2015
DOI: 10.1016/j.fuproc.2015.04.017
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A two-step biodiesel production process from waste cooking oil via recycling crude glycerol esterification catalyzed by alkali catalyst

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Cited by 86 publications
(41 citation statements)
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“…The acidified oil is composed of 43.15 wt% oleic, 35.19 wt% linoleic, 13.34 wt% palmitic, 5.09 wt% linolenic and 3.23 wt% stearic. The main components in the feedstock are oleic acid, linoleic acid and palmitic acid, which are consistent with the data from Cai et al [30].…”
Section: Fatty Acid Composition Of Feedstocksupporting
confidence: 91%
“…The acidified oil is composed of 43.15 wt% oleic, 35.19 wt% linoleic, 13.34 wt% palmitic, 5.09 wt% linolenic and 3.23 wt% stearic. The main components in the feedstock are oleic acid, linoleic acid and palmitic acid, which are consistent with the data from Cai et al [30].…”
Section: Fatty Acid Composition Of Feedstocksupporting
confidence: 91%
“…Alkali catalysts are relatively lower in cost with high biodiesel yield [9,10] while acid catalysts are more suitable for high free fatty acids (FFA) feedstocks. [11,12] Two-step acid then alkali catalysts are used for very high FFA content in the oil (up to 4%) where acid is added first then alkali transesterification is performed.…”
Section: Biodiesel Production Theorymentioning
confidence: 99%
“…However, each of them has its own drawbacks. In case of homogeneous catalysts, soap formation [6], water washings and glycerol purity have a telling impact on the cost of the process, whereas in heterogeneous systems, requirement of higher reaction temperatures and pressures greatly influence the cost of production.…”
Section: Introductionmentioning
confidence: 99%