2016
DOI: 10.1016/j.jfoodeng.2015.08.004
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Solubility of virgin coconut oil in supercritical carbon dioxide

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Cited by 51 publications
(19 citation statements)
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“…However, a high pressure (35 MPa) produced by SC-CO 2 could limit the application because of the high cost at production scale, and the 17.34% oil yield indicated the low processing capacity. Though CO 2 is the most utilized solvent, n -butane can be a good choice because its critical pressure is relatively lower than that of CO 2 , leading to a better interaction with the non-polar substances [ 37 ]. In addition, n -butane is easily accepted, cheaper and has a higher dissolving capacity compared to CO 2 , thus decreasing the n -butane consumption, increasing efficiency and shortening extraction time [ 23 , 28 ].…”
Section: Resultsmentioning
confidence: 99%
“…However, a high pressure (35 MPa) produced by SC-CO 2 could limit the application because of the high cost at production scale, and the 17.34% oil yield indicated the low processing capacity. Though CO 2 is the most utilized solvent, n -butane can be a good choice because its critical pressure is relatively lower than that of CO 2 , leading to a better interaction with the non-polar substances [ 37 ]. In addition, n -butane is easily accepted, cheaper and has a higher dissolving capacity compared to CO 2 , thus decreasing the n -butane consumption, increasing efficiency and shortening extraction time [ 23 , 28 ].…”
Section: Resultsmentioning
confidence: 99%
“…Ghosh et al showed that the recovery of eugenol from Ocimum sanctum was decreased significantly by amplifying temperature at lower pressure and vice versa, and the upper cross-over pressure was noted at 200 bar [ 60 ]. Other examples where extract yield and SCF density effects have been noted are for γ-oryzanol with a cross-over effect at 300 bar [ 97 ], 350–375 bar for avocado oil [ 61 ], as well as 295 bar for coconut oil [ 98 ].…”
Section: Operating Parametersmentioning
confidence: 99%
“…However, Zuknik et al. (2016) found the contradictive results that the Chrastil model has a higher error compared to the DVa model in the solubility of virgin coconut oil at pressures between 31.0 and 34.5 MPa (0.93 > 0.39). This is due to more adjustable parameters gives the small error between the model data and experimental data.…”
Section: Resultsmentioning
confidence: 99%
“…Duba et al (2016) also stated that the Chrastil model also successfully correlated the solubility of grape seed oil with a low error below than 1% compared to the Adachi-Lu model, where the TA B L E 3 Experimental and calculated solubility of TPC and TFC in mixture solvents (ScCO 2 and ethanol) from peanut skin temperature effect is dominant to increase the solubility. However, Zuknik et al (2016) found the contradictive results that the Chrastil model has a higher error compared to the DVa model in the solubility of virgin coconut oil at pressures between 31.0 and 34.5 MPa (0.93 > 0.39). This is due to more adjustable parameters gives the small error between the model data and experimental data.…”
Section: Ta B L Ementioning
confidence: 95%
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