Analytical Supercritical Fluid Extraction Techniques 1998
DOI: 10.1007/978-94-011-4948-8_4
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Supercritical fluid extraction strategies of liquid-based matrices

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Cited by 6 publications
(9 citation statements)
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“…Due to the relatively high pressure of 200 bar in our experiments, the CO 2 /MeOH mixture remains in the supercritical state even when increasing to an equipotential portion of the co-solvent. This is reflected in the high extraction efficiency for more polar natural products such as the cittilins and the DKxanthenes. , Our data suggests that secondary metabolites such as myxovirescin A (CLog P = 5.80), myxalamid A (CLog P = 3.40), myxochromid A3 (CLog P = 5.30), and indiacen A (CLog P = 3.68) exceeding a log P of 3 show best extraction using 20% EtOAc as a co-solvent. Secondary metabolites such as cittilin A (CLog P = 1.85), DKxanthen 560 (CLog P = 2.22), myxochelin A (CLog P = 2.34), and terrestribisamid A (CLog P = 2.34) with log P values below 3 are better extractable using more polar and protic co-solvents such as i PrOH and MeOH (see Figure ).…”
Section: Resultsmentioning
confidence: 70%
“…Due to the relatively high pressure of 200 bar in our experiments, the CO 2 /MeOH mixture remains in the supercritical state even when increasing to an equipotential portion of the co-solvent. This is reflected in the high extraction efficiency for more polar natural products such as the cittilins and the DKxanthenes. , Our data suggests that secondary metabolites such as myxovirescin A (CLog P = 5.80), myxalamid A (CLog P = 3.40), myxochromid A3 (CLog P = 5.30), and indiacen A (CLog P = 3.68) exceeding a log P of 3 show best extraction using 20% EtOAc as a co-solvent. Secondary metabolites such as cittilin A (CLog P = 1.85), DKxanthen 560 (CLog P = 2.22), myxochelin A (CLog P = 2.34), and terrestribisamid A (CLog P = 2.34) with log P values below 3 are better extractable using more polar and protic co-solvents such as i PrOH and MeOH (see Figure ).…”
Section: Resultsmentioning
confidence: 70%
“…This phenomenon allows separation of polar phenolic compounds from olive oil in an ecofriendly (green) fashion. Many different researchers have provided insights into separation of different compounds from aqueous based matrices (Ramsey et al, 1998(Ramsey et al, , 2011. However, ours is arguably the first step towards separation of phenolic compounds from oil matrix (olive oil).…”
Section: Phenolic Compositionmentioning
confidence: 99%
“…The phenolic compounds present in olive oil vary in compound polarity. There are certain reports in which researchers have executed the extraction of different valuable compounds from aqueous matrices through SFE equipped with varying hardware (Ramsey et al, 1998(Ramsey et al, , 2011. However, literature on extraction of phenolic or other valuable components from liquid matrices through supercritical fluid extraction is scanty, and to the best of the authors' knowledge, there are no reports on extraction of phenolic compounds from olive oil using supercritical fluid extraction.…”
Section: Introductionmentioning
confidence: 99%
“…These combined systems offer various application advantages under different analytical conditions. The SFE-SFC system utilizes the strengths of supercritical technology to enhance analysis efficiency and accuracy [9,22,29,[34][35][36][37][38]. The SFE-HPLC system combines the supercritical technology for simplified pretreatment ability with mature sepa-ration methods to provide innovative ideas for analyzing complex component samples.…”
Section: Introductionmentioning
confidence: 99%