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Chloride removal from industrial cooling water using a two-stage ultra-high lime with aluminum process

机译:两级超高石灰铝工艺从工业冷却水中去除氯化物

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This study evaluates the feasibility of chloride removal from industrial cooling water using a two-stage ultra-high lime with aluminum (UHLA) process. This two-stage UHLA process was employed to treat recycled cooling water collected from an industrial plant containing high concentrations of carbonate ions and suspended solids. The presence of anions such as carbonate and bicarbonate limits the removal of the desired ions, namely sulfate and chloride ions. The two-stage UHLA process was used in which lime is added at the first stage to remove carbonate ions, and both lime and sodium aluminate are added at the second stage to remove chloride and sulfate ions. Experimental results showed that chloride removal can be achieved at reasonable lime and sodium aluminate dosages. The results of equilibrium experiments indicate that the most cost-effective performance in the two-stage configuration occurred with lime dosages in the first and second stages equal to 50 mM and an aluminum dosage equal to 30 mM. These dosages achieved a 56% chloride removal.
机译:这项研究评估了使用两级超高铝铝石灰(UHLA)工艺从工业冷却水中去除氯化物的可行性。此两阶段的UHLA工艺用于处理从含有高浓度碳酸根离子和悬浮固体的工业工厂收集的循环冷却水。阴离子如碳酸根和碳酸氢根的存在限制了所需离子即硫酸根和氯离子的去除。使用两阶段UHLA工艺,其中在第一阶段添加石灰以去除碳酸根离子,在第二阶段同时添加石灰和铝酸钠以去除氯离子和硫酸根离子。实验结果表明,在合理的石灰和铝酸钠用量下可以实现氯化物的去除。平衡实验的结果表明,在两阶段配置中,最具成本效益的性能发生在第一和第二阶段的石灰剂量等于50 mM和铝剂量等于30 mM的情况下。这些剂量实现了56%的氯化物去除率。

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