Extraction of Co(II) from aqueous solution using emulsion liquid membrane

The extraction equilibrium of Co(II) from thiocyanate medium by CYANEX 923 (mixture of straight chain alkylated phosphine oxides) in cyclohexane was studied. The stoichiometry of the extraction reaction was postulated based on slope analysis method and the extraction constant Kex was calculated. The stripping percentage of Co(II) with sulphuric acid from the loaded CYANEX 923 was found to increase with the increase in acid concentration. The extraction of Co(II) from aqueous thiocyanate medium into emulsion liquid membrane using CYANEX 923 extractant was also studied. The influence of different parameters such as stirring speed, surfactant concentration, pH of the extractant phase, carrier concentration, internal phase stripping acid concentration, initial Co(II) concentration as well as temperature on the emulsion stability were investigated. The applicability of the emulsion liquid membrane (ELM) process using CYANEX 923 as extractant and SPAN 80 as surfactant for the removal and the concentration of Co(II) from thiocyanate solution was investigated. The results show that it is possible to recover 95% of cobalt in the inner phase after 10 min of contacting time with a concentration factor of 5.     

乳状液膜法提取青霉素G的研究

使用青霉素Ｇ钠盐纯品溶液,模拟考察了乳状液膜法分离青霉素的条件．着重研究了提取率与膜中载体类型、Ｓｐａｎ－８０用量的关系,优化出最佳提取条件,在最佳条件下青霉素的提取率可达９２％,浓缩比可达９．     

乳化液膜法脱除乙二醇中H_2S的研究

采用乳化液膜法对含H2S的乙二醇溶液进行脱硫研究.膜相由膜溶剂煤油、表面活性剂、流动载体乙二胺、膜稳定剂液体石蜡组成;内相试剂为NaOH.考察了传质时间、表面活性剂的种类及浓度、流动载体浓度、内相NaOH浓度、膜溶剂与内相试剂之比、乳化液与外相溶液之比、乙二醇溶液的初始硫含量以及传质搅拌速率对H2S脱除率的影响.试验结果表明,乳化液膜法用于含硫乙二醇溶液的脱硫是可行的,H2S脱除率可达到98%以上.     

乳状液膜法从发酵液中提取青霉素的研究

研究了用乳状液膜法从发酵液中提取青霉素Ｇ时,石蜡用量、搅拌速率、载体用量、内相碳酸钠溶液浓度和表面活性剂用量对青霉素提取的影响,在最佳条件下提取率可达７６．５％,浓缩比为６．０。     

支撑液膜法提取柠檬酸——膜配方的研究

采用了支撑液膜法从柠檬酸的发酵液中提取柠檬酸,考察了膜的装配方法和载体浓度对传递通量及体系稳定性的影响,在该体系和一定的操作条件下,确定了合适的支撑液膜体系为聚丙烯微孔膜为支撑体,煤油为溶剂,TOA为载体,用湿法装配.     

液膜法处理高氟废水研究

利用Ｎ２０５－Ｎ１９２３－煤油液膜体系，ＣａＣｌ２溶液作内相，对高氟废水的处理进行了研究。利用正交实验确定了影响最大的因素，并研究了各种因素对处理的影响。经３０ｍｉｎ处理，外相Ｆ＾－浓度可由０．５００ｇ／Ｌ降至０．０１０ｇ／Ｌ以下，可达到工业排放标准。     

乳状液膜法提取模拟湿法磷酸中的稀土镧

采用自制的磺化聚丁二烯(LYF)作表面活性剂,以二(2-乙基己基磷酸,P204)为萃取剂,以4mol/L HCl为内相,液体石蜡为膜稳定剂,制成乳状液膜,从模拟湿法磷酸中萃取稀土镧.在膜内比为1.2∶1,制乳搅拌,搅拌速度为2 000r/min,时间为20min,提取搅拌速度为250r/min,时间为10min,水乳体积比为2∶1,磷酸质量分数为10%P2O5,La3+含量为300mg/L时,镧离子的迁移率达到86.67%.同时利用液液萃取通过斜率分析法讨论P204从磷酸中提取镧离子的反应机理.对P204萃取镧离子进行热力学研究,结果表明,萃取反应属于放热反应,反应热为-7.697 1kJ/mol.     

The role of some compounds on extraction of chromium(VI) by amine extractants

The extraction of hexavalent chromium, Cr(VI), from hydrochloric acid aqueous solution using Aliquat 336 and Alamine 336 extractants was performed under different experimental conditions. The data clarify that one molecule of amine extractants shares with approximately one molecule of HCl to extract two molecules of Cr(VI) from 1M HCl aqueous solutions. The extraction is an exothermic process and possesses enthalpy change values of -41.02 and -28.08 kJ mol(-1) for the extraction by Aliquat 336 and Alamine 336, respectively. The presence of potassium chloride greatly increases the extraction of Cr(VI) by amine extractants while the addition of some phenolic compounds such as phenol, dichlorophenol, o-nitrophenol and beta-naphthol decreases this extraction under the same experimental conditions.     

Separation and subsequent determination of low radioactivity levels of radium by extraction scintillation

A method is developed for separation and subsequent determination of low (226)Ra levels based on its extraction efficiency by various organic extractants followed by direct interaction with mixed scintillation cocktail (SC) in toluene as the most suitable solvent. Three organic extractants including Tricaprylmethyleammonium chloride (Aliquat-336), triphenylphosphine sulphide (TPPS) and tri-n-octylphosphine oxide (TOPO) are individually embedded in 1-phenyl,4-phenyloxazole (PPO) as a primary scintillator and 1,4-di-2-(4-methyl, 5-phenyl oxazoyl) benzene (POPOP) as a second scintillator. Different parameters affecting the extraction process including shaking time, type and concentration of extractant, aqueous/organic volume ratio as well as various levels of (226)Ra are individually investigated. Based on the optimized condition, it was found that the extraction of (226)Ra by Aliquat-336 is highly selective with efficient separation capability from (133)Ba, which is necessary to determine the yield and recovery of (226)Ra in related measurements. The combination of extraction with direct scintillation processes is mainly elaborated to overcome the heterogeneity problem and hence the slow scintillation rate that often exists in conventional liquid scintillation counting especially with low radioactivity levels.     

Extraction kinetics of heavy metal-containing sludge

In order to remove and recover copper, zinc, cadmium, and chromium from the wastewater treatment sludge generated by an electroplating process, the heavy metal extraction kinetics was studied in a batch reactor using two different extraction agents (nitric and citric acid) at constant agitation speed (150 rpm) and solid to liquid ratio (10 g/L), but varying acid concentrations (0.02-0.10 N), temperatures (25-85 degrees C in nitric acid solution, 25-95 degrees C in citric acid solution), and sludge particle sizes. The shrinking-core model and empirical kinetic model were adopted to analyze the experimental data. Although both models could fit the experimental kinetic data well, the obtained parameters of the shrinking-core model did not show reasonable trends varying with the experimental variables while the empirical model parameters showed significant trends. The experimental and modeling results showed that the metal extraction rates increased with acid concentration, temperature, but decreased with increasing particle size. Nitric acid was found to be more effective than citric acid to extract the heavy metals from the sludge. The extraction activation energies obtained in this study suggested that both a physical diffusion process and a chemical reaction process might play important roles in the overall extraction process.     

乳状液膜法提取亮氨酸

研究了亮氨酸的乳状液膜提取方法．考察了外相溶液组成、内相 Ｈ＋ 浓度、外相ｐ Ｈ 值及载体用量对提取率的影响，从而确立了各影响因素的最佳值     

Membrane optode for mercury(II) determination in aqueous samples

A color changeable optode for Hg(II) was prepared by the immobilization of a dye 4-(2-pyridylazo)resorcinol (PAR) and a liquid ion-exchanger trioctylmethylammonium chloride (Aliquat-336) in the tri-(2-ethylhexyl) phosphate plasticized cellulose triacetate matrix. Hg(II) and CH₃Hg⁺ from aqueous samples could be quantitatively preconcentrated in this transparent optode producing a distinct color change (λ_max = 520 nm) within 5 min equilibration time in bicarbonate aqueous medium or 30 min in natural water. Whereas optode sample without Aliquat-336 did not change its color corresponding to Hg–PAR complex on equilibrium with the same aqueous solution containing Hg(II) ions. The uptake of Hg(II) was found to be pH dependant with a maximum (>90%) at a pH 7.5. The uptake of ions like Cu(II), Fe(II), Zn(II) and Pb(II) was negligible in the optode where as the uptake of Cd(II) and Zn(II) ions was 10–15% at pH 7.5. The optode developed in the present work was studied for its analytical application for Hg(II) in the aqueous samples by spectrophotometry, radiotracer (²⁰³Hg), Energy Dispersive X-ray Fluorescence (EDXRF) analyses and Instrumental Neutron Activation Analysis (INAA). The minimum amount of Hg(II) required to produce detectable response by spectrophotometry, INAA and EDXRF were found to be 5.5, 1 and 12 μg, respectively. This optode showed a linear increase in the absorbance at λ_max = 520 nm over a concentration range of 0.22–1.32 μg/mL of Hg(II) ions in aqueous solution for 5 min. The preconcentration of Hg(II) from large volume of aqueous solution was used to extend the lower limit of concentration range that can be quantified by the spectrophotometry of optode. It was observed that preconcentration of 11 μg Hg(II) in 100 mL (0.11 μg/mL) in aqueous samples gives a distinct color change and absorbance above 3σ of the blank absorbance. The optode developed in the present work was found to be reusable.     

Removal of chromium (VI) ions from aqueous solution by adsorption onto two marine isolates of Yarrowia lipolytica

The removal of chromium (VI) ions from aqueous solutions by the biomass of two marine strains of Yarrowia lipolytica (NCIM 3589 and 3590) was studied with respect to pH, temperature, biomass, sea salt concentration, agitation speed, contact time and initial concentration of chromium (VI) ions. Maximum biosorption was observed at pH 1.0 and at a temperature of 35 °C. Increase in biomass and sea salts resulted in a decreased metal uptake. With an agitation speed of 130 rpm, equilibrium was attained within 2 h. Under optimum conditions, biosorption was enhanced with increasing concentrations of Cr (VI) ions. NCIM 3589 and 3590 displayed a specific uptake of Cr (VI) ions of 63.73 ± 1.3 mg g⁻¹ at a concentration of 950 ppm and 46.09 ± 0.23 mg g⁻¹ at 955 ppm, respectively. Scatchard plot analysis revealed a straight line allowing the data to be fitted in the Langmuir model. The adsorption data obtained also fitted well to the Freundlich isotherm. The surface sequestration of Cr (VI) by Y. lipolytica was investigated with a scanning electron microscope equipped with an energy dispersive spectrometer (SEM-EDS) as well as with ED-X-ray fluorescence (ED-XRF). Fourier transform infrared (FTIR) spectroscopy revealed the involvement of carboxyl, hydroxyl and amide groups on the cell surfaces in chromium binding.     

Removal of dyes and their mixtures from aqueous solution using liquid emulsion membrane

Extraction of dyes from aqueous solution was studied using liquid emulsion membrane. Study was carried out using two dyes, namely, crystal violet (CV) and methylene blue (MB). Extraction of single component system of each dye and their binary mixture were investigated. Liquid emulsion membrane was formed using n-heptane as membrane phase, sodium hydroxide solution as the internal phase and dye solution as the external phase. Surfactant span 80 was used as the emulsion stabilizer. Effects of concentration of span 80, concentration of NaOH, stirring speed, composition of feed solution and the volume ratio of the oil phase to the aqueous phase (O/A) were studied in detail both for single and binary system. Maximum extraction of MB was found to be 99% and that for CV was about 95% in single component system. In binary mixture, these values were 97% and 90%, respectively.     

液膜接触法处理含铜废水的实验研究

探讨以P204为流动载体的液体表面活性剂膜从酸性水溶液中分离二价铜离子的过程，并对影响二价铜离子透过液膜的重要变量进行分析，这些变量主要是外部水相中的起始铜浓度、外相溶液中的起始pH值、液膜流动载体浓度、乳水比、内相峻浓度等．实验结果表明：较佳膜相组成的液膜能把废水溶液中铜离子浓度从100mg/L降到0．9mg/L;铜萃取率大于99％．     

Facilitated transport of uranium(VI) across supported liquid membranes containing T2EHDGA as the carrier extractant

Facilitated transport of uranyl ion from nitric acid feed solutions was investigated across PTFE supported liquid membranes using N,N,N',N'-tetra-2-ethylhexyl-3-pentane-diamide (T2EHDGA) in n-dodecane as the carrier extractant containing 30% iso-decanol as the phase modifier. Solvent extraction studies indicated extraction of species of the type, UO(2)(NO(3))(2)·T2EHDGA. The distribution coefficients increased in the presence of NaNO(3) as compared to equivalent concentration of HNO(3) which was exactly the opposite of what was reported for Am(III)-TODGA extraction system. Supported liquid membrane studies indicated about 11h were required for quantitative transport of U(VI) from a feed of 3M HNO(3) using 0.2M T2EHDGA in n-dodecane containing 30% iso-decanol as the carrier extractant. Effect of various parameters such as feed acidity, T2EHDGA concentration, and nature of the strippant on the transport rate was investigated. The transport was found to be diffusion controlled in the membrane phase and the permeability coefficient was calculated to be (3.20 ± 0.13)× 10(-4)cm/s for the feed composition of 3M HNO(3), receiver phase composition of 0.01 M HNO(3) and membrane carrier phase of 0.2M T2EHDGA in n-dodecane containing 30% iso-decanol. The present results may be useful for the separation of U from lean solutions or radioactive wastes considered hazardous due to the presence of alpha-particle emitting radionuclides.     

Permeation liquid membrane metal transport: studies of complex stoichiometries and reactions in Cu(II) extraction with the mixture 22DD-laurate in toluene/phenylhexane

The role of lauric acid (LAH) in the transport of copper(II) through a permeation liquid membrane (PLM) comprising 1,10-didecyldiaza-18-crown-6 (22DD) and lauric acid (ratio 1:1) in 1:1 v/v toluene/phenylhexane has been investigated by determining the stoichiometry of metal extraction and of the metal complex formed in the organic phase by performing 1H NMR and liquid/liquid and liquid/membrane extraction measurements. In the absence of copper(II), the 1H NMR data suggest that there is a strong interaction between the proton of LAH and the nitrogen of the 22DD macrocycle but no interaction between the aliphatic long chains of LAH and 22DD. Thus, in the organic solution, the two compounds are associated as (22DD-H)(+)-LA-, the laurate being away from (22DD-H)+. The signal intensity of the acidic proton was found to decrease when the metal Pb(II) was incorporated by the carrier after its extraction from the aqueous phase. Additionally, liquid/liquid as well as liquid/membrane extraction results reveal that Cu(II) extraction proceeds via the loss of two protons from the organic phase. The Cu(II) is found to be located in the 22DD cavity and the stoichiometry of the complex in the organic phase is (22DD-Cu)(2+)-2LA-. Metal extraction is governed by 22DD and laurate acts only as counteranion. An unexpected feature was observed in the liquid/liquid extraction which was that, at low 22DD and LAH concentrations, the slope for log(Kp) = f(pH) was 2 whereas it was much lower at high carrier concentration. This unexpected result seems to stem from impurities present in 22DD: only 0.1 mol% of impurity can indeed influence the exchange ratio of Cu(II) and H+. This type of anomaly, however, is not found in the normal procedure of liquid/membrane extraction possibly due to the lower carrier/metal molar ratio which is used in the classical PLM conditions.     

乳状液膜法提取赖氨酸

研究了用乳状液膜法提取赖氨酸的液膜配方及一些重要操作参数 ,初步得出了既能相对减少溶胀 ,又能保持较高分离效率的膜组成及最佳工艺条件 .赖氨酸提取的液膜组成为 :载体二 - (2 -乙基己基 )磷酸脂 7% (质量分数 ) ,表面活性剂 (Span - 80 ) 5 % (质量分数 ) ,膜溶剂 5 0 % (体积分数 )液体石蜡和 5 0 %煤油 .内相选用 0 .5mol/L的HCl溶液 ,处理比为 3.75 ,提取率可达 72 .6 %     

油内比和表面活性剂浓度对（稀型）乳状液膜工业过程的影响

在当前破乳技术的基础上,用稀型乳状液膜法治理粘胶纤维工业酸性含锌废水、选择稀型乳状液的油内比Ｒｏｉ大于３,表面活性剂Ｔ１５４的体积分数降至０．６％的条件,在工业上实现了含锌废水的处理,这过程既无二次污染,又 收锌资源,具有一定的经济效益。     

Extraction of lanthanide(III) nitrates with composite solid extractants based on a polymeric support impregnated with trialkylmethylammonium nitrate or TBP

Extraction of lanthanides(III) and Y(III) from 1–5 M aqueous NaNO₃ with composite solid extractants based on a polymeric support impregnated with trialkylmethylammonium nitrate (Aliquat-336) or TBP was studied, and the extraction constants were determined. The extraction isotherms were analyzed assuming that lanthanides are extracted with the solid extractants in the form of complexes (R₄N)₂[Ln(NO₃)₅] and Ln(NO₃)₃(TBP)₃.