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PURIFICATION OF CaCl2 SOLUTIONS USING PUROLITE S930 RESIN DYNAMIC STUDIES

机译:利用纯S930树脂动力学研究纯化CaCl2溶液

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Resin Purolite S930 is used with numerous applications in refining salt solutions concerning transition metals. This work presents the influence of experimental conditions(?) to remove Fe(II) from 34% CaCl 2 solutions using chelating resin Purolite S930 in dynamic regime and also the experimental conditions about desorbtion efficiency. The resuls show that under circumstances ( T=22 0 C, volume of resin = 10,2 ml, layer heihgt=13 cm, pH=2.3), usable breakthrough capacity decrease with the increasing of feeding flow and increasing of the concentration of Fe(II) in feeding solution . The volume of refined solution decreases with the increasing of Fe(II) concentration in feeding solution. Usable capacity for sorbtion in dynamic regime is 197 mg Fe(II)/g. Desorbtion effiency increase with height of resin bad and HCl concentration . Increasing the concentration of HCl from 2N to 10% and resin dose from 2 grames to 4 grames desorbtion effiency increases from 50 to 520 times.
机译:树脂Purolite S930可广泛用于精炼有关过渡金属的盐溶液。这项工作提出了在动态条件下使用螯合树脂Purolite S930从34%CaCl 2溶液中去除Fe(II)的实验条件的影响,以及解吸效率的实验条件。结果表明,在一定条件下(T = 22 0 C,树脂体积= 10,2 ml,层高= 13 cm,pH = 2.3),可用的进料量随进料流量的增加和Fe浓度的增加而降低(二)进料溶液。精制溶液的体积随着进料溶液中Fe(II)浓度的增加而减小。在动态条件下吸附的可用容量为197 mg Fe(II)/ g。解吸效率随树脂高度和HCl浓度的增加而增加。 HCl浓度从2N增加到10%,树脂剂量从2克增加到4克,解吸效率从50倍提高到520倍。

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