{"title":"Uranium and Plutonium Extraction by N,N-dialkylamides Using Multistage Mixer-settler Extractors","authors":"Yasutoshi Ban, Shinobu Hotoku, Nao Tsutsui, Asuka Suzuki, Yasuhiro Tsubata, Tatsuro Matsumura","doi":"10.1016/j.proche.2016.10.022","DOIUrl":null,"url":null,"abstract":"<div><p><em>N,N</em>-Dialkylamides (monoamides) are known as extractants for U and Pu, and many studies have been carried out mainly by single-stage batch method. We have focused on two monoamides: <em>N,N</em>-di(2-ethylhexyl)-2,2-dimethylpropanamide (DEHDMPA) and <em>N,N</em>-di(2-ethylhexyl)butanamide (DEHBA), and proposed a multistage extraction process for recovering U and Pu by these monoamides. A continuous counter-current experiment was carried out to demonstrate the validity of this process. This process consisted of two cycles, and the 1st cycle and the 2nd cycle employed DEHDMPA and DEHBA as extractants, respectively. The feed solution for the 1st cycle was 5.1<!--> <!-->mol/dm<sup>3</sup> (M) nitric acid containing 0.92<!--> <!-->M U, 1.6<!--> <!-->mM Pu, and 0.6<!--> <!-->mM Np. The raffinate collected in the 1st cycle was used as the feed for the 2nd cycle. The ratios of U recovered in the U fraction and U-Pu fraction were 99.1% and 0.8%, respectively, and the ratios of U in the used solvents were <0.04%. The ratio of Pu recovered in the U-Pu fraction was 99.7%, and the ratio of Pu in the used solvents was in the order of 10<sup>–3</sup>–10<sup>–4</sup>%. The concentration ratio of U with respect to Pu in the U-Pu fraction was 9, and this indicated that Pu was not isolated. The decontamination factor of U with respect to Pu in the U fraction was obtained as 4.5×10<sup>5</sup>. These results supported the validity of the proposed process.</p></div>","PeriodicalId":20431,"journal":{"name":"Procedia Chemistry","volume":null,"pages":null},"PeriodicalIF":0.0000,"publicationDate":"2016-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/j.proche.2016.10.022","citationCount":"5","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Procedia Chemistry","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S187661961630064X","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 5
Abstract
N,N-Dialkylamides (monoamides) are known as extractants for U and Pu, and many studies have been carried out mainly by single-stage batch method. We have focused on two monoamides: N,N-di(2-ethylhexyl)-2,2-dimethylpropanamide (DEHDMPA) and N,N-di(2-ethylhexyl)butanamide (DEHBA), and proposed a multistage extraction process for recovering U and Pu by these monoamides. A continuous counter-current experiment was carried out to demonstrate the validity of this process. This process consisted of two cycles, and the 1st cycle and the 2nd cycle employed DEHDMPA and DEHBA as extractants, respectively. The feed solution for the 1st cycle was 5.1 mol/dm3 (M) nitric acid containing 0.92 M U, 1.6 mM Pu, and 0.6 mM Np. The raffinate collected in the 1st cycle was used as the feed for the 2nd cycle. The ratios of U recovered in the U fraction and U-Pu fraction were 99.1% and 0.8%, respectively, and the ratios of U in the used solvents were <0.04%. The ratio of Pu recovered in the U-Pu fraction was 99.7%, and the ratio of Pu in the used solvents was in the order of 10–3–10–4%. The concentration ratio of U with respect to Pu in the U-Pu fraction was 9, and this indicated that Pu was not isolated. The decontamination factor of U with respect to Pu in the U fraction was obtained as 4.5×105. These results supported the validity of the proposed process.
N,N-双基酰胺(单酰胺)被认为是U和Pu的萃取剂,许多研究主要是通过单级间歇法进行的。以N,N-二(2-乙基己基)-2,2-二甲基丙酰胺(DEHDMPA)和N,N-二(2-乙基己基)丁酰胺(DEHBA)两种单酰胺为研究对象,提出了用这两种单酰胺多级提取U和Pu的工艺。通过连续逆流实验验证了该方法的有效性。该工艺分为两个循环,第一个循环和第二个循环分别采用DEHDMPA和DEHBA作为萃取剂。第一个循环的进料液为5.1 mol/dm3 (M)硝酸,含0.92 M U、1.6 mM Pu和0.6 mM Np。第一个循环收集的萃余液作为第二个循环的进料。U馏分和U- pu馏分中U的回收率分别为99.1%和0.8%,废溶剂中U的回收率为0.04%。U-Pu馏分中Pu的回收率为99.7%,废溶剂中Pu的回收率为10-3-10-4%。U-Pu馏分中U与Pu的浓度比为9,说明Pu未被分离。U对U馏分中Pu的去污系数为4.5×105。这些结果支持了所提议的过程的有效性。