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    • 1. 发明授权
    • Process for purifying wet-processed phosphoric acid
    • 净化湿法磷酸的方法
    • US4596703A
    • 1986-06-24
    • US557111
    • 1983-12-01
    • Reinhard GradiGero HeymerGunther Schimmel
    • Reinhard GradiGero HeymerGunther Schimmel
    • C01B25/234C01B25/46C01B25/16C01B15/16C01B25/26
    • C01B25/461C01B25/462
    • 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 the extraction in a single process step--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; and(c) for the aqueous phosphoric acid raffinate produced in stage (a), if desired after prior removal of residual solvent therefrom, to be directly utilized or subjected to known purifying treatment.
    • 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进行萃取,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; 和(c)如果需要,在步骤(a)中制备的磷酸残液水溶液中,在预先除去残余溶剂之后,直接使用或进行已知的纯化处理。
    • 7. 发明授权
    • Continuous process for complete removal or organic impurities from and
complete decolorization of prepurified wet-process phosphoric acid
    • 用于完全去除或有机杂质的连续方法和完全脱湿的湿法磷酸完全脱色
    • US4906445A
    • 1990-03-06
    • US311640
    • 1989-02-16
    • Gunther SchimmelGerhard BettermannGero HeymerFriedrich Kolkmann
    • Gunther SchimmelGerhard BettermannGero HeymerFriedrich Kolkmann
    • C01B25/234C01B25/235C01B25/46
    • C01B25/461C01B25/235
    • A continuous process is indicated for complete removal of organic impurities from and complete decolorization of pre-purified wet-process phosphoric acid which has been purified by an extractive method using an organic solvent, freed from residual hydrofluoric acid by steam stripping and treated with hydrogen peroxide at elevated temperature, which comprises mixing the pre-purified wet-process phosphoric acid and the hydrogen peroxide in a mixing zone at a temperature of from 100.degree. to 200.degree. C., preferably 140.degree. to 160.degree. C., and allowing them to react at this temperature for a further 1 to 4 hours, cooling to from 85.degree. to 90.degree. C. the pre-purified wet-process phosphoric acid treated in this way and pumping it at this temperature with exclusion of air firstly through an activated charcoal bed which has been prepared on the basis of peat and has been steam-activated and has a BET surface area of from 800 to 1000 m.sup.2 /g, and subsequently through a silicon carbide and/or graphite bed while maintaining a pumping rate of less than 0.5 m.sup.3 /h of wet-process phosphoric acid per m.sup.3 of activated charcoal bed.
    • 指示完全除去有机杂质并完全脱色预纯化的湿法磷酸的连续方法,其通过萃取方法使用有机溶剂纯化,通过汽提除去残留的氢氟酸并用过氧化氢处理 在高温下,其包括在预先纯化的湿法磷酸和过氧化氢的混合区中在100至200℃,优选140至160℃的温度下混合,并使它们 在该温度下再反应1至4小时,冷却至85℃至90℃,预纯化的湿法磷酸以此方式处理并在该温度下泵送,首先通过活性炭排除空气 基于泥炭制备并已蒸汽活化并具有800至1000m2 / g的BET表面积的床,随后通过碳化硅和/或石墨b 同时保持每立方米活性炭床的湿法磷酸的泵送速率小于0.5m 3 / h。