Industrial & Engineering Chemistry Research · 2014 · 63 citations · 32 references
EngineeringChemical EngineeringFood ProcessingSeparation ProcessesSeparation ScienceKinetic ModelingMass TransferOilseed ProcessingSolvent ExtractionDiffusion CoefficientsExtraction KineticsFree Energy ChangesOil ExtractionTemperature Effects On ExtractionThermodynamics Of Extraction
In this study, the kinetics and thermodynamics of oil extraction from castor cake using ethanol were investigated. Castor cake had a total oil content of 14.78 ± 0.12% in mass and the average particle diameter was 0.446 mm. Oil extractions were carried out in a stirred batch extractor system at various temperatures (20, 30, 40, and 55 °C). The fit of three different kinetic models to the experimental data was tested, with a modified Fick’s Law model being the most appropriate to describe the extraction kinetics ( r 2 ≥ 0.960 and ARE ≤ 3.25%). Effective diffusion coefficients were determined, ranging from 4.52 × 10 –13 m 2 s –1 at 20 °C to 5.60 × 10 –13 m 2 s –1 at 55 °C. Change in Gibbs’ free energy (Δ G °) was determined to be negative (−4.55 kJ mol –1 at 20 °C to −6.56 kJ mol –1 at 55 °C), while changes in enthalpy (Δ H °) and entropy (Δ S °) were positive (12.27 kJ mol –1 and 57.41 J mol –1 K –1, respectively).
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An Empirical Model for the Description of Moisture Sorption Curves
Micha Peleg · Journal of Food Science · 1988 · 1.2K citations
Polyurethanes from Vegetable Oils
Zoran S. Petrovìć · Polymer Reviews · 2008 · 912 citations
Natural Sciences, Chemical Engineering, Materials Science +17