Abstract
Decaffeination of fresh green tea was carried out with supercritical CO2 in the presence of ethanol as co-solvent. The solubility of caffeine in supercritical CO2 varied from 44.19×10(-6) to 149.55×10(-6) (mole fraction) over a pressure and temperature range of 15 to 35MPa and 313 to 333K, respectively. The maximum solubility of caffeine was obtained at 25MPa and 323K. Experimental solubility data were correlated with the theoretical equation of state models Peng-Robinson (PR), Soave Redlich-Kwong (SRK), and Redlich-Kwong (RK). The RK model had regressed experimental data with 15.52% average absolute relative deviation (AARD). In contrast, Gordillo empirical model regressed the best to experimental data with only 0.96% AARD. Under supercritical conditions, solubility of caffeine in tea matrix was lower than the solubility of pure caffeine. Further, solubility of caffeine in supercritical CO2 was compared with solubility of pure caffeine in conventional solvents and a maximum solubility 90×10(-3)mol fraction was obtained with chloroform.
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