2020
DOI: 10.1016/j.cherd.2019.12.003
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Techno-economic evaluation of squalene recovery from oil deodorizer distillates

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Cited by 11 publications
(11 citation statements)
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“…Optimization of Reaction Conditions. A mixture containing SODD, methanol, and lipase MAS1-H108A were added to a 100 mL conical flask with constant shaking at 200 rpm for 24 h. The reaction parameters, such as the oil/ methanol molar ratio (1:1, 1:1.5, 1:2, 1:2.5, 1:3, 1:4, and 1:5), enzyme loading (5,15,25,35, and 45 U/g SODD), and temperature (30,35,40,45, and 50 °C), were varied for optimization. In particular, to reduce the inactivation rate of immobilized MAS1-H108A and increase the conversion of FAME, methanol was a three-step average added at 0, 2, and 4 h, respectively.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…Optimization of Reaction Conditions. A mixture containing SODD, methanol, and lipase MAS1-H108A were added to a 100 mL conical flask with constant shaking at 200 rpm for 24 h. The reaction parameters, such as the oil/ methanol molar ratio (1:1, 1:1.5, 1:2, 1:2.5, 1:3, 1:4, and 1:5), enzyme loading (5,15,25,35, and 45 U/g SODD), and temperature (30,35,40,45, and 50 °C), were varied for optimization. In particular, to reduce the inactivation rate of immobilized MAS1-H108A and increase the conversion of FAME, methanol was a three-step average added at 0, 2, and 4 h, respectively.…”
Section: Methodsmentioning
confidence: 99%
“… 22 Also, supercritical CO 2 extraction and crystallization processes were applied for the isolation of phytosterols from saponified rapeseed oil deodorizer distillate. 23 Although many studies have focused on the production of biodiesel by SODD or the recovery of bioactive compounds from SODD, 24 , 25 the one-step synthesis of biodiesel and recovery of bioactive compounds from SODD were scarcely reported. The generated FAME has a lower boiling point than the corresponding FFA and that results in an easy separation between FAME and the bioactive compounds.…”
Section: Introductionmentioning
confidence: 99%
“…Finally, squalene and phytosterols have been extracted from natural sources using supercritical carbon dioxide (CO2) (SFE) [157]. In addition, high levels of these same substances have been found in deodorization distillates during the refining of some vegetable oils, such as palm and olive [158,159]. Furthermore, the most widely used techniques to quantify the compounds mentioned above include gas chromatography with flame ionization detector (FID) and gas chromatography coupled to mass spectrometry [72].…”
Section: Available Technologies To Extract Concentrate And/or Purify Palm Phytochemicalsmentioning
confidence: 99%
“…In literature, sources that regard of FAs in the vapor phase. 5,21,24,25 However, UNIFAC-based models generally do not result in good predictions for lipid systems. 18 In addition, UNIFAC models cannot be used for FA distillation, as their applicability is limited to temperatures below 425 K. 20 Othman and (3) demonstrating the applicability of the lumping approach in a case study by building and validating a comprehensive simulation, using the proper property methods, of an industrial FA distillation plant for optimizing the product yield, purity and heat duty of the process.…”
Section: Study Processmentioning
confidence: 99%
“…In literature, sources that regard FAs as nonpolar, use Redlich Kwong Soave (RKS)‐based equation of state models such as RKS with Boston–Mathias (RKS) and RKS with Wong‐Sandler or the predictive Soave–Redlich–Kwong (PSRK) model 14,21‐23 . Sources that regard FAs as polar compounds, use property methods based on the nonrandom two‐liquid (NRTL), universal quasichemical (UNIQUAC), or UNIQUAC Functional‐group Activity Coefficients (UNIFAC) model, often in combination with the Nothnagel (NTH) or Hayden–O'Conell (HOC) model to describe the dimerization of FAs in the vapor phase 5,21,24,25 . However, UNIFAC‐based models generally do not result in good predictions for lipid systems 18 .…”
Section: Introductionmentioning
confidence: 99%