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Solid superacid catalyzed glycerol esterification of free fatty acids in waste cooking oil for biodiesel production
Authors:Yong Wang  Shun Ma  Lili Wang  Shuze Tang  William W. Riley  Martin J. T. Reaney
Affiliation:1. Department of Food Science and Engineering, Jinan University, Guangzhou, P.R.China;2. Department of Plant Science, University of Saskatchewan, Saskatoon, SK, Canada
Abstract:The free fatty acids (FFAs) of waste cooking oil (WCO) are readily esterified with crude glycerol in the presence of the solid superacid SOurn:x-wiley:14387697:media:EJLT201100111:tex2gif-stack-1/ZrO2–Al2O3. This reaction lowers the acidity of WCO before biodiesel production. The solid superacid SOurn:x-wiley:14387697:media:EJLT201100111:tex2gif-stack-2/ZrO2–Al2O3 catalyzes both FFA esterification and TAG glycerolysis during the reaction. The conversion of FFA in the WCO with an acid value of 88.4 ± 0.5 mg KOH/g to acylglycerols was 98.4% under optimal conditions (mole ratio of glycerol to FFA = 1.4:1; reaction time = 4 h; reaction temperature = 200°C; catalyst loading = 0.3 wt%) obtained through an orthogonal experiment. The final FAME product with a FAME content of 96.9 ± 0.3 wt% yield was 94.8 wt%, after transesterification of the esterified WCO with methanol, catalyzed by potassium hydroxide. The FAME composition of the products produced by transesterification were identified and quantified by GC–MS. The results suggest that this new glycerol esterification process, using a solid superacid catalyst, affords a promising method to convert oils with high FFA levels, like WCO, to biodiesel. The process has the inherent advantage of easy separation steps for removing excess alcohol and significant savings in energy, when compared to acid catalyzed reactions with methanol to lower acidity. Practical applications : In this work, WCO with a high acid value was esterified with crude glycerol catalyzed by solid super acid, whose formula was expressed as SOurn:x-wiley:14387697:media:EJLT201100111:tex2gif-stack-3/ZrO2–Al2O3. There are distinct advantages to this new esterification process, which include easy separation of the excess crude glycerol by sedimentation or centrifugation, the use of the low cost reactant crude glycerol direct from the byproducts of transesterification, the potential to achieve a very low content of FFAs by post‐refining to improve the yield of the final product, and time and energy saving are found as compared to the traditional methanol esterification process. This new technology provides a promising alternative method for processing feedstocks of high acid value, such as WCO, for the production of biodiesel.
Keywords:Biodiesel  Esterification  Sulfated zirconia  Waste cooking oil
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