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    • 4. 发明授权
    • Solvent extraction method of phosphoric acid
    • 磷酸溶剂萃取法
    • US4377562A
    • 1983-03-22
    • US309774
    • 1981-10-08
    • Yoichi HiragaOsamu Watanabe
    • Yoichi HiragaOsamu Watanabe
    • C01B25/234C01B25/46C01B25/16
    • C01B25/462C01B25/461
    • A method for solvent extraction of phosphoric acid comprises counter-currently contacting an impure phosphoric acid solution containing at least 45 wt. % of P.sub.2 O.sub.5 with a partially water-miscible solvent in the presence of sulfuric acid, and which is characterized in that(a) as said solvent, a solvent in which from 3 to 10 wt. % of water is soluble, is used, and(b) sulfuric acid is added to a place where the H.sub.3 PO.sub.4 concentration in the aqueous phase is at most 3 mol./l so as to bring the relation between the free sulfuric acid concentration (Y (mol/l)) and the H.sub.3 PO.sub.4 concentration (X (mol/l)) in the aqueous phase of the same place to satisfy the formula5.0-0.83X.gtoreq.Y.gtoreq.2.5-0.83X within the range of the H.sub.3 PO.sub.4 concentration in the aqueous phase being from 0.5 to 3 mol/l.
    • 溶剂萃取磷酸的方法包括与含有至少45wt。 %的P 2 O 5与部分水混溶性溶剂在硫酸的存在下反应,其特征在于:(a)作为所述溶剂,其中3-10wt。 使用%的水溶解,并且(b)将硫酸加入水相中的H 3 PO 4浓度为3摩尔/升以下的地方,以使游离硫酸浓度(Y (mol / l))和H 3 PO 4浓度(X(mol / l))在满足公式5.0-0.83X> / = Y> / = 2.5-0.83X的范围内 水相中的H 3 PO 4浓度为0.5-3mol / l。
    • 7. 发明授权
    • Crud handling circuit
    • Crud处理电路
    • US4190633A
    • 1980-02-26
    • US785947
    • 1977-04-08
    • Jay C. SmithRonald J. ManuelJames E. McAllister
    • Jay C. SmithRonald J. ManuelJames E. McAllister
    • C01B25/234B01D11/04C01B25/238C01B25/46C22B60/02C01B25/16
    • C22B60/026B01D11/04C01B25/238C01B25/461
    • A method for handling the problem of crud formation in the solvent extraction of wet-process phosphoric acid is described. Crud is the name ordinarily given to the thick interfacial layer of semi-floatable material which tends to form and accumulate, and which interferes with many of the extraction processes and, in particular, with the solvent extraction of wet-process phosphoric acid. The method described provides for the operation of the solvent extraction stages in a manner that allows the formation and temporary accumulation of crud in those stages whereupon the solvent and the crud are then removed from the extraction stages and treated in a series of operations which include a clarification step, an acid removal step, a water wash step and a caustic treatment step, which steps effectively separate the solvent from the crud, and remove the crud components from the system and regenerate otherwise unusable solvent.The invention is particularly applicable to the solvent extraction of wet-process phosphoric acid for the recovery of uranium by the reductive stripping technique.
    • 描述了在湿法磷酸的溶剂萃取中处理粗屑形成问题的方法。 Crud是通常给予易于形成和积聚的半浮性材料的厚界面层的名称,并且其干扰许多提取方法,特别是与湿法磷酸的溶剂萃取。 所描述的方法提供了溶剂萃取阶段的操作,其允许在那些阶段中形成和临时堆积原油,然后从萃取阶段除去溶剂和原油,并在一系列操作中进行处理,这些操作包括 澄清步骤,酸去除步骤,水洗步骤和苛性碱处理步骤,其有效地将溶剂与原油分离,并从系统中除去原油组分并再生不可用的溶剂。 本发明特别适用于通过还原剥离技术用于回收铀的湿法磷酸的溶剂萃取。
    • 10. 发明授权
    • Purification of phosphoric acid
    • 磷酸的纯化
    • US4877594A
    • 1989-10-31
    • US283560
    • 1988-12-13
    • Laurence W. BiermanMichael L. LopezJames E. Perkins, III
    • Laurence W. BiermanMichael L. LopezJames E. Perkins, III
    • C01B25/46
    • C01B25/461C01B25/462
    • A mixture of hydrophobic and hydrophilic extractants is used to separate phosphate values from impurities found in phosphoric acid. In one approach, impurities are removed from phosphoric acid and the phosphate values are recovered, by introducing polyphosphates and ammonium ions into the impure acid, and contacting the impure acid with a mixture of low and high molecular weight alcohols, one of which is hydrophilic and the other hydrophobic, in a single stage. The phosphate values segregate to the high molecular weight alcohol fraction, and the impurities segregate to the low molecular weight alcohol fraction. After separation of the alcohol solutions, the phosphate values and the impurities are separated from their respective extractant solutions, and the alcohols recirculated. Polyphosphates and ammonia are preferably provided by reacting a portion of the original feed acid with ammonia at elevated temperature in a pipe reactor.
    • 使用疏水和亲水萃取剂的混合物将磷酸盐与在磷酸中发现的杂质分离。 在一种方法中,从磷酸中除去杂质,通过将多磷酸盐和铵离子引入不纯的酸中并将不纯的酸与低分子量和高分子量醇的混合物接触,其中一种是亲水的和 另一个疏水,在一个阶段。 磷酸盐分离成高分子量醇馏分,杂质分离成低分子量醇馏分。 在分离醇溶液后,将磷酸盐值和杂质从它们各自的萃取剂溶液中分离出来,醇再循环。 聚磷酸盐和氨优选通过使一部分原始进料酸与氨在升高的温度下在管式反应器中反应来提供。