2010
DOI: 10.1016/j.biortech.2010.03.089
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A comprehensive study of reaction parameters in the enzymatic production of novel biofuels integrating glycerol into their composition

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Cited by 37 publications
(60 citation statements)
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“…Thus, reactions were carried out with 0.8 g of 10 wt% supported KF on the three inorganic solids, Al 2 O 3 , ZnO and MgO, at 65 ºC reaction temperature with 12 mL of sunflower oil (32 cSt, kinematic viscosity) and 2.43 mL of methanol. According to the results, with all the three KF supported catalysts studied, under the indicated experimental conditions, were obtained similar results as those achieved in the enzymatic processes [19][20][21][22][23][24], where instead of glycerol are obtained the monoacylglycerol that are soluble in the FAME mix. The experimental conditions currently applied were clearly softer than those required for the production of conventional biodiesel with supported KF catalysts [29][30][31][32][33][34][35][36].…”
Section: Influence Of the Inorganic Solid Used As Support Of Kf On Prsupporting
confidence: 72%
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“…Thus, reactions were carried out with 0.8 g of 10 wt% supported KF on the three inorganic solids, Al 2 O 3 , ZnO and MgO, at 65 ºC reaction temperature with 12 mL of sunflower oil (32 cSt, kinematic viscosity) and 2.43 mL of methanol. According to the results, with all the three KF supported catalysts studied, under the indicated experimental conditions, were obtained similar results as those achieved in the enzymatic processes [19][20][21][22][23][24], where instead of glycerol are obtained the monoacylglycerol that are soluble in the FAME mix. The experimental conditions currently applied were clearly softer than those required for the production of conventional biodiesel with supported KF catalysts [29][30][31][32][33][34][35][36].…”
Section: Influence Of the Inorganic Solid Used As Support Of Kf On Prsupporting
confidence: 72%
“…As carrier gas helium is used, with a flow of 1.5 ml/min, it has been applied a heating ramp from 50 °C to 200 °C at a rate of 7 °C/min, followed by another ramp from 200 °C to 360 °C at a rate of 15 ºC/min, maintaining the oven temperature at 360 °C for 10 minutes using as internal standard n-hexadecane (cetane) to quantify the content of methyl esters and glycerides (-mono, di and triglycerides) with the help of some commercial standard fatty acid esters, respectively. This method allows us to obtain a complete analysis of the sample in a single injection and in a time not higher than 65 minutes, which simplifies the process and increases the speed of analysis [19][20][21][22][23][24].…”
Section: Methodsmentioning
confidence: 99%
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“…This reaction also simplifies the downstream processing of the process because both the products of the reaction (fatty acid alkyl ester and triacetin) can be utilized as biodiesel . Verdugo et al (2010) have also developed a method for the integration of glycerol into the composition of biofuel via pig pancreatic lipase catalysed transesterification of sunflower oil. The greatest advantage with the methods involving integration of glycerol into the composition of biofuels is that they involve no impurities to be removed from the final mixture and reduce the negative environmental impact of the process.…”
Section: Sco As Future Biodiesel?mentioning
confidence: 99%