Microalgae from domestic wastewater facility’s high rate algal pond: Lipids extraction, characterization and biodiesel production

[Display omitted] •Microalgae biomass recovery from a real-scale HRAP by pH increase.•Methods of Folch and Hara modified by ultrasounds irradiation for extraction of lipids.•Supercritical CO2 lipid extract has the highest unsaturated fatty acids content.•Microwave assisted extractive-transesterifica...

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Published inBioresource technology Vol. 206; pp. 239 - 244
Main Authors Drira, Neila, Piras, Alessandra, Rosa, Antonella, Porcedda, Silvia, Dhaouadi, Hatem
Format Journal Article
LanguageEnglish
Published England Elsevier Ltd 01.04.2016
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ISSN0960-8524
1873-2976
DOI10.1016/j.biortech.2016.01.082

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Summary:[Display omitted] •Microalgae biomass recovery from a real-scale HRAP by pH increase.•Methods of Folch and Hara modified by ultrasounds irradiation for extraction of lipids.•Supercritical CO2 lipid extract has the highest unsaturated fatty acids content.•Microwave assisted extractive-transesterification of the HRAP’s biomass and micro-biodiesel production. In this study, the harvesting of a biomass from a high rate algal pond (HRAP) of a real-scale domestic wastewater treatment facility and its potential as a biomaterial for the production of biodiesel were investigated. Increasing the medium pH to 12 induced high flocculation efficiency of up to 96% of the biomass through both sweep flocculation and charge neutralization. Lipids extracted by ultrasounds from this biomass contained around 70% of fatty acids, with palmitic and stearic acids being the most abundant. The extract obtained by supercritical CO2 contained 86% of fatty acids. Both conventional solvents extracts contained only around 10% of unsaturated fats, whereas supercritical CO2 extract contained more than 40% of unsaturated fatty acids. This same biomass was also subject to direct extractive-transesterification in a microwave reactor to produce fatty acid methyl esters, also known as, raw biodiesel.
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ISSN:0960-8524
1873-2976
DOI:10.1016/j.biortech.2016.01.082