气相色谱端值法测定稀溶液的气液平衡

本文提出了一种由气相色谱测定的γ_1~(∞)和(dln γ_1/dx_1)x_1→∞推算稀溶液气液平衡的方法。经较严格的推导, 得到(dlnγ_1/dx_1)x_1→∞的新测定公式; 与现有公式比较, 本文式更严格、具一般性,也更易于应用。将所得公式用于确定稀溶液活度系数模型参数, 进而推算气液平衡, 与直接测定值相比较, 得到了满意的结果。     

气相色谱端值法测定稀溶液的气液平衡

本文提出了一种由气相色谱测定的γ_1~(?)和(dln γ_1/dx_1)x_1→∞推算稀溶液气液平衡的方法。经较严格的推导,得到(dlnγ_1/dx_1)x_1→∞的新测定公式;与现有公式比较,本文式更严格、具一般性,也更易于应用。将所得公式用于确定稀溶液活度系数模型参数,进而推算气液平衡,与直接测定值相比较,得到了满意的结果。     

聚合物-溶剂-非溶剂三元相图的计算

改进了Pouchly提出的Flory-Huggins半经验展开式,详细推导了相应的计算三元相图中双结点溶解度曲线(Binodal线)和亚稳均相极限线(Spinodal线)的方程;计算了非溶剂和溶剂的相互作用参数g₁₂、溶剂和醋酸纤维素的相互作用参数g₂₃同时依浓度变化的三元相图。结果表明:新的Flory-Huggins方程更具有普适性。     

气液色谱法测量芳烃在芳烃衍生物中的活度系数

用气液色谱法测量了C_6～C_8芳烃在芳烃衍生物中的无限稀活度系数。以Hildebrand-Scatchard-Flory-Huggins公式进行处理,得到了非极性或微极性溶剂的溶解度参数δ,以修正的Hildebrand-Scatchard-Flory-Huggins公式进行处理,得到了芳烃溶质与各极性溶剂相互作用常数ι_(12)。     

气液色谱法测定二苯甲酮与二苯胺的相互作用参数及二苯甲酮与某些芳烃的分子络合常数

本文包括两部分内容:(1)运用三元系的Flory-Huggins公式,测定二苯甲酮与二苯胺的相互作用参数;(2)以联苄为参考溶剂,测定某些芳烃与络合溶剂二苯甲酮的分     

氨基酸在甲醇-水混合溶剂中粘度的研究

报导了在293.15及298.15 K下, 氨基乙酸和DL-氨基丙酸在甲醇-水混合溶剂中的密度及粘度数据; 计算了在无限稀释条件下, 这些体系中氨基酸的粘度B系数及偏摩尔体积。实验结果表明: 在甲醇-水的质量比值(W_B)分别约为0.15及0.25处, 两种氨基酸的B系数均出现极小值。讨论了氨基酸的引入对溶剂结构的影响; 并应用流动过渡状态理论计算了两种氨基酸在甲醇水溶液中的流动活化参数。     

气液色谱法研究二元混合固定液的无限稀活度系数

用气液色谱法测定若干烃类溶质在二元混合固定液中的无限稀活度系数,所研究的二元混合液为具有不同极性的四种类型:(1)正廿二烷-正十六烷;(2)邻苯二甲酸二壬酯-角鲨烷;(3)环丁砜-碳酸丙烯酯;(4)环丁砜-己二腈。用最小二乘法拟合三元系的Flory-Huggins公式,得到各种相互作用参数。     

二氧化碳-甲苯体系的气-液平衡研究

采用了改进的Novak和Conway气体溶解度实验装置,在低压下测定了298.15K,303.15K和316.15K时二氧化碳在甲苯中的溶解度,回归得到了常压下Henry常数与温度的关联式。借助于实测的溶解度数据,求得了不同温度下P-R方程中的二元作用参数δ_(12),推算了不同温度下,该体系的高压气-液平衡数据,温度范围从298K到477K,压力从常压下推算到15.3MPa。推算值与文献值的一致,说明我们的实验数据和从已知温度、总压推算二元系x、y的方法是合理的。同时,用R-R方程计算了CO_2在C_(?)H_(?)CH_3中的偏摩尔体积。     

正庚烷-甲苯-苯酚三元系统氣液平衡计算

应用一种新型的气液平衡器测定了正庚烷-甲苯,正庚烷-苯酚系统的平衡数据。然後以正庚烷-甲苯、正庚烷-苯酚、甲苯-苯酚等三个二元系统数据按van Laar(two suffix)公式推出正庚烷-甲苯-苯酚三元系统的气液平衡。推算结果基本上与实验结果相符合。该三元系统中正庚烷和甲苯间相对挥发度的对数值与苯酚浓度(分子百分数)变化呈直线关系,且不同浓度正庚烷,甲苯的相对挥发度直线均相交於一点,由此获得了从二元系统平衡数据推算该三元系统气液平衡新的简便方法。     

溶剂-导体界面电子转移溶剂重组能的球-界面模型

在连续介质理论基础上, 根据热力学基本原理, 用一个外加电场Eex将非平衡态2[Enon2, Dnon2]变成约束平衡态[E*2, D*2], 推导出了正确普适的溶剂重组能公式. 基于球-界面近似, 推导出了正确的溶剂-导体界面电子转移溶剂重组能公式. 和Marcus的公式相比, 本文的结果多了(εs-εop)/(εop(εs-1))因子. 对极性溶剂, 预测的溶剂重组能约为Marcus模型所得结果的一半. 以C343(Coumarin 343)-TiO2体系为算例, 计算了溶剂重组能并与实验值进行了比较.     

Liquid-liquid phase transitions in supercooled water studied by computer simulations of various water models

Liquid-liquid and liquid-vapor coexistence regions of various water models were determined by Monte Carlo (MC) simulations of isotherms of density fluctuation-restricted systems and by Gibbs ensemble MC simulations. All studied water models show multiple liquid-liquid phase transitions in the supercooled region: we observe two transitions of the TIP4P, TIP5P, and SPCE models and three transitions of the ST2 model. The location of these phase transitions with respect to the liquid-vapor coexistence curve and the glass temperature is highly sensitive to the water model and its implementation. We suggest that the apparent thermodynamic singularity of real liquid water in the supercooled region at about 228 K is caused by an approach to the spinodal of the first (lowest density) liquid-liquid phase transition. The well-known density maximum of liquid water at 277 K is related to the second liquid-liquid phase transition, which is located at positive pressures with a critical point close to the maximum. A possible order parameter and the universality class of liquid-liquid phase transitions in one-component fluids are discussed.     

Liquid-vapor and liquid-liquid phase equilibria of the Brodholt-Sampoli-Vallauri polarizable water model

Liquid-vapor and liquid-liquid phase equilibria of the polarizable Brodholt-Sampoli-Vallauri water model have been investigated by Gibbs ensemble Monte Carlo computer simulations. The coexisting liquid and vapor densities and energy of vaporization of the model is found to be in a reasonable agreement with experimental data in the entire temperature range of liquid-vapor coexistence. The critical temperature and density of the model are found to be 615 K and 0.278 gcm(3), respectively, close to the experimental values of 647.1 K and 0.322 gcm(3). In the supercooled state two distinct liquid-liquid coexistence regions are observed. The existence of liquid-liquid phase separation of a polarizable water model is demonstrated for the first time.     

Some Properties of a Model Liquid of C 60 Buckyballs

Utilizing the results of published simulations for the liquid C 60 phase using a model of rigid C 60 molecules, it is pointed out that the liquid phase has a critical compressibility ratio Z c = p c /( c k B T c ) in terms of the usual critical thermodynamic variables (critical pressure p c , critical density c and critical temperature T c ), of 0.32. This is to be compared with the value 0.29 for the heavy condensed rare gases Ar, Kr and Xe, in spite of their much lower T c , and with the prediction of 0.27 from Dieterici's phenomenological equation of state. The global shape of the coexistence curve, as embodied in the behaviour of the normalized difference density ( l m g )/ c versus the average density ( l + g )/2 c , where l and g are the liquid and the gas densities, respectively, is also consistent with the shape of the coexistence curve of insulating fluids. Going beyond the assumption of rigid C 60 molecules has interesting consequences on the stability and observability of the liquid phase, and those effects are discussed.     

Monte Carlo simulations of squalane in the Gibbs ensemble

We investigate the liquid–vapour coexistence curve of 2,6,10,15,19,23-hexamethyltetracosane (squalane) near the critical point with a new Lennard–Jones parameter set and compare our results to existing simulation data as well as to recent experimental vapour pressure data. Comparison of the liquid–vapour coexistence curve to previous simulation data reveals that this new force field, which includes tail corrections to the truncation of the non-bonded interactions increases the liquid density. We determine the critical temperature to 829 K and 825 K (with roughly 1% error) for two different system sizes, 72 and 108 molecules, and the critical density to 0.211 g/cm³ and 0.228 g/cm³, respectively. We extrapolate experimental vapour pressure data by use of Antoine's law to the temperature range covered by simulation and yield good agreement between simulation and experiment. We note that the vapour pressure in simulation is essentially governed by the ideal vapour pressure.     

Simple model of membrane proteins including solvent

We report a numerical simulation for the phase diagram of a simple two-dimensional model, similar to the one proposed by Noro and Frenkel [J. Chem. Phys. 114, 2477 (2001)] for membrane proteins, but one that includes the role of the solvent. We first use Gibbs ensemble Monte Carlo simulations to determine the phase behavior of particles interacting via a square-well potential in two dimensions for various values of the interaction range. A phenomenological model for the solute-solvent interactions is then studied to understand how the fluid-fluid coexistence curve is modified by solute-solvent interactions. It is shown that such a model can yield systems with liquid-liquid phase separation curves that have both upper and lower critical points, as well as closed loop phase diagrams, as is the case with the corresponding three-dimensional model.     

Pressure effects on the transitions between disordered phases in supercooled liquid silicon

We investigate the pressure effects on the transitions between the disordered phases in supercooled liquid silicon through Monte Carlo simulations and efficient methods to compute free energies. Our calculations, using an environment dependent interatomic potential for Si, indicate that at zero pressure the liquid-liquid phase transition, between the high density liquid and the low density liquid, occurs at a temperature 325K below melting. We found that the liquid-liquid transition temperature decreases with increasing pressure, following the liquid-solid coexistence curve. As pressure increases, the liquid-liquid coexistence curve approaches the region where the glass transition between the low density liquid and the low density amorphous takes place. Above 5 GPa, our calculations show that the liquid-liquid transition is suppressed by the glassy dynamics of the system. We also found that above 5 GPa, the glass transition temperature is lower than that at lower pressures, suggesting that under these conditions the glass transition occurs between the high density liquid and the high density amorphous.     

The liquid–liquid coexistence curves of {x dimethyl adipate + (1 − x) n-octane} and {x dimethyl adipate + (1 − x) n-nonane} in the critical region

The liquid–liquid coexistence curves of (dimethyl adipate + n-octane) and (dimethyl adipate + n-nonane) have been determined within about 10 K from the critical temperatures, from which the critical amplitudes and the critical exponents are deduced. The critical exponents corresponding to the coexistence curve β are consistent with the 3D-Ising values. The experimental results have been analyzed to determine Wegner-correction terms and to discuss the asymmetric behaviour of the diameters of the coexistence curves by the complete scaling theory. Molar mass-dependences of the critical amplitude and the critical volume fraction have been shown to be consistent with the theoretical prediction.     

Isomolar semigrand ensemble molecular dynamics: development and application to liquid-liquid equilibria

An extended system molecular dynamics method for the isomolar semigrand ensemble (fixed number of particles, pressure, temperature, and fugacity fraction) is developed and applied to the calculation of liquid-liquid equilibria (LLE) for two Lennard-Jones mixtures. The method utilizes an extended system variable to dynamically control the fugacity fraction xi of the mixture by gradually transforming the identity of particles in the system. Two approaches are used to compute coexistence points. The first approach uses multiple-histogram reweighting techniques to determine the coexistence xi and compositions of each phase at temperatures near the upper critical solution temperature. The second approach, useful for cases in which there is no critical solution temperature, is based on principles of small system thermodynamics. In this case a coexistence point is found by running N-P-T-xi simulations at a common temperature and pressure and varying the fugacity fraction to map out the difference in chemical potential between the two species A and B (mu(A)-mu(B)) as a function of composition. Once this curve is known the equal-distance/equal-area criterion is used to determine the coexistence point. Both approaches give results that are comparable to those of previous Monte Carlo (MC) simulations. By formulating this approach in a molecular dynamics framework, it should be easier to compute the LLE of complex molecules whose intramolecular degrees of freedom are often difficult to properly sample with MC techniques.     

Phase behavior and local structure of a binary mixture in pores: mean-field lattice model calculations for analyzing neutron scattering data

We investigate the phase behavior of an asymmetric binary liquid A-W mixture confined between two planar homogenous substrates (slit pore). Molecules of species W interact preferentially with the solid walls via a long-range potential. Assuming nearest-neighbor attractions between the liquid molecules, we employ a lattice-gas model and a mean-field approximation for the grand potential. Minimization of this potential yields the density profiles of thermodynamically stable phases for fixed temperature, chemical potentials of both species, pore width and strengths of attraction. This model is used to analyze experimental small-angle neutron-scattering (SANS) data on the microscopic structure of the binary system isobutyric acid (iBA)+heavy water (D2O) inside a mesoscopic porous matrix (controlled-pore glass of about 10 nm mean pore width). Confinement-independent model parameters are adjusted so that the theoretical liquid-liquid coexistence curve in the bulk matches its experimental counterpart. By choosing appropriate values of the pore width and the attraction strength between substrates and water we analyze the effect of confinement on the phase diagram. In addition to a depression of the liquid-liquid critical point we observe surface induced phase transitions as well as water-film adsorption near the walls. The temperature dependence of the structure of water-rich and iBA-rich phases of constant composition are discussed in detail. The theoretical predictions are consistent with results of the SANS study and assist their interpretation.     

硝基苯与正十六烷二元溶液在临界区域的浊度

测量了硝基苯与正十六烷二元溶液在临界区域不同波长及温度下的浊度, 结合与关联长度、渗透压缩系数、共存曲线有关的三个指前因子(x0, ξ0, B)的比例关系: R=ξ0[B^2/(4kBTcx0)]^1^/^3(kB和Tc分别为玻尔兹曼常数与临界温度)及R的理论值(0.65-0.67), 用Ornstein-Zernike方程拟合浊度-温度-波长数据, 得到临界指数γ与ν, 在误差范围内与值一致。将γ与ν固定在理论值1.241和0.63, 求得ξ0为0.168nm(R=0.65)和0.174nm(R=0.67), x0为2.81×10^-^9m^3.J^-^1(R=0.65)和2.85×10^-^9m^3.J^-^1(R=0.67)。