Supercritical fluid carbon dioxide extraction (SFE-CO2)

HA Hadil Alaydi
PD Peter Downey
MM Michelle McKeon-Bennett
TB Tanya Beletskaya
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SFE-CO2 was performed on Super Critical Extraction system MV-10 ASCFE which consists of thermocube chiller, fluid delivery module (co-solvent pump and CO2 pump), extraction oven (extraction vessels), automatic backpressure regulator (ABPR) and fraction collection module with makeup pump by Waters (Dublin, Ireland). 3 g of powdered sample was placed into a 3 ml sample vessel and extracted under the following parameters: CO2 flow rate at 10 ml min−1, ethanol co-solvent flow rate at 0.05 ml min−1, and make-up solvent flow rate was 0.6 ml min−1. All flow rates were kept constant throughout the process. A three factors, four levels orthogonal array design of L16 (43)29 was employed for the optimisation of extraction parameters, temperature (C), pressure (bar), dynamic time (min) (Table (Table1).1). Sixteen experiments were performed in order to identify the best parameters for the extraction of polyprenol from selected plant species (Supplementary Table S1).

The parameters factors and levels of the orthogonal array design L16.

Further optimisation experiments were carried out to investigate the effect of the extended dynamic time. These extractions were conducted with dynamic time of up to 7 h. The temperature and pressure selections for these further time experiments were 200 bar and 70 C. Those temperature and pressure set-points were selected based on the initial development process being the best parameters which resulted in the highest polyprenol yield.

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