A strategy for the highly efficient production of docosahexaenoic acid by Aurantiochytrium limacinum SR21 using glucose and glycerol as the mixed carbon sources
Introduction
Docosahexaenoic acid (DHA, 22:6) is a particularly important omega-3 fatty acid due to its benefits to human health and commercial use in infant formula (Borowitzka, 2013). Marine fish oil has long been a primary commercial source of DHA, but is associated with many problems, such as unstable quality, a fishy odor, environmental pollution, high processing costs and a tendency to oxidize (Ward and Singh, 2005). Single cell oils (SCOs) avoid these disadvantages of fish oils, and their production may readily be scaled up via biotechnological methods. Algae-derived DHA has thus become the subject of intensive research, and Schizochytrium sp. has been commercially utilized to produce DHA by fermentation (Ratledge, 2004).
Glucose is the most commonly used carbon source for heterotrophic cultures of microalgae, as far higher rates of growth and respiration are obtained than with any other substrate (Perez-Garcia et al., 2011). Bailey et al. (2003) achieved dry cell weight (DCW) of 171.5 g/L and DHA concentration of 35.33 g/L with glucose metabolized by Schizochytrium sp. ATCC20888, proposing the control strategy of stepwise dissolved oxygen (DO). However, turning sugar into algal oil is very expensive because of the high cost of the raw materials and the low conversion rates achieved by the oleaginous microorganisms. Attention has thus focused on ways to decrease production costs. It has been suggested that Aurantiochytrium limacinum SR21, previously called Schizochytrium limacinum SR21 (Yokoyama and Honda, 2007), may be used with cheap carbon sources such as crude glycerol from the biodiesel industry (Ethier et al., 2011). Although previous studies have shown that the yield of DHA from glycerol or crude glycerol is comparable to that from glucose (Chi et al., 2007, Yokochi et al., 1998), the activity of the key enzymes involved in glycerol assimilation, such as glycerol kinase (GK) and glycerol-3-phosphate dehydrogenase (G-3-PDH), may be inhibited by the reduced oxygen availability due to the increasing algal mass and the glycerol concentration expounded in our previous work (Chang et al., 2013b). Strategies to effectively use various substrates and to enhance DHA productivity should therefore be investigated.
Fermentation of the MCSs is an effective strategy for enhancing target metabolic products, and has been widely used in the fermentation industry (Chen et al., 2012). Glucose/glycerol co-fermentation has been used to produce propionic acid by Propionibacterium freudenreichii (Wang and Yang, 2013), 1,3-propanediol by Clostridium butyricum (Abbad-Andaloussi et al., 1998), ε-poly-l-lysine by Streptomyces sp. (Chen et al., 2012), H2 by Escherichia coli (Trchounian and Trchounian, 2013) and β-carotene by Blakeslea trispora (Mantzouridou et al., 2008). Easterling et al. (2009) indicated that mixing glycerol with either dextrose or xylose served to decrease the saturation of fatty acid methyl esters produced by Rhodotorula glutinis, and dextrose/glycerol co-fermentation achieved the highest accumulation of triacylglycerol. When glucose was mixed with the same amount of glycerol in the medium for producing polyunsaturated fatty acids by Thraustochytrium sp., glycerol was consumed preferentially in the early stages of culture (Scott et al., 2011).
However, various strategies to improve the production of DHA by Schizochytrium sp. using glucose or glycerol as individual carbon sources have been explored, few reports on glucose and glycerol as the MCSs have been published. In the current study, we attempt to develop a glucose and glycerol co-fermentation strategy that is conducive to the enhancement of DHA yield and productivity by A. limacinum SR21.
Section snippets
Microorganism
The strain A. limacinum SR21 was obtained from the American Type Culture Collection (ATCC) and maintained on a medium of 30 g/L of artificial seawater salt, 5 g/L of glucose, 1 g/L of yeast extract, 1 g/L of peptone, and 15 g/L of agar.
Shake flask cultures
The algal inoculum medium consisted of (g/L): glucose, 30; yeast extract, 5; NaCl, 0.3; Na2SO4, 15; sodium glutamate, 5; K2SO4, 1; MgSO4·7H2O, 3; K2HPO4, 2; KH2PO4, 3; CaCl2, 0.02; vitamin B1, 0.005; vitamin B6, 0.002; vitamin B12, 0.005. The fermentation medium
Flask cultivation
To understand the fermentation stages with different cellular behaviors and investigate the effects of glucose and glycerol on DHA productivity, A. limacinum SR21 flask cultivations were firstly performed with 100 g/L of glucose and glycerol respectively (group A and B). As shown in Fig. 1, the glucose exhaustion time was 4 days, at which time the highest DCW (39.27 ± 1.35 g/L) was obtained and the lipid and DHA contents were 66.58 ± 2.15% and 41.23 ± 0.79% respectively. When glycerol was used as the
Conclusion
Shake flask cultures indicate that glucose is superior for algal growth and lipid synthesis in the early phase of fermentation, while glycerol promotes DHA accumulation in the late stage. Glucose and glycerol co-fermentation can serve as an efficient strategy for DHA production by A. limacinum SR21 in both flask and fed-batch cultures. The maximum DHA yield and productivity of 32.36 g/L and 337.1 mg/L/h were obtained. The MCSs strategy could provide an alternative to conventional DHA production.
Acknowledgements
This work was supported by “National Natural Science Foundation of China (Grant Nos. 31401619)” and “The Natural Science Foundation of Jiangsu Province (BK20140156)”.
References (30)
- et al.
Multiple effects of glycerol on plant cell metabolism: phosphorus-31 nuclear magnetic resonance studies
J. Biol. Chem.
(1994) - et al.
Improvement of docosahexaenoic acid production on glycerol by Schizochytrium sp. S31 with constantly high oxygen transfer coefficient
Bioresour. Technol.
(2013) - et al.
Fatty acid shifts and metabolic activity changes of Schizochytrium sp. S31 cultured on glycerol
Bioresour. Technol.
(2013) - et al.
A laboratory study of producing docosahexaenoic acid from biodiesel-waste glycerol by microalgal fermentation
Process Biochem.
(2007) - et al.
Continuous culture of the microalgae Schizochytrium limacinum on biodiesel-derived crude glycerol for producing docosahexaenoic acid
Bioresour. Technol.
(2011) - et al.
A fermentation strategy for producing docosahexaenoic acid in Aurantiochytrium limacinum SR21 and increasing C22:6 proportions in total fatty acid
Bioresour. Technol.
(2012) - et al.
Heterotrophic cultures of microalgae: metabolism and potential products
Water Res.
(2011) Fatty acid biosynthesis in microorganisms being used for single cell oil production
Biochimie
(2004)- et al.
Compositional shift in lipid fractions during lipid accumulation and turnover in Schizochytrium sp
Bioresour. Technol.
(2014) - et al.
Use of raw glycerol to produce oil rich in polyunsaturated fatty acids by a thraustochytrid
Enzyme Microb. Technol.
(2011)