皂化P204/煤油微乳体系分离L-苯丙氨酸的研究

研究了P204-煤油-NaOH组成的微乳液膜配方及其稳定性。通过该液膜体系对L-苯丙氨酸水溶液进行提取实验,考察了P204的浓度、乳水比、外水相pH值、膜相重复使用次数、分离时间等对提取效率的影响。实验结果表明,微乳液膜不仅稳定性好,无明显溶胀和泄漏,分离速度快,而且分离效果好,可自动破乳,油相可重复多次使用,对L-苯丙氨酸的一次性提取率达88.25%。     

液膜预富集水相痕量镍的分析研究

研究了液膜体系对水相中痕量镍离子的富集方法,镍离子从外相水溶液被膜相载体通过液膜运进含有反萃取剂的内相,从而达到富集效果,液膜富集一次回收率达98％,二闪富集倍数250倍,试验了载体,表面活性剂,液体石蜡,膜与内相水的水／油比,乳化液与外相水的乳／水比,内相酸度,外相PH值,富集时间的破乳剂用量等因素的影响,利用正交分析试验选出了最佳试验条件,并比较在相同条件下液膜法与萃取法提取镍的效果,通过液膜富集,使原子吸收法测定痕量镍达到了10^-9级。     

亲水性混合纤维素酯微孔膜对O/W乳液的破乳

亲水性混合纤维素酯微孔膜对O/W乳液的破乳;破乳机理;膜污染和清洗;混合纤维素酯膜     

谷氨酸在Span80-AOT-APS体系中的迁移行为

报道了谷氨酸在乳状液膜体系中的迁移行为,采用失水山梨醇单油酸酯(span80)-乙基己基琥珀酸酯磺酸钠(AOT)为表面活性剂,对氨基苯磺酸(APS)为载体,煤油为膜溶剂,氯化钾为内相试剂.讨论了制乳时间和乳液与外相混合时间、表面活性剂和流动载体浓度、内相试剂浓度、水乳比和油内比对分离效果的影响.确定了最佳分离条件为制乳...     

适用于稀土离子提取的微乳液的制备及其提取条件初探

研究了由表面活性剂、油性溶剂及盐酸水溶液制备的油包水 (W/O)型微乳液对稀土离子RE3 +从料液相 (水相 )提取到微乳相中的行为 ,初步考察了表面活性剂浓度、水乳比、温度及载体浓度对提取率的影响 ,从而确定了适于稀土离子提取的微乳体系及提取条件。     

镍在乳状液膜体系中的迁移行为

研究了镍在乳状液膜分离体系中的迁移行为。在此分离体系中,以煤油作为膜溶剂,span80为表面活性剂,磷酸三丁酯(TBP)为载体。详细讨论了制乳时间和混合时间、span80和TBP浓度、乳水比和油内比、内相NH。和外相HCl的浓度对镍迁移率的影响,确立了最佳分离条件。     

Pickering乳液模板法制备Janus粒子

本文以SiO₂粒子稳定的水包油(O/W)型Pickering乳液作为模板, 在乳液连续相进行SI-ATRP, 将聚合物刷接枝到SiO₂粒子外半表面, 破乳得到半修饰的Janus粒子.     

基于壳聚糖/透明质酸钠胶体的温敏性Pickering乳液及其在生物催化中的应用

本文以负载脂肪酶的自组装胶体粒子为乳化剂,以十六烷为油相制备Pickering乳液,通过温度调控乳液的稳定性,提高脂肪酶的循环使用性能。首先,在荷正电的壳聚糖(CS)溶液中依次加入脂肪酶(CRL)和荷负电的天然大分子透明质酸钠(HA),利用壳聚糖与透明质酸钠之间的静电作用自组装形成脂肪酶@壳聚糖/透明质酸钠胶体(CRL@CS/HA CPs),将脂肪酶负载于胶体粒子内,提高CRL@CS/HA CPs的稳定性;以相变材料十六烷为油相,在高速均质作用下将CRL@CS/HA CPs组装到十六烷-水界面,构建温敏性Pickering乳液,应用于脂肪酶的界面催化;通过改变温度,诱导油相发生凝固-溶解实现破乳,回收CRL@CS/HA CPs,提高脂肪酶的循环使用性能。     

基于酸碱相互作用制备染料杂化的聚磷腈微粒及其乳化性能

利用罗丹明B(RhB)通过酸碱相互作用对聚(环三膦腈-co-4,4′-二羟基二苯砜)(PZS)微粒进行表面改性,得到一种染料杂化的聚磷腈胶体粒子(PZS@RhB),对其结构、形貌、亲-疏水性及pH响应性进行了表征;进一步以PZS@RhB微粒为颗粒乳化剂,研究了其乳化性能,并探讨了乳液的破乳条件及机理.结果表明:PZS微粒表面吸附RhB后,疏水性增加,且RhB结构中的羧基赋予了微粒pH响应性;当水相中PZS@RhB微粒的质量浓度达到14 mg/mL时,可乳化甲苯形成较为细腻的W/O型乳液;乳液呈现出显著的pH响应性,当增加水相pH至强碱性(pH≥10.11)时,乳液可发生相反转,由W/O型转变为O/W型;此外,通过向乳液中加入三乙胺,可有效破环PZS微粒与RhB之间的酸碱相互作用,从而方便实现乳液的破乳.     

核壳乳液在电解质作用下的破乳过程

核壳乳液在电解质作用下的破乳过程;分光光度计;核壳乳液;电解质;乳液破乳     

Concentration of amino acids by a liquid emulsion membrane with a cationic extractant

The concentration of -phenylalanine in a liquid emulsion membrane system was studied using a cation complexing agent, di-2-ethylhexyl phosphoric acid (D2EHPA), as a carrier. The membrane formulation, the pH in the internal phase of the acid concentration in the external phase were optimized with respect to concentration performance and membrane stability. It was found that a liquid emulsion membrane obtained by demulsification of the emulsion by an electrostatic coalescer could be reused. Based on the laboratory tests, a continuous multistage process for the concentration of amino acids was proposed (with the development of a commercial process in mind) and its technical feasibility was discussed.     

Emulsion stability and potassium leakage in emulsion liquid membrane systems

Potassium leakage was studied in liquid membrane systems containing various emulsifiers and compared with emulsion, stability in the storage test. The effects of various parameters upon emulsion stability and the leakage of standard traces are discussed. The transfer of cations can be caused by emulsion breaking, by transport with the specific carrier and/or with surfactants used as emulsifiers. The latter case becomes especially important when hydrophilic surfactants, e.g. ones containing polyoxyethylene chains, are present in liquid membranes. In systems containing hydrophobic emulsifiers the transfer of potassium is relatively low. In each case considered the effect of emulsifiers upon the transfer of the standard tracer should be checked prior to using the leakage test to characterize emulsion stability.     

乳状液膜法分离水中的铬

乳状液膜法由于其独特的物理化学性质,已广泛用于金属离子的萃取分离[1～3]。本文以span80-煤油-NaOH液膜体系分离水中铬。不加流动载体,利用内、外相中被分离物的浓度梯度实现物质迁移。当Cr2O2-7进入内相时,与内相的NaOH发生反应,在内相高浓度的NaOH存在下,可保持Cr2O2-7在液膜两侧有最大的浓度梯度,促使Cr2O2-7的迁移,实现Cr2O2-7与外相溶液的分离。1　实验部分1 1　仪器与试剂D40-1型电动搅拌器(杭州仪表电机厂),78-1型磁力加热搅拌器(江苏金坛新一佳仪器厂),721型分光光度计(上海第三分析仪器厂)。铬标准溶液(100ml/L):准…     

铜在乳状液膜体系中的迁移行为

近年来膜分离技术在环境治理方面得到广泛应用。本文研究了铜在span80-TBP（磷酸三丁酯）-煤油-NH3液膜分离体系中的迁移行为。用TBP作为载体,在溶液中迁移时,在外相与膜相界面上形成中性络合物后穿过膜相,在膜相与内相界面上络合物再与NH3反应,生成铜氨络离子,释放出来的TBP又返回膜相。     

Extraction and enrichment of cadmium and manganese from aqueous solution using a liquid membrane

A liquid membrane containing 4% di-2-ethylhexyl phosphoric acid and 5% sorbitan monooleate in kerosene is used in the form of an emulsion for the simultaneous extraction and concentration of cadmium and manganese from aqueous solutions. When 4% tri-n-octylamine is included in the membrane composition, only manganese is extracted while cadmium remains in the sample solution. The extracted elements in the concentrate are recovered by breaking the emulsion with n-butanol. Recoveries of cadmium and manganese range from 92-104% for 60-ml samples containing 2-9 mug of each element.     

Multi-stage premix membrane emulsification for preparation of agarose microbeads with uniform size

Uniform-sized agarose beads with diameters less than 10 μm and agarose content as high as 14 wt% were prepared by premix membrane emulsification. Agarose aqueous solution was used as the water phase. A mixture of liquid paraffin and petroleum ether containing hexaglycerin penta ester (PO-500) was used as the oil phase. The water phase was mixed with the oil phase at 60 °C and a coarse W/O emulsion was produced in a homogenizer. Then, the coarse emulsion was extruded through a hydrophobic membrane under high pressure to form an emulsion, which was slowly cooled under gentle agitation to form gel beads. The effects of preparation conditions on emulsification results were investigated and it showed that the pressure, number of passes, petroleum ether/liquid paraffin (v/v) in the oil phase, the concentration of PO-500 and concentration of agarose in the water phase, all affected the size and uniformity; coarse emulsion did not affect the emulsification results. The coefficient variation (C.V.) of agarose beads under optimal preparation conditions was 9.8%. This method realized microbeads with both uniform sizes and high agarose contents that are difficult to be prepared by conventional emulsion methods.     

Liquid membrane extraction of Cephalosporin-C from fermentation broth

The extraction of Cephalosporin-C (CPC) from dilute fermentation broth of Cephalosporium acremonium was studied in a bulk liquid membrane as well as in an emulsion liquid membrane system. Aliquat-336 was used as the extracting agent to provide facilitated transport of CPC via liquid–liquid ion exchange mechanism. By maintaining an appropriate pH gradient in the feed and receiving phases, facilitated uphill transport could be achieved in the bulk liquid membrane system. The culture broth contains CPC and deacetyl CPC (DCPC) which are structurally almost similar, but CPC is more hydrophobic in nature. Selective separation of CPC could be achieved in a suitably formulated liquid membrane system. A simple mass transfer model predicts the permeation rate in the bulk liquid membrane. The permeation process in an emulsion liquid membrane appears to be controlled by the aqueous boundary layer resistance and diffusion in the emulsion globule. This is perhaps the first demonstration of the liquid membrane as an effective technique for selective extraction of CPC from fermentation broth of Cephalosporium acremonium.     

Removal of Mercury by Emulsion Liquid Membranes: Studies on Emulsion Stability and Scale Up

Emulsion liquid membranes (ELM) have received significant attention in the separation of various metal ions from industrial wastewater. Still efforts are needed to get the desired level of stability to overcome the hindrance in the application of ELM at industrial scale. In this paper, the effects of various parameters such as emulsification speed, concentration of cosurfactant, surfactant, carrier and impeller speed during extraction on the stability of an emulsion liquid membrane are studied. Dispersion destabilization of w/o emulsion is checked by Turbiscan. Drop size distribution and photomicrographs of the emulsions are also analyzed to evaluate stability of the emulsion. Instability of emulsion liquid membrane during extraction process is measured in terms of membrane breakage. A stable emulsion is used for the extraction of mercury from aqueous solution in small scale as well as in large scale.     

Emulsion liquid membrane extraction of zinc by a hollow-fiber contactor

Emulsion liquid membranes (ELMs) can contribute to process intensification of zinc extraction, by significantly reducing the solvent and carrier requirements in comparison with conventional solvent extraction. Di(2-ethylhexyl)phosphoric acid (D2EHPA) was used as a highly selective carrier for the transport of zinc ions through the emulsified liquid membrane. The hollow-fiber extractor appears to offer significant advantages over conventional liquid–liquid contactors for this separation because emulsion leakage and swell are practically eliminated even when treating high concentration feeds. Various hydrodynamic and chemical parameters, such as variation in feed pH; zinc concentration in feed; variation in concentrations of D2EHPA; variation in feed/emulsion volume ratios and variation in feed and emulsion flow rates, were investigated. The content of sulfuric acid as an internal did not show in the studied range any significant influence on zinc extraction through the ELM, although a minimum hydrogen ion concentration is suggested in the internal aqueous solution to ensure acidity gradient between both aqueous phases to promote the permeation of zinc ions toward the internal phase. The experimental mass-transfer coefficients have shown a stronger dependence on hydrodynamic conditions in both the external feed phase and emulsion among the parameters studied. For emulsion flow rate, mass-transfer coefficient increased from 16.3 × 10⁻⁶ m/s at 200 ml/min to 31.2 × 10⁻⁶ m/s at 640 ml/min. Significant increasing in mass-transfer coefficient observed with increasing aqueous flow rate from 9.7 × 10⁻⁶ m/s at 170 ml/min to 37.2 × 10⁻⁶ m/s at 740 ml/min. The overall mass-transfer coefficient increases from 12 × 10⁻⁶ m/s at 2% D2EHPA to 28 × 10⁻⁶ m/s at 8% D2EHPA. This means that this process is chemically controlled and the interfacial resistance has a more significant role in the extraction of zinc by emulsion liquid membrane through hollow-fiber contactor. From the results obtained, it seems that the diffusion processes in aqueous feed phase and the membrane phase have the same importance as the chemical process.