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Simulation of N-Propanol Dehydration Process Via Heterogeneous Azeotropic Distillation Using the NRTL Equation

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Numerical values of the NRTL equation parameters for calculation of the vapour - liquid - liquid equilibria (VLLE) at atmospheric pressures have been presented for 5 ternary mixtures. These values were fitted to the experimental VLLE and vapour - liquid equilibrium (VLE) data to describe simultaneously, as accurately as possible, the VLE and the liquid - liquid equilibria (LLE). The coefficients of this model called further NRTL-VLL were used for simulations of n-propanol dehydration via heterogeneous azeotropic distillation. The calculations performed by a ChemCAD simulator were done for 4 mixtures using hydrocarbons, ether and ester as an entrainer. In majority simulations the top streams of the azeotropic column had composition and temperature similar to the corresponding experimental values of ternary azeotropes. The agreement between the concentrations of both liquid phases formed in a decanter and the experimental values of the LLE was good for all four simulations. The energy requirements were the most advantageous for the simulation with di-npropyl ether (DNPE) and isooctane. Simulations were performed also for one mixture using the NRTL equation coefficients taken from the ChemCAD database. In that case the compositions of the liquid organic phases leaving the decanter differed significantly from the experimental LLE data.
Rocznik
Strony
163--175
Opis fizyczny
Bibliogr. 24 poz., tab., rys.
Twórcy
autor
  • Institute of Organic Chemistry and Technology, University of Technology, 31 - 155 Kraków, Poland
Bibliografia
  • 1. Arifin S., Chien I.L., 2007. Combined preconcentrator/recovery column design for isopropyl alcohol dehydration process. Ind. Eng. Chem. Res., 46, 2535-2543. DOI: 10.1021/ie061446c.
  • 2. Cairns B.P., Furzer I., 1990. A multicomponent three-phase azeotropic distillation. 3. Modern thermodynamic models and multiple solutions. Ind. Eng. Chem. Res., 29, 1383-1395. DOI: 10.1021/ie00103a042.
  • 3. Chang W.T., Huang C.T., Cheng S.H., 2012. Design and control of a complete azeotropic distillation system incorporating stripping columns for isopropyl alcohol dehydration. Ind. Eng.Chem. Res., 51, 2997-3006. DOI: 10.1021/ie202021g.
  • 4. Chemcad VI. Process Flowsheet Simulator, 6.4.0.5052 version, Chemctations Inc., Huston 2010.
  • 5. Font A., Asensi J.C., Ruiz F., Gomis V., 2003. Application of isooctane to the dehydration of ethanol. Design of a column sequence to obtain absolute ethanol by heterogeneous azeotropic distillation. Ind. Eng. Chem. Res., 42, 140-144. DOI: 10.1021/ie0204078.
  • 6. Gomis V., Font A., Pedraza R., Saquete M.D., 2005. Isobaric vapor – liquid and vapor – liquid – liquid equilibrium data for the water + ethanol + cyclohexane system. Fluid Phase Equil., 235, 7-10. DOI: 10.1016/j.fluid.2005.07.015.
  • 7. Gomis V., Font A., Saquete M.D., 2006. Vapour – liquid – liquid and vapour – liquid equilibrium of the system water + ethanol + heptane at 101.3 kPa. Fluid Phase Equil., 248, 206 – 210. DOI: 10.1016/j.fluid.2006.08.012.
  • 8. Gomis V., Font A., Pedraza R., Saquete M.D., 2007a. Isobaric vapor – liquid and vapor – liquid – liquid equilibrium data for the water – ethanol – hexane system. Fluid Phase Equil., 259, 66-70. DOI: 10.1016/j.fluid.2007.04.011.
  • 9. Gomis V., Pedraza R., Frances O., Font A., Asensi J.C. 2007b. Dehydration of Ethanol Using Azeotropic Distillation with Isooctane. Ind. Eng. Chem. Res., 46, 4572 - 4576. DOI: 10.1021/ie0616343.
  • 10. Gomis V., Pedraza R., Saquete, M. D., Font A., García-Cano J., 2015. Ethanol dehydration via azeotropic distillation with gasoline fractions as entrainers: A pilot-scale study of the manufacture of an ethanol–hydrocarbon fuel blend. Fuel, 139, 568-574. DOI: 10.1016/j.fuel.2014.09.041.
  • 11. Horsley L.H., 1962. Azotropic Data; Advances in Chemistry Series Number 35; American Chemical Society: Washington, DC.
  • 12. Lee L.S., Shen H.C., 2003. Azeotropic behavior of a water + n-propanol + cyclohexane mixture using cyclohexane as an entrainer for separating the water + n-proponal mixture at 760 mmHg. Ind. Eng. Chem. Res., 42, 5905 - 5914. DOI: 10.1021/ie0208220.
  • 13. Lladosa E., Monton J. B., Burguet M.C., Munoz R., 2006. Isobaric vapor–liquid equilibria for the binary systems 1-propyl alcohol + dipropyl ether and 1-butyl alcohol + dibutyl ether at 20 and 101.3 kPa. Fluid Phase Equil., 247, 47 - 53. DOI: 10.1016/j.fluid.2006.06.017.
  • 14. Lladosa E., Monton J.B., Burguet M.C., de la Torre J., 2008. Isobaric (vapour+liquid+liquid) equilibrium data for (di-n-propyl ether+n-propyl alcohol+water) and (diisopropyl ether+isopropyl alcohol+water) systems at 100kPa. J. Chem. Therm., 40, 867-873. DOI: 10.1016/j.jct.2008.01.002.
  • 15. Mączyński A., Mączyńska Z.,1981. Verified vapour-liquid equilibrium data. Binary one-liquid systems of water and organic compounds. PWN, Warszawa, Vol. 5, p. 102, data 8.
  • 16. Mączyński A., Biliński A., Oracz P., Treszczanowicz T., 1982. Verified vapour-liquid equilibrium data. Binary systems of C4+ hydrocarbons and alcohols. PWN, Warszawa, Vol. 6, p. 106, data 9.
  • 17. Mączyński A., Biliński A., Mączyńska Z., 1984. Verified vapour-liquid equilibrium data. Binary systems of alcohols and oxygen compounds. PWN, Warszawa, Vol. 8, p. 237, data 1.
  • 18. Pienaar C., Schwarz C.E., Knoetze J.H., Burger, A.J., 2013. Vapour−liquid−liquid equilibria measurements for the dehydration of ethanol, isopropanol, and n-propanol via azeotropic distillation using DIPE and isooctane as entrainers. J. Chem. Eng. Data, 58, 537-550. DOI: 10.1021/je300847v.
  • 19. Pla-Franco J., Lladosa E., Loras S., Monton J.B., 2014a. Thermodynamic analysis and process simulation of ethanol dehydration via heterogeneous azeotropic distillation. Ind. Eng. Chem. Res., 53, 6084-6093. DOI: 10.1021/ie403988c.
  • 20. Pla-Franco J., Lladosa E., Loras S., Monton J.B., 2014b. Isobaric vapour−liquid−liquid equilibria for the ternary systems ethanol + water + propyl acetate and 1-propanol + water + propyl acetate. J. Chem. Eng. Data, 59, 2054-2064. DOI: 10.1021/je500191j.
  • 21. Wu Y.C., Chien I.L., 2009. Design and control of heterogeneous azeotropic column system for the separation of pyridine and water. Ind. Eng. Chem. Res., 48, 10564-10576. DOI: 10.1021/ie901231s.
  • 22. Wyczesany A., 2011. Wykorzystanie symulatora Chemcad do modelowania destylacji hetero azeotropowej mieszanin zawierających wodę i etanol. Przem. Chem., 90, 1419-1424.
  • 23. Wyczesany A., 2014. Calculation of vapour−liquid−liquid equilibria at atmospheric and high pressures. Ind. Eng. Chem. Res., 53, 2509-2519. DOI: 10.1021/ie403418p.
  • 24. Young S., 1902. The preparation of absolute alcohol from strong spirit. J. Chem. Soc., Trans., 81, 707-717. DOI: 10.1039/CT9028100707.
Uwagi
PL
Opracowanie ze środków MNiSW w ramach umowy 812/P-DUN/2016 na działalność upowszechniającą naukę (zadania 2017)
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-a0a6ab1a-e264-406c-bfb9-341b90545c75
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