Phase equilibria for the system diethyl succinate - Ethanol - Water

A. Oriuela, D. J. Miller, C. T. Lira, D. T. Vu, A. J. Yanez

Research output: Chapter in Book/Report/Conference proceedingConference contribution

Abstract

Phase equilibria information, particularly VLE and liquid-liquid equilibria (LLE), is critical for reliable reactive distillation (RD) process design. To obtain activity model parameters for the design of a diethyl succinate RD process, binary P-x-y data for diethyl succinate + ethanol were collected at 323.15 K, and ternary LLE data for diethyl succinate + ethanol + water were obtained at 303.15 and 313.15 K. The experimental data were fitted with a modified UNIQUAC equation for the liquid phase, and an association model for the vapor phase (Hayden O'Connell) using ASPEN PLUS® data regression tool. Binary parameters obtained fitted reasonably well the experimental and reported data, and were satisfactory for design purposes. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montréal, Quebec, Canada 8/23-27/2009).

LanguageEnglish (US)
Title of host publication8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering
StatePublished - 2009
Event8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering - Montreal, QC, Canada
Duration: Aug 23 2009Aug 27 2009

Other

Other8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering
CountryCanada
CityMontreal, QC
Period8/23/098/27/09

Profile

Phase equilibria
Distillation
Ethanol
Water
Liquids
Chemical Engineering
Quebec
Canada
Chemical engineering
Process design
Vapors
diethyl succinate
Association reactions

ASJC Scopus subject areas

  • Biotechnology
  • Chemical Health and Safety
  • Process Chemistry and Technology
  • Renewable Energy, Sustainability and the Environment

Cite this

Oriuela, A., Miller, D. J., Lira, C. T., Vu, D. T., & Yanez, A. J. (2009). Phase equilibria for the system diethyl succinate - Ethanol - Water. In 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering

Phase equilibria for the system diethyl succinate - Ethanol - Water. / Oriuela, A.; Miller, D. J.; Lira, C. T.; Vu, D. T.; Yanez, A. J.

8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering. 2009.

Research output: Chapter in Book/Report/Conference proceedingConference contribution

Oriuela, A, Miller, DJ, Lira, CT, Vu, DT & Yanez, AJ 2009, Phase equilibria for the system diethyl succinate - Ethanol - Water. in 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering. 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering, Montreal, QC, Canada, 8/23/09.
Oriuela A, Miller DJ, Lira CT, Vu DT, Yanez AJ. Phase equilibria for the system diethyl succinate - Ethanol - Water. In 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering. 2009.
Oriuela, A. ; Miller, D. J. ; Lira, C. T. ; Vu, D. T. ; Yanez, A. J./ Phase equilibria for the system diethyl succinate - Ethanol - Water. 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering. 2009.
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