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Metallic anion recovery from aqueous streams and removal agent recycle in the polymer–surfactant aggregate process

机译:从含水流和去除剂中回收聚合物 - 表面活性剂聚集体加工的金属阴离子

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摘要

In a previous contribution, a new application of the polymer–surfactant aggregate (PSA) process was developed; the removal of metallic anions from dilute aqueous solutions. A subsequent pH adjustment method has been developed to recover the metallic anions from the flocculated PSAs into a concentrated solution and then to recover the polymer (PAA) and surfactant (MTAB) for recycling. The PSA is a colloidal structure that is formed by micelle-like aggregates associating with the oppositely charged polymer chains. The PSA can then bind with metallic anions, and will eventually flocculate out of the solution under colloidal destabilisation. In the work presented, a small volume of 0.1 M NaOH is firstly added to the flocs to leach out the bound metallic anions in 15 min, and then a coarse filter is used to separate out the basic solution containing 5–20 times more concentrated metallic anions than the original effluent. After the metallic anion recovery, the flocs can be completely dissolved in a small volume of 0.05 M H 2 SO 4 . This acidic solution, containing PAA and MTAB, is then reused in the next treatment cycle; meanwhile, the pH of the feed is adjusted to 5.3 by adding NaOH. The results show that the recovery efficiency of CrO 4 2 − at an optimum pH of 12 is 94%, and the recovery efficiency of PAA–MTAB at its optimum pH of 1.4 is 94%. The kinetics of the recovery process is quick; both the basification and acidification steps can be completed within 15–20 min. In addition, the removal efficiency of 0.2 mM CrO 4 2 − solution remains at the same level when using previously recycled PAA and MTAB (with a small makeup of the MTAB to cover leakage at the metallic anion removal stage). In short, the sequential pH adjustment method is able to recover and concentrate the metallic anions from the flocculated PSAs, and then recover the removal agent for recycling into the process with little deterioration of removal ability.
机译:在以前的贡献中,开发了聚合物 - 表面活性剂聚集体(PSA)过程的新施用;从稀水溶液中除去金属阴离子。已经开发出随后的pH调节方法以将金属阴离子从絮凝的PSA恢复成浓缩溶液,然后回收聚合物(PAA)和表面活性剂(MTAB)进行再循环。 PSA是一种胶体结构,其由胶束聚集体形成,其与相对带电的聚合物链相关联。然后,PSA可以与金属阴离子结合,并最终将在胶体稳定化下的溶液中絮凝。在所呈现的工作中,首先将少量0.1米NaOH加入到絮凝物中以在15分钟内浸出结合的金属阴离子,然后使用粗过滤器将含有5-20倍的浓缩金属的碱性溶液分离出来阴离子而不是原始污水。在金属阴离子恢复之后,絮状物可以完全溶解在0.05m H 2 SO 4的少量体积中。然后将该酸性溶液,含有Paa和mtab在下一次治疗循环中重复使用;同时,通过添加NaOH将饲料的pH调节至5.3。结果表明,CRO 4 2的回收效率为12的12%是94%,并且Paa-mtab的恢复效率为1.4的最佳pH为94%。恢复过程的动力学很快;碱化和酸化步骤都可以在15-20分钟内完成。另外,当使用先前再循环的PAA和MTAB时,0.2mM CRO 4 2 - 溶液的去除效率保持在相同的水平(用MTAB的小化妆,以在金属阴离子去除阶段覆盖泄漏)。简而言之,序列pH调节方法能够从絮凝的PSA恢复和浓缩金属阴离子,然后回收去除剂以再循环到过程中,除去能力很小。

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    L.C. Shen; N.P. Hankins;

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