Abstract

The utilization of crude glycerol, generated as a by-product from the biodiesel production process, for the production of high value-added products represents an opportunity to overcome the negative impact of low glycerol prices in the biodiesel industry. In this study, the biochemical behavior of Yarrowia lipolytica strains FMCC Y-74 and FMCC Y-75 was investigated using glycerol as a carbon source. Initially, the effect of pH value (3.0–7.0) was examined to produce polyols, intracellular lipids, and polysaccharides. At low pH values (initial pH 3.0–5.0), significant mannitol production was recorded. The highest mannitol production (19.64 g L−1) was obtained by Y. lipolytica FMCC Y-74 at pH = 3.0. At pH values ranging between 5.0 and 6.0, intracellular polysaccharides synthesis was favored, while polyols production was suppressed. Subsequently, the effect of crude glycerol and its concentration on polyols production was studied. Y. lipolytica FMCC Y-74 showed high tolerance to impurities of crude glycerol. Initial substrate concentrations influence polyols production and distribution with a metabolic shift toward erythritol production being observed when the initial glycerol concentration (Gly0) increased. The highest total polyols production (=56.64 g L−1) was obtained at Gly0 adjusted to ≈120 g L−1. The highest polyols conversion yield (0.59 g g−1) and productivity (4.36 g L−1 d−1) were reached at Gly0 = 80 g L−1. In fed-batch intermittent fermentation with glycerol concentration remaining ≤60 g L−1, the metabolism was shifted toward mannitol biosynthesis, which was the main polyol produced in significant quantities (=36.84 g L−1) with a corresponding conversion yield of 0.51 g g−1.

Highlights

  • Global economic growth has led to extensive demand for energy and other resources

  • The effect of pH value on biomass, mannitol, intracellular lipids, and endopolysaccharides production by two Y. lipolytica yeast strains was initially investigated in shake-flask cultures using glycerol as a carbon source at an initial concentration of c. 40 g L−1

  • The obtained results for Y. lipolytica strains FMCC Y-74 and FMCC Y-75 are presented in Tables 1 and 2, respectively

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Summary

Introduction

Global economic growth has led to extensive demand for energy and other resources. Biodiesel is one of the most prominent biofuels worldwide due to its high biodegradability and minimal toxicity [1]. It has been projected that the global biodiesel production will reach 39 billion liters by 2024, implying that approximately 4.2 billion gallons of crude glycerol would be produced [3]. The purification of glycerol for subsequent use in food, pharmaceutical, and cosmetic industries is an expensive process, and alternative methods for its valorization/management have been proposed, including combustion, composting, anaerobic digestion, animal feed, and biotechnological conversions using prokaryotic or eukaryotic microbial cells [1,2,4]. Many promising applications have been proposed for the valorization of crude glycerol through fermentation routes including its transformation into microbial oil, citric acid, poly (3-hydroxybutyrate), 1,3-propanediol, succinic acid, and polyols [5,6,7,8]

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