Article ID Journal Published Year Pages File Type
6375560 Industrial Crops and Products 2015 7 Pages PDF
Abstract
The aim of the present work is to determine the solubility of castor oil by using supercritical carbon dioxide as extracting solvent. A simple dynamic technique was used to obtain the solubility of castor oil in supercritical carbon dioxide. The solubility was measured at temperatures ranging from 313 to 335 K and pressures from 20 to 36 MPa. Under extraction conditions, the measured solubilities were in the range from 1.29 × 10−3 to 4.88 × 10−3 (g of oil)/(g of CO2). Measurements confirmed that temperature and pressure have direct effects on solubility-enhancement factors. Five semi-empirical models were tested for their ability to correlate experimental data: the Chrastil, Del Valle Aguilera (VA), Bartle, Kumar and Johnston (KJ), and Mendez-Santiago and Teja (MST) models. Over the temperature and pressure ranges studied, solubilities from these models had the following average absolute relative deviations from experimental data: Chrastil, VA, Bartle, KJ and MST models with an average absolute relative deviation percent (AARD%) of 0.05%, 0.30%, 0.38%, 5.98% and 28.4%, respectively. Thus, the Chrastil, VA and Bartle models correlated the castor oil solubility data with the lowest AARD%.
Related Topics
Life Sciences Agricultural and Biological Sciences Agronomy and Crop Science
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