2013
DOI: 10.12777/wastech.1.1.6-9
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Biodiesel Production from Microalgae by Extraction – Transesterification Method

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Cited by 4 publications
(6 citation statements)
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“…It was reported that biodiesel of good quality can be produced from microalgae in the reaction condition of 3.4:1 methanol to dry biomass (v/w) ratio with 0.6:1 catalyst loading to dry algae (v/w) temperature at 75 ⁰C in 35 minutes and fatty acid were analysed using GC (Thao et al, 2013). In this study, algal oil extraction procedure was adapted from the protocol described by Bligh andDyer in 1959 (Bligh &Dyer, 1959).…”
Section: Fatty Acid Extractionmentioning
confidence: 99%
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“…It was reported that biodiesel of good quality can be produced from microalgae in the reaction condition of 3.4:1 methanol to dry biomass (v/w) ratio with 0.6:1 catalyst loading to dry algae (v/w) temperature at 75 ⁰C in 35 minutes and fatty acid were analysed using GC (Thao et al, 2013). In this study, algal oil extraction procedure was adapted from the protocol described by Bligh andDyer in 1959 (Bligh &Dyer, 1959).…”
Section: Fatty Acid Extractionmentioning
confidence: 99%
“…Biodiesel production from microalgae through experimental investigation of transesterification conditions reported that 3.4:1 methanol dry algal biomass ratio with 35 minutes reaction time and 0.6:1 catalyst to dry biomass ration was the most efficient in experimental process. In this condition, 60% lipids could be achieved from dry algal biomass (Thao et al, 2013). (Lee et al, 2011) 7…”
Section: Best Outputs Of Different Studiesmentioning
confidence: 99%
“…Due to low cost and higher reactivity, methanol is preferred for this reaction but other alcohols such as ethanol, propanol, amyl alcohol, butanol also shows good reactivity. Microalgae lipids consist of triglyceride chains which undergoes transesterification reaction in three steps, yielding diglyceride in first step, followed by formation of monoglyceride in second step and subsequently forming fatty acid methyl ester as the final product and glycerol as the byproduct in third step (Thao et al 2013;El-Sheekh et al 2016). The overall reaction can be represented as:…”
Section: Lipidsmentioning
confidence: 99%
“…Similarly, the reaction temperature and time remains directly proportional to the biodiesel yield. The catalyst such as strong acid (H 2 SO 4 ) drives the reaction forward and increase the rate of reaction (Thao et al 2013;Cao et al 2013). The choice of catalyst is based on the free fatty acid (FFA) content of the lipid.…”
Section: Lipidsmentioning
confidence: 99%
“…This was brought about by the interaction of other molecules/compounds resulting in increased amounts of by-products. The addition of the catalyst in excess gives rise to the formation of an emulsion, which leads to an increase in viscosity and in the process to the formation of gels [36]. One other disadvantage of high catalyst concentrations, in general, is their corrosive nature which hinders the transesterification reaction [35].…”
Section: Rsm For Optimization Of the Processmentioning
confidence: 99%