High-yield production of erythritol from raw glycerol in fed-batch cultures of <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

An acetate-negative mutant of Yarrowia lipolytica Wratislavia K1 was selected that, when grown with 300 g raw glycerol l⁻¹ at pH 3, produced 170 g erythritol l⁻¹ after 7 days, corresponding to a 56% yield and a productivity of 1 g l⁻¹ h⁻¹. The Wratislavia K1 strain did not produce citric acid.     

High-yield production of citric acid by Yarrowia lipolytica on glycerol in repeated-batch bioreactors

An acetate negative mutant of Yarrowia lipolytica Wratislavia AWG7 was found to be suitable for the production of high amounts of citric acid in long-term repeated-batch cultures. When 40% of fresh replaced medium was fed, this strain produced 154 g l⁻¹, on average, which corresponded to a 0.78 g g⁻¹ yield and a productivity of 1.05 g l⁻¹ h⁻¹. The activity of the culture remained stable for more than 1,650 h, i.e., 16 cycles of the repeated-batch bioreactors.     

Excretion of citric and isocitric acids by the yeast Saccharomycopsis lipolytica

Summary We investigated the excretion of citric and isocitric acids in a strain of Saccharomycopsis lipolytica grown on either n-paraffins, glucose, or glycerol. These acids were excreted in the ratio of 67:33 on n-paraffins and roughly 92:8 on either glucose or glycerol. However, with all the carbon sources used, the relative amount of isocitric acid in the intracellular pool remained below 10%. The assimilation of citric and isocitric acids was prevented when glucose or glycerol were the carbon sources, but not when n-paraffins were used. Citric acid stopped isocitric acid assimilation. These phenomena of selective assimilation and/or uptake might explain the variations observed in the ratio of citric to isocitric acids excreted on different carbon sources.     

Engineering Yarrowia lipolytica for the selective and high-level production of isocitric acid through manipulation of mitochondrial dicarboxylate–tricarboxylate carriers

During cultivation under nitrogen starvation, Yarrowia lipolytica produces a mixture of citric acid and isocitric acid whose ratio is mainly determined by the carbon source used. We report that mitochondrial succinate–fumarate carrier YlSfc1 controls isocitric acid efflux from mitochondria. YlSfc1 purified and reconstituted into liposomes transports succinate, fumarate, oxaloacetate, isocitrate and α-ketoglutarate. YlSFC1 overexpression determined the inversion of isocitric acid/citric acid ratio towards isocitric acid, resulting in 33.4 ± 1.9 g/L and 43.3 ± 2.8 g/L of ICA production in test-tube cultivation with glucose and glycerol, respectively. These titers represent a 4.0 and 6.3-fold increase compared to the wild type. YlSFC1 gene expression was repressed in the wild type strain grown in glucose-based medium compared to olive oil medium explaining the reason for the preferred citric acid production during Y. lipolytica growth on carbohydrates. Coexpression of YlSFC1 and adenosine monophosphate deaminase YlAMPD genes together with inactivation of citrate mitochondrial carrier YlYHM2 gene enhanced isocitric acid accumulation up to 41.4 ± 4.1 g/L with an isocitric acid/citric acid ratio of 14.3 in a small-scale cultivation with glucose as a carbon source. During large-scale cultivation with glucose pulse-feeding, the engineered strain produced 136.7 ± 2.5 g/L of ICA with a process selectivity of 88.1%, the highest reported titer and selectivity to date. These results represent the first reported isocitric acid secretion by Y. lipolytica as a main organic acid during cultivation on carbohydrate. Moreover, we demonstrate for the first time that the replacement of one mitochondrial transport system for another can be an efficient tool for switching product accumulation.     

Enhanced production of erythritol by Yarrowia lipolytica on glycerol in repeated batch cultures

Erythritol is an important natural sweetener, industrially produced only by fermentation on glucose media. Glycerol is an important renewable feedstock as it is the major by-product of the biodiesel production process; here we present an alternative way to convert this low-cost substrate into value-added products, such as erythritol. Repeated batch cultures (RBC) were performed to improve the productivity of erythritol from pure and crude glycerol. An acetate negative mutant of Yarrowia lipolytica Wratislavia K1 was found to be applicable for the production of high amounts of erythritol in RBC. When 20 % of fresh replaced medium was added, the strain Wratislavia K1 was able to produce 220 g l ^?1 erythritol, which corresponded to a 0.43 g g^?1 yield and a productivity of 0.54 g l^?1 h^?1. Additionally, the activity of the culture remained stable for more than 1,000 h, i.e., 11 cycles of the repeated batch bioreactors.     

Characteristics of the growth on rapeseed oil and synthesis of citric and isocitric acids by <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> yeasts

The native strain Yarrowia lipolytica VKMY-2373 grown in a complete medium exhibited the maximum lipase activity at the concentration of rapesseed oil of at least 5.0 g/l. In the course of yeast growth, no considerable changes were observed in the glycerol concentration, the proportions of the major free fatty acids formed via oil hydrolysis, or the fatty acid composition of oil. Under nitrogen limitation of cell growth, the accumulation of citric acids reached 77.1 g/l with predominance of isocitric acid at pH 6.0, whereas at pH 4.5, almost equal amounts of citric and isocitric acids were produced. Cultivation of the mutant strain Y. lipolytica N 1 at pH 4.5 resulted in the predominant accumulation of citric acid (66.6 g/l) with an insignificant amount of isocitric acid. In the period of intense acid synthesis, high production of lipase was observed.     

Regulation of NAD<Superscript>+</Superscript>-dependent isocitrate dehydrogenase in the citrate producing yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

The mechanism of the increased accumulation (overproduction) of citric acids in the yeast Yarrowia lipolytica while growing in the presence of glucose under nitrogen deficiency was investigated. The limitation of the yeast growth by the source of nitrogen decreases the total content of nucleotides and increases the ratios of ATP/AMP and NADH/NAD⁺. NAD⁺-Dependent isocitrate dehydrogenase, an enzyme of the tricarboxylic acid cycle playing a key role in the regulation of biosynthesis of citric and isocitric acids, was isolated from Y. lipolytica. The molecular weights of the native enzyme and its subunits were found to be 412 and 52 kD, respectively. It is concluded that the enzyme is a homooligomer consisting of eight subunits. Investigation of the effect of some intermediates of the tricarboxylic acid cycle on the activity of this enzyme suggests that the enhanced excretion of citric acids can be caused by the inhibition of NAD⁺-dependent isocitrate dehydrogenase due to the decrease in the content of AMP and increase in the NADH/NAD⁺ ratio in the cells of Y. lipolytica under depletion of nitrogen.Translated from Biokhimiya, Vol. 69, No. 12, 2004, pp. 1706–1714.Original Russian Text Copyright © 2004 by Morgunov, Solodovnikova, Sharyshev, Kamzolova, Finogenova.     

Effect of agitation and aeration on the citric acid production by Yarrowia lipolytica grown on glycerol

The effects of agitation rates from 400 to 900 rpm and aeration rates ranging from 0.18 to 0.6 vvm on biomass and citric acid production on glycerol media by acetate-negative mutants of Yarrowia lipolytica, Wratislavia 1.31 and Wratislavia AWG7, in batch culture were studied. The agitation rates of 800 and 900 rpm (at a constant aeration rate of 0.36 vvm) and aeration rates within the range of 0.24-0.48 vvm (at a constant agitation rate of 800 rpm), which generated dissolved oxygen concentration (DO) higher than 40%, were found the best for citric acid biosynthesis from glycerol. An increase in agitation rate (higher than 800 rpm) and aeration rate (higher than 0.36 vvm) had no impact on DO and citric acid production. The highest citric acid concentration (92.8 g/L) and yield (0.63 g/g) were obtained with Wratislavia 1.31 strain at 0.24 vvm. The highest volumetric citric acid production rate (1.15 g/Lh) and specific citric acid production rate (0.071 g/gh) were reached at 0.48 vvm.     

Overexpression of the <Emphasis Type="Italic">ICL1</Emphasis> gene changes the product ratio of citric acid production by <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

The yeast Yarrowia lipolytica secretes high amounts of various organic acids, like citric (CA) and isocitric (ICA) acids, triggered by growth limitation caused by different factors and an excess of carbon source. Depending on the carbon source used, Y. lipolytica strains produce a mixture of CA and ICA in a characteristic ratio. To examine whether the CA/ICA product ratio can be influenced by gene-dose-dependent overexpression or by disruption of the isocitrate lyase (ICL)-encoding gene ICL1, recombinant Y. lipolytica strains were constructed, which harbour multiple ICL1 copies or a defective icl1 allele. The high-level expression of ICL in ICL1 multicopy integrative transformants resulted in a strong shift of the CA/ICA ratio into direction of CA. On glycerol, glucose and sucrose, the ICA proportion decreased from 10–12% to 3–6%, on sunflower oil or hexadecane even from 37–45% to 4–7% without influencing the total amount of acids (CA and ICA) produced. In contrast, the loss of ICL activity in icl1-defective strains resulted in a moderate 2–5% increase in the ICA proportion compared to ICL wild-type strains on glucose or glycerol.     

A Review of: “North-Holland Publishing Company,Amsterdam, New York,Oxford, 1976; Softbound, 290 pages, $ 19.25.”

Several factors affecting erythritol production from glycerol by Yarrowia lipolytica Wratislavia K1 strain were examined in batch fermentations. Ammonium sulfate, monopotassium phosphate, and sodium chloride were identified as critical medium components that determine the ratio of polyols produced. The central composite rotatable experimental design was used to optimize medium composition for erythritol production. The concentrations of ammonium sulfate, monopotassium phosphate, and sodium chloride in the optimized medium were 2.25, 0.22, and 26.4 g L^?1, respectively. The C:N ratio was found as 81:1. In the optimized medium with 100 g L^?1 of glycerol the Wratislavia K1 strain produced 46.9 g L^?1 of erythritol, which corresponded to a 0.47 g g^?1 yield and a productivity of 0.85 g L^?1 hr^?1. In the fed-batch mode and medium with the total concentration of glycerol at 300 g L^?1 and C:N ratio at 81:1, 132 g L^?1 of erythritol was produced with 0.44 g g^?1 yield and a productivity of 1.01 g L^?1 hr^?1.     

Aconitase overexpression changes the product ratio of citric acid production by <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

The yeast Yarrowia lipolytica secretes high amounts of various organic acids, like citric acid (CA) and isocitric acid (ICA) under an excess of carbon source and several conditions of growth limitation. Depending on the carbon source used, Y. lipolytica strains produce a mixture of CA and ICA in a characteristic ratio. To examine whether this CA/ICA product ratio can be influenced by gene–dose-dependent overexpression of aconitase (ACO)-encoding gene ACO1, a recombinant Y. lipolytica strain was constructed containing multiple copies of ACO1. The high-level expression of ACO in the ACO1 multicopy integrative transformant resulted in a shift of the CA/ICA product pattern into the direction of ICA. On sunflower oil, a striking increase of the ICA proportion from 35–49% to 66–71% was observed compared to wild-type strains without influencing the total amount of acids (CA and ICA) produced. On glycerol, glucose or sucrose, the ICA proportion increased only moderately from 10–12% to 13–17%. This moderate shift into the direction of ICA was also observed in an icl1-defective strain.     

The citric acid production from raw glycerol by Yarrowia lipolytica yeast and its regulation

The optimal cultivation conditions ensuring the maximal rate of citric acid (CA) biosynthesis by glycerol-grown mutant Yarrowia lipolytica NG40/UV7 were found to be as follows: growth limitation by inorganic nutrients (nitrogen, phosphorus, or sulfur), 28 °C, pH 5.0, dissolved oxygen concentration (pO₂) of 50 % (of air saturation), and pulsed addition of glycerol from 20 to 80 g L^?1 depending on the rate of medium titration. Under optimal conditions of fed-batch cultivation, in the medium with pure glycerol, strain Y. lipolytica NG40/UV7 produced 115 g L^?1 of CA with the mass yield coefficient of 0.64 g g^?1 and isocitric acid (ICA) amounted to 4.6 g L^?1; in the medium with raw glycerol, CA production was 112 g L^?1 with the mass yield coefficient of 0.90 g g^?1 and ICA amounted to 5.3 g L^?1. Based on the activities of enzymes involved in the initial stages of raw glycerol assimilation, the tricarboxylic acid cycle and the glyoxylate cycle, the mechanism of increased CA yield from glycerol-containing substrates in Y. lipolytica yeast was explained.     

Multiple gene integration to promote erythritol production on glycerol in Yarrowia lipolytica

Objective

Erythritol (1,2,3,4-butanetetrol) is a 4-carbon sugar alcohol that occurs in nature as a metabolite or storage compound. In this study, a multiple gene integration strategy was employed to enhance erythritol production in Y. lipolytica.

Results

The effects on the production of erythritol in Y. lipolytica of seven key genes involved in the erythritol synthesis pathway were evaluated individually, among which transketolase (TKL1) and transaldolase (TAL1) showed important roles in enhancing erythritol production. The combined overexpression of four genes (GUT1, TPI1, TKL1, TAL1) and disruption of the EYD1 gene (encoding erythritol dehydrogenase), resulted in produce approximately 40 g/L erythritol production from glycerol. Further enhanced erythritol synthesis was obtained by overexpressing the RKI1 gene (encoding ribose 5-phosphate isomerase) and the AMPD gene (encoding AMP deaminase), indicating for the first time that these two genes are also related to the enhancement of erythritol production in Y. lipolytica.

Conclusions

A combined gene overexpression strategy was developed to efficiently improve the production of erythritol in Y. lipolytica, suggesting a great capacity and promising potential of this non-conventional yeast in converting glycerol into erythritol.

     

Chemostat study of citric acid production from glycerol by Yarrowia lipolytica

The aim of the study was to examine how the dilution rate and the chemical composition of the production medium impacts on the synthesis of citric acid by the Yarrowia lipolytica strain Wratislavia AWG7 from glycerol in a chemostat culture. The yeast Y. lipolytica Wratislavia AWG7, an acetate (acet(-)) and morphological (fil(-)) mutant, was cultured in a nitrogen- and phosphorus-limited medium at the dilution rate of 0.009-0.031h(-1) in the chemostat. Under steady-state conditions, the increase in the dilution rate was paralleled by the decrease in citric acid concentration (from 86.5 to 51.2gL(-1)), as well as by the increase in the volumetric rate (from 0.78 to 1.59gL(-1)h(-1)) and specific rate (from 0.05 to 0.18gg(-1)h(-1)) of citric acid production. The yield of the production process varied from 0.59 to 0.67gg(-1). In a 550-h continuous culture of the yeast test, at a dilution rate of 0.01h(-1), in a medium with enhanced concentrations of carbon, nitrogen and phosphorus sources, the concentration of citric acid, the concentration of biomass and the volumetric rate of citric acid production were 97.8gL(-1), 22.2gL(-1) and 0.98gL(-1)h(-1), respectively. The yield of the process decreased to 0.49gg(-1). The number of dead cells did not exceed 1% while that of the budding cells accounted for about 20%. Owing to the low content of isocitric acid and polyols, the fermentation process was characterized by a high purity. This study has produced the following finding: the double mutant Y. lipolytica AWG7 is an effective citric acid producer, with the ability to preserve its properties unchanged during the long run of the continuous chemostat process. This is a valued technological feature of such mutants.     

Citric acid production from glycerol-containing waste of biodiesel industry by Yarrowia lipolytica in batch, repeated batch, and cell recycle regimes

Yarrowia lipolytica A-101-1.22 produces high citric acid (112 g l⁻¹) with a yield of 0.6 g g⁻¹ and a productivity of 0.71 g l⁻¹ h⁻¹ during batch cultivation in the medium with glycerol-containing waste of biodiesel industry. However, it was observed that the specific citric acid production rate, which was maximal at the beginning of the biosynthesis, gradually decreases in the late production phase and it makes continuation of the process over 100 h pointless. The cell recycle and the repeated batch regimes were performed as ways for prolongation of citric acid synthesis by yeast. Using cell recycle, the active citric acid biosynthesis (96–107 g l⁻¹) with a yield of 0.64 g g⁻¹ and a productivity of 1.42 g l⁻¹ h⁻¹ was prolongated up to 300 h. Repeated batch culture remained stable for over 1000 h; the RB variant of 30% feed every 3 days showed the best results: 124.2 g l^-1 citric acid with a yield of 0.77 g g^-1 and a productivity of 0.85 g l^-1 h^-1.     

Lipid production by yeasts grown on crude glycerol from biodiesel industry

The main carbon source used for growth by four yeast strains (Yarrowia lipolytica CCMA 0357, Y. lipolytica CCMA 0242, Wickerhamomyces anomalus CCMA 0358, and Cryptococcus humicola CCMA 0346) and their lipid production were evaluated, using different concentrations of crude and pure glycerol and glucose. Whereas crude glycerol (100?g/L) was the main carbon source used by Y. lipolytica CCMA 0357 (nearly 15?g/L consumed at 120?hr) and W. anomalus CCMA 0358 (nearly 45.10?g/L consumed at 48?hr), pure glycerol (150?g/L) was the main one used by C. humicola CCMA 0346 (nearly 130?g/L consumed). On the other hand, Y. lipolytica CCMA 0242 used glucose (100?g/L) as its main source of carbon (nearly 96.48?g/L consumed). Y. lipolytica CCMA 0357 demonstrated the highest lipid production [about 70% (wt/wt)], forming palmitic (45.73% of fatty acid composition), stearic (16.43%), palmitoleic (13.29%), linolenic (10.77%), heptadecanoic (4.07%), and linoleic (14.14%) acids. Linoleic acid, an essential fatty acid, was produced by all four yeast strains but in varying degrees, representing 70.42% of the fatty acid profile of lipids produced by C. humicola CCMA 0346.     

Citric acid production from glucose. I. Growth and excretion kinetics in a stirred fermentor

The growth and citric acid production kinetics of Saccharomycopsis lipolytica on glucose are investigated in an aerated stirred fermentor. Cellular growth first proceeds exponentially until exhaustion of ammonia in the fermentation medium. Cells then continue to grow at a reduced rate with a concomitant decrease in intracellular nitrogen content. Citric and isocitric acid production starts at the end of the growth phase. During about 80 hr excretion proceeds at a constant rate of 0.7 g/liter/hr for citric acid and 0.1 g/liter/hr for isocitric acid. The final citric and isocitric acid concentrations are 95 and 10g/liter, respectively. During acid excretion cellular respiration accounts for 60 and 35% of consumed oxygen and glucose. Both acid and CO₂ production rates follow a Michaelis–Menten-type dependence on oxygen concentration with Michaelis–Menten constants of 0.9 and 0.15 mg/liter for acid and CO₂ productions, respectively.     

Glycerol/Glucose Co-Fermentation: One More Proficient Process to Produce Propionic Acid by <Emphasis Type="Italic">Propionibacterium acidipropionici</Emphasis>

Cosubstrates fermentation is such an effective strategy for increasing subject metabolic products that it could be available and studied in propionic acid production, using glycerol and glucose as carbon resources. The effects of glycerol, glucose, and their mixtures on the propionic acid production by Propionibacterium acidipropionici CGMCC1.2225 (ATCC4965) were studied, with the aim of improving the efficiency of propionic acid production. The propionic acid yield from substrate was improved from 0.475 and 0.303 g g⁻¹ with glycerol and glucose alone, respectively, to 0.572 g g⁻¹ with co-fermentation of a glycerol/glucose mixture of 4/1 (mol/mol). The maximal propionic acid and substrate conversion rate were 21.9 g l⁻¹ and 57.2% (w/w), respectively, both significantly higher than for a sole carbon source. Under optimized conditions of fed-batch fermentation, the maximal propionic acid yield and substrate conversion efficiency were 29.2 g l⁻¹ and 54.4% (w/w), respectively. These results showed that glycerol/glucose co-fermentation could serve as an excellent alternative to conventional propionic acid fermentation.     

Characterization of biotechnological processes and products using high-performance liquid chromatography (HPLC). III. Quantitative analysis of organic acids in the α-ketoglutaric acid synthesis

A HPLC technique for the analysis of organic acids in the production of α-ketoglutaric acid was developed. The method was applied and optimized for the quantitative determination of citric acid, pyruvic acid, isocitric acid and α-ketoglutaric acid in fermentation solutions. As microorganism the yeast Yarrowia lipolytica and as substrates glucose or paraffins were used. The chromatographic separations were carried out by means of 50 and 100 × 8 mm i.d. glass columns packed with an anion-exchange resin based on an 8% cross-linked polystyrene-divinylbenzene copolymer. The relative errors ranged from 2.1% (α-ketoglutaric acid) to 5.2% (isocitric acid). The percent recovery values varied between 94.4% (isocitric acid) and 107.7% (pyruvic acid). The contents of organic acids in fermentation solutions after the microbial synthesis based on paraffins or glucose were compared.