1997
DOI: 10.1007/bf02707049
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Measurement and modeling solubility of bioactive coumarin and its derivatives in supercritical carbon dioxide

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Cited by 12 publications
(9 citation statements)
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“…Critical temperature (T c = 794.77 K), critical pressure (P c = 4.347 MPa), and acentric factor (w = 0.3945) of coumarin used in the PR-EoS were obtained using the Constantinou and Gani method (Poling et al, 2000). Similar values were found by Yoo et al (1997) using the Lyderson-Forman-Thodos method. The values of same properties for CO 2 were obtained from Poling et al (2000).…”
Section: Thermodynamic Modelingsupporting
confidence: 86%
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“…Critical temperature (T c = 794.77 K), critical pressure (P c = 4.347 MPa), and acentric factor (w = 0.3945) of coumarin used in the PR-EoS were obtained using the Constantinou and Gani method (Poling et al, 2000). Similar values were found by Yoo et al (1997) using the Lyderson-Forman-Thodos method. The values of same properties for CO 2 were obtained from Poling et al (2000).…”
Section: Thermodynamic Modelingsupporting
confidence: 86%
“…In addition, it is not possible to visualize both a homogeneous phase and phase transition through the extractive method. Yoo et al (1997) determined solubility values of coumarin in supercritical CO 2 using a microscale apparatus through the analytical method. The authors observed lower values than those found in the present work.…”
Section: Resultsmentioning
confidence: 99%
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“…Food processing industry is a major user of the supercritical fluid carbon dioxide extraction process, and the applications include extraction and fractionation of fats, oils, essences, pigments, and functional or bioactive compounds (Reverchon 1997). Majority of the published work on coumarin extraction using supercritical fluid carbon dioxide has focused on solubility of coumarin and its derivatives in supercritical fluid carbon dioxide (Ehlers et al 1996;Yoo et al 1997;Choi et al 1998;Rodrigues et al 2008). However, the information on coumarin extraction from C. reflexa using supercritical fluid carbon dioxide is still lacking in literatures.…”
Section: Introductionmentioning
confidence: 99%
“…Beside this, the production of plant extracts is currently limited by safety and regulatory constraints to the concentration of toxic residues of conventional organic solvents [14]. Supercritical fluid extraction has been widely employed as an alternative to organic solvent for the extraction of a variety of compounds from different matrices [15][16][17][18][19][20][21]. Carbon dioxide (CO 2 ) is probably the most widely used supercritical fluid because of its critical temperature (31.1 o C), which makes it an ideal solvent for extracting thermally labile materials.…”
Section: Introductionmentioning
confidence: 99%