YO1.5—CaO—MgO系的热力学计算

由评估的实测相图数据。用最小二乘法对YO_(1.5)-CaO,CaO-MgO二元系进行了热力学优化和计算。计算结果表明,同前人工作相比本文报道的参数能更准确地描述YO_(1.5)CaO和CaO-MgO二元相图。计算的三元相图可望减少并指导YO_(1.5)-CaO-MgO三元系相平衡和热力学测定工作。     

Fe-P体系热力学再优化

基于最新的实验热力学数据和相图数据,采用CALPHAD技术对Fe-P体系进行热力学再优化.其中,溶液相(液相、α-Fe和γ-Fe)的Gibbs自由能用替换溶液模型描述,其余化合物(Fe3P、Fe2P、FeP、FeP2和FeP4)看作严格计量比化合物.整个优化过程在Thermo-Calc软件包中完成,优化所得热力学数据和相图信息与实验信息吻合较好,为Fe基合金和含P多元合金体系的进一步优化提供了一组自洽可靠的热力学参数.     

Zr-X(X=Li,Na,K,Sc,Hf)体系的二元相图理论研究

采用相图计算(CALPHAD:Calculation of phase diagrams)方法对Zr-X(X=Li,Na,K,Sc,Hf)5个二元体系进行了相图热力学研究.基于实验数据,通过热力学优化计算获得了一套描述液相及(αZr),(βZr),(Li),(Na),(K),(αSc),(βSc),(αHf)和(βHf)相的热力学参数.Zr-Li,Zr-Na和Zr-K体系中的气相视为理想气体.与实验相图数据对比发现,本文获得的热力学参数能够准确地描述实验相平衡数据.     

TmCl3-ACl（A=Na，K，Rb，Cs）体系相图的热力学优化计算

综合实验相图信息和热力学数据运用CALPHAD技术优化和计算了TmCl3-ACl体系的相图。液相的吉布斯全摩尔自由能采用新改进的用于短程有序体系的以近似似化学模型进行描述。借助计算机辅助分析，一系列的热力学函数被优化得到。计算的相图和热力学参数是热力学自恰一致的。     

La2O3掺杂对SrTiO3压敏电容双功能陶瓷显微结构及电性能的影响

用CALPHAD技术优化计算了稀土卤化物熔盐TbCl3-ACl(A=Li，Na，K，Rb，Cs)五个二元系相图以及其热力学性质。优化采用了短程有序-扩展似化学模型，得到了热力学性质和相图自洽一致的结果，并与相应的实验相图进行了比较，对其中差异的部分进行了分析和修正。讨论了热力学优化结果，并探讨了过剩热力学性质变化的规律和特征。     

TbCl3-ACl（A=Li，Na，K，Rb，Cs）相图的优化和计算

用CALPHAD技术优化计算了稀土卤化物熔盐TbCl3-ACl(A=Li，Na，K，Rb，Cs)五个二元系相图以及其热力学性质。优化采用了短程有序-扩展似化学模型，得到了热力学性质和相图自洽一致的结果，并与相应的实验相图进行了比较，对其中差异的部分进行了分析和修正。讨论了热力学优化结果，并探讨了过剩热力学性质变化的规律和特征。     

RECl3—CaCl2—LiCl（RE=La,Ce,Pr,Nd）三元相图的优化和计算机

基于对９个侧边二元系ＲＥＣｌ３－ＬｉＣｌ，ＲＥＣｌ３－ＣａＣｌ２－ＬｉＣｌ热力学数据和实验相图信息的评估、优化以及三元系相关热力学性质的分析，计算了ＲＥＣｌ３－ＣａＣｌ２－ＬｉＣｌ系列４个三元系相图，计算结果与实验相图吻合较好。     

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。     

硝酸盐型卤水体系的综合热力学模型与多温相图预测

硝酸盐型卤水是盐湖卤水、 硝酸盐工业、 废水处理中普遍遇到的电解质溶液体系. 硝酸盐具有极高的溶解度, 实现硝酸盐型复杂电解质体系物性和相平衡的精准热力学表达依然具有挑战性. 以煤化工废水的典型体系Na⁺//NO₃^- , Cl^-, SO₄^{2 -} -H₂O为对象, 以改进的eNRTL模型为基础, 由活度系数模型、 溶液物性模型、 物种热力学模型和固液相平衡模型构成了电解质体系的综合热力学模型. 利用二元体系的冰点、 饱和蒸汽压、 等压摩尔热容、 活度系数和渗透压系数等物性数据和三元体系等温相平衡数据, 采用多目标优化方法, 获得了表达研究体系的多温特性的12组液相特征参数和7个固相物种的热力学参数. 据此完成了3个二元体系、 3个三元体系等温相平衡的准确计算和三元、 四元完整相图的预测, 适用温度达到实验所及的全部温度范围(254.65~543.15 K); 适用浓度达到饱和程度, 其中NaNO₃的浓度高达226.88 mol/kg. 三元、 四元体系的多温相图预测结果与实验数据相吻合, 并给出了9个三元、 5个四元体系零变点的完整信息.     

LiF-CrF3二元系的热力学模拟

采用相图计算(CALPHAD)技术对LiF-CrF3体系进行了相图的优化计算.对液相分别采用置换熔体模型与缔合物模型进行描述,中间化合物Li3CrF6则采用准化学计量比化合物模型描述.模型参数的优化选取实验相平衡数据及第一性原理预测的数据,优化结果表明,缔合物模型比置换熔体模型更能准确地描述液相的实验相平衡数据.     

Phase behavior and structure formation in ternary blends: studies on blends of PVDF/PMMA/PVAC

The phase behavior of ternary blends was analyzed on the basis of the lattice approach. Both compatibilization and incompatibilization effects are predicted to occur depending on the relative magnitudes and the sign of the interaction parameters of the binary subsystems. Thermodynamic, structural and kinetic properties were investigated for a ternary model blend composed of poly(vinylidene fluoride), poly(methyl methacrylate) and poly(vinyl acetate). This particular ternary system is characterized by a specific symmertry with respect to the interactions in the binary subsystems. This symmetry affects both thermodynamic and structural properties. The experimentally determined interaction parameters were used to model the phase diagram on the basis of the lattice model: the theoretical phase diagram was found to be close to the experimental one. The crystallization processes were analyzed both for the binary and the ternary systems on the basis of a modified Turnbull–Fisher equation. The conclusions are that the properties of the ternary systems can be understood to a first approximation on the basis of those of the corresponding binary systems and the symmetry of the interactions.     

Al-Zn-Sn Phase Diagram X-ray diffraction study at various temperatures

Further studies of the ternary phase diagram Al-Zn-Sn have been carried out by X-ray diffraction at various temperatures and by thermodilatometry in order to confirm our earlier experimental results which have been refuted by some recent work based on thermodynamic optimization. These new results, in particular the change with temperature of the crystallized fraction for Al-Zn-Sn mixtures containing up to 31.5 mass% of tin, confirm our previous results on the existence of a significant retrograde miscibility of tin in a solid solution α′ss (in the temperature range 286 to 335°C) which protrudes into the ternary system starting from the Al-Zn binary up to a tin concentration of about 50 mass%. This disagreement between theory and experiment highlights the difficulties of a thermodynamic optimization approach based on solid state solubilities in the binary systems and on ternary liquidus data which disregards the ternary interaction parameters in the solid state. Besides, this experimental study highlights the difficulties in understanding the phenomena which depend on phase stabilities. This revised version was published online in July 2006 with corrections to the Cover Date.     

Isopiestic Determination of Water Activity on the System LiNO<Subscript>3</Subscript>+KNO<Subscript>3</Subscript>+H<Subscript>2</Subscript>O at 273.1 and 298.1 K

Water activities in the ternary LiNO₃+KNO₃+H₂O system and its sub-binary systems have been measured by the isopiestic method at 273.1 and 298.1 K. The measured results were treated by a Pitzer-Simonson-Clegg thermodynamic model, from which the predicted solubility isotherms were compared with the experimental results. Based on this comparison, the reliability of the measured results was discussed. The measured results help in predicting the phase diagram of the ternary system, as well as other multi-component systems based on the ternary system.     

A new molecular thermodynamic model for multicomponent Ising lattice

A new molecular thermodynamic model is developed for multicomponent Ising lattice based on a generalized nonrandom factor from binary system. Predictions of the nonrandom factor and the internal energy of mixing for ternary and quaternary systems match accurately with simulation results. Predictions of liquid-liquid phase equilibrium for ternary systems are in nearly perfect agreement with simulation results, and substantially improved from Flory-Huggins theory and the lattice-cluster theory. The model also satisfactorily correlates the experimental data of real ternary systems. The concise expression and the accuracy of the new model make it well suited for practical engineering applications.     

Phase diagrams of liquid-liquid equilibria for the systems water-phosphoric acid-solvent entrainer at 313.15 and 333.15 K

Liquid-liquid equilibria data have been determined for the ternary system of water + phosphoric acid + solvent entrainer (1,4-dimethylbenzene, 1,2-dichloroethane, and n-hexane) at 313.15 and 333.15 K. Experiments were carried out at atmospheric pressure using stirred and thermo-regulated cells. The ternary phase diagrams were obtained by the experimental solubility and tie-line data. The Othmer-Tobias equation was used to correlate the tie-line compositions. The measured liquid-liquid equilibrium data were compared with the non-random two liquid activity coefficient model. Root mean square deviations between experimental and calculated compositions were considered satisfactory. It was showed that the non-random two liquid model of all ternary systems presented very good satisfactory results with root mean square deviations so that this model was highly appropriate to calculate thermodynamic properties of the ternary solutions. The liquid-liquid equilibrium thermodynamic properties of water + phosphoric acid + solvent entrainer can be used in research on the nature of mixing behavior of the ternary system for molecular models and industrial applications in concentration the phosphoric acid aqueous solution.     

Liquid–liquid phase equilibrium of methanol + ethylbenzene + isooctane + ethanol system at 303 K

The phase equilibrium data for methanol + ethanol + isooctane systems were obtained at 303.15 K. Data for methanol + ethylbenzene + isooctane system were taken from literature. The effect of ethanol addition on the system equilibrium was investigated at the same temperature. The distribution curves for ternary and quaternary system was analyzed. The experimental results for ternary systems were correlated with UNIQUAC and NRTL equations. For the ternary systems studied here, the NRTL equation is more accurate than the UNIQUAC. The equilibrium data for the three ternary systems were used to determine interactions parameters for the UNIQUAC equation. For the quaternary system, the experimental data can be fitted more accurately to UNIQUAC equation than by the UNIFAC method.