正丁醇/正戊醇+JP-10二元体系的体积性质

在常压下测定了298.15 K时正丁醇/正戊醇+挂式四氢双环戊二烯(C₁₀H₁₆, JP-10)二元体系的黏度和密度. 根据Eyring液体黏性流动理论, 关联了二元体系的黏滞性活化参数, 结果表明, 焓驱动起主要作用. 利用密度数据计算了醇+JP-10二元体系的超额摩尔体积、 超额偏摩尔体积、 表观摩尔体积及偏摩尔体积等体积性质, 结果表明此二元体系的超额摩尔体积为正值.     

直链烷烃与JP-10混配二元体系的体积性质

测定了正壬烷、 十一烷、 十二烷、 十三烷和十四烷5种正构烷烃与挂式四氢双环戊二烯(C₁₀H₁₆, JP-10)组成的二元体系在293.15, 298.15, 303.15和313.15 K下的黏度和密度. 利用所得实验数据分别计算了各个二元体系的体积性质, 从分子结构和分子间相互作用角度讨论了二元体系体积性质的变化规律. 根据Eyring液体黏性流动理论, 关联了二元体系的黏滞性活化参数. 结果表明, 焓驱动居于主导地位.     

N-甲基哌嗪与乙酸乙酯、乙酸丁酯二元混合体系在298.15～313.15K的体积及黏度性质

测定了N-甲基哌嗪+乙酸乙酯和N-甲基哌嗪+乙酸丁酯2个二元混合体系在298.15,303.15,308.15和313.15 K的密度和黏度数据,并计算了N-甲基哌嗪+酯二元混合体系的超额摩尔体积(VEm)和黏度偏差(Δη),用Redlich-Kister多项式关联了二元体系的超额摩尔体积与组成的关系,用4个半经验公式关联黏度数据并关联了二元体系的黏滞性活化参数.结果表明,N-甲基哌嗪+乙酸乙酯和N-甲基哌嗪+乙酸丁酯二元体系在所测温度范围内的超额摩尔体积为正值,黏度偏差为负值,且二元混合体系在混合过程中焓驱动居于主导地位.     

对甲氧基苯甲醛与N,N-二甲基甲酰胺密度黏度的测定与关联

在常压,298.15K~353.15K条件下,采用U形振动管密度计测定了对甲氧基苯甲醛-N,N-二甲基甲酰胺二元物系的密度,采用乌氏黏度计测定其黏度;并由密度和黏度数据分别计算了该二元物系超额摩尔体积VE和混合黏度的变化Δη.在不同的温度和组成下超额摩尔体积和混合黏度的变化都是负值,同时对不同温度下的超额摩尔体积与组成的关系以及混合黏度的变化与组成的关系都按Redlich-Kister方程进行了拟合,计算值与实验值的最大标准偏差小于7%.     

二元体系C6H6-DMF在293.15 K下的体积性质

利用Anton Paar DMA4500振动管密度计, 测量了293.15 K时二元体系C6H6-DMF(苯-N,N-二甲基甲酰胺)溶液的密度, 利用最小二乘法确立了溶液密度与组成的函数关系. 利用密度数据分别计算了二元体系中C6H6和DMF的表观摩尔体积, 并利用非线性最小二乘拟合法, 分别拟合得到了优化的C6H6和DMF的表观摩尔体积和摩尔分数的函数关系, 以及C6H6和DMF的表观摩尔体积和质量分数的函数关系. 通过对函数关系的极限运算得到了C6H6和DMF的标准偏摩尔体积和摩尔体积. 此外, 还计算了不同组分下体系的超额摩尔体积, 数据可用四参数Redlich-Kister方程很好地关联拟合, 得到方程系数及体系的超额摩尔体积极值位置.     

二元体系C6H5CH3-DMF在293.15 K时的体积性质

利用Anton Paar DMA4500振动管密度计测量了293.15 K时二元体系甲苯-N,N-二甲基甲酰胺(C6H5CH3-DMF)在C6H5CH3(摩尔分数0~1)中的溶液密度, 利用最小二乘法关联了溶液密度与组成的函数关系, 关联精度为±0.005 kg/m3. 通过密度数据分别计算了二元体系中C6H5CH3和DMF的表观摩尔体积, 并利用非线性最小二乘拟合法, 分别拟合得到了优化的C6H5CH3和DMF的表观摩尔体积和摩尔分数的函数关系, 以及C6H5CH3和DMF的表观摩尔体积和质量分数的函数关系. 通过对函数关系的极限运算得到了C6H5CH3和DMF的极限偏摩尔体积、标准偏摩尔体积和摩尔体积. 还计算了不同组分下体系的超额摩尔体积, 数据可用四参数Redlich-Kister方程关联拟合得到方程系数. 计算关联了C6H5CH3和DMF的超额偏摩尔体积与摩尔分数的关系. 由三参数多项式极限法得到组分的极限超额偏摩尔体积值与Redlich-Kister系数法得到的值在误差范围内一致.     

咪唑离子液体+1,2-丙二醇/1-丙醇二元体系在多温下的物理化学性质和超额性质

本文测定了温度288.15～333.15 K和常压下溴化1-己基/辛基-3-甲基咪唑离子液体([C_6mim]Br/[C_8mim]Br)+1,2-丙二醇/1-丙醇二元体系的密度(ρ)、折光率(nD)和黏度(η),计算获得了超额摩尔体积(V_m~E)和折光率偏差(Δn_D),并用Redlich-Kister方程对衍生性质数据进行拟合.密度、折光率和黏度值随组成的变化用多项式方程进行了拟合,讨论了醇、离子液体以及温度对二元体系物化性质的影响.     

用FRKS状态方程预测三元系超额体积

利用改进的立方状态方程－ＦＲＫＳ方程，并以二元互作用函数代替单一数值的二元互作用参数关联二元系的超额体积，得到二元参数，在不引入任何三元参数的情况下，直接用组分二元系作用函数的引入预测三元系的超额体积，对十二个三元系及其组分二元系的计算结果表明，二元互作用函数的引入明显提高了二元超额体积的拟合精度，从而使状态方程法能精确地预测三元系的超额体积。     

线形高分子共混熔体的平衡态性质

采用分子动力学模拟的方法研究了长短链二元线形高分子共混熔体在平衡态下的结构、动力学性质以及黏度.结果表明:共混对组分的结构性质没有影响,共混体系中2组分各自的均方回转半径以及均方末端距均与单分散体系中相同;共混显著地影响动力学性质,即长链在共混体系中的扩散和松弛会加快,相反,短链的扩散和松弛则会变慢;另外,该共混体系的黏度符合简单的线性叠加.     

气相色谱灰色分析体系中未知组分保留指数的预测

提出在部分组分已知的气相色谱灰色体系中,利用已知组分的保留指数和保留时间推算死时间和正构烷烃的保留时间,再计算未知组分保留时间的方法,结果显示,在已知组分不是太少的情况下,该方法计算的死时间和正构烷烃的保留时间与实验值吻合,预测的保留指数也有较高的精度.     

Density,Viscosity and Volatility of Binary Mixtures of Isopropyl Ether and <Emphasis Type="Italic">exo</Emphasis>-Tetrahydrodicyclopentadiene

Measurements of density, viscosity and vapor pressure for binary mixtures of exo-tetrahydrodicyclopentadiene (JP-10) with isopropyl ether are reported at temperatures of (293.15, 298.15, 303.15, 308.15, and 313.15) K over the entire composition range. The excess molar volumes, viscosity deviation and excess Gibbs energies of activation for the binary systems were calculated from the experimental values and fitted with the Redlich–Kister equation. Isopropyl ether was added to enhance the vapor pressure of JP-10. Experimental vapor pressure data were correlated by the Antoine equation. Several semi-empirical equations were used to correlate the viscosity data. The McAllister equation gives relatively satisfactory results for the correlation. The experimental and correlated data could be used in the development of models for mixtures of hydrocarbons with oxygenates.     

Excess thermodynamics properties of propyl propanoate+hexane+cyclohexane at 298.15 K

Summary In this paper we present excess molar volumes and excess molar enthalpies of binary and ternary mixtures containing propyl propanoate, hexane and cyclohexane as components at 298.15 K. Excess molar volumes were calculated from the density of the pure liquids and mixtures. The density was measured using an Anton Paar DMA 60/602 vibrating-tube densimeter. Excess molar enthalpies were obtained using a Calvet microcalorimeter     

Volumetric Properties for Binary and Ternary Mixtures Containing Benzyl Alcohol,Ethyl Butyrate and Diethyl Malonate at <Emphasis Type="Italic">T</Emphasis> = (293.15–313.15) K and <Emphasis Type="Italic">p</Emphasis> = 0.087 MPa

The densities of binary and ternary mixtures of benzyl alcohol + ethyl butyrate and/or diethyl malonate were measured at T = (293.15–313.15) K and p = 0.087 MPa. From these data, the excess molar volumes, partial molar volumes, excess partial molar volumes, partial molar volumes at infinite dilution, thermal expansion coefficients and their excess values were calculated. The Redlich–Kister equations were fitted to the excess molar volumes data. The results show that the excess molar volumes for all considered binary and ternary systems are negative and decrease with increasing temperature. The same behavior was observed for the excess thermal expansion coefficients. Data for excess volumes in ternary system were fitted with the Nagata–Tamura and Cibulka models for which the Cibulka equation showed better fitting. The intermolecular interactions between molecules in these mixtures are discussed and explained based on these experimental data.     

Volumetric properties of {PEG 200 (or 300) (1) + water (2)} mixtures at several temperatures and correlation with the Jouyban–Acree model

Molar volumes and excess molar volumes were investigated from density values for {PEG 200 (1) + water (2)} and {PEG 300 (1) + water (2)} binary mixtures at temperatures from 278.15 to 313.15 K. Both systems exhibit negative excess volumes probably due to increased interactions such as hydrogen bonding and/or large differences in molar volumes of components. Volume thermal expansion coefficients were also calculated for both binary mixtures and pure solvents. The Jouyban–Acree model was used for density and molar volume correlations of the studied mixtures at different temperatures. The mean relative deviations between experimental and calculated density data were 0.02% and 0.04%, for aqueous mixtures of PEG 200 and PEG 300, respectively; whereas the corresponding values for molar volume data were 1.76% and 2.72%.     

The bulk properties of ethylene glycol-dimethylsulfoxide mixtures over the temperature range 278–323 K at <Emphasis Type="Italic">p</Emphasis> = 0.1 MPa

The densities of ethylene glycol-dimethylsulfoxide binary mixtures were measured over the temperature range 278–323.15 K at atmospheric pressure using a vibrational densimeter. The excess molar volumes, apparent molar volumes, partial molar volumes of mixture components, volumetric thermal expansion coefficients, and partial molar volumetric thermal expansion coefficients were calculated. The excess molar volumes were described by the Redlich-Kister equation, and the partial molar volumes were calculated by two methods. The density-composition dependence contained a weak maximum, which disappeared as the temperature increased. The excess molar volumes were negative, and deviations from ideality increased as the temperature grew.     

Study of some volumetric and refractive properties of {PEG 300 (1) + ethanol (2)} mixtures at several temperatures

Molar volumes and excess molar volumes were investigated from measured density values for {PEG 300 (1) + ethanol (2)} binary mixtures at temperatures from 278.15 to 313.15 K. Both systems exhibit negative excess volumes probably due to increased interactions like hydrogen bonding and/or large differences in molar volumes of the components. Volume thermal expansion coefficients were also calculated for both binary mixtures and pure solvents. Refractive indices were also determined for all these non-aqueous mixtures and neat solvents at all temperatures. Furthermore, the Jouyban–Acree model was used for density, molar volume and refractive index correlations of the studied mixtures at different temperatures. The mean relative deviations between experimental and back-calculated density, molar volume and refractive index data were 0.07%, 0.99% and 0.01%, respectively.     

Vapor pressures and flash points for binary mixtures of tricyclo [5.2.1.0] decane and dimethyl carbonate

Bubble-point vapor pressures, equilibrium temperatures and flash points for binary mixtures of a high energy density hydrocarbon fuel, tricyclo [5.2.1.0^2.6] decane (JP-10), and dimethyl carbonate (DMC) were measured. Correlation between vapor pressures and equilibrium temperatures for each mixture was given by the Antoine equation. The binary system of JP-10 and DMC appears with very large positive deviations of vapor pressure from the Raoult's law. The experimental vapor pressures are correlated and the flash points are then predicted using Scatchard-Hildeband, Van Laar and Wilson models of liquid phase activity coefficients with satisfactory results.