Mathematical modeling of supercritical fluid extraction of flax seed oil in a pilot plant system: tocopherol content
Litsenziya: cc-by-nc
Annotatsiya
Recent research has focused on the application of supercritical fluid extraction (SFE) at pilot scale. This study specifically addresses the SFE of flaxseed oil and its mathematical modeling in a pilot plant system, utilizing the BIC (Broken and Intact model) model. Particle size was found to have an effect on the mass transfer coefficient of the solid phase (ksa, s⁻¹). However, solubility values fluctuated (ranging from 0.169 to 0.06 g/g CO₂) as the pressure increased from 35 MPa to 45 MPa. The study also examined the influence of enzymatic action and t 0 (the extraction time before the process variables were fixed) on solubility. Besides, above-mentioned circumstances the results of the laboratory and pilot scale studies were close each other. Tocopherol content analysis revealed that optimal extraction conditions for bioactive compound preservation (35 MPa, 55°C: 0.125 µg/mg γ-tocopherol) differed from conditions maximizing extraction rate, demonstrating the importance of integrating quality parameters with mathematical modeling for pilot-scale process design. This provides new optimization criteria beyond conventional yield-based approaches.
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