首页> 外文期刊>International Journal of Nonferrous Metallurgy >Extraction Kinetics of Ni(II) in the Ni2+- SO42--Ac-(Na+, H+)-Cyanex 272 (H2A2)-Kerosene-3% (v/v) Octan-1-ol System Using Single Drop Technique
【24h】

Extraction Kinetics of Ni(II) in the Ni2+- SO42--Ac-(Na+, H+)-Cyanex 272 (H2A2)-Kerosene-3% (v/v) Octan-1-ol System Using Single Drop Technique

机译:单滴技术在Ni2 + -SO42--Ac-(Na +,H +)-Cyanex 272(H2A2)-煤油3 %(v / v)Octan-1-ol体系中萃取Ni(II)的动力学

获取原文
           

摘要

The kinetics of extraction of Ni(II) in the Ni2+-SO4 2_AC- (Na+, H+)-Cyanex 272 (H2A2)-kerosene-3% (v/v) octan-1-ol system using the single falling drop technique have been reported. The flux of Ni2+ transfer (F) at 303 K in presence of 3% (v/v) octan-1-ol (de-emulsifier) can be represented as:.Depending on reaction parameters, the activation energy (Ea) and enthalpy change in activation (DH±) varies within 17 - 58 kJ/mol and 17 - 67 kJ/mol, respectively. Entropy change in activation (DS±) is always negative. Based on the empirical flux equation, Ea and DS± values, mechanisms of extractions in different parametric conditions are proposed. At low and [Ac-], and pH, the chemical controlled step is: Ni2+ + A- → NiA+; and this reaction occurs via an SN2 mechanism. But in most parametric conditions, the process is under intermediate control; and at high SO42- and [Ac-], and pH, the extraction process is under diffusion control.
机译:使用单滴滴技术在Ni2 + -SO4 2_AC-(Na +,H +)-Cyanex 272(H2A2)-煤油-3 %(v / v)辛烷-1-醇体系中萃取Ni(II)的动力学已经报道。在3%(v / v)的octan-1-ol(反乳化剂)存在下,303 K时Ni2 +的转移通量(F)可以表示为:根据反应参数,活化能(Ea)和活化焓变化(DH±)分别在17-58 kJ / mol和17-67 kJ / mol之间。激活的熵变(DS±)始终为负。基于经验通量方程,Ea和DS±值,提出了不同参数条件下的萃取机理。在较低的[Ac-]和pH值下,化学控制步骤为:Ni2 + + A-→NiA +;并且该反应通过SN2机制发生。但是在大多数参数条件下,该过程处于中间控制之下。在高SO42-和[Ac-]以及pH值下,萃取过程处于扩散控制之下。

著录项

相似文献

  • 外文文献
  • 中文文献
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号