华南理工大学学报(自然科学版) ›› 2006, Vol. 34 ›› Issue (8): 18-21,26.

• 化学化工 • 上一篇    下一篇

仲丁醇-水-氟化钾及仲丁醇-水-碳酸钾体系的液-液相平衡

许文友1 周晓云2 王景阳2 刘文正2   

  1. 1.烟台大学 化工制造工程重点实验室,山东 烟台 264005;2.中国石油兰州石油化工公司 助剂厂,甘肃 兰州 730060
  • 收稿日期:2005-11-08 出版日期:2006-08-25 发布日期:2006-08-25
  • 通信作者: 许文友(1963-),男,博士,教授,主要从事分离工程研究 E-mail:xuwenyou@ytu.edu.cn
  • 作者简介:许文友(1963-),男,博士,教授,主要从事分离工程研究
  • 基金资助:

    山东省科技攻关计划项目(2005GGA06705)

Liquid-Liquid Equilibrium for Sec-Butanol-Water-KF and Sec-Butanol-Water-K2CO3 Systems

Xu Wen-you1  Zhou Xiao-yun2  Wang Jing-yang2  Liu Wen-zheng2   

  1. 1.Key Laboratory of Chemical Manufacture Engineering,Yantai Univ.,Yantai 264005,Shandong,China;2.CNPC Lanzhou Petroleum and Chemical Corporation Solvent Factory,Lanzhou 730060,Gansu,China
  • Received:2005-11-08 Online:2006-08-25 Published:2006-08-25
  • Contact: 许文友(1963-),男,博士,教授,主要从事分离工程研究 E-mail:xuwenyou@ytu.edu.cn
  • About author:许文友(1963-),男,博士,教授,主要从事分离工程研究
  • Supported by:

    山东省科技攻关计划项目(2005GGA06705)

摘要: 将氟化钾或碳酸钾加入到仲丁醇-水体系中时,可产生水富集相(水相)和仲丁醇富集相(仲丁醇相).文中通过实验测定了仲丁醇-水-氟化钾、仲丁醇-水-碳酸钾体系在25℃时的液-液相平衡数据,发现当水相中氟化钾或碳酸钾含量分别大于或等于26.38%(质量分数,下同)或28.76% 时产生的仲丁醇相中含有可以忽略的盐、水相中含有可以忽略的仲丁醇,因此用氟化钾或碳酸钾可以有效地分离仲丁醇-水体系.分别采用Pitzer方程和UNIQUAC方程计算水相和仲丁醇相中水的活度,将二者结合对液-液相平衡数据进行理论计算.理论计算值与实验值吻合较好,对仲丁醇-水-氟化钾体系实验值与计算值的绝对平均偏差水相为1.57%,有机相为0.33% ;对仲丁醇-水-碳酸钾体系实验值与计算值的绝对平均偏差水相为1.40% ,有机相为0.39%.

关键词: 仲丁醇-水-氟化钾体系, 仲丁醇-水-碳酸钾体系, 液-液相平衡, Pitzer方程, UNIQUAC方程, 理论计算, 分离

Abstract:

Both the water-rich phase(water phase)and the see-butanol-rich phase(see-butanol phase)can be form ed when adding KF or K2CO3 into the see-butanol-water system.In this paper,the data about the liquid-liquid equilibrium (LLE)of see-butanol-water-KF and see-butanol-water-K2CO3systems are measured at 25℃,showing that the see·-butanol phase contains negligible salt and the water phase contains negligible see-butanol when the
mass fraction of KF or K2CO3 in the water phase is not less than 26.38% or 28.76% ,respectively.Thus,water can be eficiently separated from the see-butanol-water system by adding KF or K2CO3 into the mixture.Moreover,a theoretical calculation of LLE data is carried out by using the Pitzer equation and the UNIQUAC equation to get the water activities respectively in the water phase and in the see-butanol phase.The calculated results are proved to be in good agreement with the experimental ones,the absolute mean deviations between the experimental data and the calculated results being 1.57% in the water phase and 0.33% in the see-butanol phase for see-butanol-wa-ter-KF system.and being 1.40% in the water phase and 0.39% in the sec-butanol phase for sec-butanol-water-K2CO3 system.

Key words: see-butanol-water-KF system, see-butanol-water-K2CO3 system, liquid-liquid equilibrium, Pitzer equation, UNIQUAC equation, theoretical calculation, separation