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process for purification by solvent extraction of phosphoric acid obtained by a wet process.

机译:通过溶剂萃取提纯由湿法获得的磷酸的方法。

摘要

A wet process phosphoric acid obtained by an solvent extraction method with n-butanol and/or isobutanol comprises (a) feeding a wet process phosphoric acid having a concentration of P2O5 of higher than 35 wt. % into an extraction battery; (b) adding sulfuric acid into a stage in fifth or higher stage from the step of discharging an extracted solution and in second or higher stage from the step of discharging raffinate in the extraction battery at a gram equivalent ratio given by subtracting the amount of sulfuric acid in the wet process phosphoric acid fed into the extraction battery from 1.2 to 2.0 times of the sum of total cation impurities in the wet process phosphoric acid fed into the extraction battery and total components of sodium, potassium and magnesium added to the purification battery; (c) discharging said extracted solution having a concentration of H3PO4 of 130 to 180 g./liter from said extraction battery; (d) adding at least one of the compounds of sodium, potassium and magnesium in second or higher stage from the step of discharging the solvent phase and in second or higher stage from the step of discharging the aqueous phase in the purification battery to give more than 0.4 equivalent per liter of the concentration of sodium, potassium and magnesium in the aqueous phase in the stage where at least one of alkali metal and magnesium compounds is added in the same battery.
机译:通过溶剂萃取法用正丁醇和/或异丁醇获得的湿法磷酸包括:(a)进料具有高于35wt。%的P 2 O 5浓度的湿法磷酸。 %放入提取电池; (b)将硫酸从排出提取液的步骤起的第五阶段或更高阶段和从排出提取液中的提余液的排出步骤的第二阶段或更高阶段中添加的克当量比中减去硫酸的量而添加到硫酸中供入萃取电池的湿法磷酸中的酸是供入萃取电池的湿法磷酸中总阳离子杂质的总和的1.2到2.0倍,以及加入纯化电池中的钠,钾和镁的总成分; (c)从所述提取电池中排出所述H 3 PO 4浓度为130-180g /升的提取液; (d)在净化电池中,从排出溶剂相的步骤的第二阶段或更高阶段以及从排出水相的步骤的第二阶段或更高阶段中,添加钠,钾和镁的至少一种化合物,以得到更多在同一电池中添加碱金属和镁化合物中的至少一种的阶段,水相中每升钠,钾和镁的浓度低于0.4当量。

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