Synthesis citric and isocitric acids by Yarrowia lipolytica during yeasts growth on rapeseed oils

The native strain Yarrowia lipolytica VKM Y-2373 grown in a complete medium exhibited the maximum lipase activity at the concentration of rapeseed 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.     

New recombinant strains of the yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> with overexpression of the aconitate hydratase gene for the obtainment of isocitric acid from rapeseed oil

The yeast Yarrowia lipolytica is capable of high-intensity synthesis (overproduction) of citric (CA) and isocitric (ICA) acids under nitrogen limitation. The ratio of the synthesized acids depends on the producing strains used and the expression level of the aconitate hydratase gene (ACO1). Recombinant variants with overexpression of the multicopy ACO1 gene have been obtained based on the natural ICA-producing strain Y. lipolytica 672. A recombinant strain Y. lipolytica 20, which has an isocitrate-citrate ratio shifted towards ICA (2.3: 1) as compared to the parental strain (1.1: 1), has been selected. Culturing of the 20 variant in a 10 L reactor has resulted in the production of 72.6 g/L of ICA and 29.0 g/L of CA with a ratio of 2.5: 1. This makes it possible to regard Y. lipolytica 20 as a promising producer for the development of an industrial process for isocitrate production.     

Organic Acid Production by the Yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>: A Review of Prospects

The review sums up the results of studies of (1) physiological growth characteristics of the yeast Yarrowia lipolytica cultured in the presence of diverse carbon sources (n-alkanes, glucose, and glycerol) and (2) superhigh synthesis of organic acids, which was performed at the Skryabin Institute of Biochemistry and Physiology of Microorganisms, Russian Academy of Sciences. Microbiological processes of obtaining α-ketoglutaric, pyruvic, isocitric, and citric acids are discussed.     

Engineering <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> for the production of cyclopropanated fatty acids

Traditional synthesis of biodiesel competes with food sources and has limitations with storage, particularly due to limited oxidative stability. Microbial synthesis of lipids provides a platform to produce renewable fuel with improved properties from various renewable carbon sources. Specifically, biodiesel properties can be improved through the introduction of a cyclopropane ring in place of a double bond. In this study, we demonstrate the production of C19 cyclopropanated fatty acids in the oleaginous yeast Yarrowia lipolytica through the heterologous expression of the Escherichia coli cyclopropane fatty acid synthase. Ultimately, we establish a strain capable of 3.03?±?0.26 g/L C19 cyclopropanated fatty acid production in bioreactor fermentation where this functionalized lipid comprises over 32% of the total lipid pool. This study provides a demonstration of the flexibility of lipid metabolism in Y. lipolytica to produce specialized fatty acids.     

Optimization of citric acid production from a carrot juice-based medium by <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> using response surface methodology

In this study, diluted and fortified carrot juice was used for modelling and optimization of citric acid production by a new mutant strain, Yarrowia lipolytica K-168. Protein concentrate obtained from fine flour -a byproduct of semolina production- was used as a nitrogen source in the fermentation medium. Interactive effects of selected independent variables, initial total sugar concentration, initial pH, initial concentration of protein concentrate obtained from fine flour of semolina and temperature, on the growth and citric acid production of the yeast were investigated. An experimental design including 30 experiments was conducted by using the method of central composite design. Modelling the effects of these independent variables on maximum citric acid concentration, maximum citric acid production rate, citric acid yield, the ratio of maximum citric acid concentration to maximum isocitric acid concentration and specific growth rate were performed by response surface methodology. The variations of all of the responses with the independent variables were defined by a quadratic model. Numeric optimization was performed by using the desireability function. The conditions with 190.83 g/L initial sugar concentration, 5.90 initial pH, 0.07 g/L initial concentration of fine flour protein concentrate and 27.86 °C were determined as optimal conditions for citric acid production. The maximum citric acid concentration reached to 80.53 g/L in optimal conditions.     

Optimization of Repeated-Batch Fermentation of a Recombinant Strain of the Yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> for Succinic Acid Production at Low pH

The capacity of a recombinant Yarrowia lipolytica yeast strain VKPM Y3753 for succinic acid biosynthesis in a laboratory bioreactor at low pH has been studied. The batch and repeated-batch modes of fermentation of the strain were compared. The optimal conditions for repeated-batch fermentation were selected; they resulted in the accumulation of 55.3 g/L of succinic acid and the maximal productivity for this compound, 2.6 g/(L h), while lowering the pH of the broth culture to 3.65 at the end of the biosynthesis process.     

Citric acid production from sucrose by recombinant Yarrowia lipolytica using semicontinuous fermentation

The genetically modified yeast strain Yarrowia lipolytica H222‐S4(p67ICL1)T5 is able to utilize sucrose as a carbon source and to produce citric and isocitric acids in a more advantageous ratio as compared to its wild‐type equivalent. In this study, the effect of pH of the fermentation broth (pH 6.0 and 7.0) and proteose‐peptone addition on citric acid production by the recombinant yeast strain were investigated. It was found that the highest citric acid production occurred at pH 7.0 without any addition of proteose‐peptone. Furthermore, two process strategies (fed‐batch and repeated fed‐batch) were tested for their applicability for use in citric acid production from sucrose by Y. lipolytica. Repeated fed‐batch cultivation was found to be the most effective process strategy: in 3 days of cycle duration, approximately 80 g/L citric acid was produced, the yield was at least 0.57 g/g and the productivity was as much as 1.1 g/Lh. The selectivity of the bioprocess for citric acid was always higher than 90% from the very beginning of the fermentation due to the genetic modification, reaching values of up to 96.4% after 5 days of cycle duration.     

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.     

Genome-scale model-driven strain design for dicarboxylic acid production in <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

Background

Recently, there have been several attempts to produce long-chain dicarboxylic acids (DCAs) in various microbial hosts. Of these, Yarrowia lipolytica has great potential due to its oleaginous characteristics and unique ability to utilize hydrophobic substrates. However, Y. lipolytica should be further engineered to make it more competitive: the current approaches are mostly intuitive and cumbersome, thus limiting its industrial application.

Results

In this study, we proposed model-guided metabolic engineering strategies for enhanced production of DCAs in Y. lipolytica. At the outset, we reconstructed genome-scale metabolic model (GSMM) of Y. lipolytica (iYLI647) by substantially expanding the previous models. Subsequently, the model was validated using three sets of published culture experiment data. It was finally exploited to identify genetic engineering targets for overexpression, knockout, and cofactor modification by applying several in silico strain design methods, which potentially give rise to high yield production of the industrially relevant long-chain DCAs, e.g., dodecanedioic acid (DDDA). The resultant targets include (1) malate dehydrogenase and malic enzyme genes and (2) glutamate dehydrogenase gene, in silico overexpression of which generated additional NADPH required for fatty acid synthesis, leading to the increased DDDA fluxes by 48% and 22% higher, respectively, compared to wild-type. We further investigated the effect of supplying branched-chain amino acids on the acetyl-CoA turn-over rate which is key metabolite for fatty acid synthesis, suggesting their significance for production of DDDA in Y. lipolytica.

Conclusion

In silico model-based strain design strategies allowed us to identify several metabolic engineering targets for overproducing DCAs in lipid accumulating yeast, Y. lipolytica. Thus, the current study can provide a methodological framework that is applicable to other oleaginous yeasts for value-added biochemical production.

     

Mutant <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> strains producing citric acid from glucose

The possibility of obtaining mutant yeasts Yarrowia lipolytica VKM Y-2373 with increased ability to synthesize citric acid from glucose by using UV irradiation and N-methyl-N’-nitro-N-nitrosoguanidine was studied. Of 1500 colonies of the Y. lipolytica treated with either UV or N-methyl-N’-nitro-N-nitrosoguanidine, three mutants were selected that displayed higher (by 23%) biosynthetic ability as compared with the initial strain. Additionally, three mutants were selected from 1000 colonies of the Y. lipolytica exposed to a combined action of UV and N-methyl-N’-nitro-N-nitrosoguanidine; their biosynthetic activity exceeded that of the initial strain by 43.9%. The selective media with citrate and acetate were developed for a rapid selection of mutants as well as the express methods for the detection of active citric acid producers on the solid media with chalk and bromocresol containing a limiting concentration of amine nitrogen and an excess of glucose.     

Regulation of the central metabolism in relation to citric acid production in Saccharomycopsis lipolytica

The mechanism of the massive extracellular production of citric and isocitric acids by Saccharomycopsis lipolytica grown on n-paraffins has been studied. When growth stops, because of nitrogen limitation, the intracellular concentration of ATP sharply rises whereas that of AMP and ADP decreases to a low level. At the same time production of acids begins. The activity of the NAD-dependent isocitrate dehydrogenase which requires AMP for activity becomes very low and prevents the oxidative function of the citric acid cycle whereas isocitrate lyase is not inhibited. As citrate synthase inhibition by ATP appears to be insufficient to stop n-paraffin degradation, citric and isocitric acids accumulation can take place. Massive excretion of these acids, however, probably still involves other physiological changes brought about by nitrogen limitation, possibly some permeabilization of the cell to these acids.This work is a part of a Doctorat de Spécialité Thesis submitted by R. Marchal to the University of Nancy (1975)     

Inactivation of the transcription factor <Emphasis Type="Italic">mig1</Emphasis> (<Emphasis Type="Italic">YGL035C</Emphasis>) in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> improves tolerance towards monocarboxylic weak acids: acetic,formic and levulinic acid

Toxic concentrations of monocarboxylic weak acids present in lignocellulosic hydrolyzates affect cell integrity and fermentative performance of Saccharomyces cerevisiae. In this work, we report the deletion of the general catabolite repressor Mig1p as a strategy to improve the tolerance of S. cerevisiae towards inhibitory concentrations of acetic, formic or levulinic acid. In contrast with the wt yeast, where the growth and ethanol production were ceased in presence of acetic acid 5 g/L or formic acid 1.75 g/L (initial pH not adjusted), the m9 strain (Δmig1::kan) produced 4.06?±?0.14 and 3.87?±?0.06 g/L of ethanol, respectively. Also, m9 strain tolerated a higher concentration of 12.5 g/L acetic acid (initial pH adjusted to 4.5) without affecting its fermentative performance. Moreover, m9 strain produced 33% less acetic acid and 50–70% less glycerol in presence of weak acids, and consumed acetate and formate as carbon sources under aerobic conditions. Our results show that the deletion of Mig1p provides a single gene deletion target for improving the acid tolerance of yeast strains significantly.     

<Emphasis Type="Italic">Alkaliphilus peptidofermentans</Emphasis> sp. nov., a new alkaliphilic bacterial soda lake isolate capable of peptide fermentation and Fe(III) reduction

A novel strain, Z-7036, of anaerobic spore-forming bacteria was isolated from a cellulolytic consortium obtained from the bottom sediments of the low-mineralization soda lake Verkhnee Beloe (Buryatia). The cells of the new strain are short motile gram-positive rods, 1.1–3.0 × 0.25–0.4 μm. The organism is an aerotolerant anaerobe and obligate alkaliphile growing within the pH range of 7.5–9.7 with an optimum at pH 9.1. The strain is mesophilic and halotolerant and grows at NaCl concentrations from 0 to 50 g/l with an optimum at 20 g/l. Carbonates are required. The microorganism ferments peptone, yeast extract, trypticase, tryptone, Bacto Soytone, meat extract, Casamino acids, ornithine, arginine, threonine, and tryptophan. The strain hydrolyzes the bacterial preparations “Gaprin” and “Spirulina”. Acetate and formate are the major fermentation products. The strain reduces amorphous ferric hydroxide (AFH), EDTA-Fe(III), anthraquinone-2,6-disulfonate (quinone), S₂O ₃ ^2? , fumarate, and crotonate. Major fatty acids are C_16:0, C1_6:1ω7c, iso-C₁₇, iso-C₁₅, and iso-C_17:1. The DNA G+C content is 33.8 ± 0.5 mol %. According to the results of the 16S rRNA gene analysis, strain Z-7036 belongs to the genus Alkaliphilus within the cluster XI of low G+C gram-positive bacteria of the family Clostridiaceae. The novel strain is closely related to A. transvaalensis SAGM1^T and A. crotonatoxidans B11-2^T (93.3 and 93.9% 16S rRNA sequence identities, respectively). On the basis of the existing genotypic and phenotypic differences, we propose that strain Z-7036 should be classified as a novel species Alkaliphilus peptidofermentans sp. nov.     

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.     

Very high gravity ethanol and fatty acid production of <Emphasis Type="Italic">Zymomonas mobilis</Emphasis> without amino acid and vitamin

Very high gravity (VHG) fermentation is the mainstream technology in ethanol industry, which requires the strains be resistant to multiple stresses such as high glucose concentration, high ethanol concentration, high temperature and harsh acidic conditions. To our knowledge, it was not reported previously that any ethanol-producing microbe showed a high performance in VHG fermentations without amino acid and vitamin. Here we demonstrate the engineering of a xylose utilizing recombinant Zymomonas mobilis for VHG ethanol fermentations. The recombinant strain can produce ethanol up to 136 g/L without amino acid and vitamin with a theoretical yield of 90 %, which is significantly superior to that produced by all the reported ethanol-producing strains. The intracellular fatty acids of the bacterial were about 16 % of the bacterial dry biomass, with the ratio of ethanol:fatty acids was about 273:1 (g/g). The recombinant strain was achieved by a multivariate-modular strategy tackles with the multiple stresses which are closely linked to the ethanol productivity of Z. mobilis. The over-expression of metB/yfdZ operon enabled the growth of the recombinant Z. mobilis in a chemically defined medium without amino acid and vitamin; and the fatty acids overproduction significantly increased ethanol tolerance and ethanol production. The coupled production of ethanol with fatty acids of the Z. mobilis without amino acid and vitamin under VHG fermentation conditions may permit a significant reduction of the production cost of ethanol and microbial fatty acids.     

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.     

Production of <Emphasis Type="Italic">cis</Emphasis>-Vaccenic Acid-oriented Unsaturated Fatty Acid in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Biodiesel is produced worldwide as an alternative energy fuel and substitute for petroleum. Biodiesel is often obtained from vegetable oil, but production of biodiesel from plants requires additional land for growing crops and can affect the global food supply. Consequently, it is necessary to develop appropriate microorganisms for the development of an alternative biodiesel feedstock. Escherichia coli is suitable for the production of biodiesel feedstocks since it can synthesize fatty acids for lipid production, grows well, and is amenable to genetic engineering. Recombinant E. coli was designed and constructed for the production of biodiesel with improved unsaturated fatty acid contents via regulation of the FAS pathway consisting of initiation, elongation, and termination steps. Here, we investigated the effects of fabA, fabB, and fabF gene expression on the production of unsaturated fatty acids and observed that the concentration of cis-vaccenic acid, a major component of unsaturated fatty acids, increased 1.77-fold compared to that of the control strain. We also introduced the genes which synthesize malonyl-ACP used during initiation step of fatty acid synthesis and the genes which produce free fatty acids during termination step to study the effect of combination of genes in elongation step and other steps. The total fatty acid content of this strain increased by 35.7% compared to that of the control strain. The amounts of unsaturated fatty acids and cis-vaccenic acid increased by 3.27 and 3.37-fold, respectively.     

Engineering <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> for poly-3-hydroxybutyrate production

Strains of Yarrowia lipolytica were engineered to express the poly-3-hydroxybutyrate (PHB) biosynthetic pathway. The genes for β-ketothiolase, NADPH-dependent acetoacetyl-CoA reductase, and PHB synthase were cloned and inserted into the chromosome of Y. lipolytica. In shake flasks, the engineered strain accumulated PHB to 1.50 and 3.84% of cell dry weight in complex medium supplemented with glucose and acetate as carbon source, respectively. In fed-batch fermentation using acetate as sole carbon source, 7.35 g/l PHB (10.2% of cell dry weight) was produced. Selection of Y. lipolytica as host for PHB synthesis was motivated by the fact that this organism is a good lipids producer, which suggests robust acetyl-CoA supply also the precursor of the PHB pathway. Acetic acid could be supplied by gas fermentation, anaerobic digestion, and other low-cost supply route.