alkali metal phosphate solutions by neutralizing wet-processed phosphoric acid with an alkali liquor and/or carbonate. To this end, the wet-processed phosphoric acid is neutralized to a pH from 4 to 9, the resulting neutralization sludge consisting substantially of insoluble aluminum and iron phosphates is separated from the alkali metal phosphate solution and scrubbed with water, the sludge so treated is mixed with alkali liquor, alkali metal phosphate solution and water-glass so as to establish in the resulting suspension a molar ratio of SiO.sub.2 to Al.sub.2 O.sub.3 of at least 2 : 1 and a molar ratio of dissolved alkali metal oxide to dissolved P.sub.2 O.sub.5 ranging from 2.9 : 1 to 3.3 : 1, the whole is heated to temperatures from 80.degree. to 100.degree. C to effect breakup of the sludge in the suspension with the resultant formation of a solid matter residue together with a trialkali metal phosphate solution, the solid matter residue is separated from the trialkali metal phosphate solution, water-scrubbed, and discarded. More particularly, crude wet-processed phosphoric acid containing more than 45 weight % of P.sub.2 O.sub.5 is diluted with a portion of the scrubbing water obtained during operation and its P.sub.2 O.sub.5 -content is thereby reduced down to 30 to 45 weight %. The acid so treated is neutralized with an alkali liquor and/or carbonate and with the trialkali metal phosphate solution originating from the processed neutralization sludge.
    • 通过用碱液和/或碳酸盐中和湿法磷酸制备纯碱金属磷酸盐溶液。 为此,湿法处理的磷酸被中和至4至9的pH,所得到的基本上由不溶性铝和磷酸铁组成的中和污泥与碱金属磷酸盐溶液分离并用水洗涤,如此处理的污泥为 与碱液,碱金属磷酸盐溶液和水玻璃混合,以在所得悬浮液中建立SiO 2与Al 2 O 3的摩尔比至少为2:1,溶解的碱金属氧化物与溶解的P2O5的摩尔比为2.9:1, 1〜3.3:1,全部加热至80〜100℃,使悬浮液中的污泥分解,形成固体物质残留物和三碱金属磷酸盐溶液,固体残渣为 与三碱金属磷酸盐溶液分离,水洗涤并弃去。 更具体地,含有大于45重量%的P 2 O 5的粗制湿法磷酸用操作中获得的一部分洗涤水稀释,并且其P2O5含量因此降低至30至45重量%。 如此处理的酸被碱液和/或碳酸盐中和,并且来源于经处理的中和污泥的三碱金属磷酸盐溶液。