BeSO4-Al2(SO4)3-Na2SO4三元熔盐体系相图的研究

热分析法研究了BeSO₄-Al₂(SO₄)3-Na₂SO₄三元熔盐体系的状态图。体系中存在三元转熔(包晶)点P,温度490℃,组成为BeSO₄18.8Wt%,Al₂(SO₄)₃15.0%,Na₂SO₄66.2%;三元低共熔(共晶)点E₁,温度为476℃,组成为BeSO₄20.0%,Al₂(SO₄)₃11.2,%,Na₂SO₄68.8%。另一低共熔点E₂温度为595℃,组成未能确定。体系中无三元化合物生成。     

三元体系MgCl2-CO(NH2)2-H2O在25℃时的等温溶度与新相研究

测定了25℃时三元体系MgCl₂-CO(NH₂)₂-H₂O的等温溶度及饱和溶液的折光率和密度,且绘制成溶度图和性质-组成图.在三元体系内形成2个三元化合物新相:MgCl₂·CO(NH₂)₂·4H₂O(记作A)和Mgcl₂·4CO(NH₂)₂·2H₂O(记作B),B为新化合物.三元体系的溶度图由4支单饱和线[对应单饱和固相为MgCl₂·6H₂O、三元化合物A和B、CO(NH₂)₂]组成,这4支单饱和线两两交于3个三元无变点[对应双饱和固相为MgCl₂·6H₂O+A、A+B、B+CO(NH₂)₂].     

微乳液体系相图的研究及其在纳米氟化物制备中的应用

绘制了十六烷基三甲基溴化铵(CTAB)/正丁醇(n-C₄H₉OH)/正辛烷(n-C₈H₁₈)/水[或NH₄F溶液、或Ba(NO₃)₂溶液、或KNO₃-Mg(NO₃)₂混合溶液]四组分微乳体系的拟三元相图.观察了电导率随水(或盐溶液)含量变化的规律,很好地印证了微乳液体系的相行为.选取相图中微乳区点作为最佳条件,制备了KMgF₃纳米粒子.     

体系Mg(NO3)2-MgCl2-H2O作为相变储能材料的相图预测

应用修正的BET热力学模型对Mg(NO₃)₂-MgCl₂-H₂O体系在273～373 K的相图进行预测, 发现两个共晶点, 并通过实验对共晶点组成材料的吸热和放热行为进行测定, 发现三元共晶点Mg(NO₃)₂•6H₂O(45.6%)-Mg(NO₃)₂•2H₂O (29.6%)-MgCl₂•6H₂O(24.8%)储能效果较差, 而二元共晶点Mg(NO₃)₂•6H₂O(61.6%)-MgCl₂•6H₂O(38.4%)在熔点附近具有很好的储放热能力, 其相变热焓经差热分析为136.8 J•g^－1, 说明该材料可用作潜在的相变储能材料.     

SDS/正戊醇-二甲苯-水(盐水)拟三元体系相图和电导研究及纳米ZnO的制备

实验绘制了十二烷基硫酸钠(SDS)/正戊醇(n-C₅H₁₀OH)-二甲苯[C₆H₄(CH₃)₂]-水[或Zn(NO₃)₂溶液]四组分微乳液体系在不同温度时的拟三元相图. 测定了电导率随水(或盐溶液)含量变化的规律, 电导的规律与相图吻合. 依据电解质理论探讨了微乳液的微观结构, 研究表明, 温度对油包水(W/O)反相微乳液区域影响不大, 电解质的加入对油包水(W/O)反相微乳液区域影响较大. 通过SDS/正戊醇-二甲苯-H₂O及SDS/正戊醇-二甲苯-盐水的拟三元体系的相图观察及实验研究, 选择乳化剂(SDS/正戊醇)与二甲苯质量比为4:6的微乳液作为最佳条件, 制备出了ZnO纳米粒子.     

四元体系KCl-K2SO4-CO(NH2)2-H2O有25℃时的等温溶度研究

测定了四元体系KCl－K₂SO₄－CO(NH₂)₂－H₂O及边界三元体系K₂SO－CO(NH₂)₂-H₂O在25℃时的溶度及饱和溶液密度值和折光率,绘制了相应的溶度图及相应的组成-性质图.测定并绘制了该四元体系K₂SO₄单饱区的溶度面、折光率面和密度面图.两个体系的溶度图均属于低共饱型,平衡固相为组份化合物.     

MgO-P2O5和CaO-P2O5体系的热力学优化

基于严格评估的相图和热力学实验数据,采用相图计算方法对MgO-P₂O₅和CaO-P₂O₅体系进行热力学优化.液相采用修正的似化学模型进行描述,考虑了对近似处理液相中存在的短程有序.为了描述M₃(PO₄)₂(M = Mg, Ca)组分处的最大短程有序,将PO₄^3-当作液相中P₂O₅的基本组成单元.体系中所有的中间相都看作线性化合物并考虑了晶型转变.获得一套合理、可靠、自洽的模型参数用来描述体系中各相的热力学性质,在实验误差范围内很好地重现了相图、焓、熵和活度实验数据,为炼钢脱磷过程中熔渣体系热力学数据库的建立打下了坚实的基础.     

CuSO4(ZnSO4)-CO(NH2)2-H2O三元体系在30℃时的等温溶度研究

报道了CuSO₄(ZnSO₄)-CO(NH₂)₂-H₂O两个三元体系在30℃时的等温溶度及饱和溶液的折光率,绘制了相应的溶度图和折光率-组成图.两个三元体系中分别形成了组成为CuSO₄·3CO(NH₂)₂·H₂O(异成分溶解)和ZnSO₄·CO(NH₂)·2H₂O(同成分溶解)的化合物,并通过元素分析、红外光谱、X射线粉末衍射及热分析对新相进行了表征.     

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。     

辛烷基酚聚氧乙烯醚反相微乳体系的相行为及纳米复合碳酸盐的制备

绘制了一系列辛烷基酚聚氧乙烯醚(OP-10)+正辛醇+环己烷+水(或CaCl₂水溶液)拟三元体系相图,分别研究了助表面活性剂正辛醇的添加比例和CaCl₂水溶液的浓度对微乳区域的影响,发现在OP-10+正辛醇+环己烷+水拟三元体系相图中,随着正辛醇/OP-10的质量比逐渐增大,微乳区的面积逐渐增大,当正辛醇/OP-10质量比为1:2.5时微乳区的面积最大,之后微乳区面积随着其质量比的增大而减小,表明适量地加入助表面活性剂正辛醇有利于微乳区的形成;但过多地增加正辛醇的量反而不利于微乳相的形成。 确定正辛醇/OP-10的质量比为1:2.5,改变CaCl₂的浓度,发现OP-10+正辛醇+环己烷+CaCl₂水溶液拟三元体系相图中,CaCl₂浓度为0.1 mol/L时微乳区面积最大。分别配制总浓度为0.1 mol/L的5种不同摩尔比的Ca²⁺/Ba²⁺微乳液,并与等摩尔的碳酸钠水溶液反应制备共沉淀碳酸盐,使用扫描电子显微镜(SEM)对所制备样品进行表征分析,发现当微乳液为钙离子盐时,主要形成大的立方形颗粒;掺入钡离子,Ca²⁺和Ba²⁺摩尔比为3:1、1:1和1:3时,形成的沉淀分别为四棱锥形、球形和玉米棒形;当微乳液为钡离子盐时,沉淀主要为不规则多面体。     

Experimental Investigation and Thermodynamic Modeling of the NaCl-NaNO3-Na2SO4 Ternary System

Molten salts as heat transfer and storage materials have been used to nuclear energy and concentrated solar power(CSP) applications. In this work, the system of molten salt mixture based on thermodynamic principles was designed as thermal energy storage(TES) materials. The substitutional solution model can be employed to describe the Gibbs energies of all liquid phase. Thermodynamic model parameters for the NaCl-NaNO₃-Na₂SO₄ subsystems were conducted by thermodynamic evaluation and optimization based on experimental phase-equilibria data. Thus, a set of self-consistent thermodynamic database was eventually obtained to reliably calculate the whole phase diagram and thermodynamic properties for the NaCl-NaNO₃-Na₂SO₄ternary system. The results manifest that the eutectic point of theternary system located at T=280℃ and x_NaCl=8.4%, x_NaNO3=86.3% and x_Na2SO4=5.3%. Moreover, the results predicted were verified experimentally using differential scanning calorimetry(DSC) and the agreement between the measured value[T=(287±2)℃] and predicted value(T=280℃) was satisfactory. Thus, the thermodynamic calculation method will be used to design and develop novel molten salt mixture as thermal energy storage materials.     

基于团簇结构模型的Na2O-Al2O3-SiO2三元体系熔体吉布斯混合摩尔自由能计算

以三元硅酸盐熔体团簇结构模型为基础,选取了Na₂O-Al₂O₃-SiO₂体系不同成分的团簇结构,采用半经验量子化学方法MNDO/d分别计算该三元体系熔体中不同结构的团簇基元在1473、1873、2000 K温度下的熵、焓、热容和自由能等热力学数据,计算得出不同团簇结构基元的混合自由能,并根据统计热力学波尔兹曼分布定律,推导计算得出Na₂O-Al₂O₃-SiO₂三元体系各成分下的混合摩尔自由能。三元硅酸盐熔体的热力学性质与该熔体的微观结构密切相关。     

Phase diagram for the system KVO3 + NH4HCO3 + NH4VO3 + KHCO3 + H2O at 303 K

Solubility data of the KVO₃ + NH₄HCO₃ + NH₄VO₃ + KHCO₃ + H₂O system at 303 K were determined under varying pressure conditions. The results were used to construct a phase diagram in the oblique projection according to Jänecke's method. At constant p and T this diagram includes two invariant points, five double saturated liquid curves, and four crystallization fields corresponding to KVO₃, NH₄HCO₃, NH₄VO₃, and KHCO₃. It has been found that ammonium meta-vanadate is a sparingly soluble salt. NH₄VO₃ and KHCO₃ compose the stable pair of salts, whereas KVO₃ and NH₄HCO₃ form the unstable salt-pair. A thorough knowledge of the solubility phase diagram for this reciprocal quaternary salt system is the theoretical basis of the carbonation process of the potassium meta-vanadate saturated ammonia solution.     

A ternary phase diagram of the Mn–Te–O system at 950 K

A ternary phase diagram of the Mn–Te–O system at 950 K has been established in the composition range in and around the MnO–TeO₂ pseudo binary line. Various preparation methods were employed to confirm the co-existence of different ternary phases. The results of these phase equilibration studies were revalidated by the invariancy of partial pressures at constant temperature during high temperature mass spectrometric vaporization experiments. The following three-phase regions have been identified: MnO+Mn₃O₄+Mn₆Te₅O₁₆ (phase region 1; PH1), Mn₃O₄+Mn₆Te₅O₁₆+MnTeO₃ (phase region 2; PH2), Mn₃O₄+MnTeO₃+Mn₃TeO₆ (phase region 3; PH3), and MnTeO₃+Mn₂Te₃O₈+Mn₃TeO₆ (phase region 4; PH4). The complex nature of the Mn–Te–O ternary system was revealed by the interesting results obtained by us with regard to preparation of samples and mass spectrometric vaporization experiments.     

Isothermal Evaporation of Quaternary System Li^＋, K^＋, Mg^2＋//Cl^--H2O at 348K

The solubilities of the quaternary system Li^＋,K^＋,Mg2^＋//Cl^--H2O were investigated at 348 K via isothermal evaporation.The densities and refractive indices of its equilibrated solution were also determined experimentally.On the basis of the obtained data,the metastable phase diagram,the water content diagram,the diagrams of the density and refractive index against the composition of this quaternary system were constructed.The quaternary system Li^＋,K^＋,Mg^2＋//Cl^--H2O at 348 K belongs to a complex type with the formation of two carnallite double salts,which are potassium carnallite（K-carnallite） and lithium carnallite（Li-carnallite）.There are five salts like potassium chloride （KCl）,lithium chloride monohydrate（LiCl.H2O）,bischofite（MgCl2·6H2O）,K-carnallite（KCl·MgCl2·6H2O） and Li-carnallite（LiCl·MgCl2·7H2O）,seven unvariant curves named AH3,BH2,CH3,DH1,EH1,H1H2 and H2H3,and three invariant points,namely H1,H2 and H3,included in this metastable phase diagram.Comparisons between the stable phase diagram at 298 K and metastable phase diagram at 348 K of this quaternary system show that all the crystalline forms of the salts are not changed,whereas the crystallization areas of salts are changed significantly with temperature.The scope of KCl crystallization increases from 82% to 95% and that of K-carnallite decreases from 15.80% to 0.32% along with the temperature increasing from 298 K to 348 K,respectively.     

Solid-liquid Equilibria in the Ternary System (NaCl+SrCl2+H2O) and (KCl+SrCl2+H2O) at 288.15 K and 0.1 Mpa

Solid-liquid phase equilibria of the two ternary systems (NaCl+SrCl₂+H₂O) and (KCl+SrCl₂+H₂O) at T=288.15 K and p=0.1 MPa were studied using the isothermal dissolution equilibrium method. Solubilities of the equilibrium liquid phase were determined, and the solids were also investigated by the Schreinemaker method of wet residues. In the ternary system (NaCl+SrCl₂+H₂O) at 288.15 K, there is one invariant point corresponding to (NaCl+SrCl₂·6H₂O) and two crystallization regions corresponding to NaCl and SrCl₂·6H₂O. The crystallized area of SrCl₂·6H₂O decreased with the increasing temperature, while that of NaCl increased slightly. In the ternary system (KCl+SrCl₂+H₂O) at 288.15 K, there is one invariant point(KCl+SrCl₂·6H₂O) and two crystallization regions corresponding to KCl and SrCl₂·6H₂O. Both systems belong to a simple eutectic type, and neither double salts nor solid solutions were formed. On the basis of Pitzer-Harvie-Weare model, the solubilities of the two systems at 288.15 K were demonstrated. A comparison showed that the calculated solubilities agreed well with the experimental data.     

Metastable Phase Equilibrium of the Quaternary System Na+, Rb+, Mg2+//Cl--H2O at 298.2 K

The component solubilities, densities and refractive indices of the quaternary system Na⁺, Rb⁺, Mg²⁺//Cl^--H₂O at 298.2 K were measured using an isothermal evaporation method. Based on the gathered data, a metastable phase diagram, a water content diagram, and a density/refractive index vs. composition diagram were constructed. The results show that this system is of a complex type with a double salt rubidium carnallite (RbCl·MgCl₂·6H₂O) formed at 298.2 K. Double salt rubidium carnallite, whose component point locates in its own crystallization zone in the dry salt phase diagram, belongs to congruent double salt at 298.2 K. Accompanied by the double salt that was formed, there are two invariant points in the phase diagram that cosaturated with three salts and an equilibrated solution. The cosaturated salts for the two invariant points are MgCl₂·6H₂O+RbCl·MgCl₂·6H₂O+ NaCl and NaCl+RbCl+RbCl·MgCl₂·6H₂O, respectively. Both invariant points are commensurate invariant points in the evaporation process, and the two invariant points are evaporative dry points. The sizes of the crystalline regions of the salts are in the order of NaCl > RbCl > RbCl·MgCl₂·6H₂O > MgCl₂·6H₂O.