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.     

含甲基叔丁基醚体系的相平衡测定

测定了在20℃下甲基叔丁基醚-甲醇-水及甲基叔丁基醚-叔丁醇-水两组三元体系的液液平衡数据和在常压下各三元体系中二元配偶物系的汽液平衡数据。并将所测定的两组三元液液平衡数据与二元系数据用NRTL 及UNIQUAC 方程所得的参数推算的结果进行了比较,获得较满意的结果。     

丙烯腈、己二腈和丙腈与水的二元体系液-液相平衡数据的测定和关联(英文)

采用平衡法测定了丙烯腈+水、己二腈+水、丙腈+水三个二元体系在不同温度(303.15、313.15、323.15、333.15K)下的液-液相平衡数据;并采用NRTL(α=0.2,α=0.3)模型和UNIQUAC模型对液-液平衡数据进行了关联.结果显示,NRTL和UNIQUAC模型对三个二元体系在不同温度下的互溶度关联的目标函数值均小于1×10-17,实验值与计算值吻合较好,绝对偏差小于0.009,关联精度较高.该研究结果可为丙烯腈、丙腈和水三元平衡溶解度数据的模拟和预测提供可靠的基础数据,并对电解二聚法生产己二腈中电解液的分离提纯工艺具有一定的指导意义.     

硫酸锂-乙醇-水体系在高原大气压下的气-液平衡研究

盐-混合溶剂体系气-液平衡研究具有重要的理论和实用意义。盐加到互溶双液系能改变组分间相对挥发度,提高蒸馏效率,分离恒沸物。达面方工作,Furter已作过详细综述。从盐-混合溶剂体系气-液平衡研究可以计算离子的溶剂化数,探索离子-溶剂和溶剂-溶剂之间的相互作用。因此,盐-混合溶剂体系气-液平衡的研究目前在国内外越来越受到人们的重视。本文研究盐饱和下的硫酸鲤-乙醇-水体系在高原大气压(530 Torr左右)下的汽-液平衡。改进的Rose釜测定体系的p-T-x-y数据。按照Jaques的假二元体系模型,使用Wilson,NRTL和修正的UNIQUAC方程关联实验数据。在计算过程中,使用一个能在计算机上顺利得到结果的计算方法。     

醋酸-水-醋酸乙烯酯三元系气液平衡的研究——Ⅰ.液相完全互溶区

本文报导了醋酸-水、醋酸-醋酸乙烯酯、水-醋酸乙烯酯等三对二元系以及醋酸-水-醋酸乙烯酯三元系在液相完全互溶区的气液平衡实验数据。文中还计算了经校正了醋酸气相缔合后的活度系数,作了热力学一致性校验,并尝试用NRTL式进行关联。当使用三对二元系的NRTL特征参数,对三元系液相完全互溶区的气液平衡进行了预测,与实验结果基本相符。三元系液相部分互溶区的实验数据与热力学关联的结果,将于第Ⅱ报中报导。     

乙酸乙酯-水二元物系汽液平衡的研究

本文使用自行设计的带机械搅拌器的平衡釜,在760mmHg压力下,测定了乙酸乙酯-水二元部份互溶物系的汽、液平衡数据.经热力学检验,该数据符合热力学一致性.用NRTL等13个活度系数方程进行热力学关联和计算,获得了满意的结果,尤以McCann方程和NRTL方程拟合的精度最佳.     

Li2SO4—EtOH—H2O体系25℃气—液—固平衡和液相物理化学性质的研究

研究Li_2SO_4-EtOH-H_2O体系25℃气液平衡及液相的粘度和密度。湿渣法确定平衡固相在整个浓度范围内均为Li_2SO_4·H_2O。用经验公式ln(y/y_0)=K_1x K_2x~2 K_2x~3对体系的溶解度和密度数据进行关联。硫酸锂加入到液相后由于盐离子静电作用对乙醇-水体系粘度的影响。按Jaques的假二元体系模型,用WILSON,NRTL方程关联气液平衡数据。     

Li2SO4-EtOH-H2O体系25℃气-液-固平衡和液相物理化学性质的研究

研究Li_2SO_4-EtOH-H_2O体系25 ℃气液平衡及液相的粘度和密度。湿渣法确定平衡固相在整个浓度范围内均为Li_2SO_4·H_2O。用经验公式ln(y/y_0)=K_1x+K_2x~2+K_2x~3对体系的溶解度和密度数据进行关联。硫酸锂加入到液相后由于盐离子静电作用对乙醇-水体系粘度的影响。按Jaques的假二元体系模型, 用WILSON, NRTL方程关联气液平衡数据。     

用二元交互作用函数预测高压下多组分体系的气液平衡

用和体系的状态有关且满足不变性条件的二元交互作用函数,结合F函数修改的立方状态--方程FRKS方程,预测高压下多组分体系的气液平衡.选择15个三元体系及其组分二元系来检验方法的可行性,这些体系覆盖了从简单的接近理想溶液行为的体系到高度非理想体系.计算结果表明,该方法不仅能相当精确地关联各种类型二元系的气液平衡,而且能在仅用组分二元系参数的条件下较准确地预测所考察的所有三元体系的气液平衡     

SiO2气凝胶负载无水四氯化锡催化顺酐与正丁醇酯化反应的研究

通过表面反应制备了气凝胶SiO2负载无水四氯化锡催化剂并应用于顺酐与正丁醇的酯化反应.结果表明,酯化产物主要为马来酸二丁酯(DBM)与富马酸二丁酯(DBF),其优化条件为:载体SiO2气凝胶焙烧温度500℃,物料摩尔比顺酐∶正丁醇:催化剂=1∶2∶0.0028,反应时间6 h.并且通过XRD,FTIR,DRUV-vis,N2物理吸附以及元素分析技术对所合成催化剂进行表征.结果表明:无水四氯化锡成功负载于SiO2气凝胶表面,在催化酯化反应当中实现了86.1%的顺酐转化率,此结果接近于国内外所报道的均相体系成果,同时在催化回收利用六次后,其活性虽逐步下降,但仍是空白的2倍.分析测试表明,反应过程中Cl的流失量较大、反应物及产物在催化剂表面产生了吸附,这些可能是导致催化活性下降的主要原因.     

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.     

Vapor–liquid equilibria for pentafluoroethane + propane and difluoromethane + propane systems over a temperature range from 253.15 to 323.15 K

This paper provides vapor–liquid equilibrium (VLE) data obtained for two binary systems of pentafluoroethane (R125)+propane (R290) and difluoromethane (R32)+R290 over a temperature range from 253.15 to 323.15 K. The measurement of VLE was performed at isothermal conditions in a vapor recirculation apparatus. Both systems form azeotropes in the temperature range of this study. The experimental results were well correlated with the Peng–Robinson equation of state (PR EoS) using one parameter van der Waals one fluid model. The binary interaction parameters were optimized using the experimental data of bubble point pressure. A comparison with published experimental VLE data has been carried out by means of the PR equation of state.     

Thermodynamics of aqueous solutions of methyldiethanolamine and diisopropanolamine

The vapour–liquid equilibrium (VLE) of the systems of water + methyldiethanolamine (MDEA) and water + diisopropanolamine (DIPA) was measured at several temperatures with a static total pressure apparatus. The solid–liquid equilibrium (SLE) of the same systems was measured at low amine concentrations by means of two experimental methods: a visual method and a Differential Scanning Calorimeter (DSC). The activity coefficients of water + MDEA were modelled with the NRTL equations. The model parameters were regressed from VLE, SLE and excess enthalpy data from this work and from the literature. The model developed in this work was compared with models found in the literature. The NRTL equations were also used to model the activity coefficients of the system of water + DIPA. The model parameters were fitted from the VLE and SLE data measured in this work.     

苯—正庚烷—乙醇三元体系加压汽液平衡的研究

用双循环武加压汽液平衡装置测定了苯-正庚烷-乙醇三元体系在101.3、302.5、506.8、709.3、810.6 kPa下的汽液平衡数据。根据有关二元体系在对应压力下的汽液平衡数据所求得的能量配偶参数,对该体系的汽液平衡进行了预测,计算值与实验值符合良好。     

Isobaric vapor-liquid equilibria of the methanol,methyl acetate and methyl acrylate system at atmospheric pressure

Isobaric vapor-liquid equilibrium (VLE) data were determined at atmospheric pressure for the binary and the ternary mixtures of methanol, methyl acetate and (stabilized) methyl acrylate. The thermodynamic consistency of the data for the three binary mixtures was tested via Herington analysis. The experimental VLE data were reduced and binary parameters for four activity coefficient models, such as Margules, Wilson, NRTL and UNIQUAC, were fitted. The four models with their best-fitted parameters were used to predict the ternary vapor-liquid equilibria. A comparison of model performances was made by using the criterion of average absolute deviations in boiling point and in vapor-phase composition.     

Measurement of ternary polymer/solvent equilibrium data by vapor-phase infrared spectroscopy

Vapor–liquid equilibrium (VLE) data for binary toluene/PVAC, methanol/PVAC and ternary toluene/methanol/PVAC systems have been measured at 100 °C by using vapor-phase infrared spectroscopy. Binary data have been compared with literature data measured by different experimental techniques and agreement between our measurements and others was found to be good. The ternary VLE data indicate that the solubility of methanol in PVAC is not influenced by the presence of toluene, while the solubility of toluene is lowered due to presence of methanol. To predict ternary VLE data, the Entropic free volume and Kannan free volume models and the Flory-Huggins theory were used. The predictive abilities of Flory-Huggins theory and the Kannan free volume model are similar and better than that of the Entropic free volume model.     

Vapor–liquid equilibria of systems containing acetic acid and gaseous components. Measurements and calculations by a cubic equation of state

Isothermal pressure-composition VLE data have been measured for four systems containing acetic acid and a gaseous component. The gaseous components are carbon monoxide, carbon dioxide, hydrogen and methane. The measurements were made in a static cell and the compositions of the gas and the liquid phases were measured by a gas chromatograph. A new correlation model (ACE, Association+Cubic Equation of state) was developed. It is based on a cubic equation of state and a model for the dimerization of acetic acid. It was applied to correlate the experimetnal VLE data with good results.     

Prediction of vapor-liquid equilibrium from excess enthalpy data for binary ether +n-alkane or cyclohexane mixtures

Vapor liquid equilibrium (VLE) is successfully predicted from excess enthalpy H^E data for binary ether + n-alkane or cyclohexane mixtures. Parameters for the continuous linear association model (CLAM) and for the UNIQUAC Model for the excess Gibbs energy G^E were determined from H^E data measured at a low temperature (ambient temperature). These parameters are used to predict VLE data at low and high temperatures. The dependence of the accuracy of predictions on the set of H^E data chosen to evaluate the parameters and on the model for G^E are discussed.     

Vapor-liquid equilibria for benzyl alcohol with carbon dioxide, ethane, or nitrogen at elevated pressures

Vapor-liquid equilibrium (VLE) phase compositions were measured for the binary systems of benzyl alcohol with carbon dioxide, ethane, or nitrogen at temperatures from 333.15 K to 453.15 K and pressures up to 19 MPa. Henry's constants were calculated from the isothermal equilibrium data. The new VLE data were correlated by the Patel-Teja equations of state with three different types of mixing rules. In general, using the one-fluid, two-parameter van der Waals mixing rule yielded the best representation for the investigated systems. The validity of a generalized Soave model was also tested with the equilibrium data of carbon dioxide + benzyl alcohol.