用于描述三元水醇系统汽液平衡的活度系数模型

In this study, three semipredictive activity coefficient models: Wilson, non-random-two liquid model (NRTL), and universal quasi-chemical model (UNIQUAC), have been used for modeling vapor-liquid equilibrium properties of ternary mixtures that include substances found in alcoholic distillation processes of wine and musts. In particular, vapor-liquid equilibrium in ternary mixtures containing water + ethanol + congener has been modeled using parameters obtained from binary and ternary mixture data. The congeners are substances that although present in very low concentrations, of the order of part per million, are important enological parameters. The results given by these different models have been compared with literature data and conclusions about the accuracy of the models studied are drawn, recommending the best models for correlating and predicting phase equilibrium properties of this type of mixtures.     

2-氯-5-氯甲基吡啶在不同溶剂中溶解度的测定与关联(英文)

2-Chloro-5-chloromethylpyridine is a crucial intermediate of pesticides. Its solid-liquid equilibrium data will provide essential support for industrial design and further theoretical studies. The solubilities of 2-chloro-5-chloromethylpyridine in water, methanol, ethanol, ethyl acetate, acetone, trichloromethane and toluene at different temperatures were measured using the synthetic method by a laser monitoring observation technique. The solubility data were correlated with the modified Apelblat equation and Wilson equation. The calculated values were in good agreement with the experimental values.     

乙酸乙酯与CnH2n+1OH（n=1,2,3）双系统在0.3MPa下的气液平衡（英文）

Vapor-liquid equilibrium data for the binary systems of ethyl acetate + methanol,ethyl acetate + ethanol and ethyl acetate + 1-propanol at 0.3 MPa were determined.The experimental data were verified with the point-to-point test of van Ness(1973).All these systems present an azeotropic point at 0.3 MPa that increases in ester composition for longer alcohol chains.The UNIFAC in different versions and ASOG prediction models were applied.     

常压下环己烯-环己醇汽液平衡的测定和关联

Many by-products are generated in the process of oxidizing cyclohexene to produce 1,2-epoxycyclohexane by hydrogen peroxide,including cyclohexanol,cyclohexanone,etc.To obtain high-purity 1,2-epoxycyclohexane, the by-products and unreacted cyclohexene must be removed through rectification,in which the vapor-liquid equilibrium(VLE)data of the system are needed.In this study,the VLE data of cyclohexene-cyclohexanol system were studied at 101.3 kPa using an improved EC-2 VLE still.The thermodynamic consistency of the data was examined by Herington’s method.The results obtained were exemplary.The VLE data were correlated by the Wilson equation. The difference between the calculated values and the experimental data is minor,indicating that the VLE data are suitable for engineering design.     

邻-间-对苯二酚固液平衡测定与关联

采用差示扫描量热法测定了邻苯二酚与间苯二酚、邻苯二酚与对苯二酚、间苯二酚与对苯二酚二元固液平衡数据,同时绘制出相应的简单低共熔型二元相图。低共熔组成和温度为：邻苯二酚(1) 间苯二酚(2),x1=0.5077,336.3K;邻苯二酚(1) 对苯二酚(3),x1=0.7879,365.8K;对苯二酚(3) 间苯二酚(2),x3=0.2305,366.1K。采用Wilson方程关联,标准偏差分别为0.48K,0.48K和0.56K。     

4-羟基苯甲醛及其溴代物固液平衡数据测定与关联

引　言香兰素 (vanillin) ,即 3 甲氧基 4 羟基苯甲醛 ,是一种广谱型香料 ,广泛应用于食品、化妆品等行业 ,需求日益增长 .近年来提出的以 4 羟基苯甲醛 (以下简称对醛或Ⅰ )为原料 ,经溴化、甲氧基化人工合成香兰素的新工艺[1～ 3 ] ,越来越受到人们的重视 .溴化反应是该工     

三乙胺—苯≡亚磷酸三甲酯三元体系汽液平衡测定及关联

亚磷酸三甲醇(简称三甲酯)是有机磷农药的重要中间体。本工作是配合三乙胺法连续化生产三甲酯小试而进行的。产品三甲酯必须从溶剂苯、缚酸剂三乙胺中分离出来,为了给此工艺过程提供必要的热力学数据,以便为选择合理的分离流程和设计合理的精馏设备提供较可靠的依据,我们于81年对三乙胺—苯—亚磷酸三甲酯三元体系的汽液平衡进行了实测和关联。在关联中,我们选用了Margules方程。由二元参数出发进行三元关联,并用实测数据进行比较,得到了较满意的结果。     

苯丙烯-苯乙酮-苯异丙醇汽液平衡测定与关联

采用单级循环汽液平衡装置测定常压下苯丙烯-苯乙酮-苯异丙醇(CA)体系中苯丙烯-苯乙酮、苯乙酮-苯异丙醇、苯丙烯-苯异丙醇二元及苯丙烯-苯乙酮-苯异丙醇三元体系的汽液平衡数据,分别以NRTL和UNIQUAC为相平衡模型对实验数据进行关联,从而确定相平衡模型及组分间的交互参数,并采用Herington面积法对二元汽液平衡...     

DDHI-DIPP二元体系固液平衡数据的测定和关联

测定了DDHI－DIPP体系的固液平衡相图,用理想溶液模型和UNIQUAC活度系数模型进行了关联;其中用UNIQUAC活度系数模型所获得的结果较满意。     

Solid-Liquid Equilibria of Several Binary and Ternary Systems Containing Maleic Anhydride

Solid-liquid equilibria (SLE) of three binary systems and seven ternary systems containing maleic an-hydride(MA) are measured by visual method. The experimental data are compared with the calculated ones with modified universal quasichemical functional group activity coefficient(UNIFAC) method in which the interaction parameters between groups come from two sources, dortmund data bank(DDB), if there's any, and correlations based on our former presented experimental SLE data of twenty binary systems. New groups of MA, ACCOO group, COO group, >C=O group and cy-CH2 group are defined and the SLE data of rnaleic anhydride in isopropyl acetate in literature are cited in order to assess the new interaction parameters, correlated with Wilson equation and the λh equation. The modified UNIFAC method with these new regressed interaction parameters is also used to predict other three binary systems containing rnaleic anhydride.     

顺丁烯二酸酐在单一溶剂和混合溶剂中的固液平衡研究

Solid-liquid equilibria (SLE) of three binary systems and seven ternary systems containing maleic anhydride(MA) are measured by visual method. The experimental data are compared with the calculated ones with modified universal quasichemical functional group activity coefficient(UNIFAC) method in which the interaction parameters between groups come from two sources, dortmund data bank(DDB), if there’s any, and correlations based on our former presented experimental SLE data of twenty binary systems. New groups of MA, ACCOO group, COO group, ＞C=O group and cy-CH2 group are defined and the SLE data of maleic anhydride in isopropyl acetate in literature are cited in order to assess the new interaction parameters, correlated with Wilson equation and the λh equation. The modified UNIFAC method with these new regressed interaction parameters is also used to predict other three binary systems containing maleic anhydride.     

催化合成水杨酸酯的工艺研究

芳基磺酸（ＡＳＡ） 催化水杨酸（２ 羟基苯甲酸） 和Ｃ４ ～Ｃ５ 醇的酯化反应,性能优于磷钨酸等其他４ 种催化剂。探讨并找到了ＡＳＡ催化合成水杨酸丁酯、戊酯的优化反应条件：原料配比ｎ（Ｃ７Ｈ６Ｏ３）∶ｎ（ＲＯＨ）＝１∶１－８,催化剂ＡＳＡ的用量为酸质量的５ ％ ～７％ ,反应温度１１０ ～１４０ ℃,反应时间４～７ ｈ,转化率达９２％ ～９７％ ,产品纯度大于９９％ 。     

2,6-DIPN与2,7-DIPN二元体系固液相图的测定和关联

绘制了2,6-二异丙基萘(2,6-DIPN)与2,7-二异丙基萘(2,7-DIPN)二元体系的固液相图,测定了2,6-DIPN和2,7-DIPN二元混合物体系的低共熔点,并用理想溶液模型进行了关联。结果表明,2,6-DIPN与2,7-DIPN二元体系固液平衡相图为简单低共熔混合物相图,低共熔点温度为-19.5℃,组成为2,7-DIPN12.2%(质量分数,下同),2,6-DIPN87.8%,由试验数据拟合得到2,6-DIPN的熔化焓为4.878kJ/mol。     

二溴苯三元物系固液平衡测定与正规溶液模型

采用差示扫描量热法,通过对一系列"拟二元"物系固液平衡数据的测定,得到了邻二溴苯、间二溴苯和对二溴苯三元物系的固液平衡数据.实验结果表明本物系为简单低共熔型,其低共熔摩尔分数组成和温度分别为:邻二溴苯(x1) 间二溴苯(x2) 对二溴苯(x3),x1=0.4259,x2=0.5345,x3=0.0396,Tcu=238.5 K.文中绘制出了其相应的低共熔三元固液平衡相图,并采用正规溶液模型,利用二元溶液的三个相互作用参数对实验数据进行了关联,温度均方根偏差仅为1.32 K,说明正规溶液模型适用于上述弱极性异构体三元物系固液平衡的计算.     

马来酸酐－醋酸异丙酯二元固液平衡的测定和关联

马来酸酐－醋酸异丙酯二元固液平衡的测定和关联陈新志侯虞钧（浙江大学化工系，杭州３１００２７）关键词固液平衡活度系数１引言相平衡数据在化工生产和研究中占有重要的地位。流体相平衡已得到了广泛的研究，并积累了大量的数据，与之相应的实验方法也较为完善，同时...     

二溴苯物系固液平衡测定与正规溶液模型

采用差示扫描量热法测定了邻二溴苯与间二溴苯、对二溴苯与间二溴苯和对二溴苯与邻二溴苯的3个二元固液平衡数据,同时绘制出相应的简单低共熔型二元相图。各物系低共熔摩尔分数组成和温度分别为：邻二溴苯(x) 间二溴苯(1-x),x=0.4485,t=240．4K;对二溴苯(x) 间二溴苯(1-x),x=0.1002,T=260.9K：对二溴苯(x) 邻二溴苯(1—x),x=0.1306,T=272.3K。采用单参数正规溶液模型计算,温度均方根偏差不大于1.1K,说明正规溶液模型适用于上述弱极性异构体物系固液平衡计算．     

Measurement and correlation for solubility of diosgenin in some mixed solvents简

The solubility data of diosgenin in mixed systems of ethanol ＋ 1-propanol （1 ： 1）, ethanol ＋ 1-butanol （1 ： 1）, ethanol ＋ isobutyl alcohol （1 ： 1）, methanol ＋ isobutyl alcohol （1 ： 1）, methanol ＋ isobutyl alcohol （1 ： 4）, ethanol ＋ 1-pentanol （1 ： 1） and carbon tetrachloride were measured over the temperature range from 289.15 K to 334.15 K by a laser monitoring observation technique at atmospheric pressure, with all mixtures mixed by volume ratio. The Apelblat equation, the ideal solution model, and the 2h equation are used to correlate the solubility data. The results show that the three models agree well with the experimental data, providing essential support for industrial design and further theoretical study.