Control of Lipid Accumulation in the Yeast Yarrowia lipolytica

A genomic comparison of Yarrowia lipolytica and Saccharomyces cerevisiae indicates that the metabolism of Y. lipolytica is oriented toward the glycerol pathway. To redirect carbon flux toward lipid synthesis, the GUT2 gene, which codes for the glycerol-3-phosphate dehydrogenase isomer, was deleted in Y. lipolytica in this study. This Δgut2 mutant strain demonstrated a threefold increase in lipid accumulation compared to the wild-type strain. However, mobilization of lipid reserves occurred after the exit from the exponential phase due to β-oxidation. Y. lipolytica contains six acyl-coenzyme A oxidases (Aox), encoded by the POX1 to POX6 genes, that catalyze the limiting step of peroxisomal β-oxidation. Additional deletion of the POX1 to POX6 genes in the Δgut2 strain led to a fourfold increase in lipid content. The lipid composition of all of the strains tested demonstrated high proportions of FFA. The size and number of the lipid bodies in these strains were shown to be dependent on the lipid composition and accumulation ratio.     

Lactate and Amino Acid Catabolism in the Cheese-Ripening Yeast Yarrowia lipolytica

The consumption of lactate and amino acids is very important for microbial development and/or aroma production during cheese ripening. A strain of Yarrowia lipolytica isolated from cheese was grown in a liquid medium containing lactate in the presence of a low (0.1×) or high (2×) concentration of amino acids. Our results show that there was a dramatic increase in the growth of Y. lipolytica in the medium containing a high amino acid concentration, but there was limited lactate consumption. Conversely, lactate was efficiently consumed in the medium containing a low concentration of amino acids after amino acid depletion was complete. These data suggest that the amino acids are used by Y. lipolytica as a main energy source, whereas lactate is consumed following amino acid depletion. Amino acid degradation was accompanied by ammonia production corresponding to a dramatic increase in the pH. The effect of adding amino acids to a Y. lipolytica culture grown on lactate was also investigated. Real-time quantitative PCR analyses were performed with specific primers for five genes involved in amino acid transport and catabolism, including an amino acid transporter gene (GAP1) and four aminotransferase genes (ARO8, ARO9, BAT1, and BAT2). The expression of three genes involved in lactate transport and catabolism was also studied. These genes included a lactate transporter gene (JEN1) and two lactate dehydrogenase genes (CYB2-1 and CYB2-2). Our data showed that GAP1, BAT2, BAT1, and ARO8 were maximally expressed after 15 to 30 min following addition of amino acids (BAT2 was the most highly expressed gene), while the maximum expression of JEN1, CYB2-1, and CYB2-2 was delayed (≥60 min).     

解脂耶罗维亚酵母产油脂的研究进展

单细胞油脂是生产生物柴油最理想的原料,随着化石能源的日益枯竭,单细胞油脂的生产受到广泛关注。解脂耶罗维亚酵母是生产单细胞油脂的最佳菌株,它能够利用诸多廉价底物作为碳源,在工业上有极大的应用前景。其遗传背景清晰,全基因组测序已完成,基因表达系统已构建。在此基础上对油脂累积途径进行了深入研究,多株油脂含量更高的菌株被构建。深入了解解脂耶罗维亚酵母的基因表达及油脂代谢系统,对日后对其进一步的代谢改造具有重要意义。     

Engineering of the Yeast Yarrowia lipolytica for the Production of Glycoproteins Lacking the Outer-Chain Mannose Residues of N-Glycans

In an attempt to engineer a Yarrowia lipolytica strain to produce glycoproteins lacking the outer-chain mannose residues of N-linked oligosaccharides, we investigated the functions of the OCH1 gene encoding a putative α-1,6-mannosyltransferase in Y. lipolytica. The complementation of the Saccharomyces cerevisiae och1 mutation by the expression of YlOCH1 and the lack of in vitro α-1,6-mannosyltransferase activity in the Yloch1 null mutant indicated that YlOCH1 is a functional ortholog of S. cerevisiae OCH1. The oligosaccharides assembled on two secretory glycoproteins, the Trichoderma reesei endoglucanase I and the endogenous Y. lipolytica lipase, from the Yloch1 null mutant contained a single predominant species, the core oligosaccharide Man₈GlcNAc₂, whereas those from the wild-type strain consisted of oligosaccharides with heterogeneous sizes, Man₈GlcNAc₂ to Man₁₂GlcNAc₂. Digestion with α-1,2- and α-1,6-mannosidase of the oligosaccharides from the wild-type and Yloch1 mutant strains strongly supported the possibility that the Yloch1 mutant strain has a defect in adding the first α-1,6-linked mannose to the core oligosaccharide. Taken together, these results indicate that YlOCH1 plays a key role in the outer-chain mannosylation of N-linked oligosaccharides in Y. lipolytica. Therefore, the Yloch1 mutant strain can be used as a host to produce glycoproteins lacking the outer-chain mannoses and further developed for the production of therapeutic glycoproteins containing human-compatible oligosaccharides.     

Production of citric acid with immobilized Yarrowia lipolytica

Summary Citric acid was produced with immobilized Yarrowia lipolytica yeast in repeated batch-shake-flask and air-lift fermentations. In active and passive immobilization methods calcium alginate, -carrageenan, polyurethane gel, nylon web and polyurethane foams were tested as carriers in repeated-batch fermentations. The highest citric acid productivity of 155 mg l^–1 h^–1 was reached with alginate-bead-immobilized cells in the first batch. A decrease in bead diameter from 5–6 mm to 2–3 mm increased the volumetric citric acid productivity threefold. In an air-lift bioreactor the highest citric acid productivity of 120 mg l^–1 h^–1 with a product concentration of 16.4 g l^–1 was obtained with cells immobilized in -carrageenan beads. Offprint requests to: H. Kautola     

Exploring the Catalytic Core of Complex I by Yarrowia lipolytica Yeast Genetics

We have developed Yarrowia lipolytica as a model system to study mitochondrial complex I that combines the application of fast and convenient yeast genetics with efficient structural and functional analysis of its very stable complex I isolated by his–tag affinity purification with high yield. Guided by a structural model based on homologies between complex I and [NiFe] hydrogenases mutational analysis revealed that the 49 kDa subunit plays a central functional role in complex I. We propose that critical parts of the catalytic core of complex I have evolved from the hydrogen reactive site of [NiFe] hydrogenases and that iron–sulfur cluster N2 resides at the interface between the 49 kDa and PSST subunits. These findings are in full agreement with the semiquinone switch mechanism according to which coupling of electron and proton transfer in complex I is achieved by a single integrated pump comprising cluster N2, the binding site for substrate ubiquinone, and a tightly bound quinone or quinoid group.     

Production of brown tyrosine pigments by the yeast Yarrowia lipolytica

AIMS: To study the mechanism of production of brown pigments from tyrosine in the yeast Yarrowia lipolytica. METHODS AND RESULTS: Pigment formation was followed during growth in tyrosine medium, and the presence of the pigment precursor in the medium was assessed by evaluating pigment formation after removing the cells at different times of incubation. It was observed that the pigment precursor accumulated outside the cells during the exponential phase of growth, but pigment formation only occurred during the stationary phase of growth and resulted from the oxidation of the precursor. Pigment formation was repressed by glucose and L-glutamine, and promoted by lactic acid, L-asparagine and glycine. Spectra of 1H and 13C-NMR revealed that the brown pigment was derived from tyrosine and was a polymer composed of a core of aromatic residues. CONCLUSION: The results indicate that pigments result from the extracellular accumulation and auto-oxidation of an intermediate of tyrosine catabolism. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first report on the mechanism of pigment production from tyrosine in a yeast species.     

Intracellular cAMP Content and the Induction of Alternative Oxidase in the Yeast Yarrowia lipolytica

The effect of cyanide, antimycin A, ethanol, and acetate on the induction of alternative oxidase in the yeast Yarrowia lipolytica VKM Y-155 was studied. The aerobic incubation of logarithmic-phase cells, whose respiration is sensitive to cyanide, in the presence of the aforementioned compounds led to the development of cyanide-resistant respiration, which could be suppressed by benzohydroxamic acid, an inhibitor of alternative oxidases. The incubation of cells with cyanide, ethanol, or acetate raised the intracellular pool of cAMP, which attained maximal values after a 2- to 3-min incubation period, then rapidly decreased to the initial value and did not change over the next three hours of incubation. The possible role of cAMP in the induction of alternative oxidase in yeast cells is discussed.     

Production of 1-decanol by metabolically engineered Yarrowia lipolytica

Medium-chain alcohols are used to produce solvents, surfactants, lubricants, waxes, creams, and cosmetics. In this study, we engineered the oleaginous yeast Yarrowia lipolytica to produce 1-decanol from glucose. Expression of a fatty acyl-CoA reductase from Arabidopsis thaliana in strains of Y. lipolytica previously engineered to produce medium-chain fatty acids resulted in the production of 1-decanol. However, the resulting titers were very low (<10 mg/mL), most likely due to product catabolism. In addition, these strains produced small quantities of 1-hexadecanol and 1-octadecanol. Deleting the major peroxisome assembly factor Pex10 was found to significantly increase 1-decanol production, resulting in titers exceeding 500 mg/L. It also increased 1-hexadecanoland and 1-octadecanol titers, though the resulting increases were less than those for 1-decanol. These results demonstrate that Y. lipolytica can potentially be used for the industrial production of 1-decanol and other fatty alcohols from simple sugars.     

Optimization of Citric Acid Production from Glucose by Yarrowia lipolytica

Citric acid (CA) is mainly produced in a biotechnological process using Aspergillus niger. In this process, large amounts of wastes have to be removed. Since the use of Yarrowia lipolytica for CA production is an environmental compatible alternative method, the CA production was optimized in regard to growth temperature and pH as well as substrate and product inhibition. The highest value of the maximum specific growth rate at pH 6.5 was found to be μ_max = 0.192 h^–1, whereas the largest amount of CA of 24.91 g/L as well as the highest selectivity of the bioprocess (89.9 % CA) and the maximum yield (0.22 g_CA/g_Glucose) were obtained at pH 6.0. During the growth phase, the temperature optimum was found to be in the range of 30–34 °C (μ_max = 0.132 h^–1). Nevertheless, the highest concentration of CA during the production phase was obtained at 30 °C (41 g/L CA, 93.1 % CA, 0.55 g_CA/g_glucose). In studying the substrate inhibition of the process, a clear tendency of decrease in the maximum specific growth rate was detected when the initial glucose concentration was increased from 50 g/L (μ_max = 0.17 h^–1) to 200 g/L (μ_max = 0.055 h^–1). The addition of 120 g/L CA to the culture broth at the start of the production phase reduced the production of CA from 32.1 g/L to 7.4 g/L.     

Role of β-Oxidation Enzymes in γ-Decalactone Production by the Yeast Yarrowia lipolytica

Some microorganisms can transform methyl ricinoleate into γ-decalactone, a valuable aroma compound, but yields of the bioconversion are low due to (i) incomplete conversion of ricinoleate (C₁₈) to the C₁₀ precursor of γ-decalactone, (ii) accumulation of other lactones (3-hydroxy-γ-decalactone and 2- and 3-decen-4-olide), and (iii) γ-decalactone reconsumption. We evaluated acyl coenzyme A (acyl-CoA) oxidase activity (encoded by the POX1 through POX5 genes) in Yarrowia lipolytica in lactone accumulation and γ-decalactone reconsumption in POX mutants. Mutants with no acyl-CoA oxidase activity could not reconsume γ-decalactone, and mutants with a disruption of pox3, which encodes the short-chain acyl-CoA oxidase, reconsumed it more slowly. 3-Hydroxy-γ-decalactone accumulation during transformation of methyl ricinoleate suggests that, in wild-type strains, β-oxidation is controlled by 3-hydroxyacyl-CoA dehydrogenase. In mutants with low acyl-CoA oxidase activity, however, the acyl-CoA oxidase controls the β-oxidation flux. We also identified mutant strains that produced 26 times more γ-decalactone than the wild-type parents.     

代谢工程构建重组耶氏解脂酵母生产中长链聚羟基脂肪酸酯

中长链聚羟基脂肪酸酯(mcl-PHA)是一大类由微生物合成的天然生物聚酯,因具有可再生性和生物降解性越来越受到人们的关注。Mcl-PHA可由一些假单胞菌类利用自身的脂肪酸合成途径或β-氧化途径来合成。耶氏解脂酵母具有很好的脂/脂肪酸分解代谢能力,但是它体内缺乏PHA合成酶不能合成mcl-PHA。采用代谢工程策略构建重组解脂酵母,外源表达来自铜绿假单胞菌PAO1(Pseudomonas aeruginosa PAO1)的PHA合成酶。在PHA合成酶的C端添加PTS1过氧化物酶体定位信号序列,使其在过氧化物酶体内发挥功能,并对其编码基因PhaC1进行密码子优化得到oPhaC1。利用pINA1312载体构建表达框,借助载体上的zeta序列元件将oPhaC1基因表达框整合至酵母基因组,完成基因的稳定表达。重组菌PSOC在葡萄糖为唯一碳源的培养基中几乎不产PHA,添加0.5%的油酸时可合成占细胞干重0.67%的mcl-PHA。在含三油酸甘油酯的培养基中发酵72h产生1.51% mcl-PHA(wt%)。实验结果充分证明重组解脂酵母作为有潜力的微生物细胞工厂可以用于生产mcl-PHA,也为将来利用富含油脂和其他营养的餐厨垃圾水解液等廉价资源生产mcl-PHA打下基础。     

Peroxisome biogenesis in the yeast Yarrowia lipolytica

Extensive perexisome proliferation during growth on oleic acid, combined with the availability of excellent genetic tools, makes the dimorphic yeast, Yarrowia lipolytica, a powerful model system to study the molecular mechanisms involved in peroxisome biogenesis. A combined genetic, biochemical, and morphological approach has revealed that the endoplasmic reticulum (ER) plays an essential role in the assembly of functional peroxisomes in this yeast. The trafficking of some membrane proteins to the peroxisomes occurs via the ER, results in their glyco-sylation in the ER lumen, does not involve transit through the Golgi, and requires the products of the SEC238, SRP54, PEX1, and PEX6 genes. The authors' data suggest a model for protein import into peroxisomes via two subpopulations of ER-derived vesicles that are distinct from secretory vesicles. A kinetic analysis of the trafficking of peroxisomal proteins in vivo has demonstrated that membrane and matrix proteins are initially targeted to multiple vesicular precursors that represent intermediates in the assembly pathway of peroxisomes. The authors have also recently identified a novel cytosolic chaperone, Pex20p, that assists in the oligomerization of thiolase in the cytosol and promotes its targeting to the peroxisome. These data provide the first evidence that a chaperone-assisted folding and oligomerization of thiolase in the cytosol is required for the import of this protein into the peroxisomal matrix.     

Lipase location in Yarrowia lipolytica cells

Lipase production by Yarrowia lipolytica was growth associated and, at the beginning of cultivation, it was mainly cell-bound. Lipase release into the culture medium started when about 50% of the carbon source (olive oil or glucose) was consumed reaching its maximum concentration in the late stationary phase.     

Evaluation of Acyl Coenzyme A Oxidase (Aox) Isozyme Function in the n-Alkane-Assimilating Yeast Yarrowia lipolytica

We have identified five acyl coenzyme A (CoA) oxidase isozymes (Aox1 through Aox5) in the n-alkane-assimilating yeast Yarrowia lipolytica, encoded by the POX1 through POX5 genes. The physiological function of these oxidases has been investigated by gene disruption. Single, double, triple, and quadruple disruptants were constructed. Global Aox activity was determined as a function of time after induction and of substrate chain length. Single null mutations did not affect growth but affected the chain length preference of acyl-CoA oxidase activity, as evidenced by a chain length specificity for Aox2 and Aox3. Aox2 was shown to be a long-chain acyl-CoA oxidase and Aox3 was found to be active against short-chain fatty acids, whereas Aox5 was active against molecules of all chain lengths. Mutations in Aox4 and Aox5 resulted in an increase in total Aox activity. The growth of mutant strains was analyzed. In the presence of POX1 only, strains did not grow on fatty acids, whereas POX4 alone elicited partial growth, and the growth of the double POX2-POX3-deleted mutant was normal excepted on plates containing oleic acid as the carbon source. The amounts of Aox protein detected by Western blotting paralleled the Aox activity levels, demonstrating the regulation of Aox in cells according to the POX genotype.     

Production of erythritol and mannitol by Yarrowia lipolytica yeast in media containing glycerol

Glycerol is a by-product generated in large amounts during the production of biofuels. This study presents an alternative means of crude glycerol valorization through the production of erythritol and mannitol. In a shake-flasks experiment in a buffered medium, nine Yarrowia lipolytica strains were examined for polyols production. Three strains (A UV'1, A-15 and Wratislavia K1) were selected as promising producers of erythritol or/and mannitol and used in bioreactor batch cultures and fed-batch mode. Pure and biodiesel-derived crude glycerol media both supplemented (to 2.5 and 3.25?%) and not-supplemented with NaCl were applied. The best results for erythritol biosynthesis were achieved in medium with crude glycerol supplemented with 2.5?% NaCl. Wratislavia K1 strain produced up to 80.0?g?l(-1) erythritol with 0.49?g?g(-1) yield and productivity of 1.0?g?l(-1)?h(-1). Erythritol biosynthesis by A UV'1 and A-15 strains was accompanied by the simultaneous production of mannitol (up to 27.6?g?l(-1)). Extracellular as well as intracellular erythritol and mannitol ratios depended on the glycerol used and the presence of NaCl in the medium. The results from this study indicate that NaCl addition to the medium improves erythritol biosynthesis, and simultaneously inhibits mannitol formation.     

Protein Production in Yarrowia lipolytica Via Fusion to the Secreted Lipase Lip2p

We established a strategy for protein production and purification via expression in Yarrowia lipolytica as Lip2p fusion protein. To evaluate the expression system a cysteine-rich miniprotein, an antibody fragment and an enzyme showing galactose oxidase activity were chosen. These proteins have varying disulfide bond content, size, and structural complexity. Endogenous lipase Lip2p was used as a fusion partner to direct the fused proteins to the extracellular medium. A linker sequence was introduced at the junction of Lip2p and the respective fused protein that contains a hexahistidine tag followed by a TEV protease cleavage site. This allows for a specific and simple purification via IMAC for capturing the secreted proteins from the supernatant followed by a second IMAC for removing all contaminants after proteolytic release of the protein of interest. Up to 174 mg/L fusion protein was obtained using shake flask cultivation. Functionality of each of the purified proteins was confirmed by individual assays. Expression of proteins of interest via Lip2p fusion not only provides a convenient expression and purification scheme but also enables for an online monitoring of accumulation of secreted fusion proteins in the medium by exploiting the intrinsic lipase activity of the fusion.