کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
9626019 | 460740 | 2005 | 10 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Liquid-liquid equilibria for pseudoternary systems: isooctane-benzene-(methanol + water)
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
مهندسی شیمی (عمومی)
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چکیده انگلیسی
Liquid-liquid equilibrium data are presented for the pseudoternary systems isooctane-benzene-(90 mass% methanol + 10 mass% water) at 298.15 K and isooctane-benzene-(80 mass% methanol + 20 mass% water) at 298.15 and 308.15 K, under atmospheric pressure. The experimental tie-line data obtained define the binodal curve for each one of the studied systems which depending on the amount of water present show type I or type II liquid-liquid phase diagrams. In order to obtain a general view of the effect of water on the partitioning of methanol and hence on the size of the two-phase region we have also determined experimentally 'isowater' tolerance curves for the system isooctane-benzene-methanol at 298.15 K, hence the tie-line data were also obtained for the ternary system. The experimental tie-line data for the four systems studied were correlated with the NRTL and UNIQUAC solution models obtaining a very good reproduction of the experimental behaviour.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 230, Issues 1â2, March 2005, Pages 121-130
Journal: Fluid Phase Equilibria - Volume 230, Issues 1â2, March 2005, Pages 121-130
نویسندگان
Blanca Estela GarcÃa-Flores, Mónica Gramajo de Doz, Arturo Trejo,