کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
201338 460545 2016 6 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Experimental isobaric (vapor + liquid) equilibrium data for the binary system N, N-dimethyl formamide + dimethyl sulfoxide and the quaternary system sec-butyl alcohol + sec-butyl acetate + N, N-dimethyl formamide + dimethyl sulfoxide at 101.3 kPa
ترجمه فارسی عنوان
داده های تعادلی ایزوباریک (بخار + مایع) برای سیستم دودویی N، N-dimethylformamide + دی متیل سولفوکسید و سیستم کواترنری سد-بوتیل الکل + sec-butyl acetate + N، N-dimethylformamide + dimethyl sulfoxide در 101.3 kPa
کلمات کلیدی
sec-butyl alcohol؛ sec-butyl acetate؛ N، N-Dimethylformamide؛ دی متیل سولفوکسید؛ تعادل بخار و مایع
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی

Isobaric vapor–liquid equilibrium (VLE) data for the quaternary system sec-butyl alcohol + sec-butyl acetate + N, N-dimethyl formamide (DMF) + dimethyl sulfoxide (DMSO) and the constituent binary system DMF + DMSO were determined at 101.3 kPa with a modified Othmer still. The measured experimental data of binary and quaternary systems were certified to be thermodynamically consistent according to the Van Ness method. And the experimental binary data were correlated by Wilson, NRTL and UNIQUAC activity coefficient models. The rest of binary interaction parameters have been obtained in our previous work. Then, the binary and quaternary vapor–liquid equilibrium were predicted by the models with the correlated parameters. The results show that the three models yield a good prediction for the binary and quaternary systems. But NRTL model performed better than the other two models in predicting VLE of the quaternary system.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fluid Phase Equilibria - Volume 409, 15 February 2016, Pages 78–83
نویسندگان
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