CIESC Journal

• 热力学 • 上一篇    下一篇

二甲醚-甲醇-水三元体系汽液平衡的测定与计算

宋怀俊;张海涛;应卫勇;房鼎业   

  1. 华东理工大学化工学院,化学工程联合国家重点实验室,上海 200237;郑州大学化工学院,河南 郑州 450002

  • 出版日期:2006-08-25 发布日期:2006-08-25

Measurement and calculation of vapor-liquid equilibrium for dimethyl ether-methanol-water ternary system

SONG Huaijun;ZHANG Haitao;YING Weiyong;FANG Dingye   

  • Online:2006-08-25 Published:2006-08-25

摘要: 利用自吸式搅拌静态平衡釜,测定了333.15、353.15、373.15、393.15 K下二甲醚-甲醇-水三元体系的等温汽液平衡数据.二甲醚在气液相中的含量随压力的提高而增大,随温度的升高而减小.采用状态方程-活度因子法,由PR方程计算气相各组分的逸度因子, NRTL方程计算液相活度因子,进行了二甲醚-甲醇-水三元体系汽液平衡数据的热力学计算.模型计算值与实验值吻合良好.

Abstract: The isothermal vapor-liquid equilibrium data for dimethyl ether-methanol-water ternary system were measured at 333.15 K,353.15 K,373.15 K and 393.15 K in a self-sucking type agitated static equilibrium cell.The effect of pressure and temperature on vapor-liquid equilibrium of dimethyl ether-methanol-water ternary system was analysed, the contents of dimethyl ether in vapor phase and liquid phase increased with increasing pressure, but decreased with increasing temperature.Thermodynamic calculation of vapor-liquid equilibrium data of dimethyl ether-methanol-water ternary system was carried out by using the method based on equation of state-activity coefficient,with PR equation for fugacity coefficients of vapor phase and NRTL equation for activity coefficients of liquid phase, and the calculated data were in agreement with the experiment data.