Published

1999-01-01

Análisis teórico de la influencia del régimen de mezclado para la producción de acetato de etilo

DOI:

https://doi.org/10.15446/ing.investig.n42.21064

Keywords:

Procesos de esterificación, Catalizadores, Reacciones químicas, Obtención de acetato de etilo (es)
Esterification processes, Catalysts, Chemical reactions, Ethyl acetate production (en)

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Authors

  • Hugo Alexander Martínez C. Universidad Nacional de Colombia
  • Luis M. Carballo S. Universidad Nacional de Colombia

Se efectúa un análisis teórico a la reacción de esterificación entre ácido acético y etanol tendiente a conocer la conveniencia de operar en modo de CSTR (reactor de mezcla total ideal) o PFTR (reactor de flujo pistón), para un conjunto dado de parámetros fisicoquímicos y cinética de esterificación de seudoprimer orden.

References

Aris, R, “The mathematical theory of diffusion and reaction in permeable catalysts”. Clarendon Press, Vol. 1, Oxford. 1975.

Fogler, S. Elements of Chemical Reaction Engineering. 2nd ed, Prentice Hall. 1992.3. FROMENT, G. Chemical Reactor Analysis and Design. 2nd ed, John Wiley. 1990.

Froment, G. Chemical Reactor Analysis and Design. 2nd ed, John Wiley. 1990.

Lapidus, L., Amundson, N. Chemical Reactor Theory a Review. Prentice — Hall, New Jersey. 1977.

Sardin, M. Villermaux, J. “Esterification catalysee par une resine echangeuse de cation dans un reacteur chromatographique”, Nouveau Journal of Chimie, Vol. 3, No. 4, p. 225. 1979.

Sawistowski, H. Pilavakis, P. “Performance of esterification in a reaction distillation column” .Chem. Eng. Sci. Vol. 43, No. 2, Pág 355, 1988.

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How to Cite

Análisis teórico de la influencia del régimen de mezclado para la producción de acetato de etilo. (1999). Ingeniería E Investigación, 42, 17-21. https://doi.org/10.15446/ing.investig.n42.21064
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Copyright (c) 1999 Hugo Alexander Martínez C., Luis M. Carballo S.

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