2005
DOI: 10.1016/j.jfoodeng.2004.07.020
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Supercritical carbon dioxide extraction of hazelnut oil

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Cited by 117 publications
(66 citation statements)
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“…The asymptotic profile obtained was characteristic of most SCCO 2 extraction reported in other microalgal studies (Cheung, 1999). The model correlated well with the experimental data for lipid evolution (compare 'Theoretical lipid yield' with 'Experimental lipid yield', r 2 60 C ¼ 0:93, r 2 80 C ¼ 0:92) and was consistent with the expected diffusion-driven nature of the SCCO 2 process, where the extraction rate was directly proportional to the amount of unextracted intracellular lipids (Ozkal et al, 2005).…”
Section: Mass Transfer Modelling For Scco 2 Extraction From Dried Micsupporting
confidence: 85%
See 1 more Smart Citation
“…The asymptotic profile obtained was characteristic of most SCCO 2 extraction reported in other microalgal studies (Cheung, 1999). The model correlated well with the experimental data for lipid evolution (compare 'Theoretical lipid yield' with 'Experimental lipid yield', r 2 60 C ¼ 0:93, r 2 80 C ¼ 0:92) and was consistent with the expected diffusion-driven nature of the SCCO 2 process, where the extraction rate was directly proportional to the amount of unextracted intracellular lipids (Ozkal et al, 2005).…”
Section: Mass Transfer Modelling For Scco 2 Extraction From Dried Micsupporting
confidence: 85%
“…In order to describe the mass transfer behaviour of lipid molecules during SCCO 2 extraction, the following kinetic model (Ozkal et al, 2005) was used:…”
Section: Mass Transfer Modelling For Scco 2 Extraction From Dried Micmentioning
confidence: 99%
“…An assumption was made that saturation of solute into the CO 2 was attained at these low velocities. The velocity employed in our study was comparable to the velocities reported in the literature dealing with dynamic method of solubility measurement (Danielski et al 2007;Ozkal et al 2005). Extraction curves are represented by the amount of CO 2 used for extraction and amount of caffeine extracted (Figs.…”
Section: Solubility Determinationsupporting
confidence: 67%
“…1 & 2). A second order polynomial equation was obtained fitting to the experimental data, and a straight line was drawn through the linear portion of the curve in order to find the initial slope (Danielski et al 2007;Ozkal et al 2005). Solubility values determined as weight fractions (kg caffeine/kg CO 2 ) were converted to mole fractions as required in the modeling equations.…”
Section: Solubility Determinationmentioning
confidence: 99%
“…El problema con muchos de los fluidos que aparecen en la Tabla 1, en comparación con el CO 2 es que hay ciertas dificultades en obtener solventes puros del fluido (Rozzi y Singh, 2002;Wark, 1985). Las ventajas de los fluidos supercríticos son: (Bruner, 2005;Hurtado, 2002;Sánchez et al, 2005;Tonthubthimthong et al, 2001;Zkal et al, 2005 1. Poseen alto coeficiente de difusión y viscosidad más baja que los líquidos; 2.…”
Section: Extraccion Con Fscunclassified