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    • 31. 发明授权
    • Process for purifying wet-processed phosphoric acid
    • 净化湿法磷酸的方法
    • US4556548A
    • 1985-12-03
    • US557349
    • 1983-12-01
    • Reinhard GradlHilmar Roszinski
    • Reinhard GradlHilmar Roszinski
    • C01B25/01C01B25/46C01B25/16C01B15/16C01B25/26C01F1/00
    • C01B25/01C01B25/461C01B25/462
    • The disclosure relates to a process for purifying crude, concentrated wet-processed phosphoric acid. To this end, the disclosure provides:(a) for the organic solvent to be mixed with the starting product in a ratio by volume of more than 4:1 to effect in a single process step the extraction--from the crude wet-processed phosphoric acid--of a quantity of phosphoric acid necessary for 40 to 70 weight % of the P.sub.2 O.sub.5 used to go into the organic phase, and for the resulting aqueous phosphoric acid raffinate to contain at most 28-32 weight % P.sub.2 O.sub.5, and for the organic phosphoric acid solution to be separated from the phosphoric acid raffinate;(b) for the separated organic phosphoric acid solution to be scrubbed with a quantity of scrubbing solution corresponding at most to 5% of the volume of the phosphoric acid solution; for the scrubbing solution to be recycled into stage (a), and for purified phosphoric acid and phosphate salt solution, respectively, to be recovered in known manner from the scrubbed phosphoric acid solution;(c) for the aqueous phosphoric acid raffinate produced in stage (a) to be neutralized, if desired, after prior removal of residual solvent, for it to be subjected to treatment with an alkaline agent with the resultant formation of a purified phosphate salt solution and precipitation of a so-called neutralization sludge, and(d) for said neutralization sludge and simultaneously obtained alkali metal phosphate solution to be separated from each other, for the sludge to be mixed with finely ground phosphate ore, and for the mixture to be made into phosphate pellets for use in electrothermal phosphorus production.
    • 本公开涉及纯化粗浓缩湿法磷酸的方法。 为此,本公开内容提供:(a)使有机溶剂与起始产物以体积比大于4:1的比例混合,以在单一工艺步骤中从粗制湿法磷酸 酸为一定量的磷酸,用于进入有机相中的40〜70重量%的P2O5,所得到的磷酸提取液含有最多28-32重量%的P2O5,对于有机磷酸 酸性溶液与磷酸提余液分离; (b)对于待洗涤的分离的有机磷酸溶液,其量为相当于磷酸溶液体积的至多5%的洗涤溶液; 将洗涤溶液再循环到阶段(a)中,分别用纯化的磷酸和磷酸盐溶液从已洗涤的磷酸溶液中以已知方式回收; (c)如果需要,在步骤(a)中制备的磷酸残液水溶液在预先除去残留溶剂之后,用碱性试剂处理,形成纯化的磷酸盐溶液 和所谓的中和污泥的沉淀,(d)对于所述中和污泥并同时获得的碱金属磷酸盐溶液彼此分离,用于与精细研磨的磷酸盐矿石混合的污泥,混合物为 制成用于电热磷生产的磷酸盐颗粒。