Cextrant 230从低品位铜矿H2SO4-NaCl浸出液中选择性提取回收铜

助浸剂NaCl可提高硫酸在常温常压下浸取低品位复杂铜矿时铜的浸出率,但也形成了含铜的混酸溶液。二(2-乙基己基)-(N-(2-乙基己基)氨基)甲基膦酸酯(Cextrant230)对混酸(H₂SO₄+HCl)溶液中Cu²⁺、Fe³⁺、Co²⁺、Mg²⁺和Al³⁺的萃取行为进行了研究。结果表明,Cextrant 230对混酸溶液中的Cu²⁺和Fe³⁺具有良好的萃取能力和选择性,而对Co²⁺、Mg²⁺和Al³⁺的萃取能力较弱;Cl^-可促进Cu²⁺的萃取,而SO₄^2-和HSO₄^-对Cu²⁺的萃取起抑制作用;Cu²⁺的萃取过程是放热反应;当水相初始pH值为1.16...     

“抑制-萃取”法从含铁酸溶液中选择性提钒

酸法浸出石煤提钒因具有环保、金属收率高的特点而备受关注,但同时进入母液的铁(高含量的Fe³⁺)严重影响了钒的富集和产品生产。 对此,本文提出一种基于“抑制-萃取”效应的钒/铁分离混合萃取体系(P507(2-乙基己基磷酸-单2-乙基己基酯)+ N235(三辛/癸烷基叔胺)+磺化煤油),并详细研究了各因素对钒铁分离和钒富集的影响规律。 结果表明,P507是钒铁萃取的主体,N235不具萃Fe³⁺能力,是产生抑制铁萃取的关键因素,其浓度越高铁萃取率越低;对于酸度较高(pH≤0.4)的原料液钒/铁的分离效果仍较好,这表明了该“抑制-萃取”混合萃取体系对高酸度浸出液钒/铁分离的适用性。 采用氨水从负载有机相中反萃取钒铁,当氨水浓度为6 mol/L时钒的反萃率99%以上,25 ℃,V(有机相)∶V(水相)=2∶1时的反萃液中钒质量浓度14.73 g/L,铁质量浓度小于0.022 g/L,m(V)/m(Fe)=669.5。 该“抑制-萃取”法分离钒/铁操作简单、经济高效,极具工业化前景。     

硫代磷酸酯萃取铊(Ⅰ)的研究

近年来,硫代磷酸酯萃取分离金属的研究日益增多^[1,2],人们较多地注意其萃取机理和萃合物组成,而以量子化学计算说明硫代磷酸酯结构与铊(Ⅰ)萃取关系的研究甚少。本文比较了二(2-乙基己基)单硫代磷酸(D₂EHMTPA)、二(2-乙基已基)二硫代磷酸(D₂EHDT-PA)]和二(2-乙基已基)磷酸(D₂EHPA)从硫酸介质中对铊(Ⅰ)的萃取行为,并通过EHMO法计算结果,对硫代磷酸醋结构与铭(Ⅰ)萃取能力的关系进行了研究。     

P-507回流萃取法富集镥的研究——Ⅰ.P-507萃取分离镱镥混合稀土的性能

本文研究了2-乙基己基膦酸单2-乙基己基酯(P-507)在盐酸和硝酸体系中萃取镱镥混合稀土的性能。说明P-507在硝酸体系中的萃取分离系数较其在盐酸体系中高,而在盐酸体系中有更高的反萃效率。与二(2-乙基己基)磷酸(P-204)相比,P-507具有萃取酸度低、易反萃和不易乳化的优点。我们还确定了回流萃取法分离镥镱的基本参数,表明P-507是一种新型的分离重稀土的良好萃取剂。     

EHEHPA萃取Co(Ⅱ)的动力学和机理的研究

本工作研究了2-乙基己基膦酸单2-乙基己基酯(即EHEHPA)从醋酸醋酸钠缓冲介质中萃取Co(Ⅱ)的动力学和机理。萃取反应在改进的恒界面池中进行,并建立了连续、自动测量萃取动力学数据的研究系统。在动力学坪区测定了一系列初始萃取速率和反萃速率,比界面积和表面活性剂等对萃取速率的影响表明化学反应发生在液液界面,低于30℃时的表观活化能为82kJ·mol^-1,高于30℃时为31kJ·mol^-1,宽的组分浓度变化也会引起传质控制过程的转变。由此可以认为:EHEHPA萃Co(II)的动力学过程在萃取速率较低时为化学反应控制,随着反应速率的加快转变为组分在界面膜的扩散控制。     

螯合-酸性磷萃取剂对铀(VI)的协同萃取

本文研究了螯合-酸性磷协同萃取体系─1-苯基-3-甲基-4-(2'-氯苯甲酰基)-5-吡唑啉酮(PMCBP)与磷酸二(2-乙基己基)酯(HDEHP)和2-乙基己基膦酸-单-2-乙基己基酯(HEHEHP)的氯仿溶液从硫酸介质中对铀(VI)的萃取。实验发现均有明显的协同效应存在。采用斜率法测定了协萃配合物的组成为UO2HA2X和UO2HA2HXX'的混合物, 计算了它们的萃取平衡常数, 讨论了协萃机理。     

纸上反相分配层析与液液萃取分离2-乙基己基膦酸单(2-乙基已基)酯对镧系元素反相分配层析研究

Cerrai^[1,2]等曾研究了二(2-乙基己基)磷酸(HDEHP)对稀土元素的反相层析,并用斜率法测定了萃合物组成.Cvjelicanin^[3]用反相层析研究了二丁基磷酸对铍、镧及铈的萃取机理和平衡常数.我们以往的研究结果说明,配位体结构的极性效应和空间效应对分离金属离子的反相层析行为与液液萃取极相似^[4,5].     

辛基膦酸单丁酯萃取钴(Ⅱ)、镍(Ⅱ)的结构-性能关系

在钴、镍的湿法冶炼工艺中,溶剂萃取技术己获得了广泛的应用.自1968年Ritcey等首次提出采用二(2-乙基己基)磷酸(DEHPA)作为硫酸盐介质中分离钻、镍的萃取剂以来,又先后出现了2-乙基己基麟酸单2-乙基己基醋(EHEHPA)和二（2,4,4-三甲基戊基）磷酸(Cyanex 272、二(1-甲基庚基)磷酸等高效钻一镍分离萃取剂.     

二(2-乙基己基)二硫代次膦酸对硝酸溶液中Am3+和Eu3+的萃取

以正十二烷作稀释剂, 研究了二(2-乙基己基)二硫代次膦酸(D2EHDTPA)对HNO₃溶液中Am³⁺和Eu³⁺的萃取行为. 考察了酸度、 萃取剂及N{\mathrm{O}}_3^{-}浓度和皂化度对萃取的影响. 在考察的pH范围(2.5~4.5)内, D2EHDTPA萃取Am³⁺和Eu³⁺的分配比(D)随pH值增大而增加; pH=3.65时, 分离因子(SF_Am/Eu)值达到最大(4000). 随D2EHDTPA浓度的增加, D_Am和D_Eu值均增加. 斜率分析表明, D2EHDTPA萃取Am³⁺和Eu³⁺主要形成3:1和2:1型的萃合物. N{\mathrm{O}}_3^{-}未直接参与D2EHDTPA对Am³⁺和Eu³⁺的萃取反应. D2EHDTPA经NaOH皂化后, 萃取能力显著增强, SF_Am/Eu值提高到10⁴量级, 萃取容量约为理论值的60%. 此外, 使用高分辨质谱、 红外光谱和等温微量热滴定方法研究了D2EHDTPA与Eu³⁺的配位化学行为, 得到了金属离子与配体的组成比、 络合物稳定常数以及配位热力学参数ΔH, ΔS和ΔG值.     

含氟硫酸体系HEH/EHP萃取铈(Ⅳ)的动力学研究

采用层流恒界面池法研究了2-乙基己基膦酸单2-乙基己基酯(HEH/EHP)萃取含氟复杂硫酸体系中铈(Ⅳ)的动力学。考察了搅拌速度、水相金属离子浓度、萃取剂浓度、酸度和温度对萃取速率的影响。试验结果表明:萃取反应为一级反应,萃取反应的正向表观活化能为50.8 kJ·mol-1,属于化学反应控制。试验得到萃取动力学方程为R=k[Ce(HF)(HSO4-)3+]1.05[H2A2]2.07[H+]-2.43,并探讨了反应机制。     

α-Fe2O3、γ-Al2O3、SiO2混合体系的表面配位反应

运用自动电位滴定技术分别研究了纳米α-Fe₂O₃、γ-Al₂O₃、SiO₂单一体系及三组分混合体系中氧化物表面的酸碱性质和对重金属离子Cu²⁺、Pb²⁺、Zn²⁺的吸附行为. 依据表面配位理论恒电容模式(CCM), 计算了相应的表面酸碱配位常数. 结果表明: α-Fe₂O₃/γ-Al₂O₃/SiO₂三组分混合体系的表面化学反应并非是单一体系的简单叠加, 而是存在着不同矿物表面间复杂的交互作用. 三组分表面酸碱反应平衡式和相应的酸碱反应平衡常数分别为: ≡XOH₂⁺?≡XOH+H⁺ (lgK_a1=-4.23), ≡XOH?≡XO^-+H⁺(lgK_a2=-8.41). 根据重金属离子Cu²⁺、Pb²⁺、Zn²⁺在α-Fe₂O₃/γ-Al₂O₃/SiO₂混合体系表面的吸附行为, 计算得到Cu²⁺、Pb²⁺、Zn²⁺在混合体系表面配位反应及其平衡常数如下: ≡XOH＋M²⁺?≡XOM⁺+H⁺; lgK=-2.20, -1.90, -3.20 (M=Cu, Pb, Zn).     

Solvent extraction studies of plutonium(IV) and americium(III) in room temperature ionic liquid (RTIL) by di-2-ethyl hexyl phosphoric acid (HDEHP) as extractant

Solvent extraction of Pu(IV) and Am(III) from aqueous nitric acid into room temperature ionic liquid (RTIL) by an acidic extractant HDEHP (di-2-ethyl hexyl phosphoric acid) was carried out. The D values indicated substantial extraction for Pu(IV) and poor extraction for Am(III) at 1M aqueous nitric acid concentration. However at lower aqueous nitric acid concentrations (pH 3), the Am(III) extraction was found to be quantitative. The least squares analysis of the extraction data for both the actinides ascertained the stoichiometry of the extracted species in the RTIL phase for Pu(IV) and Am(III) as [PuH(DEHP)₂]³⁺, AmH(DEHP)²⁺. From the D values at two temperatures, the thermodynamic parameters of the extraction reaction for Pu(IV) was calculated.     

Membrane extraction for separation of copper cations from acid solution using polypropylene hollow fibre membrane

The membrane extraction of copper ions was carried out using hydrophobic poly(propylene) (PP) hollow fiber membrane modules and kerosene solutions containing organic extractant. The influences of different extractant on the extraction yield, mass transfer performance and mass transfer mechanism were studied. Compared with 2‐ethylhexyl phosphoric acid (2EHPA) and 2‐methyl‐5‐sulpho benzaldoxime (2M5SB), di‐(2‐ethylhexyl)phosphoric acid (D2EHPA) extractant system with high distribution coefficient exhibited higher extraction yield of 99.7%. The extraction equilibrium time, the final extraction yield and the total mass transfer coefficient were independent of the flow rates of two phases. The extraction equilibrium time and the final extraction yield at different flow rates of two phases were 80 min and near 99.5%, respectively. A mass transfer model of a complexation reaction describing the overall mass transfer resistance was controlled by interfacial reactions rather than the aqueous and organic boundary layer which could explain the effect of flow rate on the final extraction yield and the total mass transfer coefficient. This model showed that the mass transfer resistance and mass transfer coefficient were independent of Cu²⁺ when copper ion concentration was more than 0.06 g/L. However, when copper concentration was less than 0.06 g/l, the mass transfer resistance increased as Cu²⁺ concentration decreased, and the mass transfer coefficient decreased as Cu²⁺ concentration decreased. Extractant entrainment in the aqueous phase and membrane fouling were investigated primarily. It was found that the solvent entrainment could reduce to 10 ppm much lower than 200 ppm of the classic liquid–liquid extraction, and that the cleaning of contaminated membranes was not complete. However, it can be still concluded from this research that the membrane extraction in PP hollow fibre with D2EHPA extractant would be an effective and promising processing means for Cu²⁺ separation from aqueous solution. Copyright © 2005 John Wiley & Sons, Ltd.     

二-（2-乙基己基）磷酸P204与三烷基叔胺N235协同萃取钼

研究了P204（二-(2-乙基己基)磷酸, HA）和N235（三烷基胺, R3N）二元体系在HCl介质中对金属钼的萃取,结果表明P204和N235混合萃取剂在萃取钼时存在协同效应,并且在N235摩尔分数为0.7时协萃系数为2.24;考察了溶液酸度、P204或N235浓度及温度对萃取钼的影响,确定了协萃络合物为(R3NH)3•HMo8O26•2(HA),并比较了负载前后有机相的红外光谱。     

D2EHDTPA-TOA反协同萃取镉的速率方程

以恒界面池法研究了D2EHDTPA（二（2-乙基己基）二硫代磷酸）-TOA（三辛胺）反协同萃取镉的界面反应速率方程.萃取历程由若干个相转移（在本体相与界面相之间的物质转移）过程和若干个反应组成.萃取的速率方程为 r=1.42*10^-7[Cd²⁺]^0.42[BHA]^0.47/[B]^0.85[H⁺]^0.21 （mol•m^-2•s^-1） 探讨了萃取速率方程中非整数反应物级数的物理意义.Freundlich因子n越大,物质在界面层所受排斥力越大.萃取过程的表观活化能E=44.2 kJ•mol－1,萃取反应的焓变ΔH=72.9 kJ•mol－1.讨论了由不同的界面模型而导致不能通融的萃取动力学机理的问题.     

Effect of external factors on the increase in the extraction rate in a vibration treatment on the dynamic interfacial layer

Vibration treatment of a dynamic interfacial layer in the extraction system constituted by an aqueous solution of a salt of a rare-earth element and a solution of di-(2-ethylhexyl)phosphoric acid in heptane (toluene) results in an increase in the process rate. This increase is characterized by an acceleration coefficient defined as the ratio between the lanthanide concentrations in the organic phase after equal intervals of time in systems with and without vibrations. It is shown that the acceleration coefficient depends on the concentration of the extractive agent, initial concentration of an element being extracted, solution pH, and phase contact duration. The observed behavior is explained in terms of the process model suggested by the authors. According to this model, the effect depends on the relative contributions made by a number of interfacial phenomena accompanying the extraction of a lanthanide with solutions of di-(2-ethylhexyl)phosphoric acid in diluents and, in particular, by the spontaneous surface convection and structuring in the interfacial layer.     

HDEHP和HEHEHP萃取Au(Ⅰ)的研究

在298±1K时以恒界面搅拌池法考察了Au(I)/(Na,H)Cl、CS(NH₂)₂/HDEHP(或HEHEHP)-煤油体系的萃取平衡和动力学过程.确定了萃取平衡机理为阳离子的交换,动力学过程的速控步骤可能发生在两相交界处,属于界面反应。     

表面活性剂对HDEHP萃取动力学的影响

用上升液滴法测定二(2-乙基己基)磷酸(HDEHP)从硫酸盐介质中萃取Co^2^+的速率。研究体系中加入不同表面活性剂所引起萃取速率的不同改变: 三辛基氧化膦(TOPO)因与HDEHP形成可萃取的Co^2^+活性分子缔合物, 降低了萃取过程活化能而使反应加速; 十二烷基磺酸钠(SDS)和十六烷基三甲基溴化铵(CTMAB)因占据发生萃取反应的界面区, 减小了HDEHP与Co^2^+反应的机会而使反应减速; SDS还因其在界面形成较强的负电场(层), 造成Co^2^+的附加势能而使萃取速率有更大幅度的降低。     

γ-Al2O3/SiO2纳米颗粒混合体系表面的酸碱性质及其对重金属离子的吸附行为

运用电位滴定技术研究了γ-Al2O3/SiO2纳米颗粒混合体系的表面酸碱性质;依据滴定数据及表面配位理论恒电容模式,利用WinSGW软件计算得出了γ-Al2O3/SiO2纳米颗粒混合体系表面的酸碱反应平衡常数:≡XOH+H+≡XOH2+(lgK1=5.06±0.05);≡XOH≡XO-+H+(lgK2=-8.45±0.10);在此基础上研究了不同pH条件下重金属离子Cu2+,Pb2+,Zn2+在γ-Al2O3/SiO2纳米颗粒混合体系表面的吸附行为,并用WinSGW软件模拟得出了Cu2+,Pb2+,Zn2+在该混合悬浮液体系中的表面配位常数:≡XOH+M2+≡XOM++H+[lgK=-2.20,-1.72,-2.90(M=Cu,Pb,Zn)].