Biorefinery of microalgal soluble proteins by sequential processing and membrane filtration

AbstractA mild biorefinery process was investigated on the microalga Nannochloropsis gaditana, to obtain an enriched fraction of water soluble proteins free from chlorophyll. After harvesting, a 100g.L−1 solution of cells was first subjected to cell disruption by either high-pressure homogenization (HPH) or enzymatic treatment (ENZ). HPH resulted in a larger release of proteins (49%) in the aqueous phase compared to the Alcalase incubation (35%). In both cases, an ultrafiltration/diafiltration (UF/DF) was then performed on the supernatant obtained from cell disruption by testing different memb... Mehr ...

Verfasser: Carl Safi
N. Engelen-Smit
Lolke Sijtsma
L.A.M. van den Broek
Giuseppe Olivieri
W.J. Mulder
Rui Pina Campos
Dokumenttyp: Artikel
Erscheinungsdatum: 2017
Schlagwörter: Netherlands / Aurora Universities Network / SP1-Cooperation / EC / FP7 / European Commission / Knowmad Institut / Food / Agriculture and Fisheries / and Biotechnology / Waste Management and Disposal / Renewable Energy / Sustainability and the Environment / General Medicine / Environmental Engineering / Bioengineering
Sprache: Englisch
Permalink: https://search.fid-benelux.de/Record/base-26811686
Datenquelle: BASE; Originalkatalog
Powered By: BASE
Link(s) : https://www.openaccessrepository.it/record/83203

AbstractA mild biorefinery process was investigated on the microalga Nannochloropsis gaditana, to obtain an enriched fraction of water soluble proteins free from chlorophyll. After harvesting, a 100g.L−1 solution of cells was first subjected to cell disruption by either high-pressure homogenization (HPH) or enzymatic treatment (ENZ). HPH resulted in a larger release of proteins (49%) in the aqueous phase compared to the Alcalase incubation (35%). In both cases, an ultrafiltration/diafiltration (UF/DF) was then performed on the supernatant obtained from cell disruption by testing different membrane cut-off (1000kDa, 500kDa and 300kDa). After optimising the process conditions, the combination of ENZ→UF/DF ended in a larger overall yield of water soluble proteins (24.8%) in the permeate compared to the combination of HPH→UF/DF (17.4%). A gel polarization model was implemented to assess the maximum achievable concentration factor during ultrafiltration and the mass transfer coefficient related to the theoretical permeation flux rate.