کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
229071 464858 2008 6 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Liquid–liquid equilibrium for the quaternary system water + tetrahydrofuran + n-heptane + butyl acetate mixture at 25 °C and atmospheric pressure
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Liquid–liquid equilibrium for the quaternary system water + tetrahydrofuran + n-heptane + butyl acetate mixture at 25 °C and atmospheric pressure
چکیده انگلیسی

Liquid–liquid equilibrium for the quaternary system water + tetrahydrofuran + n-heptane + butyl acetate mixture was measured at 25 °C and atmospheric pressure. Binodal curves, tie-lines, distribution, and selectivity for the quaternary system have been determined in order to investigate the effect of using binary solvents, n-heptane and butyl acetate, on extracting tetrahydrofuran from aqueous solution. In addition, these experimental tie-line data were also compared with the values predicted by the UNIFAC model. It is found that the UNIFAC group interaction parameters used for LLE could not provide a good prediction.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Journal of Industrial and Engineering Chemistry - Volume 14, Issue 5, September 2008, Pages 602–607
نویسندگان
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