SCI和EI收录∣中国化工学会会刊

Chin.J.Chem.Eng. ›› 2012, Vol. 20 ›› Issue (4): 723-730.

• CHEMICAL ENGINEERING THERMODYNAMICS • Previous Articles     Next Articles

Vapor-Liquid Equilibrium of Ethyl Acetate+CnH2n+1OH(n=1, 2, 3) Binary Systems at 0.3 Mpa

SUSIAL P., RODRIGUEZ-HENRIQUEZ J. J., SOSA-ROSARIO A., RIOS-SANTANA R.   

  1. School of Industrial and Civil Engineering, University of Las Palmas de Gran Canaria, Canary Islands, Spain
  • Received:2011-03-31 Revised:2012-02-28 Online:2012-09-15 Published:2012-08-28

Vapor-Liquid Equilibrium of Ethyl Acetate+CnH2n+1OH(n=1, 2, 3) Binary Systems at 0.3 Mpa

SUSIAL P., RODRIGUEZ-HENRIQUEZ J. J., SOSA-ROSARIO A., RIOS-SANTANA R.   

  1. School of Industrial and Civil Engineering, University of Las Palmas de Gran Canaria, Canary Islands, Spain
  • 通讯作者: SUSIAL P., E-mail:psusial@dip.ulpgc.es

Abstract: 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.

Key words: vapor-liquid equilibrium, vapor-liquid equilibrium isobaric data, ethyl ester, alcohol

摘要: 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.

关键词: vapor-liquid equilibrium, vapor-liquid equilibrium isobaric data, ethyl ester, alcohol