期刊文献+

水-醋酸-二异丙醚三元体系液液相平衡数据的测定 被引量:1

Measurement of Liquid-Liquid Equilibrium Data for the Ternary System of Water + Acetic acid + Diisopropyl Ether
下载PDF
导出
摘要 实验测定了水-醋酸-二异丙醚三元体系在293.15 K、303.15 K的液液相平衡数据。分别采用Othmer-Tobias和Bachman方程对实验数据进行了可靠性检验,相关性系数均大于0.983。绘制了三元液液平衡相图。 Liquid–liquid equilibrium(LLE) data for the ternary system of water + acetic acid + diisopropyl ether at 293.15 K and 303.15 K have been measured under atmospheric pressure.The experimental data were correlated by the equations of Othmer-Tobias and Bachman,respectively.All the linear correlation coefficients are greater than 0.983.The LLE phase diagram of the investigated system at different temperature was given.
作者 庄六星 白璐
出处 《上海化工》 CAS 2011年第6期10-12,共3页 Shanghai Chemical Industry
关键词 液液平衡 二异丙醚 液液平衡相图 Liquid-liquid equilibrium Diisopropyl ether LLE phase diagram
  • 相关文献

参考文献7

  • 1Fahim M A, Al-Muhtaseb S A. Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + l-Hexanol[J]. J. Chem. Eng. Data,1997, 42:183-186.
  • 2Fahim M A, Al-Muhtaseb S A. Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + 2-Methyl-2-butanol [J]. J. Chem. Eng. Data, 1996, 41: 1 311-1 314.
  • 3Ince E. Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + Dimethyl Adipate [J]. Fluid Phase Equilib, 2005, 230:58-63.
  • 4Colombo A, Battilana P, Ragaini V, et al. Liquid-Liquid Equilibria of the Ternary Systems Water + Acetic Acid + Ethyl Acetate and Water + Acetic Acid + Isophorone (3,5,5-Trimethyl-2-cyclohexen-l-one)[J]. J. Chem.Eng. Data, 1999, 44:35-39.
  • 5Xiangyang Miao, Hongxun Zhang, Tiangui Wang, et al. Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + Methyl tert-Butyl Ether [J]. J. Chem. Eng. Data, 2007, 52:789-793.
  • 6SUNGJIN L, HWAYONG K. Liquid- Liquid Equilibria for the Ternary Systems Sulfolane + Octane + Benzene, Sulfolane + Octane + Toluene, and Sulfolane + Octane + p- Xylene at Elevated Temperatures [J]. J. Chem. Eng. Data, 1998, 43(3) : 358-361.
  • 7陈东初,叶红齐,吴浩.庚烷-苯-N-甲酰吗啉体系液液平衡研究[J].湖南科技大学学报(自然科学版),2007,22(3):113-117. 被引量:3

二级参考文献13

  • 1[1]TRIPATHI R P,RAJA R A,RAO P B.Liquid-Liquid Equilibriums in Ternary System Toluene-n-Heptane-Sulfolane[J].J Chem Eng Data,1975,20(3):261-264.
  • 2[2]ASHOUR I,ABU-EISHAH S I.Liquid-Liquid Equilibria for Cyclohexane + Ethylbenzene + Sulfolane at (303.15,313.15,and 323.15) K[J].Chem Eng Data,2006,51 (3):859-863.
  • 3[3]MOHSEN-NIA M,MODARRESS H,DOULABI F,et al.Liquid +Liquid Equilibria for Ternary Mixtures of (Solvent + Aromatic Hydrocarbon + Alkane)[J].The Journal of Chemical Thermodynamics,2005,37(10):1 111-1 118.
  • 4[4]AHMAD S A,TANWAR R S,GUPTA R K,et al.Interaction Parameters for Multi-Component Aromatic Extraction with Sulfolane[J].Fluid Phase Equilibria,2004,220(2):189-198.
  • 5[5]SUNGJIN L,HWAYONG K.Liquid-Liquid Equilibria for the Ternary Systems Sulfolane + Octane + Benzene,Sulfolane + Octane + Toluene,and Sulfolane + Octane + p-Xylene at Elevated Temperatures[J].J Chem Eng Data,1998,43(3):358-361.
  • 6[6]TAHER A.Al-Sahhaf,Emina Kapetanovic,Measurement and Prediction of Phase Equilibria in the Extraction of Aromatics from Naphtha Reformate by Tetraethylene Glycol[J].Fluid Phase Equilibria,1996,118(2):271-285.
  • 7[7]GUPTA S K.Isothermal Vapor-Liquid Equilibria of o-,m-,and P-Xylene with N-Methylpyrrolidone at 373.15 K and 393.15 K[J].J Chem Eng Data,1999,44(1):23-25.
  • 8[8]TAHER A A S,Emina K.Measurement and Prediction of Phase Equilibria in the Extraction of Aromatics from Naphtha Reformate by Tetraethylene Glycol[J].Fluid Phase Equilib,1996,118(2):271-285.
  • 9[9]CINCOTTI A,MURRU M,CAO G,et al.Liquid-Liquid Equilibria of Hydrocarbons with N-Formylmorpholine[J].Chem Eng Data,1999,44(3):480-483.
  • 10[10]MOHAMED A Q,TAHER A A,MOHAMED A F.Liquid-Liquid Equilibria in Some Binary and Ternary Mixtures with N-Formylmorpholine[J].J Chem Eng Data,1995,40(1):88-90.

共引文献2

同被引文献18

  • 1李猛,刘俊东,那宏壮.丁酮肟的应用及合成进展[J].化学工程师,2006,20(7):42-43. 被引量:15
  • 2ZHAO Jun-ming(赵俊明).Simulation and optimization of the reactive extraction process for MEKO production with HPO process(磷酸羟胺法制丁酮肟反应萃取过程的模拟与优化)[D].Shanghai(上海):East China University of Science and Technology(华东理工大学),2013.
  • 3Huddleston J G,Willauer H D,Swatloski R P,et al.Room temperature ionic liquids as novel media for‘clean’liquid-liquid extraction[J].Chemical Communications,1998(16):1765-1766.
  • 4Seddon K R.Ionic liquids for clean technology[J].Journal of Chemical Technology and Biotechnology,1997,68(4):351-356.
  • 5Liu J F,Chi Y G,Jiang G B.Screening the extractability of some typical environmental pollutants by ionic liquids in liquid-phase micro-extraction[J].Journal of Separation Science,2005,28(1):87-91.
  • 6Pereiro A B,Araújo J M M,Oliveira F S S,et al.Solubility of inorganic salts in pure ionic liquids[J].The Journal of Chemical Thermodynamics,2012,55(12):29-36.
  • 7Bachman I.Tie lines in ternary liquid systems[J].Industrial and Engineering Chemistry,Analytical Edition,1940,12(1):38-39.
  • 8Xu D M,Wu C X,Zhang Q,et al.Liquid–liquid equilibrium for the ternary systems water+2-methyl-1-propanol+butyl acetate and water+2-methyl-2-propanol+butyl acetate at(298.15 and 323.15)K[J].Fluid Phase Equilibria,2014,381(11):60-66.
  • 9Chen Y,Wang Z,Li L B.Liquid–liquid equilibria for ternary systems:methyl butyl ketone+phenol+water and methyl butyl ketone+hydroquinone+water at 298.15 K and 323.15 K[J].J Chem Eng Data,2014,59(9):2750-2755.
  • 10Quzhou Jinhua Chemical Co.Ltd(衢州锦华化工有限公司),Zhejiang University(浙江大学).Acceptance materials on science and technology projects of Zhejiang Province:development and application of reaction-separation intergration technologies(浙江省科技计划项目验收资料:反应-分离集成技术的开发及其推广应用)[Z].2009.

引证文献1

二级引证文献3

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部