Efficient production of S-adenosyl-l-methionine from dl-methionine in metabolic engineered Saccharomyces cerevisiae

S-Adenosyl-l -methionine (SAM) is an important small molecule compound widely used in treating various diseases. Although l -methionine is generally used, the low-cost dl -methionine is more suitable as the substrate for industrial production of SAM. However, d -methionine is inefficient for SAM formation due to the substrate-specificity of SAM synthetase. In order to increase the utilization efficiency of dl -methionine, intracellular conversion of d -methionine to l -methionine was investigated in the type strain Saccharomyces cerevisiae BY4741 and an industrial strain S. cerevisiae HDL. Firstly, via disruption of HPA3 encoding d -amino acid-N-acetyltransferase, d -methionine was accumulated in vivo and no N-acetyl-d -methionine production was observed. Further, codon-optimized d -amino acid oxidase (DAAO) gene from Trigonopsis variabilis (Genbank MK280686) and l -phenylalanine dehydrogenase gene (l -PheDH) from Rhodococcus jostii (Genbank MK280687) were introduced to convert d -methionine to l -methionine, SAM concentration and content was increased by 110% and 72.1% in BY4741 (plasmid borne) and increased by 38.2% and 34.1% in HDL (genome integrated), by feeding 0.5 g/L d -methionine. Using the recently developed CRISPR tools, the DAAO and l -PheDH expression cassettes were integrated into the HPA3 and SAH1 loci while SAM2 expression was integrated into the SPE2 and GLC3 loci of HDL, and the resultant strain HDL-R2 accumulated 289% and 192% more SAM concentration and content, respectively, by feeding 0.5 g/L dl -methionine. Further, in a 10 L fed-batch fermentation process, 10.3 g/L SAM were accumulated with the SAM content of 242 mg/g dry cell weight by feeding 16 g/L dl -methionine. The strategies used here provided a promising approach to enhance SAM production using low-cost dl -methionine.     

Enhanced arsenate uptake in Saccharomyces cerevisiae overexpressing the Pho84 phosphate transporter

Arsenate is a major toxic constituent in arsenic-contaminated water supplies. Saccharomyces cerevisiae was engineered as a potential biosorbent for enhanced arsenate accumulation. The phosphate transporter, Pho84p, known to import arsenate, was overexpressed using a 2μ-based vector carrying PHO84 under the control of the late-phase ADH2 promoter. Arsenate uptake was then evaluated using a resting cell system. In buffer solutions containing high arsenate concentrations (12,000 and 30,000 ppb), the engineered strains internalized up to 750 μg of arsenate per gram of cells, a 50% improvement over control strains. Increasing the cell mass 2.5-fold yielded a proportional increase in the volumetric arsenate uptake, while maintaining the same level of specific uptake. At high levels of arsenate, loss from the intact cells to the medium was observed with time; knockouts of two known arsenic extrusion genes, ACR3 and FPS1, did not prevent this loss. At trace level concentrations (120 ppb), rapid and total arsenate removal was observed. The presence of 50 μM phosphate reduced uptake by approximately 15% in buffer containing 80 μM (6,000 ppb) arsenate. At trace levels of arsenate (70 ppb), the phosphate reduced the initial rate of uptake, but not the total amount removed. PHO84 mRNA levels were nearly 30 times higher in the engineered strains relative to the control strains. Uptake may no longer be a limiting factor in the engineered system and further increases should be possible by upregulating the downstream reduction and sequestration pathways.     

酿酒酵母产油脂条件的优化

微生物细胞通常仅含2%3%油脂,但少数微生物含油脂率却可达70%以上,所以高含油脂量使微生物油脂实际开发成为可能。目前用于生产多不饱和脂肪酸的微生物主要为藻类和真菌。尽管微生物油脂是当前的研究热点,已经引起广大研究者的重视,但目前国内外研究大都集中在含油脂量在干重20%以上的微生物,如浅白色隐性酵母、粘红酵母等,而对于酿酒酵母来说,则很少见到研究其产油脂的相关报道。     

Methionine catabolism in Saccharomyces cerevisiae

The catabolism of methionine to methionol and methanethiol in Saccharomyces cerevisiae was studied using (13)C NMR spectroscopy, GC-MS, enzyme assays and a number of mutants. Methionine is first transaminated to alpha-keto-gamma-(methylthio)butyrate. Methionol is formed by a decarboxylation reaction, which yields methional, followed by reduction. The decarboxylation is effected specifically by Ydr380wp. Methanethiol is formed from both methionine and alpha-keto-gamma-(methylthio)butyrate by a demethiolase activity. In all except one strain examined, demethiolase was induced by the presence of methionine in the growth medium. This pathway results in the production of alpha-ketobutyrate, a carbon skeleton, which can be re-utilized. Hence, methionine catabolism is more complex and economical than the other amino acid catabolic pathways in yeast, which use the Ehrlich pathway and result solely in the formation of a fusel alcohol.     

Ethanol production by Saccharomyces cerevisiae in biofilm reactors

Biofilms are natural forms of cell immobilization in which microorganisms attach to solid supports. At ISU, we have developed plastic composite-supports (PCS) (agricultural material (soybean hulls or oat hulls), complex nutrients, and polypropylene) which stimulate biofilm formation and which supply nutrients to the attached microorganisms. Various PCS blends were initially evaluated in repeated-batch culture-tube fermentation with Saccharomyces cerevisiae (ATCC 24859) in low organic nitrogen medium. The selected PCS (40% soybean hull, 5% soybean flour, 5% yeast extract-salt and 50% polypropylene) was then used in continuous and repeated-batch fermentation in various media containing lowered nitrogen content with selected PCS. During continuous fermentation, S. cerevisiae demonstrated two to 10 times higher ethanol production in PCS bioreactors than polypropylene-alone support (PPS) control. S. cerevisiae produced 30 g L⁻¹ ethanol on PCS with ammonium sulfate medium in repeated batch fermentation, whereas PPS-control produced 5 g L⁻¹ ethanol. Overall, increased productivity in low cost medium can be achieved beyond conventional fermentations using this novel bioreactor design. Received 20 May 1997/ Accepted in revised form 29 August 1997     

Genome-scale analysis of Saccharomyces cerevisiae metabolism and ethanol production in fed-batch culture

A dynamic flux balance model based on a genome-scale metabolic network reconstruction is developed for in silico analysis of Saccharomyces cerevisiae metabolism and ethanol production in fed-batch culture. Metabolic engineering strategies previously identified for their enhanced steady-state biomass and/or ethanol yields are evaluated for fed-batch performance in glucose and glucose/xylose media. Dynamic analysis is shown to provide a single quantitative measure of fed-batch ethanol productivity that explicitly handles the possible tradeoff between the biomass and ethanol yields. Productivity optimization conducted to rank achievable fed-batch performance demonstrates that the genetic manipulation strategy and the fed-batch operating policy should be considered simultaneously. A library of candidate gene insertions is assembled and directly screened for their achievable ethanol productivity in fed-batch culture. A number of novel gene insertions with ethanol productivities identical to the best metabolic engineering strategies reported in previous studies are identified, thereby providing additional targets for experimental evaluation. The top performing gene insertions were substrate dependent, with the highest ranked insertions for glucose media yielding suboptimal performance in glucose/xylose media. The analysis results suggest that enhancements in biomass yield are most beneficial for the enhancement of fed-batch ethanol productivity by recombinant xylose utilizing yeast strains. We conclude that steady-state flux balance analysis is not sufficient to predict fed-batch performance and that the media, genetic manipulations, and fed-batch operating policy should be considered simultaneously to achieve optimal metabolite productivity.     

Acetoin production in Saccharomyces cerevisiae wine yeasts

Abstract One hundred strains of Saccharomyces cerevisiae were examined for the capacity to produce acetoin in synthetic medium and in grape must. The low production of acetoin was found to be the more common pattern in this species. Most strains exhibited a similar distribution in both media, production ranging from non-detectable amounts to 12 mg 1⁻¹. Only four strains produced high quantities of acetoin, up to 29.5 mg l⁻¹ in synthetic medium and up to 194.6 mg l⁻¹ in grape must. This biometric study showed the existence of two phenotypes, "low and high acetoin production", that could be selected for conferring a desirable flavour of the final product.     

Rapid identification and differentiation of Saccharomyces cerevisiae, Saccharomyces bayanus and their hybrids by multiplex PCR

AIMS: To develop a multiplex PCR assay for the specific identification and differentiation of Saccharomyces cerevisiae, S. bayanus and their hybrids. METHODS AND RESULTS: Two sets of primers with sequences complementary to the region YBR033w were used. A single amplicon of 1710 bp or 329 bp was obtained with species S. cerevisiae and S. bayanus, respectively, while the presence of both bands was observed in S. pastorianus because of its hybrid nature. Both amplification products were also obtained after amplification from DNA of several laboratory S. cerevisiae x S. bayanus hybrid strains. CONCLUSIONS: Multiplex PCR was optimized for the rapid and reliable identification of S. cerevisiae, S. bayanus and their hybrids. SIGNIFICANCE AND IMPACT OF THE STUDY: The procedure may be used for routine detection of the most common Saccharomyces sensu stricto yeasts involved in industrial fermentation processes, overcoming the problems of conventional techniques.     

Acetaldehyde production in Saccharomyces cerevisiae wine yeasts

Abstract Eighty-six strains of Saccharomyces cerevisiae were investigated for their ability to produce acetaldehyde in synthetic medium and in grape must. Acetaldehyde production did not differ significantly between the two media, ranging from a few mg/l to about 60 mg/l, and was found to be a strain characteristic. The fermentation temperature of 30°C considerably increased the acetaldehyde produced. This study allowed us to assign the strains to different phenotypes: low, medium and high acetaldehyde producers. The low and high phenotypes differed considerably also in the production of acetic acid, acetoin and higher alcohols and can be useful for studying acetaldehyde production in S. cerevisiae , both from the technological and genetic point of view.     

Enhanced butanol production by eukaryotic Saccharomyces cerevisiae engineered to contain an improved pathway

Compared with ethanol, butanol has more advantageous physical properties as a fuel, and biobutanol is thus considered a promising biofuel material. Biobutanol has often been produced by Clostridium species; however, because they are strictly anaerobic microorganisms, these species are challenging to work with. We attempted to introduce the butanol production pathway into yeast Saccharomyces cerevisiae, which is a well-known microorganism that is tolerant to organic solvents. 1-Butanol was found to be produced at very low levels when the butanol production pathway of Clostridium acetobutylicum was simply introduced into S. cerevisiae. The elimination of glycerol production pathway in the yeast contributed to the enhancement of 1-butanol production. In addition, by the use of trans-enoyl-CoA reductase in the engineered pathway, 1-butanol production was markedly enhanced to yield 14.1 mg/L after 48 h of cultivation.     

补料方式对酵母菌生产谷胱甘肽的影响

比较了酵母菌发酵生产谷胱甘肽（GSH）的几种补料分批培养方式。实验发现补料可以明显地促进酵母菌的生长和谷胱甘肽的合成,同时还发现不同的补料方式对发酵液中的菌体浓度和GSH浓度有不同的影响。采用指数流加方式可获得极高的菌体浓度,但菌体中的GSH浓度较低;而采用恒－pH补料分批培养既可以达到较高菌体浓度,菌体中又含有较高的GSH含量,因此,其总的GSH产量最高,可达到977.8mg/L。     

Ethanol production from nonsterilized carob pod extract by free and immobilized Saccharomyces cerevisiae cells using fed-batch culture

The production of ethanol from carob pod extract by free and immobilized Saccharomyces cerevisiae cells in batch and fed-batch culture was investigated. Fed-batch culture proved to be a better fermentation system for the production of ethanol than batch culture. In fed-batch culture, both free and immobilized S. cerevisiae cells gave the same maximum concentration (62 g/L) of final ethanol at an initial sugar concentration of 300 g/L and F = 167 mL/h. The maximum ethanol productivity (4.4 g/L h) was obtained with both free and immobilized cells at a substrate concentration of 300 g/L and F = 334 mL/h. In repeated fed-batch culture, immobilized S. cerevisiae cells gave a higher overall ethanol concentration compared with the free cells. The immobilized S. cerevisiae cells in Ca-alginate beads retained their ability to produce ethanol for 10 days. (c) 1994 John Wiley & Sons, Inc.     

Maximum glucoamylase production by a temperature-sensitive mutant of Saccharomyces cerevisiae in batch culture

In order to maximize the glucoamylase production by recombinant Saccharomyces cerevisiae in batch culture, first a temperature-controlled expression system for a foreign gene in S. cerevisiae was constructed. A temperature-sensitive pho80 mutant of S. cerevisiae for the PHO regulatory system, YKU131, was used for this purpose. A DNA fragment bearing the promoter of the PHO84 gene, which encodes an inorganic phosphate (P_i) transporter of S. cerevisiae and is derepressed by P_i starvation, was used as promoter. The glucoamylase gene connected with the PHO84 promoter was ligated into a YEp13 vector, designated pKU122. When the temperature-sensitive pho80 ^ts mutant harboring the plasmid pKU122 is cultivated at a lower temperature, the expression of glucoamylase gene is repressed, but at a higher temperature it is expressed. Next the effect of temperature on the specific growth rate, μ, and specific production rate, ρ, was investigated. Maximum values of ρ and ρ at various temperatures were at 30°C and 34°C, respectively. The optimal cultivation temperature strategy for maximum production of glucoamylase by this recombinant strain in batch culture was then determined by the Maximum principle using the relationships of μ and ρ to the cultivation temperature. Finally, the optimal strategy was experimentally realized by changing the cultivation temperature from Tμ (30°C) to Tρ (34°C) at the switching time, t_s. Received 18 September 1997/ Accepted in revised form 07 January 1998     

Fermentative production of L-glycerol 3-phosphate utilizing a Saccharomyces cerevisiae strain with an engineered glycerol biosynthetic pathway

Interest in L-glycerol 3-phosphate (L-G3P) production via microbial fermentation is due to the compound's potential to replace the unstable substrate dihydroxyacetone phosphate (DHAP) in one-pot enzymatic carbohydrate syntheses. A Saccharomyces cerevisiae strain with deletions in both genes encoding specific L-G3Pases (GPP1 and GPP2) and multicopy overexpression of L-glycerol 3-phosphate dehydrogenase (GPD1) was studied via small-scale (100 mL) batch fermentations under quasi-anaerobic conditions. Intracellular accumulation of L-G3P reached extremely high levels (roughly 200 mM) but thereafter declined. Extracellular L-G3P was also detected and its concentration continuously increased throughout the fermentation, such that most of the total L-G3P was found outside the cells as fermentation concluded. Moreover, in spite of the complete elimination of specific L-G3Pase activity, the strain showed considerable glycerol formation suggesting unspecific dephosphorylation as a mechanism to relieve cells of intracellular L-G3P accumulation. Up-scaling the process employed fed-batch fermentation with repeated glucose feeding, plus an aerobic growth phase followed by an anaerobic product accumulation phase. This produced a final product titer of about 325 mg total L-G3P per liter of fermentation broth.