HEHEHP与PMBP协同萃取希土元素(Ⅲ)的机理研究

本文研究了2-乙基己基膦酸单(2-乙基己基)酯(HEHEHP,HL)和1-苯基-3-甲基-4-苯甲酰基吡唑啉酮-5(PMBP,HA)的苯溶液在不同矿物酸(H_2SO_4,HCl HNO_3)介质中对希土元素(Ⅲ)的协同萃取。并以Nd~(3+),Yb~(3+),Lu~(3+)为例,研究了HEHEHP-PMBP苯溶液从HNO_3介质中协同萃取希土元素(Ⅲ)的机理,用斜率法确定了协萃配合物的组成,轻希土元素为Nd(HL_2)·A_2,重希士元素为Yb(HL_2)·A,Lu(HL_2)_2·A,计算了协萃反应的平衡常数,还研究了温度对协萃反应的影响,求出了萃取过程的热力学函数。观测了协萃配合物的IR及NMR谱。

有机磷（膦）酸双溶剂体系及离子液基体系对稀土萃取的研究

本文系统研究了由酸性磷（膦）类萃取剂所构成的双溶剂萃取体系对稀土的协同萃取效应；考察了添加剂对磷（膦）类萃取体系的分离能力，反萃性能，界面性质及动力学机理的影响；运用绿色溶剂---室温离子液体替代挥发性有机溶剂为稀释剂，研究了磷（膦）类萃取剂在离子液体中萃取稀土的性能，具体的研究内容如下： 1． 考察了HDEHP， HHEOIPP， Cyanex272， Cyanex302，Cyanex301分别与HEHEHP构成混合萃取体系在盐酸介质中对RE3+的萃取和分离性能，推导了协萃反应方程式，计算了相邻稀土元素间的分离系数，讨论了各混合体系对部分稀土相互分离的可能性，并从萃取剂结构方面对不同萃取体系萃取能力的差别给出了解释。 2． 用层流恒界面池法研究了添加剂isooctanol对HEHEHP萃取体系萃取Yb3+的传质动力学的影响，综合搅拌速率判别法，界面判别法，温度判别法，得出了萃取过程为伴随有界面化学反应的扩散传质。考察了水相酸度、有机相浓度等因素对反应速率的影响，提出了萃取速率方程及动力学传质机理，计算了扩散层厚度及扩散速率常数，建立了传质模型。 3． 考察了甲庚醇浓度、温度、离子强度等因素对HEHEHP-isooctanol体系界面活性的影响，并定性探讨了极性添加剂isooctanol对HEHEHP-Yb3+-HCl体系萃取动力学的影响。 4． 选择室温离子液体[C8mim][PF6] 作为溶剂，系统研究了磷(膦)类萃取剂HEHEHP对稀土的萃取能力，计算了HEHEHP- IL体系的分离系数，推测了萃取体系的反应机理，并与相同萃取条件下庚烷体系中HEHEHP对稀土的萃取性能进行了比较。

Cyanex302及CA-12萃取稀土动力学的研究

随着萃取技术的不断发展，人们日益要求更加深入的了解萃取过程的机制及其动力学特性。以便有效地控制和强化萃取过程，提高萃取效率，或者利用萃取动力学的差异来实现某些分离嘴过程。尽管许多萃取过程进行得很快，但是人们也发现不少的金属鳌合物萃取体系，其萃取过程相当缓慢。因而这类体系的萃取机制和萃取动力学问题已日益引人注目。除此而外，在设计，放大或改进萃取设备时，研究和掌握有关萃取过程的动力学规律也有十分重要意义。在本文中主要对稀土萃取动力学进行了研究，得到主要结果如下：1．研究了硫代有机磷酸Cyan.ex302萃取饵的动力学。通过测定各种萃取条件对萃取速率的影响，获得了萃取速率方程，并讨论了萃取的控制过程。实验发现萃取剂中的杂质对萃取具有较大的加速作用，这对工业生产具有一定的实际意义。2.用两相滴定法测定了两种新合成的J梭酸萃取剂CA-12和CA-100的某些重要的物理常数。这将有助于深入研究它们的萃取性质及机理。3．用层流恒界面池研究了CA-12萃取La, Gd,Er, Yb和Y的动力学。考察了各种因素对萃取速率的影响，获得了它们的萃取速率方程，实验发现了它们的萃取控速步骤并推测了其萃取机理。4．研究了HEHEHP对CA-12萃取Yb和Y的动力学的影响。实验发现在CA一12中加入少量的HEHEHP后，萃取活化能显著降低，萃取速率明显加快。由于加入HEHEHP后，萃取Yb的活化能的降低要比萃取Y的活化能降低的程度大'，所以使Yb和Y的萃取分离因素加大。5．用两相滴定法研究了HEHEHP萃取铭的机理，CA-12萃取稀土及其相关离子的机理。并计算了它们相应的平衡常数。

Extraction and separation of rare earths from chloride medium with mixtures of 2-ethylhexylphosphonic acid mono-(2-ethylhexyl) ester and sec-nonylphenoxy acetic acid

BACKGROUND: 2-ethylhexylphosphonic acid mono-(2-ethylhexyl) ester (HEHEHP, H(2)A(2)) has been applied extensively to the extraction of rare earths. However, there are some limitations to its further utilization and the synergistic extraction of rare earths with mixtures of HEHEHP and another extractant has attracted much attention. Organic carboxylic acids are also a type of extractant employed for the extraction of rare earths, e.g. naphthenic acid has been widely used to separate yttrium from rare earths. Compared with naphthenic acid, sec-nonylphenoxy acetic acid (CA100, H2B2) has many advantages such as stable composition, low solubility, and strong acidity in the aqueous phase. In the present study, the extraction of rare earths with mixtures of HEHEHP and CA100 has been investigated. The separation of the rare earth elements is also studied.

Influence of isooctanol on the interfacial activity and mass transfer of ytterbium(III) using 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester as an acidic extractant

BACKGROUND: Introducing an adduct into an extractant system is an effective method of improving extraction performance. The effect of additives upon extraction is very important, especially in the case of interfacial behaviour. In most work published in the literature, there is little data on the interfacial behaviour of extractants and modifiers. As the mass transfer must pass through an interface, the influence of isooctanol on the interfacial activity and mass transfer of ytterbium(III) using 2-ethylhexylphosphonic acid mono-2-ethlhexyl ester has been investigated.RESULTS: With increasing amounts of isooctanol, the interfacial tension and surface excess (Gamma(max)) of the 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester(HEHEHP)-isooctanol system decreased, and the area of the absorbed HEHEHP molecule (Amin) increased. The interfacial activity of the HEHEHP-isooctanol system varied significantly depending on ionic strength and temperature and the mass transfer flux decreased with increasing isooctanol content.

The extraction of rare earths using mixtures of acidic phosphorus-based reagents or their thio-analogues

The solvent extraction of rare earths from chloride solution has been investigated using mixtures of 2-ethylhexylphosphonic acid mono-(2-ethylhexyl) ester (HEHEHP, P507) and organophosphorus acids [di-(2-ethylhexyl)phosphoric acid (HDEHP, P204), isopropylphosphonic acid 1-hexyl-4-ethylocryl ester (HHEOIPP), bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272), bis(2,4,4-trimethylpentyl)monothiophosphinic acid (Cyanex 302), and bis(2,4,4-trimethypentyl)dithiophosphinic acid (Cyanex 301)]. Results show that the extractability of the selected extractants for rare earths decreases in the order: HEHEHP/HDEHP > HEHEHP/Cyanex 301 > HEHEHP/HHEOIPP > HEHEHP/Cyanex 302 > HEHEHP/Cyanex 272. A possible explanation of the different extractabilities is given based on the structure of the extractants. Furthermore, the possibilities of the separation of adjacent rare earths with these mixtures were investigated according to the extractabilities; the results show the possibility of separating the rare earths.

两相滴定法研究2-乙基己基膦酸单2-乙基己基酯从盐酸介质中萃取钕(Ⅲ)的动力学

本文利用两相滴定法作为分析手段,用恒界面池搅拌法考察了多种因素对2-乙基己基膦酸单2-乙基己基酯(HEHEHP,HA)从盐酸介质中萃取Nd(Ⅲ)动力学的影响,从实验结果推论出萃取过程为界面化学反应控制型机理。