TODGA-DHOA体系萃取金属离子 Ⅲ.对Am(Ⅲ)和三价镧系离子的萃取

    Extraction of Metal Ions From Aqueous Nitric Acid Solutions With TODGA and DHOA Ⅲ. Extraction of Am(Ⅲ) and Trivalent Lanthanides Ions

    • 摘要: 研究了以N,N,N’,N’-四辛基-3-氧戊二酰胺(TODGA)和N,N-二己基辛酰胺(DHOA)为萃取剂、正十二烷为稀释剂对Am(Ⅲ)和三价镧系元素的萃取行为,主要考察了萃取剂浓度、HNO3浓度、NaNO3浓度、金属离子浓度和温度的影响。结果表明:随着TODGA浓度的增加,TODGA/正十二烷和TODGA-DHOA/正十二烷两种萃取体系对Am(Ⅲ)和三价镧系元素的萃取分配比显著增加,DHOA对三价锕系和镧系萃取能力很弱,而DHOA的加入,对TODGA/正十二烷萃取Am(Ⅲ) 和三价镧系元素具有一定抑制作用。TODGA萃取三价镧系元素的分配比随着镧系原子序数的增加而增加,Am的分配比与Eu相近。TODGA萃取稀土元素是放热反应,萃取过程中焓变起主导作用,吉布斯自由能变(-ΔG)变化的规律也表明随着镧系原子序数的增加,TODGA对其萃取能力增强。通过对TODGA萃取Am(Ⅲ)和三价镧系元素机理探讨,得到萃取反应方程式均为:
      M3+aq+3NO-3,aq+3TODGAorg→M(NO3)3•3TODGAorg

       

      Abstract: In the present paper, extraction characteristics of N,N,N’,N’-tetraoctyl diglycolamide (TODGA) and N,N-dihexyl-octamide(DHOA), for Am(Ⅲ) and some trivalent lanthanides from nitric acid solutions were studied. The effects of extractant concentration in n-dodecane, metal ions concentration, acidity of the aqueous phase, ionic strength of salting out agent and temperature on distribution ratios were examined. The results show that the distributions of Am(Ⅲ) and some trivalent lanthanides increase remarkably with increasing the concentration of TODGA, HNO3 and NaNO3, Am(Ⅲ) and some trivalent lanthanides are hardly extracted by DHOA. After adding DHOA to TODGA/dodecane system, the distribution ratios of Am(Ⅲ) and trivalent lanthanides decrease with increasing of the concentration of DHOA, but the distribution ratios are large enough for their recovery from HNO3. The extraction distribution ratios of trivalent lanthanides with TODGA increase with increasing atomic number of them in conditions of our experiments. The enthalpy change, the entropy change and Gibbs energy change are obtained at 298.15K. The composition of the extracted species and the mechanism of extraction are also studied, and the extraction equation of Am(Ⅲ) and trivalent lanthanides by TODGA is deduced as follows: M3+aq+3NO-3,aq+3TODGAorg→M(NO3)3•3TODGAorg

       

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