title: Lipids rich in ω-3 polyunsaturated fatty acids from microalgae.
abstract: Despite microalgae recently receiving enormous attention as a potential source of biodiesel, their use is still not feasible as an alternative to fossil fuels. Recently, interest in microalgae has focused on the production of bioactive compounds such as polyunsaturated fatty acids (PUFA), which provide microalgae a high added value. Several considerations need to be assessed for optimizing PUFA production from microalgae. Firstly, a microalgae species that produces high PUFA concentrations should be selected, such as Nannochloropsis gaditana, Isochrysis galbana, Phaeodactylum tricornutum, and Crypthecodinium cohnii, with marine species gaining more attention than do freshwater species. Closed cultivation processes, e.g., photobioreactors, are the most appropriate since temperature, pH, and nutrients can be controlled. An airlift column with LEDs or optical fibers to distribute photons into the culture media can be used at small scale to produce inoculum, while tubular and flat panels are used at commercial scale. Depending on the microalgae, a temperature range from 15 to 28 °C and a pH from 7 to 8 can be employed. Relevant conditions for PUFA production are medium light irradiances (50-300 μmol photons m(-2) s(-1)), air enriched with (0-1 % (v/v) CO2, as well as nitrogen and phosphorous limitation. For research purposes, the most appropriate medium for PUFA production is Bold's Basal, whereas mixotrophic cultivation using sucrose or glucose as the carbon source has been reported for industrial processes. For cell harvesting, the use of tangential flow membrane filtration or disk stack centrifugation is advisable at commercial scale. Current researches on PUFA extraction have focused on the use of organic solvents assisted with ultrasound or microwaves, supercritical fluids, and electroporation or are enzyme assisted. Commercial-scale extraction involves mainly physical methods such as bead mills and expeller presses. All these factors should be taken into account when choosing a PUFA production system, as discussed in this review.
authors.affiliation: Instituto de Agroindustrias, Universidad Tecnológica de la Mixteca, C.P. 69000, Huajuapan de León, Oaxaca, Mexico.
authors.forename: N F
authors.initials: NF
authors.lastname: Santos-Sánchez
authors.affiliation: Instituto de Agroindustrias, Universidad Tecnológica de la Mixteca, C.P. 69000, Huajuapan de León, Oaxaca, Mexico.
authors.forename: R
authors.initials: R
authors.lastname: Valadez-Blanco
authors.affiliation: Instituto de Agroindustrias, Universidad Tecnológica de la Mixteca, C.P. 69000, Huajuapan de León, Oaxaca, Mexico.
authors.forename: B
authors.initials: B
authors.lastname: Hernández-Carlos
authors.affiliation: Laboratorio de Biotecnología de Microalgas, Instituto de Industrias, Universidad del Mar, C.P. 70902, Puerto Ángel, Oaxaca, Mexico.
authors.forename: A
authors.initials: A
authors.lastname: Torres-Ariño
authors.affiliation: Instituto de Agroindustrias, Universidad Tecnológica de la Mixteca, C.P. 69000, Huajuapan de León, Oaxaca, Mexico.
authors.forename: P C
authors.initials: PC
authors.lastname: Guadarrama-Mendoza
authors.affiliation: Instituto de Agroindustrias, Universidad Tecnológica de la Mixteca, C.P. 69000, Huajuapan de León, Oaxaca, Mexico. rsalas@mixteco.utm.mx.
authors.forename: R
authors.identifier: http://orcid.org/0000-0002-5458-0157
authors.initials: R
authors.lastname: Salas-Coronado
mesh_terms: D003470:Culture Media / Q000737:chemistry; D005231:Fatty Acids, Unsaturated / Q000302:isolation & purification* / Q000378:metabolism*; D006863:Hydrogen-Ion Concentration; D058086:Microalgae / Q000254:growth & development* / Q000378:metabolism*; D058433:Photobioreactors / Q000382:microbiology*; D013696:Temperature
chemical_list: D003470:Culture Media; D005231:Fatty Acids, Unsaturated
keywords: Extraction; Harvesting; Microalgae cultivation; Photobioreactors; ω-3 PUFA production