کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
687834 | 889358 | 2010 | 5 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Feasibility of 1,3-butanediol as solvent for limonene and linalool separation
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
تکنولوژی و شیمی فرآیندی
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چکیده انگلیسی
Liquid–liquid equilibrium of the system limonene + linalool + 1,3-butanediol has been studied at two different temperatures. The obtained data were satisfactorily correlated with the NRTL activity coefficient model, in order to obtain the binary interaction parameters of the mixture. Later on, an extraction column was simulated with ASPEN PLUS® software, to ascertain the feasibility of 1,3-butanediol as solvent for limonene and linalool separation and to determine the advantages of this solvent over the employed previous ones in this process. The influence of the number of theoretical stages and the solvent/feed ratio over the amount and purity of the recovered limonene and linalool were also studied.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering and Processing: Process Intensification - Volume 49, Issue 11, November 2010, Pages 1183–1187
Journal: Chemical Engineering and Processing: Process Intensification - Volume 49, Issue 11, November 2010, Pages 1183–1187
نویسندگان
Mª. Dolores Romero, Eduardo Díez, Ismael Díaz,