Kinetic Study of Mercury(II) Transport through a Bulk Liquid Membrane Using Cyanex 301 as Carrier

A kinetic study of Hg(II) ions transport through a bulk liquid membrane (BLM) was investigated. The commercially available liquid bis(2,4,4‐trimethyl(pentyl) dithiophosphinic acid) (Cyanex 301) was employed as mobile carrier. The influences of the carrier concentration in the liquid membrane, HNO₃ concentration in the feed phase, type of organic solvent, composition of the receiving phase, and stirring speed on mass transfer were studied. Various solvents including CH₂Cl₂, CHCl₃, C₂H₄Cl₂ and CCl₄ were used as organic membrane. Among the solvents, CHCl₃ provided the superior results. The kinetic parameters (k₁, k₂, R_m^max, t^max, J_d^max, and J_a^max) were calculated for the interface reaction assuming two consecutive, irreversible first‐order reactions. The analysis of Hg(II) accumulation in liquid membrane and the rate‐controlling step under different experimental conditions were elucidated. The experiments demonstrated that Cyanex 301 is an appropriate carrier for Hg(II) transport through liquid membrane.     

厚体液膜动力学拆分普萘洛尔外消旋体

以S,S-酒石酸正十二酯和H3BO生成的配合物为手性载体, 通过量热分析结果初步证明该配合物的存在, 采用厚体液膜拆分了普萘洛尔外消旋体. 考察了S,S-酒石酸十二酯浓度和水相pH值对拆分性能的影响, 优化了其拆分操作条件, 同时进行了动力学分析. 得出厚体液膜拆分的一般规律, 即其拆分属于动力学拆分过程, 适当提高手性载体的浓度有利于提高对映单体流量和拆分的立体选择性, 水相pH值对于拆分性能有着重要的影响. 其拆分过程中萃取反应过程为控速步骤, 对映单体的跨膜传递可以用两个串联的准一级不可逆过程进行描述.     

Electrochemical Elucidation of the Facilitated Ion Transport Across a Bilayer Lipid Membrane in the Presence of Neutral Carrier Compounds

The ion transport facilitated by neutral carrier compounds (valinomycin, nonactin) has been investigated by cyclic voltammetry in the several electrolyte solutions (KF, KCl, KBr, KNO₃, KSCN, KClO₄), and we demonstrated the effect of the counter anions on the facilitated transport of K⁺ from the viewpoint of electroneutrality. Voltammograms for the ion transport were generated at steady state and the current density between W1 and W2, j_W1–W2, increased with the absolute value of the applied membrane potential, E_W1–W2. Then, the magnitude of j_W1–W2 at a certain E_W1–W2 increased with the hydrophobicity of the counter anion. It was proved that the logarithm of |j_W1–W2|at a certain E_W1–W2 is almost proportional to the hydration energy of the counter anion. This indicates that not only K⁺ but also the counter anion distributes into the BLM. Therefore, the magnitude of j_W1–W2 at a certain E_W1–W2 increased with an increase of pH, because the hydroxide ion was served as a counter anion. Based on the variation of the zero‐current potential in case of various asymmetrical ionic compositions, it is found that the amount of cation transport is much larger than that of anion transport.     

厚体液膜拆分克伦特罗外消旋体及其动力学研究

以D-( )-二苯甲酰酒石酸(D-( )-DBTA)为流动载体,研究了克伦特罗(clenbuterol,Cle)对映体的厚体液膜法拆分,建立了手性拆分条件和动力学拆分模型。考察了D-( )-DBTA浓度、缓冲液pH值对手性拆分性能的影响,进行了动力学分析,并测定了膜-料液界面的萃取反应表观速率常数k1和膜-反萃相界面的反萃取表观速率常数k2。结果表明:在优化的实验条件下(pH为7,手性载体与Cle浓度比为1∶4),Cle外消旋体能被含有手性载体D-( )-DBTA的厚体液膜有效拆分,分离因子大于1.08;Cle单体的跨膜迁移过程可以用两个串联的准一级不可逆过程进行描述。     

含氟共聚物与钴卟啉复合膜的制备及促进氧输送性能

研究了甲基丙烯酸八氟戊酯-乙烯基咪唑共聚物与钴卟啉复合膜的制备及钴卟啉与氧络合、促进输送性能.共聚物中的咪唑基与钴卟啉的第五配位点在溶液中络合,制得的复合膜具有快速和可逆的氧结合特性.温度降低,钴卟啉与氧络合的平衡常数增加;膜中的钴卟啉与氧络合平衡常数大于N,N-二甲基甲酰胺(DMF)溶液中的平衡常数.钴卟啉与氧络合和选择性地促进氧的输送使共聚物/钴卟啉复合膜的氧渗透系数和氧/氮选择系数提高.     

Continuous Transport of Zn(II) by Ammonium Chloride Media via Supported Liquid Membrane System

With the gradual depletion of traditional zinc resources, the full use of various non-traditional zinc-containing resources has received intensive attention. However, the efficient recovery of zinc ions with low concentrations remains challenging. Here efficient and continuous recovery of zinc ions in ammoniacal chloride media by a flat supported liquid membrane system is achieved, using Cyanex923 and TBP mixed extractant as the membrane phase. This article discusses the synergistic effect between Aliquat336, Cyanex923 and TBP, the effects of feed pH, total ammonia concentration, Cl⁻ concentration and temperature on Zn(II) transport.     

Facilitated Transport of Cr(VI) through Polymer Inclusion Membrane System Containing Calix[4]arene Derivative as Carrier Agent

Chromium(VI) is one of the major toxic elements present in environmental samples. The polymer inclusion membrane (PIM), has been developed to provide metal ion transport with high selectivity. This study was conducted to discover efficient methods for removing Cr(VI) from wastewater. A functionalized calix[4]arene carrier 1 in a PIM system was used to transport Cr(VI) from an acidic aqueous donor phase solution to an acceptor phase that contained an acetic acid/ammonium acetate solution at pH 6. The prepared PIM was characterized with Fourier Transform Infrared (FT-IR) spectroscopy and the Atomic Force Microscopy (AFM) techniques as well as with contact angle measurements. The efficiency of Cr(VI) transport through the PIM was investigated by studying the effects of carrier concentration on the membrane phase as well as by measuring the amount of plasticizer in the membrane, the pH in the acceptor phase and the membrane's stability and thickness. The kinetic parameters were calculated as rate constant (k), permeability coefficient (P), flux (J) and diffusion coefficient (D_o). The transport efficiency of Cr(VI) was observed to be 98.61% after 10 h under optimized conditions. The experimental results show that Cr(VI) can transport from the donor phase to the acceptor phase with high efficiency through the PIM. The results also suggest that the transport efficiency of the PIM was reproducible and that a PIM is effective for long-term separation processes.     

Separation of Trivalent Samarium through Facilitated Stripping Dispersion Hollow Fiber Liquid Membrane Using p204 as Mobile Carrier

The separation of Sm(III) through stripping dispersion hollow fiber liquid membrane system (SDHFLM) containing feed phase adding acetate buffer solution and dispersion solution with HCl solution as the stripping solution and membrane solution of di(2‐ethylhexyl) phosphoric acid (p204) dissolved in kerosene, has been studied. A set of factors were studied, including pH value, initial concentration of Sm(III) and different ionic strength of feed phase, volume ratio of membrane solution and stripping solution (O/W), HCl concentration, carrier concentration, different stripping agents of dispersion phase on Sm(III) separation. Experimental results indicate that the optimum separation conditions of Sm(III) were obtained as that HCl concentration was 4.00 mol/L, p204 concentration was 0.150 mol/L, and volume ratio of membrane solution and stripping solution (O/W) was 1.00 in the dispersion phase, and pH value was 4.60 in the feed phase. Ionic strength had no obvious effect on separation of Sm(III). When initial Sm(III) concentration was 1.00×10^?4 mol/L, the separation rate of Sm(III) was up to 93.5% in 85 min. The kinetic equation was developed in terms of the law of mass diffusion and the theory of interface chemistry. The modeled results were in good agreement with the experiment data.     

Selective Transport of Saccharides Through a Liquid Membrane Using Cyclodextrin Dimer

A new effective transport system for saccharides through a liquid membranewas constructed. The transport rate of d-ribose in the condition of theliquid membrane with cyclodextrin dimer (2) as a transporter is 2.5 timerlarger than that without the transporter, whereas the transport rate of d-ribosein the condition of the liquid membrane with cyclodextrin monomer (1) isalmost the same as that without the transporter. The transport rate of methyld-glucoside by 2 is over twice than that by 1. The transport rate of d-deoxyribose by 2 is larger than that by 1.     

苯酚在N-503/煤油支撑液膜体系中的传输分离

研究了以多孔聚丙烯膜为支撑体,N,N′-二(1-甲基庚基)乙酰胺(N-503)为膜流动载体的苯酚支撑液膜传输行为;用液-液萃取法测定了N-503/煤油体系中苯酚萃合物组成为1∶1,及在相应的条件下萃取常数Ke′x为53.7;考察了料液相的pH值、载体浓度、实验温度、起始浓度以及解析相NaOH的浓度对苯酚传输的影响,并对该体系分离、传输苯酚的最佳条件进行了讨论;从界面化学和扩散传质角度提出了苯酚的传输动力学方程,采用直线斜率法对苯酚在N-503/煤油支撑液膜体系中的扩散层厚度和膜内扩散系数进行了测定,取得满意结果。     

用甲基丙烯酸十二酯/丙烯酸共聚物作乳状液膜稳定剂迁移锌(Ⅱ)

用甲基丙烯酸十二酯/丙烯酸共聚物作乳状液膜稳定剂迁移锌(Ⅱ);两亲高分子;乳状液膜;迁移;锌离子     

青霉素G酶促裂解液的高效液相色谱分析

建立了用反相高效液相色谱测定青霉素Ｇ酶促裂解产物的方法。以与分离程度和分析时间有关的ＣＲＦ为目标函数，用改进的单纯形法对流动相进行优化选择。结果表明本法快速、准确、简便。     

杯[4]芳烃衍生物对Pb2＋的液膜传输动力学

以3类含不同基团的杯[4]芳烃衍生物作为离子载体在H2O-CHCl3-H2O液膜传输体系下分别对Pb2＋进行液膜传输实验. 简要讨论了以杯[4]芳烃衍生物作为离子载体对Pb2＋液膜传输的动力学机理. 重点研究了不同载体种类, 载体浓度, 搅拌速度, 传输时间等因素对Pb2＋传输的影响. 实验结果表明: 以含Br原子的杯[4]芳烃衍生物和含S原子的杯[4]芳烃衍生物作为离子载体对Pb2＋有明显的传输效果. 可以用本文的动力学模型来描述整个传输体系的动力学特性.     

杯芳烃衍生物液－液萃取和液膜传输银的对比研究及机理探讨

以4类含硫、硒、氮等杂原子基团二取代的杯[4]芳烃五衍生物（1－14）为中 性载体，在H2O-CHCl3-苦味酸体系萃取银和H2O-CHCl3-H2O液膜体系中传输银进行 了对比研究。萃取和传输结果具有一致性，除了苯并噻唑取代的杯[4]芳烃衍生物 （3－6）外，其它10个含硫、硒、氮的杯[4]芳烃衍生物1－14均对软重金属银和汞 有很高的选择性，而吡啶取代的杯[4]芳烃衍生物7－10对铅有一定的萃取选择性， 其中羟基硫醚取代的杯[4]芳烃衍生物11－14对银的萃取率和传输速率最大。并且 就杯[4]芳烃衍生物对银的传输机理进行了探讨，发现传输速率随源相中金属离子 浓度和有机相中载体浓度的增加而增大，因此推论这是由金属离子浓度梯度推动下 的传输。     

N263和TBP为协同流动载体的液膜体系分离钐(Ⅲ)和钆(Ⅲ)的研究

研究了N263和TBP为协同载体的液膜体系分离钐和钆的行为.考察了膜相添加剂、内水相反萃剂、外水相盐析剂和膜相中载体浓度对传质分离的影响.当用TBP作为膜相添加剂时,N263能很好地溶解在煤油中.N263-TBP-LMA-1-煤油和NH₄NO₃协同流动载体液膜体系在迁移稀土离子时表现出"倒序"特性,与单纯的N263体系相比,该体系对钐、钆具有较高的选择性.     

Transport of Ca^2＋ Ion through a Bubbling Pseudo—emulsion Liquid Membrane with Calixarenes and Calixcrowns as Carriers

ＩｎｔｒｏｄｕｃｔｉｏｎＣａｌｉｘａｒｅｎｅｓｃｏｎｓｔｉｔｕｔｅａｖｅｒｓａｔｉｌｅｃｌａｓｓｏｆｍａｃｒｏｃｙｃｌｉｃｃｏｍｐｏｕｎｄｓｔｈａｔｃａｎｂｅｅａｓｉｌｙｆｕｎｃｔｉｏｎａｌｉｚｅｄ ,ｔｈｕｓａｆｆｏｒｄ ｉｎｇａｌａｒｇｅｖａｒｉｅｔｙｏｆｎｅｗｍｕｌｔｉｆｕｎｃｔｉｏｎａｌｒｅｃｅｐｔｏｒｓ .1Ｉｎｔｈｅｐａｓｔｔｗｏｄｅｃａｄｅｓ ,ｔｈｅｙｈａｖｅｐｌａｙｅｄａｎｉｍｐｏｒｔａｎｔｒｏｌｅｉｎｓｕｐｒａｍｏｌｅｃｕｌａｒｃｈｅｍｉｓｔｒｙａｓｕｓｅｆｕｌｂｕｉｌｄｉｎｇｂｌｏ…     

以正十六胺为载体的乳状液膜迁移分离镉(Ⅱ)

以正十六胺为载体的乳状液膜迁移分离镉(Ⅱ)     

乳状液膜迁移分离铋(Ⅲ)

用三异辛胺（ＴＩＯＡ）０Ｓｐａｎ ＳＯ－甲苯乳太液膜迁移Ｂｉ（Ⅲ）的研究表明,在合适的制乳和迁移条件下,Ｂｉ（Ⅲ）可以快速完全地迁入内相,并能与Ｆｅ＾３＋、Ｃｏ＾２＋、Ｎｉ＾３＋、ＡＩ＾３＋、Ｃｒ＾３＋、Ｍｍ＾３＋、Ｃｕ２＋、Ｐｂ＾＋、Ｃｄ＾２＋、Ｃ完全分离。     

反胶团相转移法提取青霉素G的研究

报道了非蛋白质类活性物质青霉素Ｇ在反胶团相转移提取中的特性和机理。结果表明，青霉素Ｇ在ＣＴＡＢ／正辛醇：氯仿（４：１，Ｖ／Ｖ）反胶团体系中的相转移提取为离子对静电作用与胶团溶解机理；在室温及ｐＨ值５～８的条件下，提取率在９０％以上，且保持了青霉素的稳定性。