氯仿－乙醇－苯三元体系加压相平衡研究

氯仿－乙醇－苯三元体系加压相平衡研究马忠明，陈庚华，王琦，韩世钧，余淑娴（浙江大学化学系，杭州，３１００２７）（江西大学化学系）关键词醇烃体系，加压汽液平衡，氯仿－乙醇－苯体系为研究氯代烃、芳烃、低级醇这类醇烃不对称体系在加压下的汽液相平衡行为［１］...     

氯仿,苯,正丁醇有关二元体系加压相平衡研究

氯仿、苯、正丁醇有关二元体系加压相平衡研究严新焕，陈庚华，王琦，韩世钧（浙江大学化学系杭州３１００２７）关键词烃醇体系，加压汽液平衡作者曾研究了氯仿、苯与乙醇构成的醇烃不对称体系的汽液平衡￣［１］。为了进一步研究低级醇与卤代烃、芳烃的相行为，本工作又...     

二氧化碳和天然气经过微波等离子体直接转化成C2烃

二氧化碳和天然气经过微波等离子体直接转化成Ｃ２烃陈栋梁雷正兰刘万楹＊⒇张承聪洪品杰戴树珊（中国科学院成都有机化学研究所，成都，６１００４１）（云南大学化学系，昆明，６５００９１）二氧化碳和甲烷都是很稳定的非极性分子，要使其分子活化，发生化学反应，转化...     

交替烃拓扑结构计数的研究

交替烃拓扑结构计数的研究余荣泮，杨良准，刘训亭，胡启山，张自先，莫宇翔，陈琼，王成瑞（武汉大学化学系武汉４３００７２）关键词拓扑结构计数，交替烃，分子轨道分子稳定性的研究是理论化学中一个重要课题，关于这方面的工作，共振论是富有成效的理论之一。在偶苯型...     

苯、萘、蒽芳烃分子稳定性和分子极化率规律的理论研究

苯、萘、蒽芳烃分子稳定性和分子极化率规律的理论研究桑兰芬，杨滢，杜秀华（长春光机学院基础部长春１３００１２）苏忠民，王荣顺（东北师范大学化学系长春１３００２４）关键词苯，分子极化率，同系物本文以苯、萘、蒽等最简单的单、稠环芳烃为例，对其体系稳定性变化...     

醇类在苯及对二甲苯中过量焓预测

醇类在苯及对二甲苯中过量焓预测裘利言，姚惟馨（南京化工学院应用化学系南京２１０００９）关键词醇，芳烃，缔合，过量焓含醇体系的热力学性质研究近来十分活跃。通常文献所报道的醇－芳烃体系中醇的摩尔分数ｘ＿Ａ在０．１～０．９，而对于极稀溶液区有关报道很少。这...     

氯仿－苯－正丁醇三元体系加压相平衡研究

本文根据氯仿、苯、正丁醇有关二元体系实测数据统一关联所得的能量参数关联式，用Ｗｉｌｓｏｎ方程对氯仿－苯－正丁醇三元体系在１０１～３０３ｋＰａ压力下的汽液平衡作了预测，并与本工作的实测数据比较，二者符合良好。实验结果表明，这三元体系与氯仿－苯－乙醇体系的汽液相平衡行为具有相似的规律。     

氯仿—苯—正丁醇三元体系加压相平衡研究

本文根据氯仿、苯、正丁醇有关二元体系测数据统一关联所得的能量参数关联式，用Ｗｉｌｓｏｎ方程对氯仿－苯－正丁醇三元体系在１０１－３０３ＫＰａ压力下的汽液平衡作了预测，并与本工作的实测数据比较，二者符合良好。实验结果表明，这三元体系与氯仿－苯－乙醇体系的汽液相平衡行为具有相似的规律。     

磷钨酸（盐）催化苯甲酸与正癸醇和鲸蜡醇酯化反应的研究

磷钨酸（盐）催化苯甲酸与正癸醇和鲸蜡醇酯化反应的研究司宗兴孙亚秋汪海涛（中国农业大学应用化学系北京１０００９４）长链化合物是一类具有广泛杀虫、杀菌和植物生长调节活性的化合物。在长链醇的酯化反应中，由于醇部分碳原子数目多，亲酯性增加，溶解度在极性溶剂中...     

乙醇对合成醇用Cu-Co-Fe催化剂的修饰效应

乙醇对合成醇用Ｃｕ┐Ｃｏ┐Ｆｅ催化剂的修饰效应徐杰王向宇杜宝石（郑州大学化学系，郑州４５００５２）辛勤李灿（中国科学院大连化学物理研究所，大连１１６０２３）关键词铜，钴，铁，合成醇，乙醇，修饰作用分类号Ｏ６４３／Ｏ６４７自７０年代以来，已对多种ＣＯ加...     

顺丁烯二酸酐与邻苯二甲酸二甲酯二元体系在4.00, 8.00和12.00 kPa下的等压气液平衡

采用沸点仪测定了顺丁烯二酸酐和邻苯二甲酸二甲酯二元体系在4.00, 8.00和12.00 kPa下的等压气液平衡数据以及纯DMP组分饱和蒸气压数据, 将实验数据回归得到了纯DMP在417~525 K范围内的Antoine方程. 根据实验平衡温度、 压力和组成数据进一步回归得到NRTL方程参数, 推算出平衡气液相组成, 并利用UNIFAC方程对实验数据进行了预测, 其结果与沸点仪测定结果及NRTL拟合的结果基本相符.     

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.     

Isobaric vapor–liquid equilibria of the binary system maleic anhydride and di-isobutyl hexahydrophthalate at 2.67, 5.33 and 8.00 kPa

Isobaric vapor–liquid equilibrium (VLE) data for the binary system maleic anhydride (MAN) + di-isobutyl hexahydrophthalate (DIBE) at 2.67, 5.33 and 8.00 kPa were measured with a modified ebulliometer. Also, saturated vapor pressures of pure DIBE were measured and Antoine constants were obtained. These data were used to calculate equilibrium vapor and liquid compositions for this binary system using the NRTL model. Prediction of the VLE was done with the universal quasi-chemical functional-group activity coefficients (UNIFAC) model. The predicted results generally agree with those from experiment.     

Isobaric (vapor + liquid) equilibria of the binary system maleic anhydride and diethyl phthalate at p = (2.67, 5.33, and 8.00) kPa

Saturated vapor pressures of pure diethyl phthalate were measured with the ebulliometer. And isobaric (vapor + liquid) equilibrium data for the binary system (maleic anhydride + diethyl phthalate) at p = (2.67, 5.33, and 8.00) kPa were determined using the ebulliometric method. The parameters of the NRTL model for the binary system were obtained by calculating equilibrium compositions of the liquid and vapor phase with the experimental equilibrium temperatures, pressures and feed compositions. Moreover, (vapor + liquid) equilibrium data for the binary system were predicted by use of the UNIFAC model. Predicted results were compared with those from the ebulliometric method, and showed good agreement.     

Vapor-liquid equilibria for the nitrogen-isobutane system

Vapor-liquid equilibria have been investigated experimentally for the nitrogen-isobutane system at temperatures from 120 K to 220 K and at pressures up to 150 bar. Below 126.5 K, two liquid phases were observed as pressure was increased to near the vapor pressure of pure nitrogen. The equilibrium ratio of nitrogen in the binary system and the Henry’s law constants for nitrogen in isobutane were determined from experimental data. The experimental phase equilibrium data were correlated by means of the Peng-Robinson equation of state.     

Isothermal vapor—liquid equilibrium of ternary mixtures formed by 1-propanol,acetonitrile and benzene

Vapor—liquid equilibrium data are presented for the ternary system 1-propanol-acetonitrile-benzene, at 45°C. The experimental vapor—liquid equilibrium results of the three constituent binary systems are well reproduced with the UNIQUAC associated-solution model and the ternary results are compared with those calculated from the model with binary parameters alone. Ternary prediction of liquid—liquid equilibria is given for the 1-propanol-acetonitrile-n-hexane and 1-propanol—acetonitrile-n-heptane systems at 25°C.     

Thermodynamic properties of new heat pump working pairs: 1,3-Dimethylimidazolium dimethylphosphate and water,ethanol and methanol

Ionic liquid 1,3-dimethylimidazolium dimethylphosphate ([MMIM][DMP]) + water/ethanol/methanol mixtures exhibit properties which render them suitable as candidates for working pairs in industrial applications of absorption heat pumps or chillers. In this paper, the thermodynamic properties including vapor pressure, density, viscosity, heat capacity as well as excess enthalpy of these binary systems were measured at various temperatures with different ionic liquid concentrations. The thermodynamic properties were correlated by different equations, respectively. The correlated values were significantly consistent with the experimental ones. In conclusion, the vapor–liquid equilibrium (VLE) data indicated that the vapor pressures of the three solvents in [MMIM][DMP] displayed a considerable negative deviation from Raoult's law, and the excess enthalpies of the three binary systems are negative. These characteristics are necessary and important for an absorption working pair.     

The prediction of isobaric phase equilibria for non-ideal multicomponent mixtures from heat of mixing data

A method for predicting isobaric binary and ternary vapor—liquid equilibrium data using only isothermal binary heat of mixing data and pure component vapor pressure data is presented. Three binary and two ternary hydrocarbon liquid mixtures were studied. The method consists of evaluating the parameters of the NRTL equation from isothermal heat of mixing data for the constituent binary pairs. These parameters are then used in the multicomponent NRTL equation to compute isobaric vapor—liquid equilibrium data for the ternary mixture. No ternary or higher order interaction terms are needed in the ternary calculations because of the nature of the NRTL equation. NRTL parameters derived from heat of mixing data at one temperature can be used to predict vapor—liquid equilibrium data at other temperatures up to the boiling temperature of the liquid mixture.For the systems studied this method predicted the composition of the vapor phase with a standard deviation ranging from 1–8% for the binary systems and from 4–12% for the ternary systems.