کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
201747 460568 2013 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Isothermal vapor – liquid and vapor–liquid–liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Isothermal vapor – liquid and vapor–liquid–liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
چکیده انگلیسی

Isothermal vapor–liquid–liquid equilibrium data were measured for the ethanol + water + diethyl carbonate (DEC) ternary system and the constituent binaries using static headspace gas chromatography (HSGC) at 353.15 and 363.15 K. Multiple headspace extraction was used to calibrate the gas chromatograph. The activity coefficients were calculated using the Gibbs–Duhem equation and thermodynamic correlations. The thermodynamic consistency of the experimental vapor–liquid and vapor–liquid–liquid equilibrium data was verified. The experimental data were correlated using NRTL and UNIQUAC models, obtaining new UNIQUAC and NRTL interaction parameters for the VLE and VLLE.


► Isothermal VLE and VLLE data for the water + DEC + ethanol ternary system at 353.15 and 363.15 K.
► Prediction of VLE and VLLE with UNIQUAC and NRTL models.
► New UNIQUAC and NRTL interaction parameters for the VLE and VLLE.
► Identification of the azeotropic points.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 339, 15 February 2013, Pages 31–39
نویسندگان
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