کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
230481 1427385 2014 6 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
High pressure vapor–liquid equilibrium for the ternary system ethanol/(±)-menthol/carbon dioxide
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
High pressure vapor–liquid equilibrium for the ternary system ethanol/(±)-menthol/carbon dioxide
چکیده انگلیسی


• VLE of the ethanol/(±)-menthol/CO2 ternary system at 313 and 323 K and 8–10 MPa.
• CO2 is more selective towards ethanol with separation factors from 1.6 to 7.6.
• The PR-MKP EOS was able to accurately correlate experimental data.

In this work the phase behavior of the ternary system ethanol/(±)-menthol/CO2 was studied at the temperatures of 313 and 323 K, in the pressure range 8–10 MPa. Experiments were performed using a high pressure phase equilibrium apparatus with a visual cell. CO2 is more selective toward ethanol, separation factors ranging from 1.6 to 7.6 at the conditions tested. The pTxy data obtained were correlated with the Peng–Robinson equation of state combined with the Mathias–Klotz–Prausnitz mixing rule. The model gave a good fitting to the data, with a total average absolute deviation of 3.7%, and was able to predict the occurrence of a three-phase region observed experimentally at 313 K and 9 MPa.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: The Journal of Supercritical Fluids - Volume 92, August 2014, Pages 282–287
نویسندگان
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