氨基酸-BrO-3-Mn2+-H2SO4-丙酮体系的振荡反应

This paper, Using potentiometric method, first reports the oscillating behavior of five amino acids (L-methionine, L-cystine, L-tryptophan, L-serine, L-tyrosine) in a new oscillating system of amino acid-BrO_3~--Mn~(2+)-H_2SO_4-acetone. The effect of many factors on oscillation have been investigated. According to Arrhenius equation, the apparent activation energy of the oscillatary induction period and oscillation period of five oscillating systems are obtained within temperature range of 20～37 ℃.     

萃取体系第三相的生成、微观结构与应用研究--三相萃取体系研究进展

液＝液萃取体系中第三相的生成将干扰取操作的顺利进行,多年来人们对第三相的研究多限于第三相的生成与防止。本文阐述了在萃取体系中第三相的形成,结构及应用方面的近期研究成果,特别是基于对第三相成因及组成,结构的进一步认识,导致人为的制备中相,并对其应用进行深入的研究。     

苯酚-KBrO3-H2SO4振荡体系的诱导期与周期

1978年,Orbán和Koros简略碰报导了苯酚-KBrO_3-H_2SO_4体系的振荡行为。直到现在,该体系详细的实验研究未见报导。近来,我们对此体系的振荡行为重新作了探讨,发现与前人的结果大不相同,具有独特的规律。实验方法与文献[2]的完全相同。所用的药品,苯酚为A.R.级,KBrO_3和H_2SO_4均为G.R.级。实验温度为298±0.5K。今将所得结果报导如下。     

GA-KBrO3-H2SO4体系化学振荡的研究

研究了GA(没食子酸)-KBrO_3-H_2SO_4体系的诱导期τ、振荡周期T_2与反应物起始浓度的依赖关系, 302 K时的经验式为τ=22.8 c~(-2.23)_(H_2SO_4) c~(-2.17)_(KBrO_3) c~(0.795)_(GA) (mol.dm~(-3))~(4.25)·sT_2=0.84 c~(-2.28)_(H_2SO-4)c~(-1.97)_(KBrO_3) exp{(0.000147(mol.dm~(-3))~2/c~2_(GA)}(mol.dm~(-3))~(4.25)·sτ及T_2都随~CGA的增加而增长, 这与B-Z反应中关于有机物的结论不同。用循环伏安法研究该体系的结果表明, GA在诱导期结束时就基本上都被氧化为中间物, GA并不象前人所认为的是维持振荡的物种, 实际参与振荡的是由GA生成的物质。本文还研究了Fe(Phen)_3~(2+)对GA-KBrO_3-H_2SO_4体系振荡的影响, 发现Br~-振荡行为随Fe(Phen)_3~(2+)的浓度而变。低~CFe(phen)_3~(2+)时,Br~-的振荡行为与GA-KBrO_3-H_2SO_4体系的基本相似, 其特征是每个振荡周期内, Br~-振荡脉冲发生前是逐渐积累的。随着~CFe(phen)_3~(2+)的增大, Br~-出现另一特征的振荡行为, 在每个振荡周期内, Br~-振荡脉冲发生前是逐渐减小。我们认为, GA-KBrO_3-H_2SO_4-Fe(Phen)_3~(2+)体系的振荡不能单一地用OKN机理加以解释, 它可能是两套振荡机理耦合的振荡。     

三元体系Na2SO4-CuSO4-H2O 25 ℃活度系数的研究

用自制的Hg-Hg_2SO_4电极和Na离子选择性电极, 在25 ℃和离子强度分别为1.0和2.0的条件下, 测定了Na_2SO_4在Na_2SO_4和CuSO_4混合水溶液中的平均活度系数。对所使用的电极组的热力学响应、重现性等性能进行了检验。根据文献提供的Pitzer方程, 推导了计算Na_2SO_-CuSO_4-H_2O体系中Na_2SO_4和CuSO_4平均活度系数的表达式, 求出了Pitzer混合参数和Harned方程系数, 计算了CuSO_4在该体系中的平均活度系数。     

MgSO4-Na2SO4-H2O三元体系100 ℃沸腾蒸发非平衡态成盐特征

采用140 ℃恒温热源, 对MgSO4-Na2SO4-H2O体系溶液进行100 ℃恒温沸腾蒸发, 蒸发强度为140～160 g/(h•L), 监测初始析盐点和固相析出后固液相组成随蒸发进程的变化, 总结成盐特征, 提出反映非平衡态成盐特征的初级成盐区、扩展成盐区等概念. 研究发现(1)平衡相图上的同成分复盐3Na2SO4• MgSO4和Na2SO4• MgSO4•2.5H2O变为异成分复盐; (2)对Na2SO4和3Na2SO4•MgSO4的平衡共饱和液蒸发, 首先析出的是Na2SO4, 其单固相析出率为60.86%, 3Na2SO4•MgSO4和Na2SO4•MgSO4•2.5H2O的共饱和液也具有相同特征; (3)蒸发过程的初级成盐区与溶解平衡相区有显著区别. 用硫酸钠的耶涅克指数表示相区宽度, Na2SO4初级成盐区宽度从平衡态的21.02扩大到32.76; 而Na2SO4•MgSO4•2.5H2O则从41.40缩减为25.71; (4)在晶种存在的条件下, 各种盐的成盐区比初级成盐区有不同程度的扩展, 如Na2SO4, 3Na2SO4•MgSO4等盐的成盐区分别扩展了7.72和8.81. 扩展成盐区与初级成盐区的交叠形成了非平衡条件下特有的条件成盐区, 析盐种类取决于晶种的种类.     

PEG/(NH4)2SO4双水相体系萃取甘草中的有效成分

甘草的主要有效成份甘草酸具有消炎解毒、抗氧自由基、调节机体免疫力等作用,目前已被广泛应用于食品、饮料、化妆品、医药、卷烟等行业。工业上广泛应用的是水提法,该法操作容易、设备简单、溶剂价廉,但提取效率不高,易造成资源浪费。双水相萃取技术(Two-aqueous phase extraction,简称．ATPS),是近年出现的新型生物化工分离技术。由于双水相萃取分离过程条件温和、可调节因素多、易于放大和操作,不存在有机溶剂残留问题,特别适用于生物物质及天然资源中有效成分的分离和提纯。     

KMnO4-Na2SO3化学发光体系测定对乙酰氨基酚

在酸性条件下, 对乙酰氨基酚对KMnO4-Na2SO3体系发光反应具有明显的增敏作用, 据此建立了流动注射化学发光测定对乙酰氨基酚的新方法. 在该发光体系中, 对乙酰氨基酚在1.0×10-8～1.0×10-5 g/mL范围内与发光强度呈良好的线性关系, 检出限(3R)为2.0 × 10-9 g/mL, 对对乙酰氨基酚进行11次平行测定, 其相对标准偏差为2.6%. 本方法应用于片剂中对乙酰氨基酚的测定, 并与药典方法进行对照.     

LaCl3和Fe2(SO4)3对化学镀Ni-W-P的影响

三氯化镧;硫酸铁;非晶沉积;LaCl3和Fe2(SO4)3对化学镀Ni-W-P的影响     

热力学模型研究KNO3-K2SO4-H2O和KNO3-KCl-H2O体系溶解度

用Pitzer-Simonson-Clegg热力学模型(PSC模型),分别拟合KCl-H2O、K2SO4-H2O、KNO3-H2O体系以及KNO3-K2SO4-H2O和KNO3-KCl-H2O体系水活度和溶解度实验数据,得到二元参数和三元离子相互作用参数,并以此计算3个二元盐水体系溶解度相图,及2个三元盐水体系在不同温度下的溶解度,结果表明计算值与实验值一致。     

Liquid-liquid extraction and recovery of indium using Cyanex 923

The extraction of In(III) from HCl, H₂SO₄, and HNO₃ media using a 0.20 mol l⁻¹ Cyanex 923 solution in toluene is investigated. In(III) is quantitatively extracted over a fairly wide range of HCl molarity while from H₂SO₄ and HNO₃ media the extraction is quantitative at low acid concentration. The extracted metal ion has been recovered by stripping with 1.0 mol l⁻¹ H₂SO₄. The stoichiometry of the In(III): Cyanex 923 complex is observed to be 1:2. The extraction of In(III) is insignificantly changed in diluents namely toluene, n-hexane, kerosene (160-200 °C), cyclohexane, and xylene having more or less the same dielectric constants, whereas, it decreases with increasing polarity of diluents such as cyclohexanone and chloroform. The extractant is stable towards prolonged acid contact and there is a negligible loss in its extraction efficiency even after recycling for 20 times. The extraction behavior of some commonly associated metal ions namely V(IV), Ti(IV), Al(III), Cr(III), Fe(III), Ga(III), Sb(III), Tl(III), Mn(II), Fe(II), Cu(II), Zn(II), Cd(II), Pb(II), and Tl(I) has also been investigated. Based on the partition data the conditions have been identified for attaining some binary separations of In(III). These conditions are extended for the recovery of pure indium from zinc blend, zinc plating mud, and galena. The recovery of the metal ions is around 95% with purity approximately 99%.     

P204-Cyanex 923混合溶剂萃取铟

磷酸;P204-Cyanex 923混合溶剂萃取铟     

Three-phase extraction study of cyanex 923-n-heptane/H(2)SO(4) system

Phase behavior of the extraction system, Cyanex 923–heptane/H₂SO₄–H₂O has been studied. The third phase appeared at different aqueous H₂SO₄ concentration with varying initial Cyanex 923 concentration and temperature affects its appearance. Almost all of H₂SO₄ and H₂O are extracted into the middle phase. The H₂SO₄ concentration in the third phase increases with the increasing aqueous acid concentration (C_H2SO4,b) while the water content first increases and then reaches a constant value at C_H2SO4,b=11.3 mol l⁻¹. In the region of C_H2SO4,b higher than 5.2 mol l⁻¹, the composition of the middle phase is only related to the equilibrium concentration of H₂SO₄ in the bottom phase. H₂SO₄ and H₂O are transferred into the middle phase mainly by their coordination with Cyanex 923 when C_H2SO4,b is less than 11.3 mol l⁻¹. When C_H2SO4,b is higher than 11.3 mol l⁻¹, excess H₂SO₄ is solubilized into the polar layer of the aggregates. In the region considered, the extracted complex changes from C923 · H₂SO₄ to C923 · H₂SO₄ · H₂O and then to C923 · (H₂SO₄)₂ · H₂O.     

磷酸三丁酯—钛—钽试剂第三相的形成与应用

本文研究了强酸性介质中，磷酸三丁酯萃取体系（ＴＢＰ．ＨＡ）第三相的形成条件；探讨了ＴＢＰ．ＨＡ对钛的萃取行为；建立了ＨＣｌＯ４－Ｈ２ＳＯ４介质中，利用ＴＢＰ．ＨＡ第三相萃取，然后用ＩＣＰ－ＡＥＳ温室痕量钛的方法。结果表明，由于第三相体积小，对钛有较高的富集倍数，降低了分析的检出限，用ＩＣＰ－ＡＥＳ检测，可以消除基体及其他大部分元素对测定的干扰，测定钛的回收率在９７％－１０１％。利用本法对钢样标准物     

Solubility in the systems Rb2SO4-H2SO4-H2O and Cs2SO4-H2SO4-H2O at 25°

Conclusions The solubility of rubidium and cesium sulfates in aqueous solutions of sulfuric acid was studied at 25°. Rubidium sulfate forms the compounds 3Rb₂SO₄· H₂SO₄, Rb₂SO₄ · H₂SO₄, Rb₂SO₄·3H₂SO₄ and Rb₂SO₄·7H₂SO₄ with sulfuric acid, while cesium sulfate forms the compounds Cs₂SO₄·H₂SO₄; Cs₂SO₄·3H₂SO₄ and Cs₂SO₄ · 7H₂SO₄.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 6, pp. 1166–1170, June, 1968.     

Extraction Behaviour of Cyanex‐923 and Cyanex‐471X Towards the Rhodium(III) from Bromide Media and Its Separation from other Platinum Metals

The extraction of Rh(III) from bromide media with Cyanex‐923 and Cyanex‐471X in toluene was studied. The quantitative extraction of Rh(III) with extractants was found by studying the different parameters like, hydrobromic acid concentration, extractant concentration, diluents and effect of temperature on extraction. The optimum condition was [HBr] = 1.0–1.5 moll^?1, [SnCl₂] = 0.2 moll^?1 with [Cyanex‐923] = 0.15 moll^?1, while it was [HBr] = 1.5–2.0 moll^?1, [SnCl₂] = 0.4 moll^?1 with [Cyanex‐471X] = 0.8 moll^?1 in toluene. The quantitative extraction was observed only in the presence of SnCl₂ for both extractants. The complete recovery of Rh(III) from the Cyanex‐923 extracted organic phase was observed with the 1:1 mixture of (4.0 moll^?1 HCl + 2.0 moll^?1 HNO₃), and that with the Cyanex‐471X extracted organic phase was found with 1:1 mixture of (2.0 moll^?1 H₂SO₄ + 1.0 moll^?1 KMnO₄). Stoichiometric ratio of Rh(III) with both extractants was 1:1. The proposed methods were employed for extraction and separation of Rh(III) from other platinum metal ions and also for recovery of Rh(III) from a synthetic solution of spent autocatalysts.     

273 K下Na2CO3-Na2SO4-Na2B4O7-H2O四元体系介稳相平衡的实验研究

采用等温蒸发法研究了四元体系Na2CO3-Na2SO4-Na2B4O7-H2O在273 K时的介稳相平衡及平衡液相的密度. 利用溶解度数据绘制了该四元体系273 K下的相图. 研究结果表明, 该四元体系有异成分复盐2Na2SO4·Na2CO3形成. 相图中有2个共饱点、5条单变量曲线和4个结晶相区. 4个结晶相区分别为盐Na2CO3·10H2O, Na2SO4·10H2O, Na2B4O7·10H2O和2Na2SO4·Na2CO3的结晶区. 复盐2Na2SO4·Na2CO3同时存在于包含Na2CO3-Na2SO4-H2O三元体系的其它四元体系或高元体系中. 在273 K介稳平衡相图中, 碳酸钠以Na2CO3·10H2O形式析出; 硫酸钠以Na2SO4·10H2O的形式析出; 硼酸钠的完整分子式为Na2B4O5(OH)4·8H2O. Na2CO3对Na2B4O7有盐析作用.     

Solvent extraction of zinc from sulphate leaching solution of a sulphide-oxide sample using D2EHPA and Cyanex 272

Solvent extraction of zinc from sulphate leach solution obtained from the treatment of a sulphide-oxide sample, was investigated using D2EHPA and Cyanex 272 diluted in kerosene in a batch reactor. According to the results, D2EHPA exhibited the higher extraction efficiencies than Cyanex 272 at the organic/aqueous ratio of 1:1. The optimum concentration and pH for D2EHPA and Cyanex 272 were distinguished to be 0.5?mol/L and 2.5, and 0.035?mol/L and 3.5, respectively. Under these conditions, extraction efficiency was found to be ～75% for D2EHPA against 41% for Cyanex 272. The plot of log D versus log [D2EHPA] confirmed the presence of 1 mole D2EHPA in dimeric form for 1 mole Zn in the extraction system. Thermodynamic data showed that the zinc extraction process is endothermic. For D2EHPA, two-stage simulated counter-current extraction experiments were performed on the basis of the McCabe-Thiele diagram and the extraction percentage of zinc was found to be about 88%. The synergistic effect of Cyanex 272 and TBP with D2EHPA was particularly investigated. It was found that the mixture of 80% D2EHPA and 20% Cyanex 272 exhibited the best synergistic effect for Zn-extraction with a synergistic coefficient of 1.04.     

Kinetics of Cerium(IV) Extraction from H(2)SO(4)-HF Medium with Cyanex 923

Studies of the extraction kinetics of cerium(IV) from H(2)SO(4)-HF solutions with Cyanex 923 in n-heptane have been carried out using a constant interfacial area cell with laminar flow. The experimental hydrodynamic conditions were chosen so that the contribution of diffusion to the measured rate of reaction was minimized. The data were analyzed in terms of pseudo-first order constants. The results were compared with those of the system without HF. It was concluded that the addition of HF reduces the activation energy for the forward rate from 46.2 to 36.5 kJ mol(-1) while it has an opposite effect on the activation energy for the reverse process(the activation energy increased from 23.3 to 90.8 kJ mol(-1)). Thus, HF can accelerate the rate of cerium(IV) extraction. At the same time, the extraction rate is controlled by a mixed chemical reaction-diffusion rather than by a chemical reaction alone. A rate equation has also been obtained.