کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
202045 460583 2011 5 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Liquid–liquid equilibrium for the ternary system isopropenyl acetate + water + acetic acid at 298.2 K, 313.2 K, 323.2 K and 333.2 K
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Liquid–liquid equilibrium for the ternary system isopropenyl acetate + water + acetic acid at 298.2 K, 313.2 K, 323.2 K and 333.2 K
چکیده انگلیسی

Liquid–liquid equilibrium data for the ternary system isopropenyl acetate + water + acetic acid were measured at 298.2 K, 313.2 K, 323.2 K, 333.2 K and atmospheric pressure. Binodal curves were obtained by the cloud point method, while compositions of tie-lines were obtained by gas chromatography. The plait points were calculated by a convenient method described by Treybal and the consistency of the tie-line data were ascertained by Ishida correlation. In addition, the experimental data were correlated by the NRTL model and UNIQUAC model. Root mean square deviations between experimental and calculated compositions were considered satisfactory.


► Determined LLE for isopropenyl acetate + water + acetic acid.
► Calculated the plait points and ascertained the consistency of the tie-line data.
► Calculated the interaction parameters in NRTL and UNIQUAC.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 311, 15 December 2011, Pages 54–58
نویسندگان
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