Issue
Korean Journal of Chemical Engineering,
Vol.29, No.5, 644-649, 2012
Vapor-liquid equilibra for cyclohexane+2-propoxyethanol and cyclohexane+2-butoxyethanol systems
2-propoxyethanol (C3E1) and 2-butoxyethanol (C4E1) are nonionic surfactants which are a particularly interesting class of substances due to both inter-molecular and intra-molecular association, related to the presence of O and OH in the same molecule. Binary (vapor+liquid) equilibrium data were measured for cyclohexane+2-propoxyethanol and cyclohexane+2-butoxy ethanol systems at temperatures ranging from 303.15 K to 323.15 K at 10 K intervals. A static apparatus was used in this study. Two systems show positive deviation from Raoult’s law and no azeotrope. The experimental data were correlated well with Peng-Robinson-Stryjek-Vera equation of state using Wong-Sandler mixing rule incorporating the non-random-two-liquid model.
[References]
  1. OH SG, KIM JG, KIM JD, Korean J. Chem. Eng., 4(1), 53, 1987
  2. Davis MI, Thermochim. Acta., 190, 259, 1991
  3. Lee HS, Lee H, J. Chem. Eng. Data, 41(6), 1358, 1996
  4. Lai HH, Chen LJ, J. Chem. Eng. Data., 44, 251, 1996
  5. Carmona FJ, Bhethanabotla VR, Campbell SW, Gonzalez JA, de la Fuente IG, Cobos JC, J. Chem. Thermodyn., 33(1), 47, 2001
  6. Carmona FJ, Gonzalez JA, Garcia de la Fuente I, Cobos JC, Bhethanabotla VR, Campbell SC, J. Chem. Eng. Data., 45, 699, 2000
  7. Jang S, Shin MS, Lee Y, Kim H, J. Chem. Thermodyn., 41(1), 51, 2009
  8. Shin MS, Kim H, J. Chem. Thermodyn., 40(7), 1110, 2008
  9. Lee Y, Jang S, Shin MS, Kim H, Fluid Phase Equilib., 276(1), 53, 2009
  10. Jang S, Hyeong S, Shin MS, Kim H, Fluid Phase Equilib., 298, 270, 2009
  11. Stryjek R, Vera JH, Can. J. Chem. Eng., 64, 323, 1986
  12. Wong DS, Sander SI, AIChE J., 38, 671, 1992
  13. Gibbs RE, Van Ness HC, Ind. Eng. Chem. Fundam., 11, 410, 1972
  14. Giles NF, Wilson HL, Wilding WV, J. Chem. Eng. Data, 41(6), 1223, 1996
  15. Renon H, Prausnitz JM, AIChE J., 14, 135, 1968
  16. Gmehling J, Fluid Phase Equilib., 107(1), 1, 1995