Isobaric Vapor-Liquid Equilibrium of Binary Mixture of Methyl Acetate with Isopropylbenzene at 97.3 kPa
Commenced in January 2007
Frequency: Monthly
Edition: International
Paper Count: 32804
Isobaric Vapor-Liquid Equilibrium of Binary Mixture of Methyl Acetate with Isopropylbenzene at 97.3 kPa

Authors: Seema Kapoor, Baljinder K. Gill, V. K. Rattan

Abstract:

Isobaric vapor-liquid equilibrium measurements are reported for the binary mixture of Methyl acetate and Isopropylbenzene at 97.3 kPa. The measurements have been performed using a vapor recirculating type (modified Othmer's) equilibrium still. The mixture shows positive deviation from ideality and does not form an azeotrope. The activity coefficients have been calculated taking into consideration the vapor phase nonideality. The data satisfy the thermodynamic consistency tests of Herington and Black. The activity coefficients have been satisfactorily correlated by means of the Margules, NRTL, and Black equations. A comparison of the values of activity coefficients obtained by experimental data with the UNIFAC model has been made.

Keywords: Binary mixture, Isopropylbenzene, Methyl acetate, Vapor-liquid equilibrium.

Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1055493

Procedia APA BibTeX Chicago EndNote Harvard JSON MLA RIS XML ISO 690 PDF Downloads 2149

References:


[1] B. K. Gill, V. K. Rattan, and S. Kapoor, "Isobaric vapor-liquid equilibrium of binary mixtures of vinyl acetate and ethyl formate with cumene at 97.3 kPa," Journal of Chemical and Engineering Data, 2008, vol. 53, pp. 145-148.
[2] B. N. Raju, R. Ranganathan, and M. N. Rao, "Vapor-liquid equilibrium still for partially miscible systems," Indian Chemical Engineer, 1965, vol. 7, pp. T33-T37.
[3] B. Kumar, and K. S. N. Raju, "Vapor-liquid equilibrium data for the systems 2-methoxyethanol-ethylbenzene, 2-methoxyethanol-p-xylene, and 2-ethoxyethanol-p-xylene," Journal of Chemical and Engineering Data, 1977, vol.22, pp.134-137.
[4] J. A. Riddick, W. B. Bunger, and T. K. Sakano, Organic Solvents: Physical Properties and Methods of Purification. 4th ed. Wiley- Interscience: New York, 1986.
[5] B. K. Sood, O. P. Bagga, and K. S. N. Raju, "Vapor-liquid equilibrium data for systems ethylbenzene-anisole and p-xylene-anisole," Journal of Chemical and Engineering Data, 1972, vol. 17, pp. 435-438.
[6] H. C. Van Ness, and M. M. Abbott, Classical Thermodynamics of Nonelectrolyte Solutions. McGraw-Hill: New York, 1982.
[7] C. L. Yen, and S. S. Woods, "A Generalized equation for computer calculation of liquid densities," AIChE Journal, 1966, vol. 12, pp. 95- 99.
[8] C. Tsonopoulos, "An empirical correlation of second virial coefficients," AIChE Journal, 1974, vol. 20, pp. 263-272.
[9] J. Gmehling, J. Lohmann, and R. Wittig, "Vapor-liquid equilibria by UNIFAC Group Contribution. 6. Revision and extension," Industrial Engineering Chemistry Research, 2003, vol. 42, pp.183-188.
[10] J. M. Resa, C. Gonzalez, R. G. Concha, and M. Iglesias, "Effect of temperature on the change of refractive index on mixing for butyl acetate + aromatic hydrocarbons," International Journal of Thermophysics, 2005, vol. 26, pp. 1437-1459.
[11] R. L. Gardas, I. Johnson, D. M. D. Vaz, I. M. A. Fonseca, and A. G. M. Ferreira, "PVT property measurements for some aliphatic esters from (298 to 393) K and up to 35 MPa," Journal of Chemical and Engineering Data, 2007, vol. 52, pp.737-751.
[12] J. M. Resa, "Mixing properties of propyl acetate + aromatic hydrocarbons at 298.15 K," Korean Journal of Chemical Engineering, 2006, vol. 23, pp. 93-101.
[13] J. M. Resa, M. Iglesias, C. Gonzalez, and J. Lanz, "Excess volumes of binary mixtures of vinyl acetate and aromatic hydrocarbons," Journal of Chemical Thermodynamics, 2001, vol. 33, pp. 723-732.
[14] J. Deng, H. Tan, Y. Yang, S. Zai, G. Ouyang, and Z. Huang, "Densities and surface tensions of propyl acetate + xylene or + ethylbenzene from (298.15 to 308.15) K," Journal of Chemical and Engineering Data, 2007, vol. 52, pp. 1131-1135.
[15] S. Kapoor, "Thermodynamic studies of binary liquid mixtures," Ph.D. Thesis, Dept. Chemical Eng. & Tech., Panjab Univ., Chandigarh, India, 2005.
[16] E. F. G. Herington, "Tests for the consistency of experimental isobaric vapor-liquid equilibrium data," Journal of Institute of Petroleum, 1951, vol. 37, pp. 457-470.
[17] C. Black, "Vapor phase imperfections in vapor-liquid equilibria. Semiempirical Equation," Industrial Engineering Chemistry, 1958, vol. 50, pp. 391-402.
[18] H. Renon, and J. M. Prausnitz, "Local compositions in thermodynamic excess functions for liquid mixtures," AIChE Journal, 1968, vol. 14, pp. 135-144.
[19] V. K. Rattan, S. Kapoor, and S. Singh, "Isobaric vapor-liquid equilibria of 1-butanol- p-xylene system," International Journal of Thermophysics, 2006, vol. 27, pp. 85 -91.
[20] J. A. Riddick, W. B. Bunger, and T. K. Sakano, Organic Solvents: Physical Properties and Methods of Purification. 3rd ed. Wiley- Interscience: New York, 1970.
[21] R. C. Reid, J. M. Prausnitz, and B. E. Poling, The Properties of Gases & Liquids. 4th ed. McGraw-Hill: New York, 1987.
[22] R. M. Stephenson, and S. Malanowski, Handbook of the thermodynamics of organic compounds. Elsevier Publications, 1987.
[23] T. Boublik, V. Fried, and E. Hala, The Vapor Pressures of Pure Substances. Elsevier: New York, 1975.