Ethanol fermentation of beet molasses by a yeast resistant to distillery waste water and 2-deoxyglucose

A flocculent killer yeast, Saccharomyces cerevisiae strain H-1, which was selected for ethanol fermentation of beet molasses, has a tendency to lose its viability in distillery waste water (DWW) of beet molasses mash after ethanol fermentation. Through acclimations of strain H-1 in DWW, strain W-9, resistant to DWW, was isolated. Strain M-9, resistant to 2-deoxyglucose was further isolated through acclimations of strain W-9 in medium containing 150 ppm 2-deoxyglucose. A fermentation test of beet molasses indicated that the ethanol productivity and sugar consumption were improved by strain M-9 compared to the parental strain H-1 and strain W-9. The concentration of ethanol produced by strain M-9 was 107.2 g/l, and the concentration of residual sugars, which were mainly composed of sucrose and fructose, were lower than those produced by the parental strain H-1 and strain W-9 at the end of fermentation of beet molasses.     

絮凝基因FLO1及FLO1c高表达提高工业酿酒酵母乙酸耐受性及发酵性能

乙酸是生物质乙醇发酵过程中酵母细胞面临的重要抑制剂之一,对细胞生长及发酵性能有强烈的抑制作用。增强酵母菌对乙酸胁迫的耐受性对提高乙醇产率具有重要意义。用分别带有完整絮凝基因FLO1及其重复序列单元C发生缺失的衍生基因FLO1c的重组表达质粒分别转化非絮凝型工业酿酒酵母CE6,获得絮凝型重组酵母菌株6-AF1和6-AF1c。同时以空载体p YCPGA1转化CE6的菌株CE6-V为对照菌株。与CE6-V相比,絮凝酵母明显提高了对乙酸胁迫的耐受性。在0.6%(V/V)乙酸胁迫下,6-AF1和6-AF1c的乙醇产率分别为对照菌株CE6-V的1.56倍和1.62倍;在1.0%(V/V)乙酸胁迫下,6-AF1和6-AF1c的乙醇产率分别为对照菌株CE6-V的1.21倍和1.78倍。可见絮凝能力改造能明显提高工业酿酒酵母的乙酸胁迫耐受性及发酵性能,而且FLO1内重复序列单元C缺失具有更加明显的效果。     

Improvement of a Wine Saccharomyces cerevisiae Strain by a Breeding Program

Hybridization by spore conjugation was used to develop new and improved wine yeasts of Saccharomyces cerevisiae. The procedure was achieved with diploid, homothallic strains with high sporulation frequency and high spore viability. The method was verified by crossing flocculent and non-H₂S-forming strains. Single-spore descendants of the hybrids were studied by tetrad analysis with regard to the aforementioned characters and the other two winemaking traits, i.e., ethanol production and fermentation rate. A highly flocculent, non-H₂S-forming wine yeast strain with a high fermentation rate and high ethanol production was obtained.     

High-level ethanol production from starch by a flocculent <Emphasis Type="Italic">Saccharomyces cerevisiae </Emphasis>strain displaying cell-surface glucoamylase

A Strain of host yeast YF207, which is a tryptophan auxotroph and shows strong flocculation ability, was obtained from SaccharomYces diastaticus ATCC60712 and S. cerevisiae W303-1B by tetrad analysis. The plasmid pGA11, which is a multicopy plasmid for cell-surface expression of the Rhyzopus oryzae glucoamylase/alpha-agglutinin fusion protein, was then introduced into this flocculent yeast strain (YF207/pGA11). Yeast YF207/pGA11 grew rapidly under aerobic condition (dissolved oxygen 2.0 ppm), using soluble starch. The harvested cells were used for batch fermentation of soluble starch to ethanol under anaerobic condition and showed high ethanol production rates (0.71 g h(-1) l(-1)) without a time lag, because glucoamylase was immobilized on the yeast cell surface. During repeated utilization of cells for fermentation, YF207/pGA11 maintained high ethanol production rates over 300 h. Moreover, in fed-batch fermentation with YF207/pGA11 for approximately 120 h, the ethanol concentration reached up to 50 g l(-1). In conclusion, flocculent yeast cells displaying cell-surface glucoamylase are considered to be very effective for the direct fermentation of soluble starch to ethanol.     

无载体固定化酵母细胞木薯淀粉质原料酒精连续发酵研究

以木薯粉糖化液为发酵底物,在总发酵体积(有效)为15L的悬浮床生物反应器中,对一株粟酒裂殖酵母变异株进行一级和二级连续发酵研究。结果表明,二级连续发酵系统可明显改善一级系统的不足,并取得了平均流加糖液浓度150g/L,发酵强度为97g/L.h,流出液酒精浓度727g/L,残糖浓度374g./L,总糖利用率达90%的较好结果;整个系统在连续一个月的运行中从未发现染菌现象,发酵操作稳定。     

Engineering of a novel Saccharomyces cerevisiae wine strain with a respiratory phenotype at high external glucose concentrations

The recently described respiratory strain Saccharomyces cerevisiae KOY.TM6*P is, to our knowledge, the only reported strain of S. cerevisiae which completely redirects the flux of glucose from ethanol fermentation to respiration, even at high external glucose concentrations (27). In the KOY.TM6*P strain, portions of the genes encoding the predominant hexose transporter proteins, Hxt1 and Hxt7, were fused within the regions encoding transmembrane (TM) domain 6. The resulting chimeric gene, TM6*, encoded a chimera composed of the amino-terminal half of Hxt1 and the carboxy-terminal half of Hxt7. It was subsequently integrated into the genome of an hxt null strain. In this study, we have demonstrated the transferability of this respiratory phenotype to the V5 hxt1-7Delta strain, a derivative of a strain used in enology. We also show by using this mutant that it is not necessary to transform a complete hxt null strain with the TM6* construct to obtain a non-ethanol-producing phenotype. The resulting V5.TM6*P strain, obtained by transformation of the V5 hxt1-7Delta strain with the TM6* chimeric gene, produced only minor amounts of ethanol when cultured on external glucose concentrations as high as 5%. Despite the fact that glucose flux was reduced to 30% in the V5.TM6*P strain compared with that of its parental strain, the V5.TM6*P strain produced biomass at a specific rate as high as 85% that of the V5 wild-type strain. Even more relevant for the potential use of such a strain for the production of heterologous proteins and also of low-alcohol beverages is the observation that the biomass yield increased 50% with the mutant compared to its parental strain.     

Characterization of very high gravity ethanol fermentation of corn mash. Effect of glucoamylase dosage, pre-saccharification and yeast strain

Ethanol was produced from very high gravity mashes of dry milled corn (35% w/w total dry matter) under simultaneous saccharification and fermentation conditions. The effects of glucoamylase dosage, pre-saccharification and Saccharomyces cerevisiae strain on the growth characteristics such as the ethanol yield and volumetric and specific productivity were determined. It was shown that higher glucoamylase doses and/or pre-saccharification accelerated the simultaneous saccharification and fermentation process and increased the final ethanol concentration from 106 to 126 g/kg although the maximal specific growth rate was decreased. Ethanol production was not only growth related, as more than half of the total saccharides were consumed and more than half of the ethanol was produced during the stationary phase. Furthermore, a high stress tolerance of the applied yeast strain was found to be crucial for the outcome of the fermentation process, both with regard to residual saccharides and final ethanol concentration. The increased formation of cell mass when a well-suited strain was applied increased the final ethanol concentration, since a more complete fermentation was achieved.     

Stress effect of ethanol on fermentation kinetics by stationary-phase cells of Saccharomyces cerevisiae

When 4% (v/v) ethanol was added progressively to two strains exhibiting different fermentative abilities, K1 (a commercial wine strain) and V5 (a strain derived of a wine yeast), the fermentation rate correlated directly to the ethanol concentration for both strains. In contrast, the effect of sudden addition of 2%, 4% or 6% (v/v) ethanol was different depending on the strain. While the same effect was observed for K1 whatever the way of ethanol addition, V5 required an adaptation period after the shock addition of ethanol.     

Batch and continuous solid-phase fermentation of Jerusalem artichoke tubers

Two strains of Kluyveromyces marxianus were evaluated for their ability to ferment Jerusalem artichoke tuber pulp to ethanol under pH levels ranging from 2.0–6.3. Bacterial contamination was prevented in batch, solid-phase fermentation when pulp was initially adjusted to pH 3.5 or less, and maximal yeast populations occurred at pH 3.0–3.5. Fermentation times were also shortest for both yeast (13–18 h) and ethanol (48–64 h) production when pulp pH was in this range. However, ethanol yields (41–53% of theoretical) and fermentation efficiencies (68–78%) were somewhat lower than expected, with only 6.6–7.2% (v/v) ethanol produced by strain Y-1598 and 5.7–6.9% produced by strain Y-1550. Based on these parameters, the continuous solid-phase fermentor was operated for 396 h using strain Y-1598. The pH of pulp entering the fermentor was adjusted to 2.5 to compensate for partial neutralization by the mild steel of the fermentor. This resulted in fermenting pulp with a pH of 3.0–3.5, and therefore no contamination. Pulp exiting the fermentor after 72 h contained 6.9 × 10⁸ yeast cells/ml and 7.3% ethanol, which represented 55.9% of the theoretical yield and a fermentation efficiency of 73.3%. Further modifications (partial acid hydrolysis, finer grinding, etc.) should permit higher yields.     

Long-term repeated fed-batch ethanol fermentation in aerated condition

In this study, we attempted to assess the process stability of long-term fed-batch ethanol fermentation in the absence and presence of aeration (0.33 vvm). To examine the effect of aeration, a long-term repeated fed-batch operation was conducted for 396 h to mimic a long-term industrial bioethanol production process. In this long-term repeated fed-batch ethanol fermentation experiments, withdrawal-fill operation were conducted every 36 h for 10 repeat cycles. The whole operation was stably sustained in a quasi-steady state. The average maximal cell concentration and the average maximal ethanol production during operation were increased by 81.63 and 12.12%, respectively, when aeration was used. In addition, since aeration was carried out, the average ethanol yield slightly decreased by 4.03% and the average specific ethanol production rate decreased by 46.75% during operation. However, the average ethanol productivity increased by 17.53% when aeration was carried out. After 396 h of long-term repeated fed-batch ethanol fermentation, 1,908.9 g of ethanol was cumulatively produced when aeration was used, which was 12.47%, higher than when aeration was not used (1,697.2 g). Meanwhile, glycerol production was greatly decreased during long-term repeated fed-batch ethanol fermentation, in which the glycerol concentration in the culture broth decreased from about 34∼15 g/L. Thus, we can conclude that cell growth was greatly improved by overcoming ethanol inhibition and glycerol production was remarkably decreased when aeration was carried out, although aeration in ethanol fermentation decreased the specific ethanol production rate and ethanol yield.     

The effect of pH,temperature and sucrose concentration on high productivity continuous ethanol fermentation using Zymomonas mobilis

Summary A flocculent strain of Zymomonas mobilis was used for ethanol production from sucrose. Using a fermentor with cell recycle (internal and external settler) high sugar conversion and ethanol productivity were obtained. At a dilution rate of 0.5 h^-1 (giving 96% sugar conversion) the ethanol productivity, yield and concentrations respectively were 20 g/l/h, 0.45 g/g and 40 g/l using a medium containing 100 g/l sucrose. At a sucrose concentration of 150 g/l, the ethanol concentration reached 60 g/l. The ethanol yield was 80% theoretical due to levan and fructo-oligomer formation. No sorbitol was detected. This fermentation was conducted at a range of conditions from 30 to 36°C and from pH 4.0 to 5.5.     

Rapid and stable production of 2,3-butanediol by an engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strain in a continuous airlift bioreactor

Utilization of renewable feedstocks for the production of bio-based bulk chemicals, such as 2,3-butanediol (2,3-BDO), by engineered strains of the non-pathogenic yeast, Saccharomyces cerevisiae, has recently become an attractive option. In this study, to realize rapid production of 2,3-BDO, a flocculent, 2,3-BDO-producing S. cerevisiae strain YPH499/dPdAdG/BDN6-10/FLO1 was constructed from a previously developed 2,3-BDO-producing strain. Continuous 2,3-BDO fermentation was carried out by the flocculent strain in an airlift bioreactor. The strain consumed more than 90 g/L of glucose, which corresponded to 90% of the input, and stably produced more than 30 g/L of 2,3-BDO over 380 h. The maximum 2,3-BDO productivity was 7.64 g/L/h at a dilution rate of 0.200/h, which was higher than the values achieved by continuous fermentation using pathogenic bacteria in the previous reports. These results demonstrate that continuous 2,3-BDO fermentation with flocculent 2,3-BDO-producing S. cerevisiae is a promising strategy for practical 2,3-BDO production.     

Ethanol vapour pressure as a control factor during alcoholic fermentation

Aqueous solutions of glucose/fructose mixtures with varying concentrations of ethanol were used to study the effects on fermentation of ethanol vapour pressure and water activity. Water vapour pressure was found to increase significantly with temperature in the range 15 to 30‡C. The effects on glucose fermentation bySaccharomyces cerevisiae Bg7FL of the variables glucose concentration, Tween 80 concentration, temperature and ammonium and ethanol concentrations were examined using central composite design. A best fit equation describing the main, quadratic and interactive effects of the five variables on yeast growth rate was produced. Further model systems were analysed in which the effects of ethanol vapour pressure, water vapour pressure and ethanol concentration on maximal growth rate of the yeast strain were studied. Above 18‡C, neither ethanol concentration nor ethanol vapour pressure controlled the fermentation rate. Ethanol toxicity was shown to be associated with its vapour pressure rather than its concentration.     

自絮凝酵母SPSC01在组合反应器系统中酒精连续发酵的研究

建立了一套由四级磁力搅拌发酵罐串联组成、总有效容积4000mL的小型组合生物反应器系统 ,其中一级罐作为种子培养罐。以脱胚脱皮玉米粉双酶法制备的糖化液为种子培养基和发酵底物 ,进行了自絮凝颗粒酵母酒精连续发酵的研究。种子罐培养基还原糖浓度为100g L ,添加 (NH₄)₂HPO₄ 和KH₂PO₄ 各 20g L ,以0.017h^-1 的恒定稀释速率流加 ,并溢流至后续酒精发酵系统。发酵底物初始还原糖浓度 220g/L ,添加 (NH₄)₂HPO₄ 15g/L和KH₂PO₄2 5g/L ,流加至第一级发酵罐 ,稀释速率分别为 0.017、0.025、0.033、0.040和0.05 0h^-1。实验数据表明 ,自絮凝颗粒酵母在各发酵罐中呈部分固定化状态 ,在稀释速率0.040h^-1 条件下 ,发酵系统呈一定的振荡行为 ,其他四个稀释速率实验组均能够达拟稳态。当稀释速率不超过 0 0 33h^-1 ,流出末级发酵罐的发酵液中酒精浓度可以达到 12 % (V/V)以上 ,残还原糖和残总糖分别在 0 11%和 0 35 % h^-1,流出末级发酵罐的发酵液中酒精浓度可以达到12%（V/V）以上,残还原糖和残总糖分别在0.11%和0.35%（W/V）以下。在稀释速率为0.033h^-1时,计算发酵系统酒精的设备生产强度指标为3.32（g·L^-1·h^-1）,与游离酵母细胞传统酒精发酵工艺相比,增加约1倍。     

Glycerol Overproduction by Engineered Saccharomyces cerevisiae Wine Yeast Strains Leads to Substantial Changes in By-Product Formation and to a Stimulation of Fermentation Rate in Stationary Phase

Six commercial wine yeast strains and three nonindustrial strains (two laboratory strains and one haploid strain derived from a wine yeast strain) were engineered to produce large amounts of glycerol with a lower ethanol yield. Overexpression of the GPD1 gene, encoding a glycerol-3-phosphate dehydrogenase, resulted in a 1.5- to 2.5-fold increase in glycerol production and a slight decrease in ethanol formation under conditions simulating wine fermentation. All the strains overexpressing GPD1 produced a larger amount of succinate and acetate, with marked differences in the level of these compounds between industrial and nonindustrial engineered strains. Acetoin and 2,3-butanediol formation was enhanced with significant variation between strains and in relation to the level of glycerol produced. Wine strains overproducing glycerol at moderate levels (12 to 18 g/liter) reduced acetoin almost completely to 2,3-butanediol. A lower biomass concentration was attained by GPD1-overexpressing strains, probably due to high acetaldehyde production during the growth phase. Despite the reduction in cell numbers, complete sugar exhaustion was achieved during fermentation in a sugar-rich medium. Surprisingly, the engineered wine yeast strains exhibited a significant increase in the fermentation rate in the stationary phase, which reduced the time of fermentation.     

Coproduction of acetaldehyde and hydrogen during glucose fermentation by Escherichia coli

Escherichia coli K-12 strain MG1655 was engineered to coproduce acetaldehyde and hydrogen during glucose fermentation by the use of exogenous acetyl-coenzyme A (acetyl-CoA) reductase (for the conversion of acetyl-CoA to acetaldehyde) and the native formate hydrogen lyase. A putative acetaldehyde dehydrogenase/acetyl-CoA reductase from Salmonella enterica (SeEutE) was cloned, produced at high levels, and purified by nickel affinity chromatography. In vitro assays showed that this enzyme had both acetaldehyde dehydrogenase activity (68.07 ± 1.63 μmol min(-1) mg(-1)) and the desired acetyl-CoA reductase activity (49.23 ± 2.88 μmol min(-1) mg(-1)). The eutE gene was engineered into an E. coli mutant lacking native glucose fermentation pathways (ΔadhE, ΔackA-pta, ΔldhA, and ΔfrdC). The engineered strain (ZH88) produced 4.91 ± 0.29 mM acetaldehyde while consuming 11.05 mM glucose but also produced 6.44 ± 0.26 mM ethanol. Studies showed that ethanol was produced by an unknown alcohol dehydrogenase(s) that converted the acetaldehyde produced by SeEutE to ethanol. Allyl alcohol was used to select for mutants with reduced alcohol dehydrogenase activity. Three allyl alcohol-resistant mutants were isolated; all produced more acetaldehyde and less ethanol than ZH88. It was also found that modifying the growth medium by adding 1 g of yeast extract/liter and lowering the pH to 6.0 further increased the coproduction of acetaldehyde and hydrogen. Under optimal conditions, strain ZH136 converted glucose to acetaldehyde and hydrogen in a 1:1 ratio with a specific acetaldehyde production rate of 0.68 ± 0.20 g h(-1) g(-1) dry cell weight and at 86% of the maximum theoretical yield. This specific production rate is the highest reported thus far and is promising for industrial application. The possibility of a more efficient "no-distill" ethanol fermentation procedure based on the coproduction of acetaldehyde and hydrogen is discussed.     

URA3基因影响青蒿酸酿酒酵母工程菌中试发酵产量

CRISPR/Cas9基因编辑技术已经被广泛应用于工程酿酒酵母的基因插入、基因替换和基因敲除,通过使用选择标记进行基因编辑具有简单高效的特点。前期利用CRISPR/Cas9系统敲除青蒿酸生产菌株酿酒酵母(Saccharomyces cerevisiae) 1211半乳糖代谢负调控基因GAL80,获得菌株S. cerevisiae 1211-2,在不添加半乳糖诱导的情况下,青蒿酸摇瓶发酵产量达到了740 mg/L。但在50 L中试发酵实验中,S. cerevisiae 1211-2很难利用对青蒿酸积累起到决定性作用的碳源-乙醇,青蒿酸的产量仅为亲本菌株S.cerevisiae 1211的20%–25%。我们推测因遗传操作所需的筛选标记URA3突变,影响了其生长及青蒿酸产量。随后我们使用重组质粒pML104-KanMx4-u连同90 bp供体DNA成功恢复了URA3基因,获得了工程菌株S. cerevisiae 1211-3。S. cerevisiae 1211-3能够在葡萄糖和乙醇分批补料的发酵罐中正常生长,其青蒿酸产量超过20g/L,与亲本菌株产量相当。研究不但获得了不加半乳糖诱导的青...     

Effects of potassium chloride on ethanol production by an osmotolerant mutant of Zymomonas mobilis

The effect of increasing the KCl concentration in the culture medium of an alcoholic fermentation of glucose using the bacterium Zymomonas mobilis was investigated. Data obtained with the wild-type strain (ZM4, ATCC 31821) and with a newly isolated osmotolerant mutant (SBE15) were compared. It was observed that, at high salt concentration, inhibition of growth occured (specific growth rate and biomass yield) while ethanol production (specific ethanol productivity and ethanol yield) was unaffected. In contrast, the specific rate of in-vitro ethanol production, using either cell-free extract or washed cells, was strongly inhibited by increasing the KCl concentration in the incubation mixture. Therefore, it was concluded that the intracellular concentration of KCl was maintained below the inhibitory concentration by an active transport system. In addition, the fermentation performances of the osmotolerant mutant strain were higher than those of the parent strain at all the KCl concentrations tested, suggesting the utility of the former to run ethanolic fermentations in crude industrial media with a high salt content. Furthermore, the fermentation data on media containing added KCl agreed well with those obtained on molasses media, suggesting that the inhibition observed on these media was due to their high osmolality. Correspondence to: J. Baratti     

Utilization of an external loop bioreactor for the isolation of a flocculating strain ofKluyveromyces marxianus

A continuous open loop bioreactor was used to induce flocculation in an originally nonflocculent strain ofKluyveromyces marxianus. The sedimentation capacity of the isolated strain was of such a magnitude that the cell concentration inside the fermentor was 50 times larger than in the effluent. Also, a batch system was used with the same objective, but no flocculation was obtained.The kinetic parameters of the flocculent strain were compared with those of the mother strain. It was shown that both maximum specific growth rate and maximum specific ethanol production rate were lower in the flocculent strain. Ethanol had a larger inhibitory effect on the kinetic parameters of the isolated strain. Also, the batch fermentations with this strain presented a larger final biomass concentration and a reduced ethanol yield.     

High productivity ethanol fermentation on a mineral medium using a flocculent strain ofZymomonas mobilis

Summary A flocculent strain ofZymomonas mobilis (ZM4F JM1) was isolated in continuous culture. The parent strain, ZM4F, had lost its flocculating properties. The isolation was done in a conical fermentor at high dilution rate. Ethanol production by the new strain was then compared on a rich and mineral medium. The mineral medium showed high performance and could be used for industrial production of ethanol since it reduced one hundred fold the vitamin cost of the fermentation.