室温离子液体对氨基苯磺酸的萃取性能

系统研究了[C₄mim][PF₆], [C₆mim][PF₆], [C₆mim][BF₄]和[C₈mim][BF₄]室温离子液体对间氨基苯磺酸、对氨基苯磺酸稀水溶液的萃取平衡. 实验结果表明: 萃取温度和相体积比的变化对分配比影响不大; 水相pH值对萃取平衡有较大的影响, 氨基苯磺酸在离子液体/水体系中的分配比在pH＝4.2时达到最大值; 水相中CaCl₂或Na₂SO₄的存在能较大幅度地提高氨基苯磺酸的分配比; 离子液体的阴离子的性质对分配比有显著的影响, 阴离子为[BF₄]^－的离子液体对氨基苯磺酸的萃取能力大于阴离子为[PF₆]^－的离子液体; 咪唑环上烷基链的长度也对萃取效果有一定的影响. 在所研究的离子液体中, [C₆mim][BF₄]和[C₈mim][BF₄]对氨基苯磺酸有较好的萃取性能, 且萃取相中的氨基苯磺酸可回收利用, 离子液体也可循环使用.     

离子液体萃取阿魏酸和咖啡酸的性能研究

以1-甲基-3-丁基咪唑六氟磷酸盐([C4mim][PF6])和1-甲基-3-己基咪唑六氟磷酸盐([C6mim][PF6])离子液体为萃取剂,采用紫外分光光度法研究了溶液pH值、温度、相比率及盐的种类和浓度对其萃取阿魏酸和咖啡酸效率的影响,考察了被萃取物的回收及离子液体的循环使用,探讨了两种离子液体替代传统有机溶剂阿魏酸和咖啡酸的可能性。实验结果表明:萃取温度和无机盐的种类及浓度对FA和CA萃取效率的影响较小;水相pH值对萃取效率有较大的影响,萃取FA适宜pH应小于3.67,萃取CA适宜pH应小于3.71;被萃取物浓度增大,萃取效率降低,而相体积比增大其萃取效率升高;两种离子液体对FA和CA的萃取效率[C4mim][PF6]大于[C6mim][PF6],同种离子液体对FA的萃取效率大于CA;在萃取相中的FA和CA可定量回收,且被萃取物中离子液体的残留[C6mim][PF6]小于[C4mim][PF6],离子液体可循环使用。     

CMPO-离子液体体系对Ce3+的萃取

本文研究了CMPO[辛基(苯基)-N,N-二异丁基氨甲酰基甲基氧化膦]溶于疏水性离子液体BmimNTf2(1-丁基-3-甲基咪唑双三氟甲磺亚酰胺盐)和BmimPF6(1-丁基-3-甲基咪唑六氟磷酸盐)对硝酸水溶液体系中Ce3+的萃取行为,详细考察了稀释剂、酸度、金属离子浓度、盐析剂、萃取剂浓度、温度等对萃取性能的影响。研究结果表明:离子液体BmimNTf2体系中Ce3+的萃取率远高于BmimPF6体系;硝酸浓度、金属离子浓度的增大会导致萃取率下降;温度升高萃取率降低;萃取剂CMPO浓度升高萃取率增大;而盐析剂(C=0.001~1 mol.L-1时)对Ce3+的萃取几乎没有影响。萃取机理的推测表明萃取反应形成三配位的配合物,其结构为Ce3+.3CMPO,萃取平衡常数为lgK=6.49,反应焓变为-47.29 kJ.mol-1。     

分离环己烷-乙醇的离子液体萃取剂的筛选

基于COSMO-RS理论模型,以乙醇的选择性系数和容量为评价指标,研究了离子液体萃取剂在强化分离环己烷-乙醇共沸体系中的应用。首先,通过与实验数据的对比分析,验证了该模型预测环己烷-乙醇体系汽液相平衡行为的可靠性。其次,从由27种阳离子和26种阴离子组合设计出的702种离子液体中筛选出性能优良的萃取剂C5A20,并考察了其对环己烷-乙醇体系汽液相平衡的影响,结果表明,在C5A20的摩尔含量仅为0.03时,即可打破该体系的共沸,用于环己烷-乙醇体系的强化分离。在此基础上,从微观分子相互作用的角度,分析了萃取剂对乙醇选择性作用机理,为进一步设计性能优异的离子液体萃取剂提供了理论依据及数据支撑。     

疏水性离子液体萃取光甘草定

选择了疏水性的离子液体1-丁基-3-甲基咪唑六氟磷酸盐([C4mim][PF6])和亲水性的离子液体1-丁基-3-甲基咪唑四氟硼酸盐([C4mim][BF4])作萃取剂,对光甘草定提取液进行了萃取,并对离子液体的再生进行了研究。结果表明,亲水性的离子液体和光甘草定提取液无法分层,而疏水性的离子液体分层清晰,并得疏水性离子液体[C4mim][PF6]萃取光甘草定最佳萃取工艺条件为:相体积比为1∶2.5(V/V),pH值为7,萃取温度为45℃,萃取时间为30 min,此时光甘草定的萃取率达85.49%。离子液体再生选用2 mol.L-1氢氧化钠和无水乙醇混合液做反萃剂,可得光甘草定的回收率大于90%,离子液体循环使用5次,萃取率未见明显下降。     

TODGA/[C_2mim][NTf_2]萃取Th~(4+)

研究了N,N,N′,N′-四辛基-3-氧戊二酰胺(TODGA)溶于疏水性离子液体咪唑类离子液体1-乙基-3-甲基咪唑双三氟甲磺酰亚胺盐([C2mim][NTf2])中对硝酸水溶液体系中四价钍离子(Th4+)的萃取行为。详细考察了接触时间、酸度、Th4+浓度、TODGA浓度、温度对TODGA/[C2mim][NTf2]体系萃取性能的影响。作为对比,我们还考察了TODGA在传统有机溶剂异辛烷中对Th4+的萃取。结果表明:TODGA/[C2mim][NTf2]体系对Th4+的萃取是吸热反应,且在50℃下,能在5 min内达到平衡。萃取体系随着酸度对Th4+的萃取性能先降后增大;Th4+浓度的增大,TODGA浓度的降低,对Th4+的萃取性能下降。TODGA在离子液体萃取体系中比在有机体系中有更好的Th4+萃取效果,特别是在低酸条件下。通过萃取机理研究,推测出在低酸下萃取反应是离子交换且TODGA与Th4+配比为2∶1,在高酸下萃取是中性配位。     

功能化离子液体/离子液体分散液-液微萃取测定水中苯氧羧酸类除草剂

建立了功能化离子液体/离子液体分散液-液微萃取(FIL/IL-DLLME)测定水中4种苯氧羧酸类除草剂的农药残留分析方法.离子液体[C4MIMBF4]有助于难溶于水的[C6HyMIMTf2N]在水相中形成液滴.离子对[LiWf2N]的引入有利于提高功能离子液体对分析物的提取效率,对影响萃取效率的重要因素进行选择和优化,最佳条件为:100 μL[C6HyMIMTf2N])作为提取剂,100 μL[C4MIMBF4]作为分散剂,在30℃下超声5 min,[LiTf2N]浓度为5％和样品溶液的pH=2.在最佳优化条件下,5～500 μg/L范围内线性良好,相关系数为0.9953 ～0.9996;对自来水、河水、田间水进行浓度为10和20 μg/L添加回收实验,回收率为70.2％～107.5％,相对标准偏差RSD＜10％,检出限为0.05 ～0.2 μg/L,得到满意的结果,说明本方法对于实际样本的检测具有可行性.     

不同离子液体双水相萃取钯

为实现贵金属钯的绿色、高效萃取,本文使用有“绿色溶剂”之称的离子液体与磷酸钾形成的双水相体系,不加入其它萃取剂对钯(Ⅱ)进行萃取,并采用浊点法对所研究的6种咪唑类离子液体的双结线和系线进行测定。 结果表明,基于氯离子和溴离子的离子液体成相能力和萃取率无显著差异。 阳离子上支链的疏水性是影响咪唑类离子液体成相能力的关键因素之一。 与不含官能团的离子液体相比,支链上嵌入氨基和腈基的离子液体,成相能力较低,但萃取率分别提高了11.57%和34.26%。 当含腈基的离子液体浓度和磷酸钾浓度分别为5.00%和39.55%时,离子液体双水相体系对钯(Ⅱ)的萃取率可达到100%。 本文的研究成果为设计/选择可利用其双水相体系高效萃取钯(Ⅱ)的离子液体提供了理论基础和数据支持。     

N,N′-二甲基-N,N′-二辛基-4-氧庚二酰胺萃取镧的研究

为了研究不同的酰胺夹醚化合物对萃取镧的性能，本文使用N,N′-二甲基-N,N′-二辛基-4-氧庚二酰胺(DMDOOHA)为萃取剂，以1-甲基-3-丁基咪唑六氟磷酸盐离子液体([C₄mim⁺][PF₆^-])为稀释剂，研究其在水相中萃取La³⁺的行为，考察了萃取时间，pH,萃取剂的的浓度、及温度对萃取分配比的影响。实验表明，萃取剂在离子液体[C₄mim⁺][PF₆^-]中对La³⁺的具有强烈的萃取能力。机理研究表明，在([C₄mim⁺][PF₆^-]体系中，萃取剂与La³⁺可能形成3∶1配合物。萃取过程为热力学自发的过程。     

咪唑离子液体及其萃取体系的辐射效应研究

离子液体因其低挥发性,高热稳定性及在萃取金属离子方面的优良表现被认为是乏燃料后处理中萃取分离放射性核素的新一代绿色溶剂。但从乏燃料后处理强辐射的应用环境来看,需要首先对离子液体及其萃取体系的辐射效应进行系统研究和评估。本文以两种常见的憎水性咪唑离子液体1-丁基-3-甲基咪唑六氟磷酸盐( )和1-丁基-3-甲基咪唑三氟甲基磺酰亚胺酸盐( )为例,综述了我们在离子液体及其萃取体系的γ辐射效应方面的最新研究进展,内容包括纯离子液体在氮气气氛下的辐射效应,硝酸对离子液体辐射效应的影响,离子液体辐解产物的分离分析及γ辐照对离子液体体系萃取金属离子的影响等。基于以上研究对离子液体用于乏燃料后处理的可行性进行了评估,同时对离子液体及其萃取体系的辐射效应研究进行了展望。     

Investigation on the extraction of strontium ions from aqueous phase using crown ether-ionic liquid systems

The extraction of strontium ions using DCH18C6 as the extractant and various ionic liquids (ILs) as solvents has been investigated. The distribution ratio of Sr²⁺ can reach as high as 10³ under certain conditions, much larger than that in DCH18C6/n-octanol system. The extraction capacity depends greatly on the structure of ionic liquids. In IIs-based extraction systems, the extraction efficiency of strontium ions is reduced by increasing the concentration of nitric acid and can also be influenced directly by the presence of Na⁺ and K⁺ in the aqueous phase. It is confirmed that the extraction proceeds mainly via a cation-exchange mechanism.     

Fluorous ionic liquids as solvents for the liquid-liquid extraction of metal ions by macrocyclic polyethers

The predominant mode of strontium ion transfer from aqueous nitrate media into a series of 1-fluoroalkyl-3-methylimidazolium bis[(trifluoromethylsulfonyl)]imides containing dicyclohexano-18-crown-6 (DCH18C6) is shown to shift from cation exchange to strontium nitrato-crown ether complex partitioning as the length of the fluoroalkyl substituent is increased. Fluoroalkyl substituents are shown to be only slightly more effective than their non-fluorous analogs at inducing this shift. At the same time, the fluorinated ionic liquids (ILs) yield strontium distribution ratios as much as an order of magnitude lower than the corresponding 1-alkyl-3-methylimidazolium (C_nmim⁺) salts. Fluorous ILs thus appear to offer no compelling advantages over C_nmim⁺ ionic liquids as extraction solvents.     

Radical channels of radiation destruction of macrocyclic component of strontium-selective extractants based on ionic liquids

Russian Chemical Bulletin - To study the radiolysis of the extractant composition based on solutions of dicyclohexano-18-crown-6 (DCH18C6) in ionic liquids containing the...     

Separation of components of the solution modeling PUREX raffinate via extraction by crown ethers to 1,1,7-trihydrododecafluoroheptanol

We study the extraction of strontium, cesium, and some other elements by dicyclohexano-18-crown-6 (DCH18C6) and its di-tert-butyl derivative (DTBDCH18C6) in the system 1,1,7-trihydrododecafluoroheptanol-water from the solution modeling PUREX raffinate. We show that strontium under these conditions is extracted in a single contact with distribution ratios of 100–200 and separates from sodium, whose distribution ratio is less than 0.01. Strontium extraction in a single contact reaches 99.5%. The stoichiometry and stability constants are determined for nitric acid complexes of the crown ethers studied with coextraction of nitric acid (1: 1). The mutual solubilities of the components in the system 1,1,7-trihydrododecafluoroheptanol-water are calculated using chromatography/mass spectrometry: water in alcohol is 0.5 wt %, and alcohol in water is 0.16 wt %.     

Screening the extractability of some typical environmental pollutants by ionic liquids in liquid-phase microextraction

The extractability of some typical environmental pollutants in ionic liquids (ILs) was screened by using a simple one-step liquid phase microextraction procedure. It was demonstrated that 1-alkyl-3-methylimidazolium hexafluorophosphate ([CnMIM][PF6], n = 4, 8), two typical ILs, could effectively extract a set of 45 typical environmental pollutants including BTEX (benzene, toluene, ethylbenzene, and xylene), polycyclic aromatic hydrocarbons, phthalates, phenols, aromatic amines, herbicides, organotin, and organomecury. Analytes in 10 mL sample solution held in a 15 mL vial were extracted by a 5 microL drop of ILs suspended on the needle of a high-performance liquid chromatography (HPLC) microsyringe; this was followed by HPLC, atomic absorption spectrometry, or cold-vapor atomic fluorescence spectrometry determination. The enrichment factors determined were in the range of 5-168 for 15 min extraction by [C4MIM][PF6] and 4-178 for 30 min extraction by [C8MIM][PF6], respectively, which indicates that ILs might be considered as potential environmentally benign alternative recyclable solvents for the enrichment of environmental pollutants.     

气态[HPro（C1）]＋和[Sac]-相互作用及质子转移机制的理论研究

质子化功能离子液体在许多重要领域具有潜在的应用价值,然而人们对其相互作用模式、质子转移行为等方面的认识尚不清晰．本文利用DFT／B3LYP和MP2方法,以脯氨酸阳离子[HPro]＋、脯氨酸甲酯阳离子[HProC1]＋和糖精阴离子[Sac]=组成的质子化离子液体（PILs）为研究对象,探讨气态离子对、分子对、双聚体团簇中的结构单元及其作用模式．利用过渡态和内禀反应坐标（IRC）理论研究气态[HPro]＋[Sac]-和[HProCl]＋[Sac]-中的质子转移反应,AIM（atomsinmolecules）理论分析给出氢键相互作用本质等．计算结果表明,气态单聚体中氢转移能垒很小,体系中存在离子对和分子对的动态平衡．质子转移发生后,体系内部基本作用单元改变,作用强度下降,形成分子对的相互作用能量远远小于离子对的相互作用能量．双聚体团簇计算说明体系中没有质子转移反应发生,在[HPro]2＋[Sac]2-中相互作用的基本结构单元为离子、分子和两性离子,酯化后双聚体[HProC1]2＋[Sac]2-中全部为阴阳离子相互作用．质子转移反应、两性离子和酯化作用等的深入研究对于理解功能化PILs的性质、结构因素及其应用具有一定的实际意义．     

Ionic liquids: solvents and sorbents in sample preparation

The applications of ionic liquids (ILs) and IL‐derived sorbents are rapidly expanding. By careful selection of the cation and anion components, the physicochemical properties of ILs can be altered to meet the requirements of specific applications. Reports of IL solvents possessing high selectivity for specific analytes are numerous and continue to motivate the development of new IL‐based sample preparation methods that are faster, more selective, and environmentally benign compared to conventional organic solvents. The advantages of ILs have also been exploited in solid/polymer formats in which ordinarily nonspecific sorbents are functionalized with IL moieties in order to impart selectivity for an analyte or analyte class. Furthermore, new ILs that incorporate a paramagnetic component into the IL structure, known as magnetic ionic liquids (MILs), have emerged as useful solvents for bioanalytical applications. In this rapidly changing field, this Review focuses on the applications of ILs and IL‐based sorbents in sample preparation with a special emphasis on liquid phase extraction techniques using ILs and MILs, IL‐based solid‐phase extraction, ILs in mass spectrometry, and biological applications.     

CO2/离子液体体系热力学性质的分子动力学模拟

超临界CO2和离子液体(ILs)是两种绿色溶剂. 离子液体可以溶解超临界CO2, 而超临界CO2不能溶解离子液体. 由此设计构成的CO2/IL二元系统, 同时具备了超临界CO2和离子液体的许多优点: 既可以降低离子液体的粘度, 还便于相分离, 是新型的耦合绿色溶剂. 其物理化学性质对于设计反应、分离等过程非常重要. 因此, 本文以CO2/IL二元系统为研究对象, 通过选择合适的分子力场和系综, 运用分子动力学(MD)模拟方法研究了CO2/[bmim][PF6]、CO2/[bmim][NO3]等体系的热力学性质. 结果表明, CO2对ILs膨胀度的影响非常小, 当CO2摩尔分数为0.5时, ILs膨胀仅为15%. CO2/ILs的扩散系数远小于CO2膨胀甲醇、乙醇溶液的扩散系数. 随着CO2含量的增加, ILs的扩散系数提高, 粘度显著下降, 表明CO2能有效地改善ILs扩散性, 减小其粘度. 因此CO2可用以改善离子液体溶剂体系的传递特性, 增强反应分离过程在其中的进行.     

Extraction and separation of a lysine-rich protein by formation of supramolecule between crown ether and protein in aqueous two-phase system

The macrocyclic calixarenes and crown ethers have recently been found to form hydrophobic complexes with the cationic protein cytochrome c (Cyt-c), by recognizing lysine residues on the protein surface. In the present study, it was found that the distribution of cytochrome c in Li₂SO₄/PEG aqueous two-phase system (ATPS) can be controlled by complexation with the crown ether dicyclohexano-18-crown-6 (DCH18C6). The protein was quantitatively extracted into the PEG-rich phase in the presence of DCH18C6 and perchlorate ion. Of various crown ethers and their analogues that were investigated, only DCH18C6 was able to extract cytochrome c into the PEG-rich phase. Extraction of cytochrome c in the ATPS using DCH18C6 is complete within 5 min. Cytochrome c complexed with DCH18C6 in the PEG-rich phase was quantitatively recovered into a salt-rich phase using K₂SO₄ by ion exchange of potassium ion and cationic protein in the cationic protein complex with DCH18C6. Selective extraction of cationic proteins was demonstrated in the ATPS. Under optimum conditions, the lysine-rich protein cytochrome c was selectively extracted over other cationic proteins using DCH18C6.     

Study on the Mechanism of Ionic Liquids Improving the Extraction Efficiency of Essential Oil Based on Experimental Optimization and Density Functional Theory: The Fennel (Foeniculi fructus) Essential Oil Case

In this work, microwave-assisted ionic liquids treatment, followed by hydro-distillation (MILT-HD), as an efficient extraction technology, was used to extract essential oil. The purpose for this was to use multivariate analysis (MVA) models to investigate the effects of potential critical process parameters on the extraction efficiency of essential oil, and explore the mechanism of ionic liquids (ILs). According to the design of experiment (DoE), under optimal process conditions, the extraction efficiency of essential oil was dramatically enhanced, and had low energy demands. Since little is known regarding those mechanisms, according to the non-covalent interaction analysis, the underlying mechanism for ILs improving extraction efficiency was explored based on the density functional theory (DFT). The results showed that ILs could form intense non-covalent bond interaction with cellulose. It helped destroy the network hydrogen bond structure of cellulose in plant cells and caused the essential oils in the cells to be more easily exposed to the extraction solution, thereby accelerating extraction efficiency. Based on this work, it is conducive to understand the MILT-HD process better and gain knowledge of the mechanism of ILs.