The Peculiarities of Extraction of Vanadium(V) by Aminophenols from Sulfuric Acid Solutions

Journal of Solution Chemistry - The effects on the extraction of Vanadium(V) by N-(2-hydroxy-5-nonylbenzyl)-β,β-dihydroxyethylamine of different factors, including pH of the medium,...     

Vanadium(V) Complexes in Hydrochloric Acid Solutions

^51V NMR, electronic, and vibrational spectroscopies were applied to study the ionic state of vanadium(V) in hydrochloric acid solutions at cHCl = 1.0-11.3 M and vanadium(V) concentration of 1 M.     

二(2-乙基己基)磷酸萃取亮氨酸平衡研究

萃取平衡;二乙基己基磷酸;二(2-乙基己基)磷酸萃取亮氨酸平衡研究     

D2EHPA和D2EHDTPA萃取银的研究

本文研究了D₂EHPA和D₂EHDTPA在硝酸体系中萃取和反萃取银的条件,并用饱和法和连续变量法测定了革合物的组成,以红外光谱和核磁共振谱探讨革合物的成键情况,通过EHMO计算结果说明了上述两种革取剂对Ag⁺萃取能力异同的原因。     

Extraction of Vanadium (IV) with DI-2-Ethylhexylphosphoric Acid

Abstract

It was established with the use of electron and ESR spectroscopic methods that in the presence of sodium sulfate, the extraction of vanadium (IV) with di-2-ethylhexylphosphoric acid takes place by a cation-exchange mechanism giving rise to two complex compounds of vanadium (IV) oxocation with sulfuric and di-2-ethylhexylphosphoric acid anions. The vanadium (IV) oxocation sulfate complex extracted in the solid state was examined with X-ray structural analysis. It was shown that the vanadium (IV) oxocation sulfate complex trihydrate crystallizes in the centrosymmetrical space group to form dimers with bridging sulfate groups.     

二(2-乙基己基)磷酸对氨基酸的萃取平衡

二（２－乙基己基）磷酸对氨基酸的萃取平衡曹汉瑾,王德宝,刘沛妍,吴子生,严忠（东北师范大学化学系,长春,１３００２４）关键词氨基酸,二（２－乙基己基）磷酸,萃取平衡,分配比迄今为止,有关氨基酸溶剂萃取的文献报道还不多［１～３］．本实验以二（２－乙基己...     

Extraction Recovery of Tantalum(V) and Niobium(V) from Hydrofluoric and Hydrofluoric-Sulfuric Acid Aqueous Solutions with Octanol

Comparative study of extraction of tantalum(V) and niobium(V) with octanol and tributyl phosphate was made. The data on distribution of tantalum(V) and niobium(V) between octanol and hydrofluoric and hydrofluoric-sulfuric acid aqueous solutions were obtained. The flowsheet for preparation of pure tantalum and niobium oxides was developed.     

HDEHP和HEH/EHP混合萃取剂在硫酸介质中协同萃取RE(Ⅲ)的机制研究

对HDEHP(H2B2)和HEH/EHP(H2L2)混合萃取剂在硫酸介质中萃取稀土元素(La,Nd,Sm,Gd)的机制进行了研究。研究表明,在水相平衡pH=2.0时,混合萃取剂萃取这几种元素的协萃系数分别为:1.96(La),3.52(Nd),5.96(Sm),5.71(Gd),并且协萃系数随水相平衡pH的升高而增加。利用斜率法分别确定了单一萃取剂HDEHP和HEH/EHP以及混合萃取剂HDEHP HEH/EHP在硫酸体系中萃取稀土元素的配合物结构式分别为RE(SO4)xH2x(HB2)3,RE(SO4)xH2x(HL2)3以及RE(HB2)2(HL2)。计算了反应的平衡常数及形成常数并确定了反应机制为阳离子交换反应。     

Extraction of Tantalum(V) Impurities from Niobium(V) Fluoride Solutions with Octanol

Fine purification of niobium(V) to remove tantalum(V) by extraction was studied at various compositions of solutions and ratios of phase volumes. Washing of tantalum(V) and niobium(V) extracts with aqueous solutions of their fluorides was considered.     

伯胺N~1~9~2~3萃取硫酸铀酰的机理研究

研究了伯胺N~1~9~2~3的正庚烷溶液从硫酸介质中萃取硫酸铀酰的机理。认为伯胺N~1~9~2~3的硫酸盐在有机相中形成了反向胶束(或胶团),并由红外光谱和透射电镜佐证。伯胺N~1~9~2~3和铀酰形成的萃合物主要存在于反向胶束准相中。可以较好地解释用斜率法无法解释的实验事实。     

二-(2-乙基己基)磷酸与仲壬基苯氧基取代乙酸混合体系对稀土元素的萃取

考察了二-(2-乙基己基)磷酸(D2EHPA,H2A2)和仲壬基苯氧基取代乙酸(CA100,H2B2)混合体系在HCl介质中对15种镧系元素(除钷)及钇的萃取性能,计算了稀土元素间的分离系数,并比较了混合萃取体系与D2EHPA单独萃取体系对稀土元素的分离能力.研究了D2EHPA-CA100混合体系对镧的协同萃取机理,用斜率法和恒摩尔法探讨了萃取反应方程式,考察了酸度、萃取剂浓度及温度对萃取性能的影响.结果表明:D2EHPA-CA100混合体系对镧系元素的协同效应随原子序数的增加而减弱.在适当的萃取剂配比下,此混合体系对某些稀土元素的分离能力优于D2EHPA,可用于这些稀土元素的分离.D2EHPA-CA100混合体系协同萃取镧的萃合物组成为LaH5A6B2,反应为吸热反应.     

Precipitation of Titanium(IV) and Iron(III) Phosphates from Sulfuric Acid Solutions

Conditions for the precipitation of phosphates from solutions of titanium(IV) sulfate containing iron(III) were studied. The precipitation of components and the mechanism of the phase formation in the system under study were considered in relation to the TiO₂ : Fe₂O₃ ratio in the starting solution.     

Electrolytic Preparation of Vanadium(V) Oxide from Saturated Solutions of Ammonium Metavanadate

A study was made of the voltammetric characteristics and dependences of the deposition rate and current efficiency on the electrolysis conditions in anodic deposition of vanadium(V) oxide on a stainless steel support from saturated solutions of ammonium vanadate, including those containing active and supporting additives.     

Gallium(III) Extraction from Hydrochloric Acid Solutions with Diacylated Diethylenetriamine Hydrochloride

Extraction of gallium(III) from hydrochloric acid solutions with hydrochloride of diethylenetriamine [N-(2-aminoethyl)ethane-1,2-diamine] N,N'-diacylated with neodecanoic acid was studied using chloroform as diluent. Gallium(III) can be effectively recovered from 6–10 M HCl solutions and selectively separated from indium(III), aluminum(III), and zinc(II). The concentration constant and thermodynamic parameters of the anion-exchange extraction of gallium(III) from 6 M HCl solutions were evaluated.     

Preparation of Titanium-Containing Sulfuric Acid Solutions

The influence exerted by fluorine-containing agents introduced into nitric acid in leaching of calcium oxide from the sphene concentrate on the possibility of performing the process under atmospheric pressure to obtain titanium dioxide of anatase structure in the solid residue was examined. The sulfatization of the titanium-silica product obtained in nitric acid breakdown of the sphene concentrate and aqueous leaching of titanium sulfates from the forming cakes were studied.     

Vanadium Catalysts Promoted with Magnesium Compounds for Production of Sulfuric Acid

The feasibility and efficiency of promotion with magnesium compounds of supported and mixed catalysts for sulfuric acid production were studied.