水＋3-甲基吡啶＋溴化钠三元溶液动-静态光散射临界行为研究

对水＋3-甲基吡啶＋溴化钠三元电解质溶液的临界跨接行为的认识存在着争议. 部分研究认为由于三甲基吡啶的聚集, 体系存在从非经典的3D-Ising(三维伊辛)行为向经典的平均场行为的非单调跨接; 另一部分研究发现该体系符合3D-Ising临界行为, 并不存在跨接. 采用动-静态光散射研究了溴化钠, 3-甲基吡啶和水三元溶液的临界性质, 得到动态关联长度和静态关联长度, 发现动态关联长度和静态关联长度一致, 且在实验温度范围内(离临界温度0.01～25 K), 体系不违背3D-Ising行为, 也观测不到显著的临界跨接现象.     

用UV-Vis法研究聚乙烯醇水溶液的透明度

用紫外可见分光光度计(UV-vis)测试了聚乙烯醇(PVA)水溶液和盐溶液的透明度,研究了PVA醇解度、电解质和温度对PVA溶液透明度的影响.实验结果表明,UV-Vis法是一种简便可行的测定PVA溶液透明度的方法.     

多功能汽液平衡测定仪的研究

研制了一种多功能液平衡测定仪－－CS-Ⅱ型VLE测定仪，阐述了该仪器的设计思想，该仪器兼有沸点仪和平衡釜的特点和功能，作为沸点仪，它具有泵结构搅拌器，可适用于拟静态法；作为平衡釜,它具有新型的汽液相取样结构和液相区冷却功能，可适用于安全互溶体系、部分互溶体系和高沸点差体系VLE的测定，本文给出了有关详细的实验考核结果。     

原油馏分热导率的测定

建立了基于点热源比较瞬时法的热导率测量装置，该装置适合于非电解质和电解质溶液，并可以使实验快速进行，用该装置测定１２个原油分在不同温度下的热导率，克服了由于原油中存在极性组分而影响实验结果的困难，关联了馏分热导率与温度，以及馏分的平均分子量，密度，运动粘度和折射率等基本物理性质之间的关系，结果满意。     

盐湖盐类水溶液298.15K时稀释热和表观摩尔焓的研究

有关溶稀释热方面的研究报导很多,例如等溶液的稀释热均已有文献值．但全是采用分批式量热法研究部分间断浓度范围内的稀释热，数据设有连续性，很不全面．在稀释热理论估算方面，Pitier的半经验溶液理论能比较满意的解决一般浓溶液的稀释热估算问题，但文献只给出了某些多数，没有计算出具体的稀释热数据[6-9]，也没有将实验测定值与理论估算值相比较．基于Debye－Hckel理论推导出的烙极限公式[10-12]在溶液表观摩尔烂的研究中已得到广泛应用．但迄今没有一篇论文比较全面地将实验测定与Pitier理论和Debye－Hhdel极限公式相结合来研究溶…     

含锂水盐体系热力学性质研究:LiCl-MgCl~2-H~O体系渗透系数和活度系数的等压测定

25℃下,用等压法测定了单盐水溶液(浓度范围分别为0.5-19.8mol.kg^-1,0.3-6.0mol.kg^-1)以及混合水溶液(离子强度范围为0.6-19.4mol.kg^-1)的水活度和渗透系数,同时测定了LiCl的溶解度.该体系的实验等水活度线符合本工作推导出的Zdanovskii规则扩展式,用Gibbs-Duhem方程和改进的Mckay-perring方法计算了单盐和混合盐水溶液的活度系数.由本实验获得的渗透系数拟合了Pitzer单盐和混合作用参数,检验了Pitzer方程对该体系渗透系数、活度系数和溶解度预测的适用性.用Pitzer方程取本工作得到的参数计算的溶解度与文献实验值基本一致.     

合成盐湖卤水体系Li-Na-K-Mg-Cl-SO_4-H_2O25℃下的等压研究和离子相互作用模型的应用

根据我国青海一里坪和东台吉乃尔盐湖晶间卤水Li-Na-K-Mg-Cl-SO_4-H_2O体 系的组成制备了两种合成卤水储备溶液，采用等压法和改进的实验装置在25 ℃下 ，从稀释到溶液中溶质NaCl达到饱和的浓度范围，对合成卤水溶液进行了等压测定 ，确定了它们的水活度a_(H_2O)，和渗透系数ψ；比较了两种卤水的热力学性质及 其变化的规律，揭示了其天然卤水浓度差异的物理化学成因。用盐湖卤水体系离子 作用模型对水活度、渗透系数的计算值与本文的实验数据比较，对于一里坪和东台 合成卤水，渗透系数的标准偏差分别为0.0078和0.0145；用该模型计算了东台晶间 卤水，及其在25 ψ等温蒸发实验不同阶段的浓缩卤水中，离子强度从9.766到20. 52mol·kg~(-1)范围可能析出的盐类的饱和度，给出了其变化规律，并与文献的盐 类沉积和析盐顺序相比较，获得了合理一致的结果，从而证实了我们在Pitzer离子 相互作用模型基础上所发展的盐湖卤水体系模型对描述和预测复杂天然盐湖卤水体 系的热力学性质和蒸发析盐规律的适用性。     

含锂水盐体系热力学性质研究:LiCl-MgCl~2-H~O体系渗透系数和活度系数的等压测定

25℃下,用等压法测定了单盐水溶液(浓度范围分别为0.5-19.8mol.kg^-1,0.3-6.0mol.kg^-1)以及混合水溶液(离子强度范围为0.6-19.4mol.kg^-1)的水活度和渗透系数,同时测定了LiCl的溶解度.该体系的实验等水活度线符合本工作推导出的Zdanovskii规则扩展式,用Gibbs-Duhem方程和改进的Mckay-perring方法计算了单盐和混合盐水溶液的活度系数.由本实验获得的渗透系数拟合了Pitzer单盐和混合作用参数,检验了Pitzer方程对该体系渗透系数、活度系数和溶解度预测的适用性.用Pitzer方程取本工作得到的参数计算的溶解度与文献实验值基本一致.     

氯化钙/水-醇溶液稀释热

电解质溶液稀释热是溶液的重要热性质之一．由它可计算不同浓度下电解质的溶解热、表现相对摩尔焓、溶液中反应热和化合物生成热等．在电解质溶液理论研究中，稀释热也是重要的基础数据．由稀释热可推算溶液中组分的活度系数、渗透系数、相对偏摩尔焓及表观摩尔热容等[1-3]．在化工生产中，稀释热是化工过程能量计算不可缺少的数据．电解质水溶液稀释热已有不少研究[2，4]．但电解质混合溶剂体系稀释热报导甚少．随着加盐精馏技术、海水淡化技术等研究的进展，急需这方面数据．本文作者已报告了CaCl2／C2H5OH－H2O体系[5]和CaCl2／n－C…     

拟静态法测定混合溶剂的汽化热和汽化熵

讨论了沸点升高法测定混和溶剂化热和汽化熵的原理，并用拟静态法测定了乙醇－丙酮，并－四氯化碳和苯，甲苯三组混和溶剂在不同组成下的正常沸点，根据沸点数据求得了混和泶微分汽化热和汽化熵，实验结果表明，二元混和溶剂与理想溶液偏离不大时，其正常汽化熵符合Ｔｒｏｕｔｏｎ规则。     

Vapor pressure measurements on nonaqueous solutions. Part IV. HNC calculations using Friedman's cosphere overlap model

Vapor pressure data for solutions of various alkali metal and tetraalkylammonium salts in methanol at 25° and NaI solutions in ethanol, 2-propanol, and acetonitrile at 25° in the concentration range 0.04–1]<0.75 are used to show the applicability of the HNC integral equation method to nonaqueous electrolyte solutions. Friedman's model of overlapping cospheres is used to express the non-electrostatic part of the ion-interaction potential. Data analysis is based on the Rasaiah-Friedman algorithm for the calculation of g₊₊ and g_+– functions. After conversion from Lewis-Randall to the McMillan-Mayer system the measured osmotic coefficients of all electrolyte solutions can be reproduced with the help of the calculated correlation functions.     

An alternative methodology for determining transport parameters of electrolytes in mixed solvents from concentration cells,without prior knowledge of activity coefficients

An alternative methodology is described for the determination of transport parameters of electrolytes in nonaqueous or aqueous-organic solvents from concentration cells, which neither requires prior knowledge of electrolyte activity coefficients nor of any other thermodynamic function related to the latter. The reliability of this new procedure is tested against the older one, using solutions of KCl in (methanol+water) and LiCl in (1,4-dioxane+water) solvent mixtures, and the conditions for its applicability to any aqueous-organic or nonaqueous electrolyte are described.     

Prediction of solubilities of salts,osmotic coefficients and vapor–liquid equilibria for single and mixed solvent electrolyte systems using the LIQUAC model

The electrolyte model LIQUAC has been used up till now to predict osmotic coefficients, mean ion activity coefficients, the vapor–liquid equilibrium (VLE) behavior, the solubility of gases in single and mixed solvent electrolyte systems, and solubilities of salts in aqueous solutions. In this paper, the required expressions for the calculation of salt solubilities not only in aqueous systems, but also in organic solvents and water–solvent electrolyte systems were deduced in detail based on the LIQUAC model with a fixed reference state and thermodynamic relations. Four salts (NaCl, KCl, NH₄Cl and NaF) and two solvent (water and methanol) were selected to test the derived expressions. The results show that the LIQUAC model with a fixed reference state can be used to predict osmotic coefficients, solubilities of salts in aqueous solutions, vapor–liquid equilibria, and the solubilities of salts in water–organic solvent systems with strong electrolytes.     

Simultaneous separation of organomercury species by nonaqueous capillary electrophoresis using methanol containing acetic acid and imidazole

A simple and rapid nonaqueous capillary electrophoresis method for simultaneous separation of four kinds of mercury species, namely inorganic mercury, methylmercury, ethylmercury, and phenylmercury, is reported. The effective mobilities of organomercury in aqueous and nonaqueous electrolytes were compared. Imidazole was confirmed not only as a co-ion for the separation but also as an online complexing reagent for mercury species. The optimum conditions for separation were achieved by using methanol solvent containing 0.15 M acetic acid and 15 mM imidazole as electrolyte. The sensitive detection of mercury species was accomplished at 191 nm.     

Isopiestic study of the solutions of MnCl2, CoCl2 and NiCl2 in methanol and ethanol at 298.15 K

Osmotic coefficients of the solutions of three divalent transition metal chlorides (MCl₂; M = Mn, Co, Ni) in methanol and ethanol have been measured by isopiestic method at 298.15 K. Vapor pressures of the solutions have been evaluated from osmotic coefficients and their depression was used for qualitative deduction of the solute–solvent interactions occurring in these solutions. The osmotic coefficients have been correlated using local composition models (including electrolyte non random two liquid (e-NRTL), non random factor (NRF) and modified NRTL (mNRTL) models) and the Pitzer model. The capability of the considered models was compared on the basis of the standard deviation in osmotic coefficients. The models give reliable results in correlation of the osmotic coefficients. However, the results show that the Pitzer and the mNRTL models successfully correlate the osmotic coefficients, however e-NRTL and NRF models give larger standard deviations.     

Osmotic and activity coefficients in the binary solutions of 1-butyl-3-methylimidazolium chloride and bromide in methanol or ethanol at T = 298.15 K from isopiestic measurements

Osmotic coefficients of the binary solutions of two room-temperature ionic liquids (1-butyl-3-methylimidazolium chloride and bromide) in methanol and ethanol have been measured at T = 298.15 K by the isopiestic method. The experimental osmotic coefficient data have been correlated using a forth-order polynomial in terms of (molality)^0.5, with both, ion interaction model of Pitzer and electrolyte non-random two liquid (e-NRTL) model of Chen. The values of vapor pressures of above-mentioned solutions have been calculated from the osmotic coefficients. The model parameters fitted to the experimental osmotic coefficients have been used for prediction of the mean ionic activity coefficients of those ionic liquids in methanol and ethanol.     

Osmotic behavior of a Nafion membrane in methanol-water electrolyte solutions

In this paper, an experimental study was carried out in order to investigate the osmotic transport of methanol-water electrolyte solutions through a Nafion membrane. The experimental data indicated that the Nafion membrane showed the typical anomalous osmotic behavior of charged membranes. The influence of some relevant parameters, such as electrolyte concentration difference, weight fraction of methanol on solution, and nature of cation was considered. The results showed that the osmotic volume flow was decreased with the presence of methanol on solvent, but did not alter the anomalous osmotic behavior of the membrane.     

Thermodynamic studies of binary methanol and ethanol solutions of 1-dodecanol and 1-tetradecanol at 25°C

The osmotic coefficients of binary methanol and ethanol solutions of 1-dodecanol and 1-tetradecanol wer measured at 25°C up to 8 mol-kg^–1 in methanol and 5.5 mol-kg^–1 in ethanol. The activity coefficients of the solute were calculated from Bjerrum's relation. From the osmotic and activity coeficients the excess Gibbs energies of solution as well as the respective partial molar functions of solute and solvent and the virial pair interaction coefficients for the excess Gibbs energies were calculated. In addition, the difference in the Gibbs energy of solvation for the solvent in solution relative to the pure solvent was calculated, as well as the partial molar volumes and excess partial molar volumes of solutes at infinite dilution, and the coefficients of pairwise contributions to the excess volume were determined. The thermodynamic parameters obtained are discussed on the basis of solute-solvent and solute-solute interactions.     

Nonaqueous capillary electrophoresis-electrospray- mass spectrometry for the analysis of fluoxetine and its related compounds

The potential of nonaqueous capillary electrophoresis was investigated for the simultaneous separation of fluoxetine hydrochloride, its meta-isomer, and other related compounds. The resolution of these compounds was compared in aqueous and nonaqueous media. Baseline separation of the studied solutes required a buffer electrolyte solution composed of 25 mM ammonium acetate and 1 M acetic acid in acetonitrile, an applied voltage of 30 kV and a temperature of 20 degrees C. Selectivity was considerably affected by the nature of the solvent (water, methanol, and acetonitrile). Moreover, substituting acetate by formate in the background electrolyte resulted in migration time changes, which were attributed to an ion-pairing phenomenon. Finally, the method was successfully coupled on-line with electrospray ionization-mass spectrometry (ESI-MS) and allowed significant selectivity and sensitivity enhancement. The effect of ESI-MS parameters, such as nebulizing gas pressure, sheath liquid composition and flow rate, on resolution and method sensitivity was also discussed.     

Association studies of tetramethylguanidinium perchlorate and tetramethylguanidinium chloride in ethanol solutions at 25°C

Practical osmotic coefficients of ethanol solutions of tetramethylguanidinium perchlorate and tetramethylguanidinium chloride were determined by the isopiestic method at 25°C. The relations for the concentration dependences of practical osmotic coefficients, mean molal activity coefficients of solutes and for the excess Gibbs free energies of solutions and partial molal excess Gibbs free energies of solutes and solvents are given in analytical form. The results obtained are compared with those reported previously; in the case of tetramethylguanidinium perchlorate with its aqueous and methanol solutions, in the case of tetramethylguanidinium chloride with its aqueous solutions. The non-ideal behavior of the systems investigated is discussed on the basis of the structure of solute species, as well as on the nature of the solvent.