Supported liquid membrane extraction to treat coal gasification wastewater containing high concentrations phenol

The hollow fiber supported liquid membrane extraction was introduced to treat coal gasification wastewater to recover phenolic compounds,with tributyl phosphate (TBP) as carrier,kerosene as the membrane solvent,sodium hydroxide solution as the stripping agent and PVDF as the membrane material. Factors having strong impact on the extraction efficiency were studied in detail,including the mass transfer mode,twophase flow rate,stripping phase concentration. As extraction system with 20% TBP-kerosene,parallel flow mass transfer,stripping phase concentration 0.1 mol/L,the optimal operating conditions could be obtained. Under the optimum operating conditions,the time required to reach equilibrium for the extraction is 50 min, and extraction efficiency of phenol is 86. 2% and the phenol concentration of effluent is 98.64 mg/L.

Supported Liquid Membrane Extraction Technology and Its Application in Detection of Meat Security

As a novel technology,supported liquid membrane extraction has gradually become the direction of the research of extraction,for the advantages of using little organic solvents,good selectivity and repeatability.This paper is based on describing the working principle,structure and infiuencing factors of supported liquid membrane,and research in domestic and foreign literatures which are in the same period, and give a review on the application of supported liquid membrane in meat security determination.

Transport Behaviour of La^（3＋） with Flat－Sheet－Sandwich Supported Liquid Membrane Extraction System

This paper suggested a modified model of SLM which could improve its stability.In the model, an organic solution was sandwiched between two layers of supported film,which we called sandwich supported liquid membrane(SSLM).The transport experiments of La3+ were performed with SSLM containing HEH(EHP)as a carrier. The permeability coefficient (p) of La3+ were measured and some factors affecting the p were investigated. The results showed that if the pH of the feed was below 4.0,the p was increased with increasing in pH. The p was also increased when the strip acidity increases.Inspite of not enough satisfactory reproducibility on test result, the stability of the model was improved.

Transport Behaviour of La^（3＋） with Hollow Fiber Sandwich Liquid Membrane Extraction System

The extraction of La￣(3+) with hollow fiber sandwich liquid membrane was described in present paper. The theoretical equations of mass transport for this system were deduced. The permeability coefficient p of mass transport and its related factors were observed experimentally. The p value was increased with increase of pH in the feed and became constant under the condition of pH over 4. The p value was the highest when the flow rate was at 30 ml/min. The value of the coefficient was lower than that of single hollow fiber supported liquid membrane under the same conditions, but the stability and concentrated capacity of the sandwich membrane was better.

Removal of Aniline from Wastewater Using Hollow Fiber Renewal Liquid Membrane

Hollow fiber renewal liquid membrane(HFRLM) method was proposed based on the surface renewal theory for removal of aniline from waste water. The system of aniline + D2 EHPA in kerosene + HCl was used. Aqueous layer diffusion in the feed phase is the rate-control step, and the influence of lumen side flow rate on the mass transfer is more significant than that on the shell side. The resistance of overall mass transfer is greatly reduced because of the mass transfer intensification in the renewal of liquid membrane on the lumen side. The driving force of mass transfer can be considered as a function of distribution equilibrium, and the overall mass transfer coefficient increases with the increase of p H in the feed solution, HCl concentration and D2 EHPA concentration, and decreases with the increase of initial aniline concentration. A mass transfer model is developed for HFRLM based on the surface renewal theory. The calculated results agree well with experimental results. The HFRLM process is a promising method for aniline wastewater treatment.

Use of Ionic Liquid-filled Semipermeable Membrane for Extraction of Polycyclic Aromatic Hydrocarbons in Water

A novel and facile sample preparation method was developed for the extraction of polycyclic aromatic hydrocarbons (PAHs) in aqueous sample solution using 1-butyl-3- methylimidazolium hexafluorophosphate ([C4MIM][PF6]) – filled semipermeable membrane. For 24 hrs extraction of naphthalene, 1-methylnaphthalene, 2-chloronaphthalene, phenanthrene, the result showed that the extraction efficiency, correlation coefficient (R2) and RSD (n=5) were in the range of 67-102 %, 0.9870-0.9962, and 2.1-5.3 %, respectively.

Extraction and Enrichment of Copper by Liquid Emulsion Membrane Using LIX 664N

Process intensification using liquid emulsion membranes (LEMs) for extraction of copper has been studied in this work. In LEM process the extraction and stripping processes are combined in one stage. The solubility of the solute or the chemical affinity between the solute and carrier reagent in the membrane results in the separation of the solute from the feed mixture. In this work the membrane phase comprised of LIX 664N as the extractant dissolved in kerosene and Span 80 as surfactant. The stripping phase was sulfuric acid with 180 g/l concentration and feed phase had copper concentration of 3.5 g/l. Effect of various process parameters such as batch contact time, speed of agitation, W:O ratio and treat ratio has been experimentally investigated to get better insight of the process. The maximum enrichment of copper in the internal phase obtained was 11.6 times with batch contact time of 10 minutes, agitation speed of 300 rpm and treat ratio of 6:1.

Effect of alkali extraction on pit membranes and liquid uptake of four commercial softwoods

The present study examined the effect of alkali extraction on pit membranes （PMs） and liquid uptake of four conifers. Af- ter alkali extraction, the deposits around the PMs almost dissolved in Cunninghamia lanceolata Hook. and Cryptomeriajaponica D. Don wood which showed good liquid uptake. In contrast, in Larix leptolepis Gordon and Pseudotsuga menziesii Franco, although the tori adhered strongly to the pit aperture preventing liquid transportation, the liquid uptake of the woods improved markedly. More- over, the combined treatment of alkali extraction-transverse compression had no synergistic effect in improving liquid uptake. These results demonstrate that alkali extraction is effective in improving the liquid uptake of wood.

Extraction of Palladium from Acidic Chloride Media into Emulsion Liquid Membranes using LIX 984N-C^®

The extraction of palladium from hydrochloric acid solutions into emulsion liquid membranes (ELMs) using LIX 984N-C as the extractant was investigated. The influential factors and the total capacities of palladium extraction were determined by a batch method. The behavior of palladium extraction by ELMs under the operational conditions-pH of the external feed phase, surfactant and extractant concentration, internal stripping phase concentration, treat ratio and agitation speed were reported. Using LIX 984N-C, palladium was effectively extracted from the external acidic chloride feed phase into the internal receiving phase of W/O emulsions. More than 92% of palladium could be extracted at a feed pH of 2 with 3% Span 80, 9% LIX 984N-C and 7M HCl at a stirring speed of 300 rpm.

Extraction of Copper from Waste Solution Using Liquid Emulsion Membrane

The extraction of copper from acidic medium using Liquid Emulsion Membrane LEM as contactors was studied. b diketone LIX 54 as an extractant ,sesqueoleate which is nonionic surfactant with HLB value 3.7 and 0.1 M H2SO4 as stripping solution were used. The influence of initial concentration of copper in the aqueous feed phase, pH of external and internal aqueous phase, stirring speed, and concentration of extractant on the extraction rate was examined. The results obtained showed that practically all the copper content was removed from the acidic feed solution. The recovery of copper attained 96–100% and concentration ratios of about 40-fold could be achieved.

Transport of yttrium metal ions through fibers supported liquid membrane solvent extraction

A novel idea of transport of yttrium(Ⅲ) metal ions through fibers supported liquid membrane in two stage processes namely source to membrane and membrane to receiving phase has been proposed.The fibers supported liquid membrane was impregnated with different concentrations carrier.The experimental variables explored were concentration of yttrium(Ⅲ) ions,pH of source phase,PC-88A concentration in membrane phase,acid concentration in receiving phase and stirring speed.The pre-concentration of yttrium(Ⅲ) ions ...

Extraction of Neodymium by Emulsion-Liquid-Membrane within Hollow-Fiber-contactor and Its Mass Transfer Properties

A non-dispersive extraction technique, using an emulsion liquid membrane within a hollow-fiber-contactor for the extraction and enrichment of Nd^3＋ from the dilute feed aqueous, was applied. The emulsion system is consisted of span80 [ sorbitian monooleate], paraffin oil, D2EHPA [ 2-（ 2-ethylhexyl- phosphonic acid）], kerosene as well as HCl solution. The extraction under various conditions such as the span80 concentrations, the flow rate of aqueous, the extraction time and HCl concentrations in receiving phase were studied. Results show that the lower the flow rates of aqueous are, the higher the extraction percentage and enrichment-fold are, and the extraction percentage increases with the increasing of HCl concentrations. When the initial Nd^3＋ concentration in feed is maintained at 1000 mg· L^-1 and the emulsion is recycled with 70 times by a counter-flow,

A Study on Continuous Extraction of Cadmium by Using Liquid Surfactant Membrane

Based on batch extraction, improved liquid-impeled loop reactor(LLR) was used in continuous pilot-plant extraction for cadmium recovery from aqueous wastes. It integrated emulsifying, extracting, separating and demulsifying. The results showed that the extracting efficiencies were better than those of batch one and surfactant concentration was decreased to 3.0 percent from 4.0 percent of batch extraction.

Recovery of Copper Ions from Wastewater by Hollow Fiber Supported Emulsion Liquid Membrane

Recovery of copper ions from wastewater using a hollow fiber supported emulsion liquid membrane (HFSELM) was studied with LIX984N as carrier, kerosene as diluents, and sulfuric acid solution as stripping phase. Effects of compositions of feed and emulsion liquid phase, flow rates on both sides of membrane, and hollow fiber module parameters were investigated. The stability of the emulsion liquid phase without surfactant and the effect of buffer in the feed phase on the extraction rate were also evaluated. It is found that the stability of the emulsion phase without surfactant is poor. Higher flow velocity gives shorter residence time for the emulsion liquid phase on the tube side, reducing the effect of particle coalescence on the separation process. The extraction rate increases with the increase of feed phase pH, carrier concentration, hydrogen ion concentration in the stripping phase, and ef- fective hollow fiber area. The phase ratio in the emulsion liquid phase has a negative effect on extraction rate. The flow rates on both sides have little influence on the extraction performance of the HFSELM, while buffer addition in the feed solution improves the extraction efficiency.

Study on Extracting Low Concentration Cadmium from Zinc Hydrometallurgy System by Liquid Membrane Crystallizing Technique

The extraction of low concentration cadmium from a system containing high concentration zinc was studied and got CdS product directly. A new liquid membrane system taking DIPSA, TIBPS as carriers, (NH 4) 2S as precipitating agent was reported. Precipitating Cd 2+ in the internal aq. phase that is used to treat sulfuric acid leaching solution of zinc oxide in zinc hydrometallurgy has gotten satisfied results of extracting cadmium from high concentration zinc. After one stage of batch process under the optimum liquid membrane conditions, 98.6% transferring rate and 98.1% extracting rate of cadmium was obtained with only less than 1.0% transferring rate of zinc, and the feed solution can be purified very well.

锌冶炼过程中提取镓的技术研究及其进展

针对镓从锌冶炼过程中回收占比低的问题,总结分析了锌冶炼过程中镓回收技术研究进展.在鼓风炉炼锌(ISP)工艺中,镓主要富集在鼓风炉炉渣里,其质量分数通常在0.025%~0.031%,从鼓风炉炉渣中回收镓主要有还原蒸发法、高温氯化挥发法、硫酸浸出法、碱熔–浸出法、还原熔炼–电解法和还原熔炼–熔融造渣法等方法,但这些工艺普遍流程长,回收率低,加工成本偏高,部分工艺环境污染大,难以工业化应用.传统的湿法炼锌工艺中,大于93.5%的镓富集在浸出渣中,浸出渣处理以火法还原挥发工艺为主,在回转窑挥发浸出渣工艺中90%的镓保留在窑渣中,导致镓的回收流程长且回收率低,湿法处理浸出渣存在镓和铁分离的难题,至今未得到有效解决.氧压浸出炼锌工艺中,镓主要富集在锌粉置换渣里,锌粉置换渣采用酸性浸出和萃取工艺分离富集镓,最终制备金属镓,镓的综合回收率达到71%.通过对火法和湿法炼锌中镓回收工艺进行分析,对镓回收工艺中存在的关键问题和分离技术进行了总结,提出萃取分离、乳状液膜和树脂吸附有望成为锌冶炼过程中回收镓的绿色高效短流程关键技术.

基于膜式固相萃取的水体全氟化合物检测方法研究

基于膜式固相萃取法和液相色谱-串联质谱法建立了一种高灵敏、快速分析环境水样中痕量全氟化合物(PFASs)的方法。采用最优条件的模式固相萃取进行样品前处理,以乙酸铵水溶液及乙腈为流动相进行梯度洗脱,经Accucore aQ C18色谱柱分离,采用电喷雾离子源、负离子采集模式和质谱多反应监测模式分析,实现了环境水样中17种全氟化合物的快速分析,17种全氟化合物检出限(S/N=3)为0.2~0.3 ng/L。将方法应用于实际环境水样中全氟化合物的分析,加标回收率为87%~95%。研究可为快速、有效地检测环境水样中痕量全氟化合物提供新方法的选择。

基于改性壳聚糖膜净化的超高效液相色谱-四极杆/静电场轨道阱质谱法测定牛奶中5种兽药残留

本研究通过在壳聚糖膜(chitosan membrane,CSM)表面接枝长碳链,获得了十八烷基三甲氧基硅烷改性的壳聚糖膜(C_(18)-CSM),将其作为分散固相萃取吸附剂对牛奶基质进行净化,并结合超高效液相色谱-四极杆/静电场轨道阱质谱(UHPLC-Q/Exactive Orbitrap MS)建立了牛奶中氧氟沙星、恩诺沙星、环丙沙星、地西泮和甲硝唑的测定方法。利用扫描电子显微镜、傅里叶变换红外光谱仪和接触角测试仪对C_(18)-CSM材料进行表征。对牛奶样品的前处理条件进行优化,最优条件如下:提取溶剂为5%甲酸乙腈,NaCl用量为1 g,萃取次数为1次,C_(18)-CSM用量为20 mg。采用Hypersil GOLD VANQUISH色谱柱(100 mm×2.1 mm,1.9μm)进行分离,以0.1%甲酸水溶液和0.1%甲酸乙腈作为流动相进行梯度洗脱,流速为0.3 mL/min,进样量为1μL,柱温为25℃,在电喷雾电离源正离子模式下进行检测。在优化的前处理条件下,5种兽药在0.5~100μg/L范围内具有良好的线性关系,相关系数(r^(2))≥0.9970,检出限(LOD)为0.2μg/L,定量限(LOQ)为0.5μg/L。5种兽药在3个加标水平(0.5、1、5μg/L)下的回收率为79.5%~115%,日内精密度为7.0%~13%(n=6),日间精密度为1.3%~11%(n=3)。实验结果表明,本文所建立方法操作简便,准确可靠,能够满足牛奶中5种兽药残留的同时检测。

新型乳状液膜萃取RE(Ⅲ)动力学条件研究

稀土元素间电子层结构和物理化学性质极其相似,导致其难以分离,因此,稀土元素萃取分离一直是稀土冶金的研究热点问题。研究了以6%D2EHPA为流动载体、5%T154为表面活性剂、3.0mol/LHCl溶液为内水相、磺化煤油为膜溶剂,控制相比(Roi)为1.5制备一种新型乳状液萃取剂。通过用该乳状液萃取剂在硫酸体系下分别萃取La^(3+)、Ce^(3+)、Sm^(3+)、Eu^(3+)、Ho^(3+)和Er^(3+)6种稀土离子,确定了乳状液膜法(ELM)萃取RE(Ⅲ)的最优动力学条件。结果表明:最优动力学条件为乳化时间5min,萃取时间6min,乳水比(Rew)0.5,萃取温度25℃,外水相为稀土元素水溶液;该条件下,La^(3+)最高萃取率为99.92%,最大富集比为3.33,传质速率k=9.35×10^(-10)m/s,ELM对低浓度La^(3+)溶液表现出优异的萃取性能和富集效果。

物理法处理含酚废水的研究进展

含酚废水来源于煤化工、石油、制药、苯酚及酚醛树脂等工业生产。含酚废水具有毒性大、难处理、污染大等特点。废水中的酚类化合物是原型毒物,对一切生物个体都有毒害作用,能够使蛋白质变性凝固。本文将着重对物理法处理含酚废水技术类型上进行探讨,综述了近年来国内外含酚废水的物理处理方法,包括萃取法、吸附法、液膜法;最后对物理法处理含酚废水发展前景进行了展望。