氯化锡催化合成马来酸二丁酯

以SnCl4·5H2 O为催化剂 ,由马来酸酐和正丁醇合成了马来酸二正丁酯。n(马来酸酐 )∶n(正丁醇 )∶n(SnCl4·5H2 O) =1∶4∶0 .0 86 ,回流分水 6 0min ,酯收率达 92 .1% ,并用类似方法合成了收率较高的马来酸二异丁酯、马来酸二正戊酯和马来酸二异戊酯     

氯化铝中萃取铁工艺

采用萃取剂N,N,N',N'-四丁基丙二酰胺(TBMA) 、N,N,N',N'-四辛基-3-氧戊二酰胺(TODGA)和甲基异丁基甲酮(MIBK)从氯化铝水溶液中萃取铁,以制备高纯氯化铝。 研究结果表明,当氯化铝溶液中盐酸浓度在4 mol/L左右时,TBMA和MIBK的萃取率在90%以上。 TODGA显示出优异的萃取分离性能。 当氯化铝溶液中Al³⁺浓度为2.0 mol/L,Fe³⁺浓度为0.0036 mol/L(0.2 g/L),HCl浓度为1.2 mol/L时,0.20 mol/L TODGA的环己烷或环己烷有机相对铁的一次萃取率达到99.9%以上,多次萃取后溶液中的铁含量低于0.01 mg/L,能深度去除氯化铝中的铁杂质,在工业化生产中有极大的应用价值。     

萃取光度法测定微量铋

铜合金中铋作为杂质量存在(<0.002%),目前的测定方法,都经沉淀、萃取等富集分离.本文提出在 0.2mol·Lˉ1HBr存在下,用乙酸丁酯-三辛胺萃取分离后,在乙酸丁酯-正丁醇中用硫脲显色,直接在有机相中测定.合金中大多数常见共存金属离子的允许量在几十毫克至克级以上,方法简便,可测定铜合金中铋0.0010%～0.0050%.     

酸性磷类萃取剂在硫酸介质中对Y(Ⅲ)的协萃机制研究

对HDEHP(H2A2),HEH/EHP(H2B2),Cyanex272(H2L2)萃取剂在硫酸介质中单独以及HDEHP-HEH/EHP和HDEHP-Cyanex272混合萃取剂萃取稀土元素Y(Ⅲ)的机制进行了研究. 研究发现,单独采用HDEHP和HEH/EHP萃取Y(Ⅲ)时,SO2-4参与了反应,造成反应过程中放出的H 个数随萃取剂浓度的变化而变化,对于单独采用Cyanex272萃取Y(Ⅲ)的过程中则是OH-参与了反应. 计算了混合萃取剂萃取Y(Ⅲ)的协萃系数(R),当水相平衡pH=1.2时,HDEHP和HEH/EHP混合萃取体系与HDEHP和Cyanex272混合萃取体系萃取Y(Ⅲ)的R分别为27.68和48.99,并且协萃系数随水相平衡pH的升高而增加. 确定了在HDEHP和HEH/EHP混合萃取体系中的协萃反应并计算了反应的平衡常数及萃合物形成反应的稳定常数,反应机制为阳离子交换反应.     

逆流色谱分离镅(Ⅲ)和铕(Ⅲ)的研究

选择0.1 mol/L NaC lO4为流动相,以二氯苯基二硫代膦酸的二甲苯溶液为固定相,研究了萃取剂浓度、流动相pH及流动相流率对逆流色谱(CCC)分离Am3 和Eu3 效果的影响。结果表明,在实验条件下,两者的分离系数随着固定相中的萃取剂浓度增加、流动相的pH升高而增大;降低流动相流率后可明显改善分离效果。通过改变分离条件,Am3 和Eu3 可基本上实现相互分离,两者间的分离系数和分离效率分别达到2.87和0.74。     

C12-2-En-C12•2Br与SDS混合水溶液的胶团化研究

与[C12H25N＋(CH3)2CH2]2•2Br－(简记为C12-2-C12•2Br)/ C12H25SO4Na(SDS)混合水溶液相比,随着联接链上乙氧基团(E)数目增加,[C12H25N＋(CH3)2]2C2H4(OC2H4)n•2Br－(简记为C12-2-En-C12•2Br, n=2,3)与SDS混合水溶液澄清区域明显增大. C12-2-E3-C12•2Br/SDS混合胶团化过程中二组分产生了协同效应,理论预测在澄清区域所能达到的最小临界胶团总浓度(cmcT,min)= 0.0339 mmol•L－1,对应的SDS在溶液体相中的摩尔分数(x2*)=0.447.当水溶液体相中SDS摩尔分数(x2)=0.5时,混合胶团总聚集数(NT)=36,混合胶团中SDS的摩尔分数(x2M)=0.43.     

高效液相色谱法测定间苯二酚反应液中间苯二酚的含量

建立了高效液相色谱法测定间苯二酚反应液中间苯二酚含量的方法。色谱柱为Diamonsil ODS(150 mm×4.6 mm,5μm),流动相为A与B的混合液(体积比为5∶95,A:乙腈,B:5 mmol/L1,8-二胺辛烷与20 mmol/L庚磺酸钠水溶液混合后调节至pH4.5),检测波长为276 nm。间苯二酚与反应液中其它杂质分离较好。间苯二酚的浓度在0.1~0.5 g/L范围内与色谱峰面积呈良好的线性。加标回收率为99.25%~99.44%,测定结果的相对标准偏差为0.85%(n=8)。     

N,N′-二(十二烷基)乙二胺二乙酸萃取汞的研究

研究了N ,N′ 二 (十二烷基 )乙二胺二乙酸 (简写为H2 R2 Y)的氯仿溶液对汞 (Ⅱ )的萃取行为。考察了酸度、萃取剂浓度、相比及温度等因素对萃取率的影响 ;用电导法及摩尔比法测得萃合物的摩尔比为 1∶1 ;测定了新试剂H2 R2 Y对Hg2 与Fe3 、Co2 、Ni2 、Zn2 、Cr3 、Mn2 等金属离子的分离效果 ;并根据分配比与温度的关系求出了萃取反应的ΔH0 、ΔS0 、ΔG0 和lgKex值 ,该萃取反应为放热反应。     

酮洛芬对映体的双相识别手性萃取分离

研究了酮洛芬在溶有酒石酸酯的有机相和β-环糊精衍生物水相萃取体系中的分配行为;考察了有机溶剂、酒石酸酯、环糊精衍生物的种类、萃取剂浓度和pH等因素对分离效果的影响。结果表明,β-环糊精衍生物优先识别S-对映体而不是R-对映体,但L-酒石酸酯的识别能力刚好相反;1,2-二氯乙烷作为有机溶剂,三甲基-β-环糊精和L-酒石酸异丁酯做手性萃取剂是最好的选择;萃取剂的浓度和pH对分离效果有明显影响;当三甲基-β-环糊精和L-酒石酸异丁酯的浓度分别为0.1mol/L和0.2mol/L、水相pH=2.5时,分离效果最好。     

利用海藻酸钙胶囊提取醋酸

我们曾进行了利用聚酰胺胶囊处理含铬废水的研究,取得了一些结果,积累了一定的经验.当前还没有找到从低浓度的醋酸废水溶液中提取醋酸的有效方法.戴猷元等人曾用中空纤维膜器中萃取方法处理低浓度的醋酸水溶液.本文利用内含磷酸三丁酯(TBP)的海藻酸钙胶囊处理低浓度的醋酸水溶液.实验表明,这种方法与利用萃取剂直接萃取法相比有明     

Emulsion liquid membrane extraction of Ni(II) and Co(II) from acidic chloride solutions using bis-(2-ethylhexyl) phosphoric acid as extractant

An emulsion liquid membrane process using bis-(2-ethylhexyl) phosphoric acid (D2EHPA) to extract and separate Ni(II) and Co(II) from acidic chloride solutions is described. Liquid membrane consists of a diluent, a surfactant (Span 80), and an extractant (D2EHPA). Hydrochloric acid was used as the stripping solution. The important parameters governing the permeation of nickel and their effect on the separation process have been studied. These parameters are stirring speed, feed phase pH, surfactant concentration, extractant concentration, stripping phase concentration, phase ratio, initial concentration of metal, and treatment ratio. The optimum conditions have been determined. The separation factors of Ni(II) with respect to Co(II), based on initial feed concentration, have been experimentally determined. Furthermore, the extraction selectivity for Co(II) over Ni(II) has been improved by using D2EHPA during the initial minutes.     

Effect of standard phase differences between gas and liquid and the resulting experimental bias in the analysis of gaseous volatile organic compounds

Liquid- or gas-phase standards can be used for the analysis of VOCs in air. Once the accuracy is secured in the standard preparation stage, the use of gas-phase standard should be more reliable with the least matrix effect. However, it is not difficult to find that the liquid-phase standard is used more preferably in many laboratories for several reasons (e.g., low expense, easy handling, etc.). As such, one needs to accurately evaluate any possible bias stemming from the use of different standard phases. To this end, standards for 8 VOCs consisting of 4 aromatic compounds (benzene (B), toluene (T), styrene (S) and p-xylene (p-X)) and 4 others (methyl ethyl ketone (MEK), methyl isobutyl ketone (MIBK), butyl acetate (BuAc), and isobutyl alcohol (i-BuAl)) were prepared in both liquid and gas phases. Each standard was analyzed by the initial collection on the adsorption tube and by the combined application of thermal-desorption–gas chromatography–mass spectrometry (TD/GC/MS). The results indicated that experimental bias between the two phases, if expressed in terms of percent difference (PD), was very low in many target VOCs (B (1.09%), T (2.41%), p-X (3.64%), MEK (6.76%), and MIBK (0.17%)), while it was not in some targets (e.g., >10%: e.g., S, i-BuAl, and BuAc). In an ancillary experiment, biases were evaluated further by (1) calibrating gaseous samples against liquid phase standard and via (2) comparison between two different types of gas phase standards. In conclusion, treatment of different standards (e.g., between the same or different phases) will inevitably induce biases in most VOCs, although certain volatiles (e.g., benzene, MIBK, etc.) are virtually unaffected by such variables in a practical sense.     

Extraction of palladium and platinum with trioctylphosphine oxide (TOPO) in various solvents from hydrochloric and hydrobromic acid media

The extraction of palladium and platinum with trioctylphosphine oxide (TOPO) in cyclohexane, chloroform, methyl isobutyl ketone (MIBK) and 2,2′-dichlorodiethyl ether (DCDE) from hydrochloric and hydrobromic acids in dependence on the concentration of the acids and the extractant has been investigated. The obtained relation have been discussed and the possibilities of the separation of palladium, platinum, gold and their simultaneous extraction have been pointed out.     

An extraction study of gallium, indium and thallium using TPASO as an extractant

A method is proposed for the extraction and individual separation of trivalent gallium, indium and thallium from salicylate media using triphenylarsine oxide dissolved in toluene as an extractant. The optimum extraction conditions are evaluated and described. The extracted metal ions are stripped and estimated spectrophotometrically following complexation with 4-(2-pyridylazo) resorcinol. A possible mechanism of the extraction is discussed. The method permits rapid and precise individual separation of gallium (III), indium (III) and thallium (III) and is applicable to the analysis of alloy samples.     

Development of a Liquid‐liquid Extraction System for Rhodium(III) by 2‐octylaminopyridine from Weak Malonate Media

We have developed the extraction method of rhodium(III) from malonate media with 2‐octylaminopyridine (2‐OAP) in xylene at pH 8.0. The quantitative extraction of rhodium(III) with extractant was found by screening of different physicochemical parameters like malonate concentration, extractant concentration, pH, diluents, effect of temperature, aq: org phase ratio, loading capacity of 2‐OAP. The optimum condition was malonate=0.025 M, pH=8.0, 2‐OAP=0.05 M in xylene. The complete stripping of rhodium(III) from the loaded organic phase was carried out with 2 M HCl. Log‐log plot was investigated to determine the stoichiometry of the extracted species and it was found to be 1 : 2 : 1 (metal : acid :extractant). The versatility of the proposed method was checked for extraction and separation of rhodium(III) from binary, ternary mixture of associated metal ions as well as platinum group metals and from the synthetic solution of rhodium minerals and alloys.     

Solvent extraction of metals with commercial oxime extractant (LIX 622)

The extraction characteristics of some selected metals from an aqueous buffered solution by LIX 622, a commercial oxime extractant have been studied. The pH_1/2 values for extracting different metals with 5 v/v% LIX 622 extractant in methyl isobutyl ketone (MIBK) have been obtained. The order of extraction of metals with LIX 622 extractant as a function of pH_1/2 value is determined and results agree well with the order obtained using salicylaldoxime as chelating ligand for the extraction of these metals.     

Synergistic Extraction and Atomic Absorption Spectrometric Determination of Managanese in Environmental Samples Using M-p-Aminophenyl-2-Furylacrylohydroxamic Acid and Trioctylmethylammonium Cation

Abstract

Fifteen new hydroxamic acids were explored in conjunction with trioctyimethylammonium cation for the extractive separation of manganese into MIBK from the anions and cations commonly associated with the metal in environmental samples. The most rapid extraction with the maximum selectivity and sensitivity for the atomic absorption spectrometric determination of the metal in the MIBK extract was achieved with N-p-aminophenyl-2-furylacrylohydroxamic acid. The method enabled the determination of manganese at sub-ppb levels and was applied in the analysis of coal, manganese ore, plant tissue, animal tissue and natural waters.     

多级离心连续逆流手性萃取模型及模拟

基于单级手性萃取数学模型和质量守恒定律,建立了多级离心手性萃取数学模型,设计了多级离心萃取数学模型程序,并对多级离心萃取分离苯基琥珀酸（PSA）对映体进行了模拟.模拟了相比、萃取剂浓度、对映体浓度、进料位置和萃取级数等工艺参数对萃取效果（产物纯度和产率）的影响.模拟结果表明,考察的工艺参数共同影响萃取相和萃余相的产物纯度及产率;采用中间位置进料和较大的W/F相比有利于对称分离.实验发现：采用中间位置进料,10级离心萃取后萃取相中苯基琥珀酸的光学纯度ee（对映体过量）达到56%以上.模拟结果还表明,采用26级离心萃取器,中间进料,逆流分级萃取,萃取相及萃余相中的光学纯度ee都能达到98%以上.     

Silver Nitrate/Oligo(ethylene Oxide) Surfactant/Mesoporous Silica Nanocomposite Films and Monoliths

A lyotropic, liquid crystalline (LC) phase of a silver nitrate/oligo(ethylene oxide), water, and acid mixture was used for one-pot synthesis of mesoporous silica materials in which Ag(+) ions are uniformly distributed. We established that the AgNO(3)-to-surfactant mole ratio is very important in a 50 wt% surfactant/water system to preserve the hexagonal LC phase before and after the addition of the silica source. Below a 0.6 AgNO(3)-to-surfactant mole ratio, the mixture is liquid crystalline and serves as a template for silica polymerization. However, between 0.6 and 0.8 AgNO(3)-to-surfactant mole ratios, one must control the composition of the mixture during the polymerization processes. Above a 0.8 mole ratio, Ag(+) ions undergo phase separation from the reaction mixture by complexing with the surfactant molecules. The resulting silica materials obtained from AgNO(3)/surfactant ratios above 0.8 have anisotropy but without a hexagonal mesophase. Here, we establish a AgNO(3) concentration range in which the LC phase is preserved to template the synthesis of mesoporous silica, and we discuss the structural behavior of the mixtures at AgNO(3)/surfactant mole ratios of 0.00-2.00, using POM, PXRD, FTIR, and UV-Vis absorption spectroscopy. Copyright 2001 Academic Press.     

Separation and concentration of cobalt from ammoniacal solutions containing cobalt and nickel by emulsion liquid membranes using 5,7-dibromo-8-hydroxyquinoline (DBHQ)

The separation and concentration of cobalt from ammoniacal solutions containing nickel and cobalt by an emulsion liquid membranes (ELMs) using 5,7-dibromo-8-hydroxyquinoline as extractant has been presented. Membrane solution consists of a diluent (kerosene), a surfactant (Span 80), a modifier (tributylphosphate), and an extractant (DBHQ). Very dilute sulphuric solution containing EDTA as complexing agent, buffered at pH 5.0, has been used as a stripping solution. pH of ammoniacal feed solution containing cobalt and nickel was adjusted to 9.0 with hydrochloric acid. The important variables governing the permeation of cobalt have been studied. These variables are membrane composition, pH of the feed solution, cobalt and nickel concentrations of the feed solution, mixing speed, surfactant concentration, extractant concentration, EDTA concentration and pH of the stripping solution, and phase ratio. After the optimum conditions had been determined, it was possible to selectively extract 99.0% of cobalt from ammoniacal feed solution containing Co²⁺ and Ni²⁺ ions. The separation factors of cobalt with respect to nickel, based on initial feed concentration, have experimentally found to be of as high as 247.5 for about equimolar Co–Ni feed solutions.