Rapid identification of target genes for 3-methyl-1-butanol production in Saccharomyces cerevisiae

Extracellular conditions determine the taste of fermented foods by affecting metabolite formation by the micro-organisms involved. To identify targets for improvement of metabolite formation in food fermentation processes, automated high-throughput screening and cDNA microarray approaches were applied. Saccharomyces cerevisiae was cultivated in 96-well microtiter plates, and the effects of salt concentration and pH on the growth and synthesis of the fusel alcohol-flavoured substance, 3-methyl-1-butanol, was evaluated. Optimal fermentation conditions for 3-methyl-1-butanol concentration were found at pH 3.0 and 0% NaCl. To identify genes encoding enzymes with major influence on product formation, a genome-wide gene expression analysis was carried out with S. cerevisiae cells grown at pH 3.0 (optimal for 3-methyl-1-butanol formation) and pH 5.0 (yeast cultivated under standard conditions). A subset of 747 genes was significantly induced or repressed when the pH was changed from pH 5.0 to 3.0. Expression of seven genes related to the 3-methyl-1-butanol pathway, i.e. LAT1, PDX1, THI3, ALD4, ILV3, ILV5 and LEU4, strongly changed in response to this switch in pH of the growth medium. In addition, genes involved in NAD metabolism, i.e. BNA2, BNA3, BNA4 and BNA6, or those involved in the TCA cycle and glutamate metabolism, i.e. MEU1, CIT1, CIT2, KDG1 and KDG2, displayed significant changes in expression. The results indicate that this is a rapid and valuable approach for identification of interesting target genes for improvement of yeast strains used in industrial processes.     

代谢工程改造酿酒酵母合成肌醇

【目的】肌醇别名环己六醇,是一种具有生物活性的糖醇,在医药、食品和饲料等领域具有重要的应用价值。为获得生产肌醇的微生物细胞工厂,通过代谢工程改造,构建生产肌醇的酿酒酵母工程菌株。【方法】对酿酒酵母肌醇合成途径的正负调控同时改造,过表达肌醇-3-磷酸合成酶基因ino1,敲除肌醇生物合成的转录抑制子基因opi1和抗性基因kan MX,获得重组菌。利用气相色谱法检测重组菌发酵液中肌醇含量。【结果】构建了生物安全性的产肌醇基因工程菌株,摇瓶培养产量为1.021 g/L。【结论】通过过表达ino1和敲除opi1来改造酿酒酵母,能够有效提高重组菌的肌醇产量,为下一步的微生物发酵法产肌醇的工业应用奠定基础。     

Metabolic engineering of Escherichia coli for 1-butanol production

Compared to ethanol, butanol offers many advantages as a substitute for gasoline because of higher energy content and higher hydrophobicity. Typically, 1-butanol is produced by Clostridium in a mixed-product fermentation. To facilitate strain improvement for specificity and productivity, we engineered a synthetic pathway in Escherichia coli and demonstrated the production of 1-butanol from this non-native user-friendly host. Alternative genes and competing pathway deletions were evaluated for 1-butanol production. Results show promise for using E. coli for 1-butanol production.     

Metabolic engineering of Saccharomyces cerevisiae for production of ginsenosides

Ginsenosides are the primary bioactive components of ginseng, which is a popular medicinal herb and exhibits diverse pharmacological activities. Protopanaxadiol is the aglycon of several dammarane-type ginsenosides, which also has anticancer activity. For microbial production of protopanaxadiol, dammarenediol-II synthase and protopanaxadiol synthase genes of Panax ginseng, together with a NADPH-cytochrome P450 reductase gene of Arabidopsis thaliana, were introduced into Saccharomyces cerevisiae, resulting in production of 0.05 mg/g DCW protopanaxadiol. Increasing squalene and 2,3-oxidosqualene supplies through overexpressing truncated 3-hydroxyl-3-methylglutaryl-CoA reductase, farnesyl diphosphate synthase, squalene synthase and 2,3-oxidosqualene synthase genes, together with increasing protopanaxadiol synthase activity through codon optimization, led to 262-fold increase of protopanaxadiol production. Finally, using two-phase extractive fermentation resulted in production of 8.40 mg/g DCW protopanaxadiol (1189 mg/L), together with 10.94 mg/g DCW dammarenediol-II (1548 mg/L). The yeast strains engineered in this work can serve as the basis for creating an alternative way for production of ginsenosides in place of extraction from plant sources.     

Metabolic engineering of Saccharomyces cerevisiae for the production of n-butanol

Background

The thermotolerant methylotrophic yeast Hansenula polymorpha is capable of alcoholic fermentation of xylose at elevated temperatures (45 – 48°C). Such property of this yeast defines it as a good candidate for the development of an efficient process for simultaneous saccharification and fermentation. However, to be economically viable, the main characteristics of xylose fermentation of H. polymorpha have to be improved.

Results

Site-specific mutagenesis of H. polymorpha XYL1 gene encoding xylose reductase was carried out to decrease affinity of this enzyme toward NADPH. The modified version of XYL1 gene under control of the strong constitutive HpGAP promoter was overexpressed on a Δxyl1 background. This resulted in significant increase in the K_M for NADPH in the mutated xylose reductase (K341 → R N343 → D), while K_M for NADH remained nearly unchanged. The recombinant H. polymorpha strain overexpressing the mutated enzyme together with native xylitol dehydrogenase and xylulokinase on Δxyl1 background was constructed. Xylose consumption, ethanol and xylitol production by the constructed strain were determined for high-temperature xylose fermentation at 48°C. A significant increase in ethanol productivity (up to 7.3 times) was shown in this recombinant strain as compared with the wild type strain. Moreover, the xylitol production by the recombinant strain was reduced considerably to 0.9 mg × (L × h)^-1 as compared to 4.2 mg × (L × h)^-1 for the wild type strain.

Conclusion

Recombinant strains of H. polymorpha engineered for improved xylose utilization are described in the present work. These strains show a significant increase in ethanol productivity with simultaneous reduction in the production of xylitol during high-temperature xylose fermentation.     

Metabolic engineering of Saccharomyces cerevisiae for itaconic acid production

Renewable alternatives for petroleum-derived chemicals are achievable through biosynthetic production. Here, we utilize Saccharomyces cerevisiae to enable the synthesis of itaconic acid, a molecule with diverse applications as a petrochemical replacement. We first optimize pathway expression within S. cerevisiae through the use of a hybrid promoter. Next, we utilize sequential, in silico computational genome-scanning to identify beneficial genetic perturbations that are metabolically distant from the itaconic acid synthesis pathway. In this manner, we successfully identify three non-obvious genetic targets (?ade3 ?bna2 ?tes1) that successively improve itaconic acid titer. We establish that focused manipulations of upstream pathway enzymes (localized refactoring) and enzyme re-localization to both mitochondria and cytosol fail to improve itaconic acid titers. Finally, we establish a higher cell density fermentation that ultimately achieves itaconic acid titer of 168 mg/L, a sevenfold improvement over initial conditions. This work represents an attempt to increase itaconic acid production in yeast and demonstrates the successful utilization of computationally guided genetic manipulation to increase metabolic capacity.     

Metabolic engineering of Saccharomyces cerevisiae for 2,3-butanediol production

Applied Microbiology and Biotechnology - Saccharomyces cerevisiae is a work horse for production of valuable biofuels and biochemicals including 2,3-butanediol (2,3-BDO), a platform chemical with...     

Metabolic engineering of Saccharomyces cerevisiae to improve 1-hexadecanol production

Fatty alcohols are important components of a vast array of surfactants, lubricants, detergents, pharmaceuticals and cosmetics. We have engineered Saccharomyces cerevisiae to produce 1-hexadecanol by expressing a fatty acyl-CoA reductase (FAR) from barn owl (Tyto alba). In order to improve fatty alcohol production, we have manipulated both the structural genes and the regulatory genes in yeast lipid metabolism. The acetyl-CoA carboxylase gene (ACC1) was over-expressed, which improved 1-hexadecanol production by 56% (from 45 mg/L to 71 mg/L). Knocking out the negative regulator of the INO1 gene in phospholipid metabolism, RPD3, further enhanced 1-hexadecanol production by 98% (from 71 mg/L to 140 mg/L). The cytosolic acetyl-CoA supply was next engineered by expressing a heterologous ATP-dependent citrate lyase, which increased the production of 1-hexadecanol by an additional 136% (from 140 mg/L to 330 mg/L). Through fed-batch fermentation using resting cells, over 1.1 g/L 1-hexadecanol can be produced in glucose minimal medium, which represents the highest titer reported in yeast to date.     

Metabolic engineering of glycerol production in Saccharomyces cerevisiae

Inactivation of TPI1, the Saccharomyces cerevisiae structural gene encoding triose phosphate isomerase, completely eliminates growth on glucose as the sole carbon source. In tpi1-null mutants, intracellular accumulation of dihydroxyacetone phosphate might be prevented if the cytosolic NADH generated in glycolysis by glyceraldehyde-3-phosphate dehydrogenase were quantitatively used to reduce dihydroxyacetone phosphate to glycerol. We hypothesize that the growth defect of tpi1-null mutants is caused by mitochondrial reoxidation of cytosolic NADH, thus rendering it unavailable for dihydroxyacetone-phosphate reduction. To test this hypothesis, a tpi1delta nde1delta nde2delta gut2delta quadruple mutant was constructed. NDE1 and NDE2 encode isoenzymes of mitochondrial external NADH dehydrogenase; GUT2 encodes a key enzyme of the glycerol-3-phosphate shuttle. It has recently been demonstrated that these two systems are primarily responsible for mitochondrial oxidation of cytosolic NADH in S. cerevisiae. Consistent with the hypothesis, the quadruple mutant grew on glucose as the sole carbon source. The growth on glucose, which was accompanied by glycerol production, was inhibited at high-glucose concentrations. This inhibition was attributed to glucose repression of respiratory enzymes as, in the quadruple mutant, respiratory pyruvate dissimilation is essential for ATP synthesis and growth. Serial transfer of the quadruple mutant on high-glucose media yielded a spontaneous mutant with much higher specific growth rates in high-glucose media (up to 0.10 h(-1) at 100 g of glucose. liter(-1)). In aerated batch cultures grown on 400 g of glucose. liter(-1), this engineered S. cerevisiae strain produced over 200 g of glycerol. liter(-1), corresponding to a molar yield of glycerol on glucose close to unity.     

Metabolic engineering of Saccharomyces cerevisiae for production of butanol isomers

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代谢工程改造酿酒酵母合成葡萄糖二酸

葡萄糖二酸是一种高附加值的有机酸,广泛用于食品、医药和化工领域。为获得生产葡萄糖二酸的微生物细胞工厂,通过共表达小鼠来源的肌醇加氧酶(MIOX)及恶臭假单胞菌来源的醛酸脱氢酶(Udh),在酿酒酵母Saccharomyces cerevisiae CEN.PK2-1C中构建了葡萄糖二酸合成途径,产量为(28.28±3.15)mg/L。在此基础上,通过调控前体肌醇的合成途径,发现肌醇-1-磷酸合成酶(INO1)是葡萄糖二酸合成途径的限速酶,过量表达INO1,葡萄糖二酸产量达到(107.51±10.87)mg/L,提高了2.8倍。进一步弱化竞争支路中磷酸果糖激酶(PFK1)的表达,最终葡萄糖二酸的产量达到(230.22±10.75)mg/L,为进一步获得高产葡萄糖二酸细胞工厂提供基础。     

Utilizing an endogenous pathway for 1-butanol production in Saccharomyces cerevisiae

Microbial production of higher alcohols from renewable feedstock has attracted intensive attention thanks to its potential as a source for next-generation gasoline substitutes. Here we report the discovery, characterization and engineering of an endogenous 1-butanol pathway in Saccharomyces cerevisiae. Upon introduction of a single gene deletion adh1Δ, S. cerevisiae was able to accumulate more than 120 mg/L 1-butanol from glucose in rich medium. Precursor feeding, ¹³C-isotope labeling and gene deletion experiments demonstrated that the endogenous 1-butanol production was dependent on catabolism of threonine in a manner similar to fusel alcohol production by the Ehrlich pathway. Specifically, the leucine biosynthesis pathway was engaged in the conversion of key 2-keto acid intermediates. Overexpression of the pathway enzymes and elimination of competing pathways achieved the highest reported 1-butanol titer in S. cerevisiae (242.8 mg/L).     

Metabolic engineering of cyanobacteria for 1-butanol production from carbon dioxide

Production of chemicals and fuels directly from CO(2) is an attractive approach to solving the energy and environmental problems. 1-Butanol, a chemical feedstock and potential fuel, has been produced by fermentation of carbohydrates, both in native Clostridium species and various engineered hosts. To produce 1-butanol from CO(2), we transferred a modified CoA-dependent 1-butanol production pathway into a cyanobacterium, Synechococcus elongatus PCC 7942. We demonstrated the activity of each enzyme in the pathway by chromosomal integration and expression of the genes. In particular, Treponema denticola trans-enoyl-CoA reductase (Ter), which utilizes NADH as the reducing power, was used for the reduction of crotonyl-CoA to butyryl-CoA instead of Clostridium acetobutylicum butyryl-CoA dehydrogenase to by-pass the need of Clostridial ferredoxins. Addition of polyhistidine-tag increased the overall activity of Ter and resulted in higher 1-butanol production. Removal of oxygen is an important factor in the synthesis of 1-butanol in this organism. This result represents the first autotrophic 1-butanol production.     

Metabolic engineering of muconic acid production in Saccharomyces cerevisiae

The dicarboxylic acid muconic acid has garnered significant interest due to its potential use as a platform chemical for the production of several valuable consumer bio-plastics including nylon-6,6 and polyurethane (via an adipic acid intermediate) and polyethylene terephthalate (PET) (via a terephthalic acid intermediate). Many process advantages (including lower pH levels) support the production of this molecule in yeast. Here, we present the first heterologous production of muconic acid in the yeast Saccharomyces cerevisiae. A three-step synthetic, composite pathway comprised of the enzymes dehydroshikimate dehydratase from Podospora anserina, protocatechuic acid decarboxylase from Enterobacter cloacae, and catechol 1,2-dioxygenase from Candida albicans was imported into yeast. Further genetic modifications guided by metabolic modeling and feedback inhibition mitigation were introduced to increase precursor availability. Specifically, the knockout of ARO3 and overexpression of a feedback-resistant mutant of aro4 reduced feedback inhibition in the shikimate pathway, and the zwf1 deletion and over-expression of TKL1 increased flux of necessary precursors into the pathway. Further balancing of the heterologous enzyme levels led to a final titer of nearly 141 mg/L muconic acid in a shake-flask culture, a value nearly 24-fold higher than the initial strain. Moreover, this strain has the highest titer and second highest yield of any reported shikimate and aromatic amino acid-based molecule in yeast in a simple batch condition. This work collectively demonstrates that yeast has the potential to be a platform for the bioproduction of muconic acid and suggests an area that is ripe for future metabolic engineering efforts.     

Metabolic engineering of Saccharomyces cerevisiae for the biotechnological production of succinic acid

The production of bio-based succinic acid is receiving great attention, and several predominantly prokaryotic organisms have been evaluated for this purpose. In this study we report on the suitability of the highly acid- and osmotolerant yeast Saccharomyces cerevisiae as a succinic acid production host. We implemented a metabolic engineering strategy for the oxidative production of succinic acid in yeast by deletion of the genes SDH1, SDH2, IDH1 and IDP1. The engineered strains harbor a TCA cycle that is completely interrupted after the intermediates isocitrate and succinate. The strains show no serious growth constraints on glucose. In glucose-grown shake flask cultures, the quadruple deletion strain Δsdh1Δsdh2Δidh1Δidp1 produces succinic acid at a titer of 3.62 g L^?1 (factor 4.8 compared to wild-type) at a yield of 0.11 mol (mol glucose)^?1. Succinic acid is not accumulated intracellularly. This makes the yeast S. cerevisiae a suitable and promising candidate for the biotechnological production of succinic acid on an industrial scale.     

Metabolic engineering of Saccharomyces cerevisiae for the production of triacetic acid lactone

Biobased chemicals have become attractive replacements for their fossil-fuel counterparts. Recent studies have shown triacetic acid lactone (TAL) to be a promising candidate, capable of undergoing chemical conversion to sorbic acid and other valuable intermediates. In this study, Saccharomyces cerevisiae was engineered for the high-level production of TAL by overexpression of the Gerbera hybrida 2-pyrone synthase (2-PS) and systematic engineering of the yeast metabolic pathways. Pathway analysis and a computational approach were employed to target increases in cofactor and precursor pools to improve TAL synthesis. The pathways engineered include those for energy storage and generation, pentose biosynthesis, gluconeogenesis, lipid biosynthesis and regulation, cofactor transport, and fermentative capacity. Seventeen genes were selected for disruption and independently screened for their effect on TAL production; combinations of knockouts were then evaluated. A combination of the pathway engineering and optimal culture parameters led to a 37-fold increase in titer to 2.2 g/L and a 50-fold increase in yield to 0.13 (g/g glucose). These values are the highest reported in the literature, and provide a 3-fold improvement in yield over previous reports using S. cerevisiae. Identification of these metabolic bottlenecks provides a strategy for overproduction of other acetyl-CoA-dependent products in yeast.     

酿酒酵母代谢工程技术

自20世纪90年代初期诞生以来,代谢工程历经了30年的快速发展。作为代谢工程的首选底盘细胞之一,酿酒酵母细胞工厂已被广泛应用于大量大宗化学品和新型高附加值生物活性物质的生物制造,在能源、医药和环境等领域取得了巨大的突破。近年来,合成生物学、生物信息学以及机器学习等相关技术也极大地促进了代谢工程的技术发展和应用。文中回顾了近30年来酿酒酵母代谢工程重要的技术发展,首先总结了经典代谢工程的常用方法和策略,以及在此基础上发展而来的系统代谢工程和合成生物学驱动的代谢工程技术。最后结合最新技术发展趋势,展望了未来酿酒酵母代谢工程发展的新方向。     

Metabolic engineering of Saccharomyces cerevisiae for production of novel lipid compounds

The yeast Saccharomyces cerevisiae has been modified successfully for production of numerous metabolites and therapeutic proteins through metabolic engineering, but has not been utilized to date for the production of lipid-derived compounds. We developed a lipid metabolic engineering strategy in S. cerevisiae based upon culturing techniques that are typically employed for studies of peroxisomal biogenesis; cells were grown in media containing fatty acids as a sole carbon source, which promotes peroxisomal proliferation and induction of enzymes associated with fatty acid beta-oxidation. Our results indicate that growth of yeast on fatty acids such as oleate results in extensive uptake of these fatty acids from the media and a subsequent increase in total cellular lipid content from 2% to 15% dry cell weight. We also show that co-expression of plant fatty acid desaturases 2 and 3 ( FAD2 and FAD3), using a fatty acid-inducible peroxisomal gene promoter, coupled the processes of fatty acid uptake with the induction of a new metabolic pathway leading from oleic acid (18:1) to linolenic acid (18:3). Finally, we show that cultivation of yeast cells in the presence of triacylglycerols and exogenously supplied lipase promotes extensive incorporation of triglyceride fatty acids into yeast cells. Collectively, these results provide a framework for bioconversion of low-cost oils into value-added lipid products.     

Metabolic engineering of Saccharomyces cerevisiae.

Comprehensive knowledge regarding Saccharomyces cerevisiae has accumulated over time, and today S. cerevisiae serves as a widley used biotechnological production organism as well as a eukaryotic model system. The high transformation efficiency, in addition to the availability of the complete yeast genome sequence, has facilitated genetic manipulation of this microorganism, and new approaches are constantly being taken to metabolicially engineer this organism in order to suit specific needs. In this paper, strategies and concepts for metabolic engineering are discussed and several examples based upon selected studies involving S. cerevisiae are reviewed. The many different studies of metabolic engineering using this organism illustrate all the categories of this multidisciplinary field: extension of substrate range, improvements of producitivity and yield, elimination of byproduct formation, improvement of process performance, improvements of cellular properties, and extension of product range including heterologous protein production.