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CMP流程处理高放废液后的锕系镧系的分离研究

CMP流程处理高放废液后的锕系镧系的分离研究[J]. 原子能科学技术, 1993, 27(3): 242-242. DOI: 10.7538/yzk.1993.27.03.0242
引用本文: CMP流程处理高放废液后的锕系镧系的分离研究[J]. 原子能科学技术, 1993, 27(3): 242-242. DOI: 10.7538/yzk.1993.27.03.0242
SHU RONGHUA;ZHAO HUGEN;HU JINGXIN;HUANG HUAIAN China Institute of Atomic Energy, P. O. Box 275, Beijing, 102413. STUDY ON THE SEPARATION OF ACTINIDES AND LANTHANIDES RECOVERED FROM HIGH-LEVEL LIQUID WASTE(HLLW) BY CMP PROCESS[J]. Atomic Energy Science and Technology, 1993, 27(3): 242-242. DOI: 10.7538/yzk.1993.27.03.0242
Citation: SHU RONGHUA;ZHAO HUGEN;HU JINGXIN;HUANG HUAIAN China Institute of Atomic Energy, P. O. Box 275, Beijing, 102413. STUDY ON THE SEPARATION OF ACTINIDES AND LANTHANIDES RECOVERED FROM HIGH-LEVEL LIQUID WASTE(HLLW) BY CMP PROCESS[J]. Atomic Energy Science and Technology, 1993, 27(3): 242-242. DOI: 10.7538/yzk.1993.27.03.0242

CMP流程处理高放废液后的锕系镧系的分离研究

STUDY ON THE SEPARATION OF ACTINIDES AND LANTHANIDES RECOVERED FROM HIGH-LEVEL LIQUID WASTE(HLLW) BY CMP PROCESS

  • 摘要: 研究了以HDEHP为萃取剂、DTPA为络合剂,在0.2—0.5mol/l HNO_3酸度下实现An~?(Ⅲ)、Ln~(2?)(Ⅲ)分离的工艺条件。结果表明,Am(Ⅲ)、Gd(Ⅲ)和 En(Ⅲ)的分配比和HDEHP浓度的平方成正比,和酸度的3次方成反比。随温度的升高和料液中金属离子起始浓度的增大而降低。Am(Ⅲ)、Gd(Ⅲ)和En(Ⅲ)的萃取反应热依次为-7.1×10~3J·mol~(-1),-9.2×10~3J·mol~(-1)和-1.9×10~3J·nol~(-1)。采用1.0 mol/l HDEHP-煤油为萃取剂,pH3.2-3.6,0.15 mol/l DTPA-2 mol/l 乳酸为反萃剂,用模拟料液进行串级实验。Am(Ⅲ)近100%被回收,和Am(Ⅲ)共存于水相的Ln~(2?)(Ⅲ)少于3%。根据实验结果提出了概念流程。

     

    Abstract: The work investigates the technique conditions for the separation of An(Ⅲ) and Ln (Ⅲ) withinthe acidity range of 0. 2--0. 5 mol/l HNO_3. The effects of varying HDEHP, DTPA, H~+ and initialmetal ion concentrations, and temperature are studied. The results show that the distribution ratio ofAm(Ⅲ), Gd(Ⅲ) and Eu(Ⅲ) are proportional to the second power of HDEHP concentration, and in-versely proportional to the third power of H~+ concentration, respectively. The extraction enthalpies ofAm(Ⅲ), Gd(Ⅲ) and Eu(Ⅲ) are -7.1×10~3 J·mol~(-1), -9.2×10~3 J·mol~(-1) and -1.9×10~3 J·mol~(-1) in turn. 1.0 mol/l HDEHP--kerosen is used for coextraction of An (Ⅲ) and Ln(Ⅲ), and a lac-tic acid--DTPA mixture solution is used for selective striping of An(Ⅲ). Counter--current cascade ex-periments are performed. Nearly 100% An(Ⅲ) is recovered, less than 3% Ln(Ⅲ) remains with An(Ⅲ). A conceptual flowsheet for the separation is suggested.

     

  • [1] 1 赵沪根,叶玉星,杨学先.双配位基有机磷萃取剂DHDECMP萃取Am(Ⅲ)的研究.原子能科学技术,1983,17(3) :332. 2 赵沪根,叶玉星,杨学先.DHDECMP萃取Pu(Ⅳ)及Pu(Ⅳ)--Am(Ⅲ)分离的研究.核化学与放射化学,1984,6(4) :236--239. 3 庄维新,邓定机,赵沪根,等.从动力堆核燃料后处理废水中提取镅(锔)和稀土元素.原子能科学技术,1983,17(4) :443. 4 Kosyakov VN, Yerin EA. Separation of Transplutonium and Rare--earth Elements by Extraction With HDEHP From DTPA Solution. Journal of Radioanalytical Chemistry, 1978, 43 (1) : 37. 5 Svantesson I, Hangstrom I, Persson G, et al. Separation of Americium and Neodymium by Selective Stripping and Subsequent Extraction With HDEHP Using DTPA--Lactic Acid Solution in a Closed Loop. Radiochem Radioanal Letters, 1979, 37(4,5) : 215--222. 6 Kolarik Z, Koch G, Kusel HH, et al. Separation of Americium and Curium From Highly Radioactive Waste Solutions: KFK--1553. 1972. 7 傅献彩,陈瑞华.物理化学(上).第3版.北京:高等教育出版社,1985. 367.
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出版历程
  • 收稿日期:  1991-09-24
  • 刊出日期:  1993-05-19

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