双相(O/W)识别手性萃取分离α-环己基扁桃酸对映体

提出一种新的手性分离技术双相(O/W)识别手性萃取. 研究了α-环己基扁桃酸对映体在D(L)-酒石酸异丁酯1,2-二氯乙烷有机相和β-环糊精衍生物水相萃取体系中的分配行为; 考察了β-环糊精衍生物种类和浓度、酒石酸酯构型和浓度、水相pH 值等因素对萃取性能的影响. 实验结果表明, 双相(O/W)识别手性萃取具有很强的手性分离能力, 羟丙基β-环糊精、羟乙基β-环糊精、甲基β-环糊精均对S-α-环己基扁桃酸对映体的识别能力大于对R-α-环己基扁桃酸对映体的识别能力, 其中以羟丙基β-环糊精的识别能力最强; 而D-酒石酸异丁酯的识别能力刚好相反; 在羟丙基β-环糊精和D-酒石酸异丁酯萃取体系中, α-环己基扁桃酸外消旋体一次萃取分离后, 水相中S-对映体e.e.%达到27.6%, R-和S-对映体的分配系数(k_R和k_S)分别为2.44和0.98, 分离因子(α)达2.49; 同时pH值和萃取剂浓度对手性分离能力有显著影响. 双相(O/W)识别手性萃取对外消旋体化合物的制备性分离有着十分重要的意义.     

手性酯类萃取剂萃取拆分α-环己基扁桃酸外消旋体

研究了α-环己基扁桃酸对映体在含有疏水性D酒石酸酯手性选择体的1,2-二氯乙烷和水两相系统萃取分配行为,考察了酒石酸酯烷基链长度、pH值和D酒石酸酯浓度对分配比和分离因子的影响。实验表明：D酒石酸酯与R-α-环己基扁桃酸对映体比与S—α-环己基扁桃酸对映体形成更稳定的非对映体复合物;随着pH值增大,分配比减小,分离因子也随之降低;同时,D酒石酸酯浓度的影响也比较大。     

混合萃取剂拆分氧氟沙星外消旋体

将混合萃取剂技术应用于氧氟沙星外消旋体的萃取分离,主要研究了氧氟沙星对映体在水和有机溶剂两相中的萃取分配行为。研究结果表明:在L-(-)-对甲基二苯甲酰酒石酸(L-DTTA)的浓度为0.18mol/L,L-(-)-二苯甲酰酒石酸(L-DBTA)的浓度为0.12mol/L,氧氟沙星浓度为0.2mg/mL,萃取温度为25℃,pH为7.00时,L型对映体和D型对映体的分配系数分别达到10.2和4.20,手性选择性达到2.43。     

反式第一菊酸对映体的手性选择剂立体选择性分离

研究反式第一菊酸(trans-CA)对映体在含有手性选择剂酒石酸酯的水-有机相双相体系中的萃取分配行为,考察有机相的种类、酒石酸酯烷基链长度、水相的pH值和酒石酸酯的浓度对分配系数K和分配因子α的影响.研究结果表明:1,2-二氯乙烷作为有机相效果较好,D-酒石酸酯与( )-反式第一菊酸对映体形成的复合物稳定性比与(-)-反式第一菊酸对映体形成的复合物稳定性要大,而L-酒石酸酯的萃取性能与此相反,它与(-)-反式第一菊酸对映体形成的复合物稳定性比与( )-反式第一菊酸对映体形成的复合物稳定性要大.酒石酸酯取代烷基链长对分配系数K和分离因子α有很大影响;分配系数K和分离因子α均随pH的升高而降低;分配系数K随着酒石酸酯浓度的增大而增大,分离因子α先随浓度增大而稳定上升,后随浓度增大而缓慢下降.     

组合手性萃取拆分克伦特罗外消旋体

以D-二苯甲酰酒石酸(D-DBTA)和D-二对甲苯甲酰酒石酸(D-DTTA)的组合作为手性选择剂,研究克伦特罗对映体在水相和有机相中的萃取分配行为,优化了手性萃取条件,考察了组合手性选择剂的不同摩尔浓度比、有机溶剂、水相pH值和亲脂性阴离子BPh4-对手性萃取性能的影响,并测定了手性萃取拆分过程中的热力学函数.在优化的手性萃取条件下,有机相中的对映体过量值(e.e.%)可大于10%,而所使用的选择剂量相对大为降低.热力学数据分析表明,该手性萃取过程为焓控过程.     

疏水性L-酒石酸异丁酯立体选择性萃取拆分氰戊菊酸对映体

合成了萃取拆分氰戊菊酸(FA)对映体的手性选择体L-酒石酸异丁酯.研究了氰戊菊酸对映体在含有手性选择体L-酒石酸异丁酯的水-有机相双相体系中的萃取分配行为.考察了有机稀释剂类型、L-酒石酸异丁酯浓度、pH值和磷酸盐浓度诸因素对分配系数(K)和分离因子(α)的影响.研究结果表明:L-酒石酸异丁酯与S对映体形成的复合物稳定性比与R对映体形成的复合物要好;1,2-二氯乙烷作为有机稀释剂更有利于萃取分离;随着L-酒石酸异丁酯浓度的增大,K逐渐增大,α先增大后减小,当L-酒石酸异丁酯浓度为0.30 mol\5L-1时,α达最大;pH值增大,K和α都降低;磷酸盐浓度对分配系数和分离因子也有较大影响.     

立体选择性萃取分离反式DV菊酸对映体

研究了反式DV菊酸对映体在含有手性选择体酒石酸酯的水-有机相双相体系中的萃取分配行为,考察了有机稀释剂种类、酒石酸酯的浓度、温度、水相的pH值、酒石酸酯烷基链长度对分配系数(D)和分配因子(α)的影响.研究表明:三氯甲烷作稀释剂时萃取分离效果较好;温度升高使分配系数增大,分离因子减小;分配系数随pH的升高而降低,随着酒石酸酯浓度的增大而增大,分离因子随pH的升高和酒石酸酯浓度的增大先增加后降低,pH和酒石酸酯浓度分别为4.50和0.40mol/L时取得较好的分离效果;取代烷基链长对分配系数(D)和分离因子(α)亦有较大影响.     

疏水性L-酒石酸酯立体选择性萃取分离氯噻酮对映体

研究了氯噻酮对映体在含有疏水性L-酒石酸酯手性选择体的水-1,2-二氯乙烷两相系统萃取分配行为,考察了pH、L-酒石酸酯烷基链长度、L-酒石酸酯浓度和磷酸盐浓度对分配系数和分离因子的影响。实验表明：L-酒石酸酯与氯噻酮I( )-对映体比与Ⅱ(-)-对映体形成更稳定的非对映体复合物;随着L-酒石酸酯取代烷基链长的增长,分配系数和分离因子增大;随着pH增大,分配系数增大,而分离因子降低;同时,L-酒石酸酯和磷酸盐浓度影响也比较大。     

L-酒石酸酯立体选择性萃取分离扁桃酸对映体

手性萃取;L-酒石酸酯立体选择性萃取分离扁桃酸对映体     

手性溶剂萃取分离顺式二氯菊酸对映体

研究了顺式二氯菊酸(cis-PA)对映体在含有酒石酸酯手性选择体的水-1-2-二氯乙烷两相溶液中的萃取分配行为,考察了有机相种类、L-酒石酸酯浓度、水相pH、L-酒石酸酯烷基链长度和萃取温度等因素对萃取分离效果的影响.结果表明,L-酒石酸酯与II对映体形成的复合物稳定性比与I对映体形成的复合物要好;1.2-二氯乙烷作为有机相效果较好;随着L-酒石酸酯浓度的增大,分配系数K逐渐增大,而分离因子α先增大然后开始减小;随着pH的增大,K和α都降低;L-酒石酸酯烷基链长度及萃取温度对K和α有较大影响.     

Emulsion liquid membrane extraction of Ni(II) and Co(II) from acidic chloride solutions using bis-(2-ethylhexyl) phosphoric acid as extractant

An emulsion liquid membrane process using bis-(2-ethylhexyl) phosphoric acid (D2EHPA) to extract and separate Ni(II) and Co(II) from acidic chloride solutions is described. Liquid membrane consists of a diluent, a surfactant (Span 80), and an extractant (D2EHPA). Hydrochloric acid was used as the stripping solution. The important parameters governing the permeation of nickel and their effect on the separation process have been studied. These parameters are stirring speed, feed phase pH, surfactant concentration, extractant concentration, stripping phase concentration, phase ratio, initial concentration of metal, and treatment ratio. The optimum conditions have been determined. The separation factors of Ni(II) with respect to Co(II), based on initial feed concentration, have been experimentally determined. Furthermore, the extraction selectivity for Co(II) over Ni(II) has been improved by using D2EHPA during the initial minutes.     

Extraction of Lanthanide Nitrates in Multicomponent Aqueous-Organic Two-Phase Systems with D2EHPA

Lanthanum nitrate distribution in three-component aqueous-organic systems with D2EHPA from acetate or acetic acid–acetate solutions has been studied, it has been shown that variation in sodium acetate concentration or composition of CH₃COONa–CH₃COOH mixture can affect metal distribution ratios. It has been found that extraction in three-component mixture of 1: 1: 1 composition (aqueous solution Ln(NO₃)₃ + CH₃COONa + CH₃COOH–D2EHPA in hexane–isopropyl alcohol) can provide lanthanide separation, which is dependent on the ratio of sodium acetate and acetic acid in aqueous phase and on D2EHPA concentration in organic phase. Lanthanide–lanthanum separation factors have been calculated for the extraction of lanthanide nitrates from acetic acid–acetate solutions.     

Investigation of molecular interactions in the complex formation of tartaric acid derivatives with di(2-ethylhexyl) phosphoric acid

The molecular interactions in the complex formation of two tartaric acid derivatives with di(2-ethylhexyl) phosphoric acid are investigated. The complex formation with a 1:1 stoichiometry between tartaric acid derivatives and D2EHPA can be obtained through UV-Vis titration, NMR chemical shifts and molecular dynamic simulations. Furthermore, the differences of the two complexes on the binding constants and strength of hydrogen bonds can also be determined. Such research will ideally provide insight into ways of regulating the complex forming properties of tartaric acid derivatives for composing or syn- thesizing new chiral resolving agents.     

二（2—乙基己基）单硫代磷酸萃取铟的研究

目前采用二(2-乙基己基)磷酸(D2EHPA)从硫酸溶液中萃取铟在生产上虽获得广泛应用,但反萃取又转入盐酸体系,腐蚀刺激性较强.改用D2EHMTPA萃取铟可能较好,有关这方面的研究至今尚未见报道,本文从硫酸溶液中考察了D2EHMTPA萃取铟的性能,并与D2-EHPA和二(2-乙基己基)二硫代磷酸(D2EHDTPA)作比较,以了解这类萃取剂结构上的差别对萃取铟的影响,这对选择及合成高效能萃取剂分子也是有意义的,还应用斜率法、饱和法确定了萃取平衡反应及萃合物组成,根据IR与NMR探讨了D2EHMTPA萃取铟的机理。     

Pertraction of cadmium and zinc ions using a supported liquid membrane impregnated with different carriers

An experimental study on the removal of Cd²⁺ and Zn²⁺ through a supported liquid membrane using a mixture of mono-(2-etylhexyl) ester of phosphoric acid (M2EHPA) and bis-(2-etylhexyl) ester of phosphoric acid (D2EHPA) as carriers is presented. Parameters affecting the Cd²⁺ and Zn²⁺ pertraction such as feed concentration, carrier concentration, pH of the stripping phase, and TBP (tributyl phosphate) concentration were analyzed using the Taguchi method. Optimal experimental conditions for Cd²⁺ and Zn²⁺ pertraction were obtained using the analysis of variance (ANOVA) after a 6 h separation with the initial feed concentration of 8.9 × 10^?4 mol L^?1, carrier concentration of 20 vol. %, TBP concentration of 4 vol. %, and pH of 0.5. Then, under optimum conditions, a comparison of M2EHPA, D2EHPA, and bis-(2,4,4-trimethylpentyl)monothiophosphinic acid (Cyanex 302) was performed. Effective pertraction of Cd²⁺ and Zn²⁺ using these carriers was observed in the following order: mixture of M2EHPA and D2EHPA, D2EHPA, Cyanex 302. It was also found that the presence of one metal ion in the feed solution reduces the pertraction rate of the other one.     

The uranium(VI) extraction mechanism of D2EHPA-TOPO from a wet process phosphoric acid

This paper reports the results of an investigation into the solvent extraction of uranium from technical grade phosphoric acid using industrially available extractants as D2EHPA and TOPO diluted in technical grade kerosene. Preliminary tests showed that, the effect of different parameters such as uranium oxidation stage, temperature and the molar ratio of D2EHPA/TOPO on the uranium recovery was in good agreement with those of previous investigations. However, a detailed investigation into the effect of phosphoric acid concentration, organic concentration and acid/organic phase ratios suggested that the mechanism of D2EHPA/TOPO synergism was rather complex and it presented a different character depending on the acid concentration.     

Pertraction of methylene blue using a mixture of D2EHPA/M2EHPA and sesame oil as a liquid membrane

An experimental study on the pertraction of methylene blue (MB) through a supported liquid membrane (SLM) using a mixture of mono-(2-etylhexyl) ester of phosphoric acid (M2EHPA) and bis-(2-etylhexyl) ester of phosphoric acid (D2EHPA) and sesame oil as the liquid membrane (LM) was performed. Parameters affecting the pertraction of MB such as initial MB concentration, carrier concentration, feed phase pH, and stripping phase concentration were analyzed. Optimal experimental conditions for MB pertraction (permeability of 5.63 × 10^?6) were obtained after a 7 h separation with the MB concentration in the feed phase of 80 mg L^?1, D2EHPA/M2EHPA concentration in membrane phase of 40 vol. %, feed pH of 6, and acetic acid concentration in the stripping phase of 0.4 mol L^?1. Kinetics of transport and stability of the SLM system were also studied and the mass transfer coefficient for this system was evaluated. Scanning electron microscopy (SEM) was used to morphologically characterize the membrane surface.     

Tb(III) Transport in Dispersion Supported Liquid Membrane System with D2EHPA as Carrier in Kerosene

The transport of Tb(III) in dispersion supported liquid membrane(DSLM) with polyvinylidene fluoride membrane(PVDF) as the support and dispersion solution including HCl solution as the stripping solution and di(2-ethylhexyl) phosphoric acid(D2EHPA) dissolved in kerosene as the membrane solution, has been studied. The effects of pH value, initial concentration of Tb(III) and different ionic strength in the feed phase, volume ratio of membrane solution to stripping solution, concentration of HCl solution, conc...     

Dysprosium pertraction through facilitated supported liquid membrane using D2EHPA as carrier

The pertraction of dysprosium (Dy) through a supported liquid membrane (SLM) system consisting of PTFE (polytetrafluoroethylene) support, D2EHPA (di-2-ethylhexyl phosphoric acid) dissolved in kerosene as membrane solution, and HNO₃ solution as stripping solution, was studied. The experiments were designed by the Taguchi method in order to investigate the effects of initial Dy concentration, feed phase pH, different stripping solution concentration, and D2EHPA concentration in the membrane phase on Dy pertraction. Optimal experimental conditions for Dy pertraction were obtained using an analysis of variance (ANOVA) (feed concentration: 130 mg L^?1, D2EHPA concentration: 0.90 M, feed phase pH: 5, stripping phase concentration: 2 M). In addition, the stability of the carrier in terms of its leaching from the membrane support was studied over a period of 6 days and was found to be satisfactory over that time.     

二-(2-乙基己基)磷酸与仲壬基苯氧基取代乙酸混合体系对稀土元素的萃取

考察了二-(2-乙基己基)磷酸(D2EHPA,H2A2)和仲壬基苯氧基取代乙酸(CA100,H2B2)混合体系在HCl介质中对15种镧系元素(除钷)及钇的萃取性能,计算了稀土元素间的分离系数,并比较了混合萃取体系与D2EHPA单独萃取体系对稀土元素的分离能力.研究了D2EHPA-CA100混合体系对镧的协同萃取机理,用斜率法和恒摩尔法探讨了萃取反应方程式,考察了酸度、萃取剂浓度及温度对萃取性能的影响.结果表明:D2EHPA-CA100混合体系对镧系元素的协同效应随原子序数的增加而减弱.在适当的萃取剂配比下,此混合体系对某些稀土元素的分离能力优于D2EHPA,可用于这些稀土元素的分离.D2EHPA-CA100混合体系协同萃取镧的萃合物组成为LaH5A6B2,反应为吸热反应.