Extraction kinetics of Sc(III), Y(III), La(III) and Gd(III) from chloride medium by Cyanex 302 in heptane using the constant interfacial cell with laminar flow

The extraction kinetics of Sc, Y, La and Gd(III) from the hydrochloric acid medium using Cyanex 302 (hereafter HL) in heptane solution have been measured by the constant interfacial cell with laminar flow. Reaction regions are explored at liquid-liquid interface. Extraction regimes are deduced to be diffusion-controlled for Sc(Ill) and mixed controlled for Y, La and Gd(Ill). Extraction mechanisms are discussed according to the dimeric model of Cyanex 302 in non-polar solution. From the temperature dependence of rate measurement, the values of E-a, Delta H-+/-, Delta S-+/- and Delta G(300)(+/-) are calculated and it is found that the absolute values of these parameters keep crescent trend for Sc, Y, La and Gd(III). At the same time, it is found that it can easily achieve the mutual separation among the Sc, Y and La(III) with kinetics extraction methods.

Studies on synergistic extraction of Sc(III) with HBTMPTP and Cyanex 925

The synergistic extraction of Sc(III) from H2SO4 solution with bis(2, 4, 4-trimethylpentyl)monothiophosphinic acid(HBTMPTP, HL) and branched chain alkyl phosphine oxide mixture (Cyanex 925, B) in n-hexane has been investigated, The results indicated that synergistic effect was showed in low acidity (c(H2SO4) < 0.25 mol/L). The composition of the extracted complex of Sc(III) has been determined to be Sc(HL2)(2)B-3(SO4)(1/2) by the method of slope analysis, The mechanism of the synergistic extraction of Sc(III) may be : Sc3+ + 2(HL)(2(O)) + 3B((O)) + 1/2SO(4)(2-)reversible arrow(K12)Sc(HL2)(2)B-3(SO4)(1/2(O)) + 2H(+) ScL(HL2)(2(O)) + 3B((O)) + H+ + 1/2SO(4)(2-)reversible arrow(beta')Sc(HL2)(2)B-3(SO4)(1/2(O)) + 1/2(HL)(2(O)) Sc(SO4)(1.5)B-2(O) + B-(O) + 2(HL)(2(O))reversible arrow(beta')Sc(HL2)(2)B-3(SO4)(1/2(O)) + 2H(+) + SO42- Their equilibrium constants have been calculated to be lgK(13)=6.77+/-0.12, lg beta'=7.71, lg beta '' = 0.10, respectively, The IR spectra and FAB-MS of the saturated synergistic extraction complex of Sc(III) have been discussed as well.

SOLVENT-EXTRACTION OF SC(III), ZR(IV), TH(IV), FE(III), AND LU(III) WITH THIOSUBSTITUTED ORGANOPHOSPHINIC ACID EXTRACTANTS

The solvent extraction of Sc(III), Zr(IV), Th(IV), Fe(III) and Lu(III) with Cyanex 302 (bis(2,4,4-trimethylpentyl)monothiophosphinic acid) and Cyanex 301 ( bis(2,4,4-trimethylpentyl) dithiophosphinic acid) in n-hexane from acidic aqueous solutions has been investigated systematically. The effect of equilibrium aqueous acidity on the extraction with these reagents was studied. The separation of Th(IV), Fe(III) and Lu(III) from Sc(III), or the separation of other metals from Lu(III) with Cyanex 302, can be achieved by controlling the aqueous acidity. However, Cyanex 301 exhibited a poor selectivity for the above metals, except for Lu(III). The extraction of these metals with Cyanex 272, Cyanex 302 and Cyanex 301 has been compared. The stripping percentages of Sc(III) for Cyanex 302 and Cyanex 301 in a single stage are near 78% and 75% with 3.5 mol/L and 5.8 mol/L sulphuric acid solutions, respectively. The effects of extractant concentration and temperature on the extraction of Sc(III) were investigated. The stoichiometry of the extraction of Sc(III) with Cyanex 302 was determined. The role of different components of Cyanex 302 in the extraction of Sc(III) was discussed.

EXTRACTION MECHANISM OF SC(III) AND SEPARATION FROM TH(IV),FE(III) AND LU(III) WITH BIS(2,4,4-TRIMETHYLPENTYL)PHOSPHINIC ACID IN N-HEXANE FROM SULFURIC-ACID-SOLUTIONS

The extraction equilibrium data of sulphuric acid and scandium(III) with bis(2,4,4-trimethylpentyl)phosphinic acid (H[BTMPP]) from sulphuric acid solutions have been obtained. There are two extraction mechanisms of scandium(III) with H[BTMPP] at different

H[DEHP]从不同介质中萃取稀土（III）(Sc、Y、Ho、Er、Yb、Lu)及Fe(III)、Zn(II)的机理

本文分另研究了H[DEHP]从不同酸性介质中萃取稀土（III）(Sc、Y、Ho、Er、yb、Lu)及Fe(III)、Zn(II)的机理及性能。一、H[DEHP]从 H_2SO_4介质中萃取Sc(III)的机理 1. H[DEHP]萃取H_2SO_4及其机理 2. H[DEHP]萃取Sc(III)的机理，用斜率法和饱和法确定了H[DEHP]的正庚烷溶液从H_2SO_4溶液中萃取Sc_2(SO_4)_3的机理及萃合物组成。研究表明，H[DEHP]萃取Sc(III)在高、低两种酸度范围内存在着两种不同的萃取机理。二、H[DEHP]从HCl介质中萃取Ln(III)和Fe(III)的性能及H[DEHP]萃取Ln(III)的机理研究了H[DEHP]的正庚烷溶液从HCl介质中萃取稀土（III）(Sc、Y、Ho、Er、Yb、Lu)和Fe(III)的性能，得出H[DEHP]在相同条件下萃取以上各金属离子的顺序是：Sc(III)>Fe(III)>Lu(III)>Yb(III)>Er(III)>Y(III)>Ho(III), 并计算了各金属离子之间的分离因素（β）。文中还讨论了Sc(III)、Fe(III)、Lu(III)之间的分离以及重稀土离子间的萃取分离，同时与相同实验条件下HEH[EHP]的萃取性能进行了比较，为新的萃取体系提供了一些参数。三、H[DEHP]从不同介质中萃取Fe(III)的机理，研究了H[DEHP]的正率烷溶液从Hcl介质中和H[DEHP]的正庚烷溶液从H_2SO_4介质中萃取Fe(III)的平衡规律；用斜率法、饱和法以及IR和NMR谱等讨论了低酸度下的萃取机理。四、H[DEHP]萃取Zn(II)的机理，研究了H[DEHP]的正率烷溶液从Hcl介中萃取Zn(II)的平衡，利用斜率法、饱和法及SR、NMR谱等讨论了低Hcl浓度下的萃取机理。

Separation of scandium(III) from lanthanides(III) with room temperature ionic liquid based extraction containing Cyanex 925

The separation of Sc(III) from Y(III), La(III) and Yb(III) in [C(8)mim][PF6] containing Cyanex 925 has been investigated, and is reported in this paper. A cation exchange mechanism of Sc(III) in [C(8)mim][PF6] and Cyanex 925 is proposed by study of the influence of anionic and cationic species on the extraction. The coefficient of the equilibrium equation of Sc(III) was confirmed by slope analysis of log D-Sc vs log [Cyanex 925], and the loading capacity also confirmed the stoichiometry of Cyanex 925 to Sc(III) was close to 3:1. Infrared data for Cyanex 925 saturated with Sc(III) in [C(8)mim][PF6] indicated strong interaction between P=O of Cyanex 925 and Sc(III). In addition, the relationship between log D-Sc and temperature showed that temperature had little influence on the extraction process, and the resulting thermodynamic parameters indicated that an exothermic process was involved.

Solvent extraction of scandium(III), yttrium(III), lanthanum(III) and gadolinium(III) using Cyanex 302 in heptane from hydrochloric acid solutions

The extractions of the selected rare earths (Sc, Y, La and Gd) from hydrochloric acid solutions have been investigated using bis(2,4,4-trimethylpentyl)-mono thiophosphinic acid (Cyanex 302, HL) in heptane as an extractant. The results demonstrate that the extractions of rare earths occur via the following reaction: Sc(OH)(2+) + 2[(HL)(2)]((O)) double left right arrow [Sc(OH)L-2 (.) 2(HL)]((O)) + 2H(+) Y3+ + 3[(HL)(2)]((O)) double left right arrow [Y(HL2)(3)]((O)) + 3H(+) La(OH)(2)(+) + 3[(HL)(2)](O) double left right arrow [La(OH)(2)L (.) 5(HL)]((O)) + H+ Gd(OH)(2+) + 3[(HL)(2)]((O)) double left right arrow [Gd(OH)L-2 (.) 4(HL)]((O)) + 2H(+) The pH(1/2) values and equilibrium constants of the extracted complexes have been deduced by taking into account the aqueous phase complexation of the metal ion with hydroxyl ligands and plausible complexes extracted into the organic phase. According to the pH(1/2) values, it is possible to realize mutual separation among Sc(III), Y(III), La(III) and Gd(III) with Cyanex 302 by controlling aqueous acidity.

Solvent extraction of scandium(III) by Cyanex 923 and Cyanex 925

The extraction equilibria of Sc(III), Zr(IV), Ti(IV), Th(IV), Fe(III) and Lu(III) from sulphuric or hydrochloric acid media by Cyanex 923 (mixture of straight chain alkylated phosphine oxides) and Cyanex 925 (mixture of branched chain alkylated phosphine oxides) were studied at various aqueous acidities. The extractant Cyanex 923 demonstrated better scandium loading and selectivity for TI(IV). Fe(III) and Lu(III) than Cyanex 925. The effects of extractant concentration on the extractions of sulphuric acid and Sc(III) by Cyanex 923 were examined. The stoichiometries of the extraction reactions were postulated based on slope analysis. The experimental results indicate that Cyanex 923 can be employed to recover scandium directly from the hydrolytic mother solution arising from TiO2 production via the sulphate process. The parameters studied were scandium loading capacity, phase ratio, concentrations of Ti(IV) scrubbing and Sc(III) stripping agents. A new solvent extraction technology of scandium recovery was developed. The purity of the final Sc(III) product is above 95% with a yield > 94%. (C) 1998 Elsevier Science B.V.

HBTMPTP与Cyanex 925协同萃取Sc(Ⅲ)的研究

研究了二（2，4，4-三甲基戊基）单硫代膦酸（HBTMPTP，HL）和支链三烷基氧化膦（Cyanex925，B）的正己烷溶液在H2SO4介质中对Sc（III）的萃取性能，结果表明，在较低酸度（CH2SO4〈0．25mol／L）时存在协同效应，用斜率法确定了Sc（III）的协萃配合物的组成为Sc（HL2）2B3（SO4）1／2，计算了协萃反应的平衡常数，讨论了协萃配合物的IR谱和FAB－MS．

Complexation of some trivalent lanthanides, scandium(III) and thorium(IV) by benzylidenepyruvates in aqueous solution

The protonation constants of 4-methylbenzylidenepyruvate (4Me-BP) and 4-isopropylbenzylidenepyruvate (4IP-BP) as well as the stability constants of their binary 1:1 complexes with Cu(II), La(III), Pr(III), Sm(III), Eu(III), Yb(III), Sc(III) and Th(IV) have been determined spectrophotometrically in aqueous solution at 25°C and ionic strength 0.500 M, maintained with sodium perchlorate. For all metal ions considered, the stability changes move in the same direction as the pKa of the ligands. Linear free energy relationships, as applied to oxygen donor substances, suggest the -COCOO- moiety as the metal binding site of the ligands. The results are discussed mainly taking into account that benzylidenepyruvates, besides the α-keto canonical form, may display other forms in aqueous solution with changing pH and the possible occurrence of extra intra-ligand charge polarization, induced by metal ions.

Complexation of some trivalent lanthanides, scandium(III) and thorium(IV) by benzylidenepyruvates and cinnamylidenepyruvate in aqueous solution

The protonation constants of benzylidenepyruvate, 2-chloro-, 4-chlorobenzylidinepyruvate and cinnamylidenepyruvate as well as the stability constants of their binary 1:1 complexes with Cu(II), La(III), Pr(III), Sm(III), Lu(III), Sc(III) and Th(IV) have been determined spectrophotometrically in an aqueous medium at 25 °C and ionic strength 0.500 M, held with sodium perchlorate. Coordination centres in the aforementioned ligands are suggested. © 1995.

伯胺N_(1923)萃取过渡金属离子机理的研究

伯胺由于其特殊的结构（R-NH_2），使它具有和仲、数胺不相同的一些性质。有较强的和矿物酸HX结合形成RNH_3X的能力，从而以离子交换机理萃取金属离子；也可以-NH_2上的氮、氢原子同以高价存在的过渡金属含氧酸以氢键方式相结合；另外，RNH_2也可通过氮原子以配位键形式与一些属于软酸类的过度金属离子形成配合物。通过伯胺萃取金属离子行为的研究，可发现新的萃取体系，扩大我国自行设计的伯胺N_(1923)萃取剂的应用领域，为金属离子的分离提纯工艺提供基本参数。我们实验室过去曾对伯胺N_(1923)萃取稀土（III）、Fe（III）、Zn （II）、Cd（II）、Ag（I）、Sc（III）等的机理进行了比较系统的研究。本工作是在此基础上，进一步完善及扩大N_(1923)对周期表中各族元素的萃取及应用。为此，我们选择了文献尚未报道的Ti（IV）、HgCl_2、Hg(CH_3COO)_2、Cu(CH_3COO)_2为研究对象，对它们的萃取机理进行了较详细的研究。结果表明，自由的N_(1923)或其盐对上述体系具有良好的萃取性能，并初步讨论了N_(1923)在金属离子萃取分离中的应用。一、伯胺N_(1923)萃取HgCl_2的机理 微量汞的萃取及分离对环境保护具有重要的实际意义。我们的研究结果表明，在pH值为3-4.5范围内，即使Cl~-浓度很低时，伯胺N_(1923)也能几乎定量地萃取HgCl_2，其盐酸盐亦能有效地萃取Hg（II），但两者的萃取机理不同。自由伯胺RNH_2可与HgCl_2形成配合物，其萃取机理为：RHN_(2(0)) + HgCl_2 <-> Hg(RNH_2)Cl_(2(0))对伯胺盐，实验证明其机理主要为加合反应，但当Cl~-浓度较高时，则为阴离子交换反应：加合反应：2RNH_3Cl_((0)) + HgCl_2 <-> (RNH_3Cl)_2HgCl_(2(0))交换反应：2RNH_3Cl_((0)) + HgCl_4~(2-) <-> (RNH_3)_2HgCl_(4(0)) + 2Cl~-通过考察温度对配位萃取反应的影响，求得反应的热效应ΔH = -48.82 KJ/mol，并分析了萃合物的IR、NMR谱。二、伯胺N_(1923)萃取Hg(CH_3COO)_2的机理 与HgCl_2体系相似，自由伯胺或其盐均能萃取Hg(CH_3COO)_2，萃取机理分别为：RNH_(2(0)) + Hg(CH_3CCO)_2 <-> Hg(RNH_2)(CH_3COO)_(2(0)) (CH_3COONH_3R)_(2(0)) + Hg(CH_3COO)_2 <-> (CH_3COONH_3R)_2Hg(CH_3COO)_(2(0))。在不同的萃取剂浓度下，上述反应的表观平衡常数基本不随萃取剂浓度的变化而改变，其对数值分别为：11.85、8.11。三、伯胺N_(1923)萃取Cu(CH_3COO)_2的机理 水相酸度对萃取反应的影响表明，RNH_2在近中性体系中具有很好的萃取性能，而在乙酸浓度较高的条件下，Cu（II）几乎不被RNH_2所萃取。说明自由伯胺能以配位机理的形式萃取Cu(Oh_3coo)_2，经确定，萃取反应式为：2RNH_(2(0)) + Cu(CH_3COO)_2 <-> Cu(RNH_2)_2(CH_3COO)_(2(0))并对该反应的表观平衡常数及热力学函数进行了计算。通过分析萃合物的IR谱，认为Cu(RNH_2)_2(CH_3COO)_2为平面型四配位的配合物。四、(RNH_3)_2SO_4从硫酸溶液中萃取Ti（IV）的研究 在低酸度（pH：0.84）的H_2SO_4溶液中，伯胺N_(1923)对Ti（IV）具有很强的萃取能力。用化学平衡法确定其反应式为：3(RNH_3)_2SO_(4(0)) + Ti(OH)_3~+ + SO_4~(2-) <-> 2(RNH_3)_3Ti(OH_3)(SO_4)_(2(0))我们用正十二胺代替N_(1923)，合成了上述萃合物的模拟物，经元素分析确定了萃合物的分子式：(RNH_3)_3Ti(OH)_3(SO_4)_2。并较详细地分析了萃合物的NMR、IR谱。变温NMR的结果表明，萃合物中存在两种含有活泼氢的基团，用D_2O交换后的NMR的结果亦证明了这一点。从萃合物的IR谱中，可得到SO_4~(2-)是以单齿配位形式同Ti（IV）相结合的信息。这些结果为所提出的萃取机理提供了直接的证据。并求出了上述萃取反应的表观平衡常数，其对数值为10.15，该值基本不随萃取剂浓度的变化而发生改变。反应的热效应ΔH = 66.49 KJ/mol，由计算得出的ΔG值可知，上述萃取反应有很大的向右进行的趋势。五、伯胺N_(1923)在萃取分离中的应用 为了扩大N_(1923)的应用，通过上述研究，我们对其在萃取分离中的应用进行了讨论，认为在以下几方面有可能得到应用：1、从环境废水中除Hg(II)；2、Hg(II)和Zn(II)、Cd(II)在CH_3COOH体系中的分离；3、CH_3COOH体系中Cu(II)、Co(II)、Ni(II)的萃取分离；4、在较高浓度的H_2SO_4体系中，应用(RNH_3)_2SO_4进行了Ti(IV)-Fe(II)的分离。

伯胺N_(1923)与其它试剂对金属离子(Zn~(2+).Cd~(2+).RE~(3+))的萃取及协同萃取

胺类萃取剂具有其独特优点，特别是伯胺，因含有活泼氢，既能作为“阴离子交换剂”，又能与被萃的含氧金属络阴离了形成氢键而溶剂化，同时伯胺为一路易斯碱，可作为配体与某些金属离子形成配位键等，因而已广泛地用于金属离子的提纯与分离工业中。然而，1）为了寻找新的、更有效的萃取及协同萃取体系，以适应分析分离各种金属离子，改善金属离子的分离工艺；2）研究萃取和协同萃取的一般规律，探寻其内在规律性，充实完善萃取化学原理的内容；3）研究多元配合物的组成、结构和机理；4）系统地研究和比较不同结构胺类萃取剂与其它萃取剂对金属离子的萃取及协同萃取的相互作用，探讨多元配合物的形成条件等，因此，研究伯胺N_(1923)与其它萃取剂在不同酸度、不同条件，不同体系中对Zn(II)、Cd(II)、Re(III)的萃取及协同萃取具有一定意义。本文分别研究了伯胺N_(1923)与中性磷试剂对ZnCl_2、CdCl_2、Zn(SCN)_2的协同萃取；伯胺N_(1923)与HPMBP对RE（III）的协同萃取以及伯胺N_(1923)在不同介质中对Sc(III)的萃取机理等，并用得到了一些有意义的结果与结论。一、伯胺N_(1923)与中性磷萃取剂(TBP, DBBP)对Zn(II)、Cd(II)的协同萃取1. 伯胺N_(1923)与TBP、DBBP对ZnCl_2的协萃取 研究了伯胺N_(1923)与TBP、DBBP的正庚烷溶液从盐酸介质中对ZnCl_2的萃取机理，用斜率法、等摩尔系列法确定了协萃配合物组成为：(RNH_3Cl)_3·ZnCl_2·B、(RNH_3Cl)_2·ZnCl_2·B (B = TBP·DBBP)协萃反应为：ZnCl_2 + (RNH_3Cl)_3_((o)) + TBP_((o)) →~(K_(12)(TBP) (RNH_3Cl)_3·ZnCl_3·ZnCl_2·TBP_((o)) ZnCl_2+Z/3(RNH_3Cl)_(3(o)) + DBBP_((o)) → (RNH_3Cl)_2 · ZnCl_2·DBBP_((o))协萃配合物生成反应为：(RNH_3Cl)_3·ZnCl_(2(o)) + TBP_((o))→~(B_(12)(TBP) (RNH_3Cl)_3·ZnCl_2·TBP_((o)) (RNH_3Cl)_3·ZnCl_(2(o)) + DBBP_((o)) →~(B_(12)(DBBP) (RNH_3Cl)_2·ZnCl_2·DBBP_((o)) + RNH_3Cl_((o))同时发现，中性磷试剂对Zn(II)的协萃效应大小影响有下列关系：DBBP>TBP。并求得了协萃反应平衡常数和协萃配合物生成反应平衡常数。在研究溶剂对协同效应影响时发现，对芳香烃及其衍生物，分配比（D）与溶剂介电常数（ε）的关系为D_∝1/ε，而对芳香烃及其衍生物，分配比（D）与介电常数（ε）的关系为D_∝ε。讨论了温度对协萃反应的影响，对协萃配合物的IR、NMR谱也进行了研究。2.伯胺N_(1923)与TBP对Zn_(SCN)_2的协同萃取研究了伯胺N_(1923)与TBP的庚烷溶液从硝酸底液中对Zn(SCN)_2的萃取机理，用等摩尔系列法、斜率法确定了TBP和Zn(SCN)_2以及伯胺N_(1923)与TBP对Zn(SCN)_2的协萃配合物组成分别为：Zn(SCN)_2·3TBP. (RNH_3)_2Zn(SCN)_4·TBP,协谇反应为：Zn(SCN)_4~(2-) + (RNH_3NO_3)_(2(o)) + TBP_((o)) → (RNH_3)_2Zn(SCN)_4·TBP_((o)) + 2NO_3~-协萃配合物三种可能生成反应为(RNH_3)_2Zn(SCN)_(4(o)) + TBP_((o)) → ~(B'12) (RNH_3)_2Zn(SCN)_4·TBP_((o)) (a) (RNH_3NO_3)_(2(o)) + Zn(SCN)_2·3TBP_((o)) + 2SCN~-→~(β"12)→(RNH_3)Zn(SCN)_4βTBP_((o))+2TBP_((o))+2NO_3~- (b) (RNH_3NO_3)_(2(o)) + (RNH_3)_2Zn(SCN)_(4(o)) + 2SCN~- + Zn(SCN)_2.3TBP_((o)) →~(β"12)→R(RNH_3)_2Zn(SCN)_4.TBP_((o)) + 2NO_3~- + TBP_((o)) (c) 求得了协萃反应及生成反应的平衡常数，并由生成反应常数可知：β"'_(12) > β'_(12) > β"_(12)，即反应（c）对协萃配合物的生成贡献最大，其次反应（a），最小的是反应（b），同时还发现，不同阴离子对协萃效应影响有下列关系：SCN~- > Cl~_。并对协萃配合物的IR谱进行了研究，讨论了温度对协萃反应的影响。3. 伯胺N_(1923)与TBP、DBBP对Cd（II）的协同萃取研究了伯胺N_(1923)与TBP、DBBP的正庚烷溶液从盐酸介质中对Cd(II)的协同萃取，用等摩尔系列法、斜率法确定了协萃配合物组成为(RNH_3Cl)_2·CdCl_2·B，协萃反应及协萃配合物生成的反应分别为：CdCl_2 + 2/3 (RNH_3Cl)_(3(o)) + B_((o)) →~(K_(12)) → (RNH_3Cl)_2·CdCl_2·B_((o)) (RNH_3Cl_3)·CdCl_2_((o)) + B_((o)) →~(BR)(RNH_3Cl)_2·CdCl_2·B_((o)) + RNH_3Cl_((o))求得了协萃反应及生成反应平衡常数，计算了协萃反应的热力学函数值，结果还发现与Zn(II)协同萃取比较，协同效应大小有下列关系：Zn(II) > Cd(II)，由实验结果证实了“萃取效应大，则协萃效应小，反之，萃取效应小，则协同效应大”这一结论。并对协萃配合物的IR、NMR谱进行了研究。二. 伯胺N_(1923)与HPMBP对RE（III）的协同萃取研究了伯胺N_(1923)与HPMBP的二甲苯溶液在盐酸介质中对RE（III）的协萃机理（RE~(3+ = La~(3+), Pr~(3+), Eu~(3+), Gd~(3+), Tb~(3+), Er~(3+), Yb~(3+)和Y~(3+)）用斜率法及等摩尔系列法确定了协萃配合物组成为RNH_3Ln(PMBP)_4。求得了关于Pr(III)的协萃反应及生成反应的平衡常数值，协萃反应及生成反应分别为：Ln~(3+) + 4HPMBP_((o)) + RNH_3Cl_((o)) → RNH_3LN(PMBP)_(4(o)) + 4H~+ + Cl~- Ln(PMBP)_(3(o)) + RNH_3Cl_((o)) → RNH_3Ln(PMBP)_(4(o)) + H~+ + Cl~- 结果还发现协萃系数（R）随稀土元素的原子序数（Z）递变而出现“双峰效应”（未见文献报道），而且随RNH_3Cl浓度增加到某一一出现反协同效应。同时研究了关于Pr(III)协萃配合物的IR、NMR谱。三、伯胺N_(1923)在硝酸盐及硫氰酸盐混合介质中对Sc(III)的萃取研究了RNH_3NO_3在硝酸盐和硫氰酸盐混合介质中萃取Sc(III)的机理，结果发现，钪是以Sc(OH)_2~+形式萃入有机相的，且SCN~-, NO_3~-对RNH_3nO_3萃取Sc(III)具有协同效应，并且斜率法、连续变化法及PH值测定确定了萃取反应为：Sc(OH)_2~+ + SCN~- + 2(RNH_3NO_3)_(2((o)) → (RNH_3nO_3)_4.Sc(OH)_2SCN_((o)) Sc(OH)_2~+ + SCN~- + NO_3~- + (RNH_3NO_3)_(2(o)) → (RNH_3NO_3)_2.Sc(OH)(SCN)NO_3 + OH~-求得了反应的平衡常数及热力学函数值。

酸性磷（膦）酸酯萃取三价稀土离子的研究

本文研究了酸性磷（膦）类萃取剂：二（2，4，4-三甲基戊基）膦酸（C272）、仲丁基膦酸2-丁基辛基酯（J040）、仲已基膦酸2-丁基辛基酯（J043）对三价稀土离子的萃取及分离性能，测定了相邻元素间在不同pH范围内的平均分离系数，讨论了C272、J040、J043萃取Sc(III)、Er(III）、Ta(III)、Ho(III)的机理，合成了J040与La(III)、Ho(III)、Y(III)、Er(III)、Cd(III)、Pb(III)的固体配合物，并对其结构进行了表征。本文还以2-乙基乙基膦酸单2-乙基已基酯（P507）为萃取剂，利用分馏串级萃取，进行了低损耗红外光纤原料的提纯研究。一、不同结构的酸性磷（膦）酸酯对三价稀土离子的萃取。二、不同结构酸性磷（膦）酸酯萃取Er(III)、Tr(III)、Ho(III)、Sc(III)的机理。本实验还考察了平衡水相酸度对萃取平衡的影响，由酸度曲线求出了一些元素对间在不同pH范围内的平均分离系数；根据萃取剂浓度对萃取平衡的影响结果分别求出了各萃取平衡反应的浓度平衡常数；研究了温度对萃取平衡的影响，由此求出了萃取平衡反应的热力学函数。对C272，还考察了萃取分配比随原子序数的变化规律。结果表明具有明显的四分组效应。