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Optimization and separation mechanism of Ni(II) removal from synthetic wastewater using response surface method

机译:响应表面法从合成废水中除去Ni(II)的优化和分离机理

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In this study, the optimization of Ni(II) removal and water recovery in the ion flotation were evaluated using the response surface method. The Ni(II) removal and water recovery were modeled and described as a function of the main variables including pH, collector concentration, and frother concentration. Seventeen experiments were performed as a central composite design by 2(3) full factorial design. The results showed that the pH and collector concentration have a significant effect on the Ni(II) removal and water recovery during the process in which they are increased with increasing the pH and collector concentration. The separation mechanism changed with changes in the pH solution, in which foam fractionation performed at pH levels of 1.3, 3, 5.5, and 8 and ion flotation at a pH of 9.7. The Ni(II) removal in the foam fractionation process increased from 11.5 to 85.5% with increasing pH from 1.3 to 5.5 and then decreased to 76.92% at a pH of 8. Subsequently, the Ni(II) removal increased to 100% at a pH of 9.7 in which the ion flotation process was performed. The results indicate that the ion flotation efficiency was more than foam fractionation efficiency for Ni(II) removal from the solution.
机译:在该研究中,使用响应表面法评估离子浮选中的Ni(II)去除和水回收的优化。将Ni(II)除去和水回收是模拟的,并描述为包括pH,收集器浓度和浓度的主要变量的函数。通过2(3)个完整因子设计,将十七个实验作为中央复合设计进行。结果表明,在随着pH和收集器浓度的增加,pH和收集器浓度对Ni(II)的去除和水回收产生显着影响。分离机制随pH溶液的变化而改变,其中在pH的pH水平为1.3,3,5.5和8和pH的pH为9.7的离子浮选时进行泡沫分馏。泡沫分馏过程中的Ni(II)除去从11.5至85.5%增加,将pH从1.3〜5.5增加到5.5,然后在8的pH下降至76.92%。随后,Ni(II)的去除在a下降至100% pH为9.7,其中进行离子浮选过程。结果表明离子浮选效率大于来自溶液中的Ni(ii)的泡沫分馏效率。

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