HBMPPT-PSO对铀(Ⅵ)、钍(Ⅳ)的协同萃取及分离

研究了以甲苯作溶剂, Ｈ Ｂ Ｍ Ｐ Ｐ Ｔ（４苯甲酰基２,４ 二氢５甲基２苯基３ Ｈ吡唑硫酮３） Ｐ Ｓ Ｏ（石油亚砜）在硝酸介质中对铀（Ⅵ）、钍（Ⅳ）的萃取行为以及萃取剂浓度、酸度等各种因素对萃取分配比的影响,以确定 ２ 个萃取剂的协同萃取及分离效果。结果表明, Ｈ Ｂ Ｍ Ｐ Ｐ Ｔ 和 Ｐ Ｓ Ｏ 对铀（Ⅵ）有较好的协同萃取效果,一定条件下,该体系对铀（Ⅵ）、钍（Ⅳ）的分离系数可达 １０００ 左右。     

HBMPPT—DOSO—甲苯体系对铀（Ⅵ）的萃取及铀（Ⅵ）,钍（Ⅳ）之间的分离

以４－苯甲酰基－２,４－二氢－５－甲基－２－苯基－３Ｈ－吡唑唑酮－３（ＨＢＭＰＰＴ）为萃取剂,二正辛基亚砚为协萃剂,研究其在硝酸介质中对铀的萃取行为,以及萃取剂浓度、酸度等各种对萃取分配比的影响,以确定两种萃取剂的协同取及分离效果。     

磷酸三丁酯从硝酸介质中萃取铀（Ⅳ）和钍（Ⅳ）的动力学研究

用上升单液滴法分别研究了磷酸三丁酯从硝酸介质中萃取铀（Ⅳ）和钍（Ⅳ）的动力学，测定了不同条件对铀（Ⅳ）、钍（Ⅳ）萃取速率的影响，得出了萃取速率的规律，并对萃取机制进行了讨论。     

二苯并-18-冠-6萃取色层法分离铀(Ⅳ)、铀(Ⅵ)和铀(Ⅵ)、钍

冠醚萃取锕系元素的报道,近年来逐渐增多。我们曾选用二苯并-18-冠-6(简称DBC)-硝基苯作萃取剂,从盐酸溶液中萃取铀(Ⅳ)和铀(Ⅵ),取得了满意的结果。本文是在前文基础上,将DBC-硝基苯溶液吸附在401有机担体上作固定相,以盐酸水溶液作流动相,研究了铀(Ⅳ)和铀(Ⅵ)的吸附分配行为,及各种条件对铀吸附分配的影响,结果均与液液萃取机理相符。     

末端基为喹啉基的两个开链冠醚与铀(Ⅵ),钍(Ⅳ)配合物的合成与表征

合成了末端基为喹啉基的两个开链冠醚2,2' (乙撑二氧)二[(8 喹啉氧基甲基)苯](L1)和2,2' (乙撑二氧)二[(8 喹哪啶氧基甲基)苯](L2)与U(Ⅵ),Th(Ⅳ)的配合物;并使用1HNMR,IR,差热 热重分析,摩尔电导率和元素分析等方法对配合物进行了表征;确定U(Ⅵ)配合物的组成为[UO2LNO3]NO3·3H2O(L=L1,L2);Th(Ⅳ)配合物的组成为[ThL(NO3)2](NO3)2·nH2O(L=L1,n=1;L=L2,n=3)。     

亚砜和磷酸三丁酯对铀(Ⅵ)、钍(Ⅳ) 萃取行为的比较

合成并研究了6种双亚砜RSO(CH2)nSOR(n=4，6；R=CH3(CH2)2CH2-，CH3CH(CH3)CH2CH2-，CH3(CH2)3CH(C2H5)CH2-)对铀(Ⅵ)、钍(Ⅳ)的萃取及分离性能，并与磷酸三丁酯(TBP)作了比较，发现6种双亚砜在各实验条件下对铀(Ⅵ)、钍(Ⅳ)的萃取及分离性能均优于TBP。还初步探讨了双亚砜类萃取剂的结构与性能的关系。     

两种新型萃取剂的合成、表征及HCBMPPT对铀(Ⅵ)萃取机理的研究

合成了4－邻氯苯甲酰基－2，4－二氢－5－甲基－2－苯基－3H－吡唑硫酮－3（HCBMPPT）和4－邻氟苯甲酰基－2，4－二氢－5－甲基－2－苯基－3H－吡唑硫酮－3（HFMBPPT）两个新萃取剂，用波谱确定了结构。研究了HCBMPPT在硝酸介质中对铀（Ⅵ）的萃取行为，其萃取分配比随萃取剂浓度、pH值的升高而增大，同时对萃合物的化学组成及萃取机理进行了分析和讨论。     

N,N-二烷基取代酰胺萃取硝酸、铀(Ⅵ)和钚(Ⅳ)的研究

研究了N,N-二甲庚基乙酰胺(DMHAA),N,N-二丁基丁酰胺(DBBA)和N,N-二丁基己酰胺(DBHA)对硝酸、硝酸铀酰和硝酸钚的萃取。这些萃取剂对铀和钚萃取能力中等,其络合物在芳香族稀释剂中有很高的溶解度,不形成三相。在实验条件下DBHA和硝酸形成1:1络合物,和硝酸铀酰形成2:1络合物。研究表明,改变酰胺取代基链长和支链化程度有可能筛选出在中等酸度下共萃铀钚,低酸下优先反萃钚,实现铀钚分离的酰胺萃取剂。     

锕系、镧系元素分离中新萃取剂的研究(Ⅲ) --新萃取剂HMBMPPT的合成及其对铀(Ⅵ)的萃取研究

通过酰基化、氯化、硫化反应合成了新的酰代吡唑硫酮,即4-(4-甲氧基)-苯甲酰基-2,4-二氢-5-甲基-2-苯基-3H-吡唑硫酮-3(HMBMPPT).产物的结构用红外、氢核磁共振谱、质谱、元素分析及X射线衍射进行了表征.研究了以氯仿为溶剂HMBMPPT 在硝酸介质中对铀(Ⅵ)的萃取行为,考察了稀释剂、萃取剂浓度、酸度、温度及盐析剂浓度对分配比的影响.同时,对萃取配合物的化学组成及萃取机理也进行了分析和讨论.     

TODGA-DHOA体系萃取金属离子Ⅱ.对Pu(Ⅲ,Ⅳ,Ⅵ)的萃取

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,正十二烷为稀释剂体系对Pu(Ⅲ)、Pu(Ⅳ)和Pu(Ⅵ)的萃取行为,主要考察了萃取剂浓度、HNO₃浓度和NaNO₃浓度的影响。结果表明：TODGA和DHOA对Pu(Ⅲ)、Pu(Ⅳ)和Pu(Ⅵ)的萃取分配比大小顺序均为：D(Pu(Ⅲ))＞D(Pu(Ⅳ))＞D(Pu(Ⅵ)),TODGA/正十二烷体系中加入DHOA时,对Pu(Ⅲ,Ⅳ,Ⅵ)萃取具有一定抑制作用,但在较高酸度范围内(≥3.0 mol/L HNO₃),不论体系中Pu的价态为何种形式,TODGA均能对其进行有效的回收。TODGA萃取Pu(Ⅲ,Ⅳ,Ⅵ)的方程式分别为： Pu³⁺+3NO^-_3a+4TODGAo→Pu(NO₃) ₃·4TODGAo Pu⁴⁺_a+4NO^-_3a+3TODGAo→Pu(NO₃)₄·3TODGAo PuO²⁺_2a+2NO^-_3a+2TODGAo→PuO₂(NO₃)₂·2TODGAo     

Synergistic extraction of U（VI） and Th（IV） from nitric acid media with HBMPPT and TBP in toluene

The sysnergistic extraction of U(VI)and Th(IV) from nitric acid solution by HBMPPT(4-benzoyl-2,4-dihydro-5-methyl-2-phenyl-3H-pyrazol-3-thione) and TBP( tributylphosphate)in toluene was studied.The extraction ability of HBMPPT for U(VI) and Th(IV) was not so high.but when a little TBP was added in,the ability to extract U(VI) and Th(IV) was improved.The extracted complexes may be presented as UO2NO3.BMPPT.TBP and UO2(BMPPT)2.TBP for U(VI).and Th(NO3)3.BMPPT.TBP and Th(NO3)2(BMPPT)2.TBP for Th(IV),respectively,in the synergistic extraction system.The synergistic effect of HBMPPT and TBP makes the separation cofeeicient of U(VI)/Th (IV) or U(VI)/Eu(Ⅲ) reach a high value.     

Extraction of U（VI） and Th（IV） with a novel extractant N,N‘—tetrahexylmalonamide （THMA） in toluene

The dependence of THMA extraction behaviour for U(VI) and Th(IV) on nitric acid concentration,THMA concentratioin and molecular structure of extracted complex has been studied.For nitric acid solutions of 3.0 mol/L a coordinative mechanism may possibly dominate in the extraction of metal catioins,The complex composition of UO2(NO3)2(THMA)2,Th(NO3)4(THMA)2 and Th(NO3)4(THMA03 are proved.     

二正辛基亚砜与TBP协萃铀的研究

亚砜萃取铀、钚、钍、镎及裂片元素已进行过研究。本文研究亚砜和TBP对铀的协同萃取。关于亚砜的协萃效应许多人已进行过研究,结果表明,亚砜不仅与不同类型的萃取剂具有协同作用,而且两种不同亚砜混合时也存在协同效应。Svbramanian     

Synergistic extraction and separation of Am(III) and Ln(III) with HBMPPT-sulfoxide-HNO3-toluene system

1 INTRODUCTIONAmericiuxn is a typical transuredum element. The Chemical properties of Am(lll)are similar to that Of trivalent lanthanides, Ln(lll). The separation of Am(lll) froman(lll) represents one of the most difficult and twortant ploblems in the separationscien..[1-7]. Actinides (ill) overlap in size with Ln(lll) and thus two groups have sedlaxcharge-to-radius ratios. Choppin[61 considered that Am(lll) and Ln(lll) both ethbit"hard acid" Character and their interaction in solutio…     

Solvent extraction of nitric acid,uranium（VI） and thorium（IV） by N,N,N‘,N’—tetrahexylsuccinylamide

A new kind of diamide N,N,N‘,N‘-tetrahexylsuccinylamide(THSA) was synthesized,characterized and used for the extraction of HNO3,U(VI)and Th(IV) in a diluent composed of 0.5 volume fraction 1,2,4-trimethy benzene(TMB) and 0.5 volume fraction kerosene(OK),Extraction distribution coefficients of U(VI) and Th(IV) as functions of aqueous nitric acid concentation,extractant concentration.temperature and salting-out agent (LiNO3) have been studied,and it is found that THSA as an extractant is superior to TBP for extraction of U(VI) and Th(IV),Back Extraction was also studied.At low acidity,the main adduct of THSA and NHO3 is HNO3 is HNO3.THSA,THSA.(HNO3)2 and THSA.(HNO3)3 are also found at high acidity.The compositions of extracted species.apparent equilibrium constants and enthalpies of extraction reactions have also been calculated.     

The dodecyltolylsulfoxide extraction of uranium （VI）

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HBMPPT/TOPO/甲苯体系从硝酸介质中分离三价镅和镧系元素的研究

HBMPPT（4－苯甲酰基－2，4二氢－5－甲基－2－苯基－3H－吡唑硫酮－3）或TOPO（三正辛基氧化膦）的甲苯溶液，在HNO3介质中对三价镅 和镧系元素在所研究的pH范围内无明显的萃取能力，但当两者混合时，其协同效应可使该体系从镧系锕系混合溶液中有选择地萃取三价镅（pH3.5-4.5)，两者的分离系数达10－156，实验结果还显示，代表三价锕系元素的镅和各镧系元素与该体系的化学反应机理也有所不同。     

Extraction of uranium(VI) with N-octanoylpyrrolidine in sulfonated kerosene

1 INTRODUCTIONaide extractants have resistance to hydrolysis, Tadiolysis and their degradationproducts do not interfere severely in the separation process. They can buxn completely,without any solid waste. Furthermore, they extract actAndes from nitric acid mediaeffectively. Therefore, abide extractants have been proposed as an alternative to TBPfor the reprocessing of nuclear m.l.[l] However, when the acidity or concentration ofurhaum is high, the system presents third phase easily. In…     

Extraction of uranium（VI）from nitric acid with N—decanoylpyrrolidine（DPOD）in toluene

The extraction behaviors of uranium(VI) from nitric acid by N-decanoylpyrrolidine (DPOD) in toluene has been studied at varying concentrations of nitric acid,extractant,salting out agent LiNo3 and at different temperatures.The mechanism of extraction is discussed in the light of the results obtained.