کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
231750 1427447 2009 8 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Pressure profile separation of phenolic liquid compounds from cashew (Anacardium occidentale) shell with supercritical carbon dioxide and aspects of its phase equilibria
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Pressure profile separation of phenolic liquid compounds from cashew (Anacardium occidentale) shell with supercritical carbon dioxide and aspects of its phase equilibria
چکیده انگلیسی

Cashew nut shell liquid (CNSL) can be separated from fragmented honeycombed cashew shell material without employing thermal techniques with a pressure profile method that uses supercritical carbon dioxide as solvent. In the method, materials are contacted with CO2 at elevated pressure (ca. 30 MPa) for a given period of time (ca. 1 h) and then pressure is released before the separation process is begun. Using the method, extraction yields of CNSL of up to 10 times those obtained by usual supercritical fluid extraction were achieved. The CNSL obtained was clear with a yellow-light brown color. Analysis with liquid chromatography of the extracts contained approximately 50 mol% anacardic acids, 29 mol% cardols, and 21 mol% cardanols including mono-, di-, and tri-ene constituents. Phase equilibrium data of the extracted CNSL with CO2 were measured at temperatures from 25 to 98 °C, at pressures from 1.7 to 11 MPa, and at CO2 weight fractions from 0.0329 to 0.1139. Liquid–liquid–vapor equilibria occurs and the CO2–CNSL system has an upper critical end point at 31.13 °C and 7.402 MPa. Liquid–vapor equilibrium data were used to develop a model for describing the solubility of the CO2 in the CNSL phase. Based on calculations with the model, it was found that the temperature has different effects on the solubility depending on the pressure. At low pressures (

Cashew nut shell liquid (CNSL) can be separated in high yields from split cashew shells by a pressurization and depressurization step made prior to the extraction. The pressure is chosen by considering the solubility of supercritical CO2 in the CNSL that can be calculated from a developed equation of state model.Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: The Journal of Supercritical Fluids - Volume 48, Issue 3, April 2009, Pages 203–210
نویسندگان
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