Issue
Korean Journal of Chemical Engineering,
Vol.31, No.12, 2245-2250, 2014
Excess properties and viscous flow thermodynamics of the binary system 1,2-ethanediamine+triethylene glycol at T=(298.15, 303.15, 308.15, and 313.15) K for CO2 capture
Liquid densities and viscosities are reported for the binary system of 1,2-ethanediamine (EDA)+triethylene glycol (TEG) at T=(298.15, 303.15, 308.15, and 313.15) K. Densities were measured using a capillary pycnometer and viscosities were determined using an Ubbelohde capillary viscometer. The experimental results are compared with data published in the literatures. Based on the density data and kinematic viscosity data, excess molar volumes (Vm E) and deviation in kinematic viscosity (Δν) were calculated and the calculated results were fitted to a Redlich-Kister equation to obtain the coefficients and estimate the standard deviations between the experimental and calculated quantities. The values of Vm E are negative in the whole composition range, whereas the values of Δν are positive over the major composition range. From kinematic viscosity data, Gibbs energies of activation of viscous flow (ΔG*), enthalpy of activation for viscous flow (ΔH*), and entropy of activation for the viscous flow (ΔS*) were also calculated.
[References]
  1. Luis P, Gerven TV, Bruggen BV, Prog. Energy Combust. Sci., 38, 419, 2012
  2. Koornneef J, Ramirez A, Harmelen T, Atmos. Environ., 44, 1369, 2010
  3. Song CF, Kitamura Y, Int. J. Greenh. Gas Con., 7, 107, 2012
  4. Ida J, Lin YS, Environ. Sci. Technol., 37, 1999, 2003
  5. Alvarez E, Cerdeira F, Gomez-Diaz D, Navaza JM, J. Chem. Eng. Data, 55(2), 994, 2010
  6. Han B, Sun YB, Fan MH, Cheng HS, J. Phys. Chem. B, 117(19), 5971, 2013
  7. Hiwale R, Hwang S, Smith R, Ind. Eng. Chem. Res., 51(11), 4328, 2012
  8. Bonenfant D, Mimeault M, Hausler R, Ind. Eng. Chem. Res., 42(14), 3179, 2003
  9. Camper D, Bara JE, Gin DL, Noble RD, Ind. Eng. Chem. Res., 47(21), 8496, 2008
  10. Park SY, Yi KB, Ko CH, Park JH, Kim J, Hong WH, Energy Fuel, 24, 3704, 2010
  11. Patil GN, Vaidya PD, Kenig EY, Ind. Eng. Chem. Res., 51(4), 1592, 2012
  12. Sada E, Kumazawa H, Butt MA, Chem. Eng. J., 13, 213, 1977
  13. Nuchitprasittichai A, Cremaschi S, Int. J. Greenh. Gas Con., 13, 34, 2013
  14. Guo ZH, Zhang JB, Zhang T, Li CP, Zhang YF, Bai J, J. Mol. Liq., 165, 27, 2012
  15. Afzal W, Mohammadi AH, Richon D, J. Chem. Eng. Data, 54(4), 1254, 2009
  16. Valtz A, Teodorescu M, Wichterle I, Richon D, Fluid Phase Equilib., 215(2), 129, 2004
  17. Li CP, Zhang JB, Zhang T, Wei XH, Zhang EQ, Yang N, Zhao NN, Su M, Zhou H, J. Chem. Eng. Data, 55(9), 4104, 2010
  18. Gladden JK, J. Chem. Eng. Data, 17, 468, 1972
  19. Saleh MA, Akhtar S, Ahmed S, J. Mol. Liq., 116, 147, 2005
  20. Ortega J, J. Indian Chem. Soc., LXIII, 961, 1986
  21. Naidu BVK, Rao KC, Subha MCS, J. Chem. Eng. Data, 48(3), 625, 2003
  22. Castellari C, J. Chem. Eng. Data, 51(2), 599, 2006
  23. Kumagai A, Mochida H, Takahashi S, Int. J. Thermophys., 14, 45, 1993
  24. Sastry NV, Thakor RR, Patel MC, Int. J. Thermophys., 29, 610, 2008
  25. Sastry NV, Patel MC, J. Chem. Eng. Data, 48(4), 1019, 2003
  26. Han F, Zhang JB, Chen GH, Wei XH, J. Chem. Eng. Data, 53(11), 2598, 2008
  27. Kapadi UR, Hundiwale DG, Patil NB, Lande MK, Fluid Phase Equilib., 25, 267, 2003