Saturated
fatty acids from palm oil are represented in this work using co-solvent
modified supercritical carbon dioxide (SC-CO 2). Saturated fatty acids are
abundant in palm oil. The purpose of this study is to see if phase equilibrium
mutual solubility techniques employing supercritical carbon dioxide are
feasible. Understanding the phase equilibrium is one of the most important
aspects of analysing the design of extraction processes guided by the
equilibrium. The temperatures used for extraction were 313.15 and 353.15 K,
with pressures ranging from 60 to 180 bars. A thermodynamic model based on the
Universal Functional Activity Coefficient was used to estimate the activity
coefficients expression for the system carbon dioxide / fatty acid (UNIFAC).
Adsorption, diffusion, mass transfer coefficient, solubility, and desorption
were all determined using mass transfer modelling.
Author(s) Details:
Mario Kabbour,
University Malaysia Perlis, 02600 Arau, Perlis, Malaysia.
Hiba Soufan,
Heriot-Watt University, 38103 Dubai, UAE.
Please see the link here: https://stm.bookpi.org/RACMS-V1/article/view/7110
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