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Thraustochytrids are marine protists with an excellent ability to produce health-beneficial docosahexaenoic acid (DHA)-rich lipids. Since the demand for DHA sources for food and feed is increasing, a deeper understanding of the potential to enhance the DHA-production in thraustochytrids is important for a sustainable DHA supply. In most thraustochytrids, including the strains used in this work, DHA is synthesized by a polyketide synthase-like pathway (PKS), and not through the common fatty acid synthetase (FAS) pathway. Both pathways use the same precursors. The aim of this study was to determine if inhibiting the production of fatty acids (FA) through the FAS pathway under nitrogen starvation would result in higher net DHA production rates measured as DHA content, and if the channeling of the synthesized fatty acids to different lipids species is similar in two different thraustochytrid strains. We found that the DHA production rates in Aurantiochytrium limacinum SR21 and Aurantiochytrium sp. T66 were not affected when treated with the FAS-inhibitor cerulenin, despite a reduction of FAS-derived FAs. This indicates that precursor availability is less likely to be the limiting factor for DHA synthesis. Still, cerulenin-treatment in the lipid accumulation phase resulted in higher concentrations of the triacylglycerol (TAG) TG(22:6/22:6/22:6) than in the untreated cells after three hours, demonstrating that FAS inhibition is a possible strategy to enhance the content of DHA-rich lipids. Moreover, the relatively high abundance of the diacylglycerol DG(22:6/22:6) suggests the presence of an obstacle for using DG(22:6/22:6) as substrate to synthesize DHA-rich TAGs, a step that potentially can be improved by metabolic engineering. • A comparative lipidomics study of two thraustochytrid species • The effect of adding FAS inhibitors in the lipid accumulation phase was explored. • DHA production did not increase even if less saturated fatty acids were synthesized. • Conversion of DG(22:6/22:6) is a potential bottleneck for DHA-rich TAG synthesis. [ABSTRACT FROM AUTHOR]

The large brown seaweeds (kelps) are potential sources of protein for animal feed. They have lower protein contents than most red and green algae, but due to potential for large-scale production, they may represent a significant future protein source. The impact of pH, temperature and polysaccharide-degrading enzymes on the solubility and extraction yields of protein from wet Saccharina latissima biomass was investigated. The protein solubility increased with increasing pH and reached maximum of 23% at pH 11, determined as total amino acids (TAA). The enzyme treatments increased the release of soluble compounds by 30–35%. The highest protein yield obtained was 19%, using a ratio of water to wet seaweed of 1:1 for extraction. Even if the yields can be increased by increasing the water amounts used for extraction, the majority of the protein would remain in the insoluble residue after separation. The strategy for production of a larger quantity of protein-enriched biomass was therefore to maintain the insoluble fraction as the product. A pilot scale production was carried out, also including the red algae Palmaria palmata. In total 750 kg S. latissima and 195 kg P. palmata were processed. The protein content in the product increased from 10 to 20% of dry weight (dw) for S. latissima and from 12 to 28% for P. palmata , with yields of 79 and 69%, respectively. The ash content was reduced from 44 to 26% and from 12 to 5% of dw, respectively, for the two species. The main protein loss was free amino acids, which constituted approximately 10% of TAA in the feedstocks. Less essential than non-essential amino acids were lost, thus, the essential amino acids were enriched in the product. • The maximum solubility of protein from Saccharina latissima was 24%. • Enzymes decreased the water binding capacity and increased the extraction yields. • Process was scaled-up, maintaining the insoluble fraction as the product. • The protein content increased from 10% in the biomass to 20% after processing. [ABSTRACT FROM AUTHOR]