Abstract:Yeast single cell oil (SCO) is a non-crop-based, renewable oil source that can be used for the production of bio-based oleochemicals. Stand-alone production of SCO for oleochemicals is currently not cost-competitive because lower-cost alternatives from petroleum and crop-based resources are available. Utilizing low-valued nutrient sources, implementing cost-efficient downstream processes and adopting biotechnological advancements such as systems biology and metabolic engineering could prove valuable in making … Show more
“…Therefore, metabolic engineering is necessary to improve lipid productivity. Additionally, the production of other value-added co-products and exploration of zero-cost waste or by-product streams such as glycerol, as feedstock, for yeast SCO production is recommended [6]. Synthetic defined media containing 6.7 g/L Yeast Nitrogen Base (YNB) w/ammonium sulfate w/o amino acids (Becton, Dickson, and company), 20 g/L glucose, and a drop-out synthetic mix minus uracil (-Ura) or minus leucine (-Leu) (US Biological) were used for the selection of knock out/in strains.…”
Increasing demand for plant oil for food, feed, and fuel production has led to food-fuel competition, higher plant lipid cost, and more need for agricultural land. On the other hand, the growing global production of biodiesel has increased the production of glycerol as a by-product. Efficient utilization of this by-product can reduce biodiesel production costs. We engineered Yarrowia lipolytica (Y. lipolytica) at various metabolic levels of lipid biosynthesis, degradation, and regulation for enhanced lipid and citric acid production. We used a one-step double gene knock-in and site-specific gene knock-out strategy. The resulting final strain combines the overexpression of homologous DGA1 and DGA2 in a POX-deleted background, and deletion of the SNF1 lipid regulator. This increased lipid and citric acid production in the strain under nitrogen-limiting conditions (C/N molar ratio of 60). The engineered strain constitutively accumulated lipid at a titer of more than 4.8 g/L with a lipid content of 53% of dry cell weight (DCW). The secreted citric acid reached a yield of 0.75 g/g (up to~45 g/L) from pure glycerol in 3 days of batch fermentation using a 1-L bioreactor. This yeast cell factory was capable of simultaneous lipid accumulation and citric acid secretion. It can be used in fed-batch or continuous bioprocessing for citric acid recovery from the supernatant, along with lipid extraction from the harvested biomass.
“…Therefore, metabolic engineering is necessary to improve lipid productivity. Additionally, the production of other value-added co-products and exploration of zero-cost waste or by-product streams such as glycerol, as feedstock, for yeast SCO production is recommended [6]. Synthetic defined media containing 6.7 g/L Yeast Nitrogen Base (YNB) w/ammonium sulfate w/o amino acids (Becton, Dickson, and company), 20 g/L glucose, and a drop-out synthetic mix minus uracil (-Ura) or minus leucine (-Leu) (US Biological) were used for the selection of knock out/in strains.…”
Increasing demand for plant oil for food, feed, and fuel production has led to food-fuel competition, higher plant lipid cost, and more need for agricultural land. On the other hand, the growing global production of biodiesel has increased the production of glycerol as a by-product. Efficient utilization of this by-product can reduce biodiesel production costs. We engineered Yarrowia lipolytica (Y. lipolytica) at various metabolic levels of lipid biosynthesis, degradation, and regulation for enhanced lipid and citric acid production. We used a one-step double gene knock-in and site-specific gene knock-out strategy. The resulting final strain combines the overexpression of homologous DGA1 and DGA2 in a POX-deleted background, and deletion of the SNF1 lipid regulator. This increased lipid and citric acid production in the strain under nitrogen-limiting conditions (C/N molar ratio of 60). The engineered strain constitutively accumulated lipid at a titer of more than 4.8 g/L with a lipid content of 53% of dry cell weight (DCW). The secreted citric acid reached a yield of 0.75 g/g (up to~45 g/L) from pure glycerol in 3 days of batch fermentation using a 1-L bioreactor. This yeast cell factory was capable of simultaneous lipid accumulation and citric acid secretion. It can be used in fed-batch or continuous bioprocessing for citric acid recovery from the supernatant, along with lipid extraction from the harvested biomass.
“…New bioremediation technologies can help to solve wastewater pollution problems and produce valuable biotechnological products. Microbial oil is defined as the accumulation of neutral storage lipids by oleaginous microorganisms . Microbial oils are renewable sources for the production of biodiesel feedstocks and polyunsaturated fatty acids (PUFAs) …”
“…Single cell oil (SCO) is a renewable alternative to crop‐based oils for the production of biofuels and oleochemicals. Oleaginous yeast are advantageous SCO producers that are capable of accumulating oil up to ∼70% of the dry cell mass . Oil or storage lipid accumulation occurs under nutrient limited conditions.…”
Section: Introductionmentioning
confidence: 99%
“…Oleaginous yeast are advantageous SCO producers that are capable of accumulating oil up to 70% of the dry cell mass. 1 Oil or storage lipid accumulation occurs under nutrient limited conditions. Fermentation techniques used for yeast SCO production often control the C:N ratio by limiting the amount of nitrogen and providing excess carbon (often in the form of glucose or some other sugar substrate).…”
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