共查询到18条相似文献,搜索用时 62 毫秒
1.
研究了以多孔聚偏氟乙烯为支撑体,N503为膜载体,煤油为膜溶剂的支撑液膜体系中Hg(Ⅱ)的迁移行为,测定了Hg(Ⅱ)与N503在煤油溶剂中的萃合物组成和条件萃取常数,考察了料液相pH值、载体浓度、料液相及反萃相中Cl-浓度等因素对Hg(Ⅱ)迁移的影响,获得Hg(Ⅱ)迁移的最佳条件:料液相pH=2.5~3.0,Cl-浓度为0.1 mol/L,载体浓度为0.706 mol/L,反萃相中Cl-浓度为0.8 mol/L.在最佳实验条件下,当Hg(Ⅱ)起始浓度为5.0×10-5 mol/L时,迁移120 min,Hg(Ⅱ)的迁移率可达99.6%.Hg(Ⅱ)在N503-煤油支撑液膜体系中的扩散层厚度δa为1.57×10-5 m,膜内扩散系数d0为7.26×10-13 m2/s,确立了Hg(Ⅱ) 的渗透系数P方程. 相似文献
2.
用磷酸三丁酯Span80-二甲苯乳状液膜体系迁移Sm(Ⅲ)的研究表明,在确定的条件下,可以快速并完全迁移Sm(Ⅲ)。许多常见离子不能在此条件下通过液膜迁移,故可从含有Fe^2+,Co^2+,Ni^2+,Cu^2+,Zn^2+,Cd^2+,Mn^2+等离子混合液中分离出Sm(Ⅲ)分离效率高。 相似文献
3.
4.
以HZ-818大孔吸附树脂为载体,甲基三辛基氯化铵(N263)为萃取剂,利用干浸渍方法制备了N263浸渍树脂。采用静态吸附法考察了在盐酸体系中盐酸浓度、金属离子浓度、温度以及时间等因素对制备的浸渍树脂吸附分离In3+、Fe3+性能的影响。结果表明,浸渍树脂吸附In3+、Fe3+的最佳盐酸浓度均为4mol/L;其吸附In3+、Fe3+的等温吸附曲线符合Langmuir等温吸附模型;298K下对Fe3+、In3+的饱和吸附容量分别为43.42mg/g、14.53mg/g。动力学研究表明,298K下浸渍树脂吸附Fe3+、In3+的平衡时间分别为6h、10h。准二级动力学方程可较好地描述浸渍树脂对In3+、Fe3+的吸附行为。混合体系中,浸渍树脂对Fe3+表现出较好的吸附性能,而对In3+基本上不吸附,从而达到了初步分离In3+、Fe3+的目的。 相似文献
5.
提出用TTA-TBPO为协同流动载体的乳状液膜分离它集抗(Ⅲ)的方法。其最佳液膜体系的组成为4%Span80.5%TTA、3%TBPO、4%液体石蜡、84%煤油和内相水溶液(4mol/L),最优实验条件,提取钪(Ⅲ)的外相试液为pH=1.3~2.3,Roi(油内比)为1:1,Rew(乳水比)为20:100。本法用于分离富集稀土元素中的微量钪(Ⅲ),其回收率可达99.1%以上,相对标准偏差为3.5%以下,结果十分满意。 相似文献
6.
7.
研究了以聚偏氟乙烯膜为支撑体, 二-(2-乙基己基)磷酸(D2EHPA)为流动载体, 煤油和D2EHPA的混合溶液作为膜溶液, 膜溶液和解析剂HCl溶液组成更新相的更新型支撑液膜(RSLM)中Gd(III)的分离行为|考察了料液pH、更新相HCl浓度、膜溶液与HCl溶液体积比、不同载体浓度对Gd(III)分离的影响, 得出了Gd(III)最优分离条件为: 更新相HCl溶液浓度4.00 mol/L, 膜溶液与HCl溶液体积比4∶3, 载体浓度控制在0.160 mol/L, 料液相中pH为4.80. 在最优分离条件下, 当Gd(III)的初始浓度为1.00×10-4 mol/L时, 35 min Gd(III)分离率达到95.7%. 最后根据传质定律和界面化学理论提出了Gd(III)在RSLM中的传质动力学方程. 相似文献
8.
我们曾报道过碱金属盐的合成.近来,这方面报道较多.本文研究了希土盐。实验一、合成称28克NaVO_3-4H_2O(分析纯)溶于500ml水中,加200ml HO_x的丙酮溶液(10克/100ml),搅匀分成七份,加热70℃时,每份分别滴加50ml溶有2克希土硝酸盐水溶液,调pH=6.2~6.8之间,搅拌30分钟,分出沉淀并干燥。二、组成分析C、H和N用元素分析仪,V和希土用原子吸收光谱仪和灼烧法。见表1。 相似文献
9.
PC-88A为流动载体的支撑液膜中Pt(Ⅳ)的迁移 总被引:1,自引:0,他引:1
研究了以烷基膦酸PC-88A为流动载体的聚偏氟乙烯支撑液膜中Pt(Ⅳ)的传输行为.考察了料液相盐酸浓度、解析相盐酸浓度、载体浓度、SnCl2浓度对Pt(Ⅳ)迁移的影响,获得了Pt(Ⅳ)迁移的最佳实验条件:料液相盐酸浓度为1.0 mol/L、解析相盐酸浓度为6.0 mol/L、载体质量分数为5.0%、SnCl2浓度为0.05 mol/L.当料液相Pt(Ⅳ)初始质量浓度为1.0 mg/L时,在最佳实验条件下,Pt(Ⅳ)可在3 h内完全迁移.将本法用于含Pt(Ⅳ)(0.8 mg/L),Cu(Ⅱ)(75.0 mg/L),Zn(Ⅱ)(75.0 mg/L),Co(Ⅱ)(75.0 mg/L)和Ni(Ⅱ)(75.0 mg/L)的模拟试样中Pt(Ⅳ)的分离,取得了满意结果. 相似文献
10.
11.
12.
The facilitated transport of penicillin G from aqueous solutions to the stripping phase through bulk liquid membrane (BLM)
containing TBP in 3% iso-octanol and n-butyl acetate was studied. Na2CO3 solution was used as the stripping phase. Experiments were performed as a function of stirring rate, TBP concentration and
type of diluent in the liquid membrane phase, pH, and initial penicillin G concentration in the feed phase, Na2CO3 concentration in the stripping phase, etc. The results showed that the BLM process could carry out the simultaneous separation
and concentration of penicillin G from dilute aqueous solutions, and arise “up-hill” effect due to the characteristic of non-equilibrium
mass transfer. The diffusion of penicillin G complex in the liquid membrane phase played an important role in BLM process.
The mass transfer mechanism of BLM for this system was also discussed. 相似文献
13.
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。 相似文献
14.
萃取色谱分离—原子发射光谱测定氧化钐,氧化铕,氧化钆中14个稀土杂质 总被引:6,自引:0,他引:6
用2-乙基己基膦酸单2-乙基己酯萃取色谱分离-原子发射光谱测定超高纯Sm2O3、Eu2O3、Gd2O3中痕量稀土杂质,可用于纯度为999999%~9999999%(不含非稀土杂质)Sm2O3、Eu2O3、Gd2O3的纯度分析,14个稀土杂质的回收率在67%~133%之间,相对标准偏差±64%~±184%,分离周期10~14h。 相似文献
15.
Zaizheng Zhang Jie Zhang Ying Chen Chuanhong Tu Jidian Zheng 《Analytica chimica acta》1997,350(3):365-369
This paper reports the determination of samarium, europium and gadolinium by Sm and Gd monoxide emission and Eu atomic emission. The enhancement effect of other rare earth elements on Sm, Eu and Gd emission was studied. Large amounts of lanthanum (La) were used as enhancing reagents and chemical interference inhibitors and the dual wavelength method was introduced to eliminate spectral interference, in which the analytical wavelengths used were Sm 651.0 nm, Eu 459.4 nm and Gd 461.6 nm and the reference wavelengths were Sm 651.4 nm, Eu 459.8 nm and Gd 461.2 nm. The method has been applied to the assay of Sm, Eu and Gd in synthetic Sm---Eu---Gd concentrates with satisfactory results. 相似文献
16.
Smita Gupta 《Journal of Dispersion Science and Technology》2013,34(12):1733-1741
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. 相似文献
17.
The Tb3+ transport in dispersion supported liquid membrane (DSLM) consisting of polyvinylidene fluoride membrane (PVDF) as the liquid membrane support and dispersion solution including HCl solution as the stripping solution and 2‐ethyl hexyl phosphonic acid‐mono‐2‐ethyl hexyl ester (P507) dissolved in kerosene as the membrane solution, has been studied. The effects of pH value, initial concentration of Tb3+ and different ionic strength in the feed phase, volume ratio of membrane solution and stripping solution, concentration of HCl solution, concentration of carrier, different stripping agents in the dispersion phase on transport of Tb3+ has also been investigated, respectively. As a result, the optimum transport conditon of Tb3+ was that concentration of HCl solution was 4.0 mol/L, concentration of P507 was 0.10 mol/L, and volume ratio of membrane solution and stripping solution was 1.0 in the dispersion phase, and pH value was 5.2 in the feed phase. Ionic strength had no obvious effect on transport of Tb3+. Under the optimum condition studied, when initial concentration of Tb3+ was 1.0×10?4 mol/L, the transport rate of Tb3+ was up to 95.2% during the transport time of 95 min. The kinetic equation was developed in terms of the law of mass diffusion and the theory of interface chemistry. The results were in good agreement with the literature data. 相似文献
18.
Liquid Membrane Oscillation of Water/Oil/Water System Containing TTAB and Recognition to Amino Acids
The liquid membrane oscillation of a novel water(aqueous tetradecyl trimethyl ammoniumbromide,TTAB and alcohol solution)/oil(picric acid in chloroform solution)/water(aqueous glucose solution) system was investigated by means of a homemade device.The results show that the water(aqueous 7 mmol/L TTAB and 0.5 mol/L n-propanol solution)/oil(0.5 mmol/L icric acid in chloroform solution)/water(0.1 mol/L glucose solution) system performed sustained and stable oscillation at 30 °C.The oscillation curve under optim... 相似文献