Ethanol-induced yeast flocculation directed by the promoter of TPS1 encoding trehalose-6-phosphate synthase 1 for efficient ethanol production

Yeast flocculation is an important trait in the brewing industry as well as in ethanol production, through which biomass can be recovered by cost-effective sedimentation. However, mass transfer limitation may affect yeast growth and ethanol fermentation if the flocculation occurs earlier before fermentation is completed. In this article, a novel type of cell-cell flocculation induced by trehalose-6-phosphate synthase 1 (TPS1) promoter was presented. The linear cassette HO-P(TPS1)-FLO1(SPSC01)-KanMX4-HO was constructed to transform the non-flocculating industrial yeast S. cerevisiae 4126 by chromosome integration to obtain a new flocculating yeast strain, ZLH01, whose flocculation was induced by ethanol produced during fermentation. The experimental results illustrated that flocculation of ZLH01 was triggered by 3% (v/v) ethanol and enhanced as ethanol concentration increased till complete flocculation was achieved at ethanol concentration of 8% (v/v). Real time PCR analysis confirmed that the expression of FLO1(SPSC01) was dependent on ethanol concentration. The growth and ethanol fermentation of ZLH01 were improved significantly, compared with the constitutive flocculating yeast BHL01 engineered with the same FLO gene but directed by the constitutive 3-phosphoglycerate kinase promoter PGK1, particularly under high temperature conditions. These characteristics make the engineered yeast more suitable for ethanol production from industrial substrates under high gravity and temperature conditions. In addition, this strategy offers advantage in inducing differential expression of other genes for metabolic engineering applications of S. cerevisiae.     

Flocculation onset in Saccharomyces cerevisiae: effect of ethanol, heat and osmotic stress

AIMS: To examine the effect of different stress conditions on the onset of flocculation in an ale-brewing strain, Saccharomyces cerevisiae NCYC 1195. METHODS AND RESULTS: Flocculation was evaluated using the method of Soares, E.V. and Vroman, A. [Journal of Applied Microbiology (2003) 95, 325]; plasma membrane integrity was accessed using propidium iodide and the staining of the yeast cell wall was performed using calcofluor white M2R. Cells in exponential phase of growth were subjected to different stress conditions. The addition of 1%, 3% and 5% (v/v) ethanol, 1% and 3% (v/v) isopropanol or a brief heat shock (52 degrees C, 5 min), did not induce an early flocculation phenotype when compared with control cells. The addition of 10% (v/v) ethanol, a continuous mild heat-stress (37 degrees C) or an osmotic stress (0.5 or 1 mol l(-1) of NaCl) did not induce a flocculent phenotype. CONCLUSIONS: Flocculation seems not to be induced as a response to different chemical (ethanol and isopropanol) and physical (heat and osmotic) stress conditions. Conversely, osmotic and ethanol [10% (v/v)] stress, as well as a continuous mild heat shock (37 degrees C), have a negative impact on the phenotype expression of flocculation. SIGNIFICANCE AND IMPACT OF THE STUDY: The findings reported here contribute to the elucidation of the control of yeast flocculation. This information might be useful to the brewing industry, as the time when the onset of flocculation occurs can determine the fermentation performance and the beer quality, as well as in other biotechnological industries where flocculation can be used as a cell separation process.     

Carbohydrate carbon sources induce loss of flocculation of an ale-brewing yeast strain

AIMS: To identify the nutrients that can trigger the loss of flocculation under growth conditions in an ale-brewing strain, Saccharomyces cerevisiae NCYC 1195. METHODS AND RESULTS: Flocculation was evaluated using the method of Soares, E.V. and Vroman, A. [Journal of Applied Microbiology (2003) 95, 325]. Yeast growth with metabolizable carbon sources (glucose, fructose, galactose, maltose or sucrose) at 2% (w/v), induced the loss of flocculation in yeast that had previously been allowed to flocculate. The yeast remained flocculent when transferred to a medium containing the required nutrients for yeast growth and a sole nonmetabolizable carbon source (lactose). Transfer of flocculent yeast into a growth medium with ethanol (4% v/v), as the sole carbon source did not induce the loss of flocculation. Even the addition of glucose (2% w/v) or glucose and antimycin A (0.1 mg l(-1)) to this culture did not bring about loss of flocculation. Cycloheximide addition (15 mg l(-1)) to glucose-growing cells stopped flocculation loss. CONCLUSIONS: Carbohydrates were the nutrients responsible for stimulating the loss of flocculation in flocculent yeast cells transferred to growing conditions. The glucose-induced loss of flocculation required de novo protein synthesis. Ethanol prevented glucose-induced loss of flocculation. This protective effect of ethanol was independent of the respiratory function of the yeast. SIGNIFICANCE AND IMPACT OF THE STUDY: This work contributes to the elucidation of the role of nutrients in the control of the flocculation cycle in NewFlo phenotype yeast strains.     

Effect of different starvation conditions on the flocculation of Saccharomyces cerevisiae

AIMS: To study the effect of different starvation conditions on the flocculation of an ale brewing yeast of Saccharomyces cerevisiae NCYC 1195. METHODS AND RESULTS: Flocculation was assessed by a micro-flocculation technique (Soares and Mota 1997). Carbon-starved cells of a NewFlo phenotype strain did not lose flocculation during a 48 h period. Cells incubated only in the presence of fermentable carbon sources (glucose, galactose and maltose at 2%, w/v), showed a progressive flocculation loss. The incubation of cells in 4% (v/v) ethanol did not induce a flocculation loss. The simultaneous incubation of cells in the presence of 2% (w/v) glucose and 15 microg ml(-1) cycloheximide hindered flocculation loss. The presence of 0.1 mmol l(-1) PMSF or 10 mmol l-1 EDTA prevented partially or completely, respectively, the loss of flocculation in the presence of glucose. CONCLUSIONS: Fermentable sugars induced a flocculation loss, which seems to require de novo protein synthesis and the involvement of different proteases. SIGNIFICANCE AND IMPACT OF THE STUDY: The findings reported here contribute to the elucidation of the role of nutrients on the physiological control of yeast flocculation.     

Flocculation onset in Saccharomyces cerevisiae: the role of nutrients

AIMS: To examine the role of the nutrients on the onset of flocculation in an ale-brewing strain, Saccharomyces cerevisiae NCYC 1195. METHODS AND RESULTS: Flocculation was evaluated using the method of Soares, E.V. and Vroman, A. [Journal of Applied Microbiology (2003) 95, 325]. For cells grown in chemically defined medium (yeast nitrogen base with glucose) or in rich medium (containing yeast extract, peptone and fermentable sugars: fructose or maltose), the onset of flocculation occurred after the end of exponential respiro-fermentative phase of growth being coincident with the attainment of the lower level of carbon source in the culture medium. Cells, in exponential respiro-fermentative phase of growth, transferred to a glucose-containing medium without nitrogen source, developed a flocculent phenotype, while these carbon source starved cells, in the presence of all other nutrients that support growth, did not flocculate. In addition, cells in exponential phase of growth, under catabolite repression, when transferred to a medium containing 0.2% (w/v) of fermentable sugar (fructose or maltose) or 2% (v/v) ethanol, showed a rapid triggering of flocculation, while when incubated in 2% (v/v) glycerol did not develop a flocculent phenotype. CONCLUSIONS: The onset of flocculation occurs when a low sugar and/or nitrogen concentration is reached in culture media. The triggering of flocculation is an energetic dependent process influenced by the carbon source metabolism. The presence of external nitrogen source is not necessary for developing a flocculent phenotype. SIGNIFICANCE AND IMPACT OF THE STUDY: This work contributes to the elucidation of the role of nutrients on the onset of flocculation in NewFlo phenotype yeast strains. This information might be useful to the brewing industry, in the control of yeast flocculation, as the time when the onset of flocculation occurs can determine the fermentation performance and the beer quality.     

Fermentation of deproteinized cheese whey powder solutions to ethanol by engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>: effect of supplementation with corn steep liquor and repeated-batch operation with biomass recycling by flocculation

The lactose in cheese whey is an interesting substrate for the production of bulk commodities such as bio-ethanol, due to the large amounts of whey surplus generated globally. In this work, we studied the performance of a recombinant Saccharomyces cerevisiae strain expressing the lactose permease and intracellular ß-galactosidase from Kluyveromyces lactis in fermentations of deproteinized concentrated cheese whey powder solutions. Supplementation with 10 g/l of corn steep liquor significantly enhanced whey fermentation, resulting in the production of 7.4% (v/v) ethanol from 150 g/l initial lactose in shake-flask fermentations, with a corresponding productivity of 1.2 g/l/h. The flocculation capacity of the yeast strain enabled stable operation of a repeated-batch process in a 5.5-l air-lift bioreactor, with simple biomass recycling by sedimentation of the yeast flocs. During five consecutive batches, the average ethanol productivity was 0.65 g/l/h and ethanol accumulated up to 8% (v/v) with lactose-to-ethanol conversion yields over 80% of theoretical. Yeast viability (>97%) and plasmid retention (>84%) remained high throughout the operation, demonstrating the stability and robustness of the strain. In addition, the easy and inexpensive recycle of the yeast biomass for repeated utilization makes this process economically attractive for industrial implementation.     

Yeast flocculation: New story in fuel ethanol production

Yeast flocculation has been used in the brewing industry to facilitate biomass recovery for a long time, and thus its mechanism of yeast flocculation has been intensively studied. However, the application of flocculating yeast in ethanol production garnered attention mainly in the 1980s and 1990s. In this article, updated research progress in the molecular mechanism of yeast flocculation and the impact of environmental conditions on yeast flocculation are reviewed. Construction of flocculating yeast strains by genetic approach and utilization of yeast flocculation for ethanol production from various feedstocks were presented. The concept of self-immobilized yeast cells through their flocculation is revisited through a case study of continuous ethanol fermentation with the flocculating yeast SPSC01, and their technical and economic advantages are highlighted by comparing with yeast cells immobilized with supporting materials and regular free yeast cells as well. Taking the flocculating yeast SPSC01 as an example, the ethanol tolerance of the flocculating yeast was also discussed.     

混合糖发酵重组酿酒酵母的菌株构建和菊芋秸秆同步糖化发酵研究

【目的】构建可用于纤维素乙醇高效生产的混合糖发酵重组酿酒酵母菌株,并利用菊芋秸秆为原料进行乙醇发酵。【方法】筛选在木糖中生长较好的酿酒酵母YB-2625作为宿主菌,构建木糖共代谢菌株YB-2625 CCX。进一步通过r DNA位点多拷贝整合的方式,以YB-2625 CCX为出发菌株构建木糖脱氢酶过表达菌株,并筛选得到优势菌株YB-73。采用同步糖化发酵策略研究YB-73的菊芋秸秆发酵性能。【结果】YB-73菌株以90 g/L葡萄糖和30 g/L木糖为碳源进行混合糖发酵,乙醇产量比出发菌株YB-2625 CCX提高了13.9%,副产物木糖醇产率由0.89 g/g降低至0.31 g/g,下降了64.6%。利用重组菌YB-73对菊芋秸秆进行同步糖化发酵,48 h最高乙醇浓度达到6.10%(体积比)。【结论】通过转入木糖代谢途径以及r DNA位点多拷贝整合过表达木糖脱氢酶基因可有效提高菌株木糖发酵性能,并用于菊芋秸秆的纤维素乙醇生产。这是首次报道利用重组酿酒酵母进行菊芋秸秆原料的纤维素乙醇发酵。     

Cell wall ultrastructure of flocculent and non-flocculent Schizosaccharomyces pombe strains. Effect of cell wall hydrolysing enzymes on flocculation and cell wall ultastructure

Scanning and transmission electron microscopic studies revealed the presence of slime-like, amorphous material on the surface of Schizosaccahromyces pombe RIVE 4-2-1 cells, independently, whether they were in flocculated or in non-flocculated state. Close contact of the adjacent cells via the merging outermost cell wall layers was found, however, only in the case of floc formation, which was induced by cultivating the cells in the presence of 6% (v/v) ethanol. Irreversible loss of the flocculation ability of the cells by treatment with proteinases suggests that proteinaceous cell surface molecules as lectins contribute to the cell-to-cell interaction during flocculation. Both proteinase K and pronase treatments removed a distinct outer layer of the cell wall, which indicated that the protein moieties of the phosphogalactomannan outer surface layer has a crucial role in the maintenance of cell wall integrity. In the case of lysing enzyme treatment the removal of the outermost layer was also observed as the first step of the cell wall digestion, while driselase treatment resulted in almost complete digestion of the cell wall.     

High level ethanol-tolerant Saccharomyces from Nigerian palm wine

Summary Eight Saccharomyces yeasts isolated from Nigerian palm wine showed high tolerance to 18% ethanol v/v and 50% sucrose. Two of the yeasts produced 12.7 and 13.1% ethanol v/v in 50% sucrose supplemented YPD-2. Soybean and groundnut supplementations yielded up to 21.5% and 19.0% ethanol v/v respectively.     

Denaturation and aggregation of hen egg lysozyme in aqueous ethanol solution studied by dynamic light scattering

We applied dynamic light scattering technique on the model system of hen egg lysozyme in salt-free aqueous ethanol solution to study the mechanism of denaturation and aggregation of protein. At low ethanol concentration [0-63% (v/v)], the fast relaxation mode was observed, which was caused by lysozyme molecules in the solution interacting with each other with strong repulsive electrostatic force. At 45 and 63% (v/v) ethanol, the slow relaxation mode was also observed, which showed translational diffusive nature, similar to that observed in salt-free polyelectrolyte solution. At 72 or 81% (v/v) ethanol, the slow mode disappeared, leaving only the fast mode. However, the mutual diffusion coefficients obtained from the fast mode at 72 and 81% (v/v) ethanol decreased by about one order of magnitude compared with those from the fast mode at 0-63% (v/v). The reported alcohol-induced conformational transformation of lysozyme molecules at >60% (v/v) ethanol from their native structure to an alpha-helix-rich structure might cause such drastic decrease in the mutual diffusion coefficients. At the highest ethanol concentration of 90% (v/v), the slow mode reappeared, and its relaxation rate was decreasing with elapsed time, which is possibly due to the growth of aggregates of lysozyme molecules. X-ray diffraction results suggested that the intermolecular beta-sheet formation caused the aggregation. Thus, our results indicated that the change in molecular structure of lysozyme closely relates to the diffusion of molecules and their aggregation.     

Mechanisms of yeast flocculation: comparison of top- and bottom-fermenting strains.

The flocculation of two brewing yeast strains, top-fermenting strain Saccharomyces cerevisiae MUCL 38485 and bottom-fermenting strain Saccharomyces carlsbergensis MUCL 28285, has been investigated by means of a turbidimetric test. The two strains showed different electrical properties, a different hydrophobicity, and a different surface chemical composition. They flocculated according to completely different mechanisms; however, no correlation between the cell physicochemical properties and the onset of flocculation was found for either strain. Flocculation of the bottom strain was governed by a lectin-mediated mechanism. It was inhibited by mannose and some other sugars, required calcium specifically, occurred in a narrow pH range different from the isoelectric point, and was not influenced by ethanol. The onset of flocculation at the end of the exponential phase was controlled both by the appearance of "active" lectins at the cell surface and by the decrease in sugar concentration in the solution. Flocculation of the top strain was not inhibited by mannose, did not require the addition of calcium, and took place at the cell isoelectric point. Low concentrations of ethanol broadened the pH range in which the cells flocculated, and flocculation was favored by an increase of ionic strength. Adsorbed ethanol may induce flocculation by reducing the electrostatic repulsion between cells, by decreasing steric stabilization, and/or by allowing the protrusion of polymer chains into the liquid phase. The onset of flocculation was controlled by both a change of the cell surface and an increase in ethanol concentration. The only evidence for an adhesin-mediated mechanism was the specific requirement for a small amount of calcium.     

Identification and functional study of a new FLO10-derivative gene from the industrial flocculating yeast SPSC01

Yeast flocculation is an important property for the brewing industry as well as for ethanol fermentation to facilitate biomass recovery by sedimentation from the fermentation broth, which is cost-effective. In this study, a new flocculating gene FLO10 (spsc) of 4,221 bp homologous to FLO10 was identified in the industrial flocculating yeast SPSC01. Sequence analysis indicated that the N- and C-terminus of the deduced protein of this new FLO gene are 99 % identical to that of FLO10, but more intragenic repeats are included. The study on the function of FLO10 (spsc) by its integrative expression in the non-flocculating industrial yeast indicated severe inhibition in the flocculation of the transformant by mannose and maltose, moderate inhibition by sucrose and glucose and no inhibition by xylose and galactose, and thus the NewFlo type was established. Meanwhile, the flocculation of the transformant was stable when the temperature was below 50 °C and the pH was in the range of 4.0-6.0. Furthermore, the medium containing 250 g/l glucose was completely fermented within 48 h by the transformant, with about 110 g/l ethanol and 5.5 g(DCW)/l biomass produced, and no significant difference in ethanol fermentation performance was observed compared to its wide-type strain. Therefore, the FLO gene and corresponding transformation strategy provide a platform for engineering yeast strains with the flocculation phenotype to facilitate biomass recovery.     

Alcohol-induced changes of beta-lactoglobulin-retinol-binding stoichiometry

It has been demonstrated using CD that ethanol induces important secondary structure changes of beta-lactoglobulin. CD spectra indicate that beta-lactoglobulin secondary structure, which is mainly composed of beta-strands, becomes mostly alpha-helical under the influence of the solvent polarity changes. The midpoint of beta-strand/alpha-helix transition in beta-lactoglobulin is observed at dielectric constant approximately 60 (35% ethanol; v/v). According to CD measurements, the ethanol-dependent secondary structure changes are reversible. The alkylation of lysines epsilon-NH2 in beta-lactoglobulin weakens the central beta-barrel structure, since the beta-strand/alpha-helix transition midpoint of alkylated beta-lactoglobulin is shifted to lower ethanol concentration (25% ethanol; v/v). beta-Lactoglobulin structural changes are triggering the dissociation of the beta-lactoglobulin-retinol complex as judged from complete quenching of its fluorescence in ethanol concentration greater than 30% (v/v). However, in 20% ethanol (v/v), beta-lactoglobulin still retains most of its native secondary structure as shown by CD and, in this condition, one beta-lactoglobulin molecule binds an additional second retinol molecule. This suggests that the highly populated species observed around 20% ethanol (v/v) might represent an intermediate state able to bind two molecules of retinol.     

Single crystals of amylose with a low degree of polymerization

Single crystals of amylose with a low degree of polymerization were prepared from dilute solution in water or mixtures of water and ethanol. Depending on the concentration of ethanol used, three different polymorphs resulted. From pure water amylose B was obtained and, respectively, from 15% (v/v) ethanol, amylose A, and from 40% (v/v) ethanol, V amylose. The crystals were studied by electron diffraction after quench-freezing and the crystallographic parameters were compared with those already reported in the literature.     

Direct production of ethanol from raw corn starch via fermentation by use of a novel surface-engineered yeast strain codisplaying glucoamylase and alpha-amylase

Direct and efficient production of ethanol by fermentation from raw corn starch was achieved by using the yeast Saccharomyces cerevisiae codisplaying Rhizopus oryzae glucoamylase and Streptococcus bovis alpha-amylase by using the C-terminal-half region of alpha-agglutinin and the flocculation functional domain of Flo1p as the respective anchor proteins. In 72-h fermentation, this strain produced 61.8 g of ethanol/liter, with 86.5% of theoretical yield from raw corn starch.     

Contamination issues in a continuous ethanol production corn wet milling facility

Low ethanol yields and poor yeast viability were investigated at a continuous ethanol production corn wet milling facility. Using starch slurries and recycle streams from a commercial ethanol facility, laboratory hydrolysates were prepared by reproducing starch liquefaction and saccharification steps in the laboratory. Fermentations with hydrolysates prepared in the laboratory were compared with plant hydrolysates for final ethanol concentrations and total yeast counts. Fermentation controls were prepared using hydrolysates (plant and laboratory) that were not inoculated with yeast. Hydrolysates prepared in the laboratory resulted in higher final ethanol concentrations (15.8 % v/v) than plant hydrolysate (13.4 % v/v). Uninoculated controls resulted in ethanol production from both laboratory (12.2 % v/v) and plant hydrolysates (13.7 % v/v), indicating the presence of a contaminating microorganism. Yeast colony counts on cycloheximide and virginiamycin plates confirmed the presence of a contaminant. DNA sequencing and fingerprinting studies also indicated a number of dissimilar communities in samples obtained from fermentors, coolers, saccharification tanks, and thin stillage.     

Simultaneous saccharification and fermentation of straw to ethanol using the thermotolerant yeast strain Kluyveromyces marxianus imb3

The thermotolerant, ethanol-producing yeast strain Kluyveromyces marxianus IMB3 was grown at 45°C on media containing 2, 4 and 6 % (w/v) pulverized barley straw and supplemented with 2% (v/v) cellulase. Maximum ethanol concentrations produced were 2, 3 and 3.6g/l, respectively. When the pulverized straw was replaced by NaOH pretreated straw (at 2, 4 and 6% (w/v); based on original untreated straw), ethanol concentrations increased to maxima of 3.9, 8, and 12g/l, respectively. The ethanol yields amount to 20g ethanol from 100g of straw.     

Stress-induced morphological and physiological changes in γ-linolenic acid production by Mucor fragilis in batch and continuous cultures

Batch and continuous cultures conditions were studied in order to increase γ-linolenic acid production by Mucor fragilis CCMI 142, in response to the presence of ethanol. Continuous cultures were used to add ethanol pulses to steady state pellet cultures. It was demonstrated that pellet size, which allowed homogeneous fungal cultures, can be obtained by means of pH adjustment, thus enabling steady state continuous growth at 2.90±0.05.

The 5 and 2% (v/v) ethanol pulses induced hyphal morphological changes with arthrospore formation. A 1% (v/v) pulse of ethanol did not immediately affect growth, but induced morphological changes, which led to autolysis at the pellet core. A 0.5% (v/v) pulse of ethanol did not affect neither the morphology nor the physiology of the microorganism to any significant extent. The 0.5 and 1% (v/v) ethanol pulses resulted in an increase in the proportion of γ-linolenic acid production up to 11%. Data from batch cultures showed a higher enhancement of ethanol, attaining 30% of γ-linolenic acid.

The increase of γ-linolenic acid content observed in batch and continuous conditions appears to be a response associated with stress induced by the ethanol which seems to be of value as an industrial medium component.     

Enhancement of apparent resistance to ethanol in Lactobacillus hilgardii

The survival of Lactobacillus hilgardii, a highly ethanol-tolerant organism, after an ethanol challenge at 25% (v/v) for 10 min, increased by several log cycles when cells, grown in the absence of ethanol, were pre-treated with 10% (v/v) ethanol, 15% (v/v) methanol or 2% (v/v) butanol for 4 h. A temperature upshift (25 to 40°C) before ethanol challenge demonstrated a similar enhancement of apparent resistance to ethanol. Ethanol shock enhanced apparent resistance to methanol, butanol and heat challenges. The addition of chloramphenicol to cells prior to any pre-treatment did not significantly diminish the increase in ethanol tolerance, suggesting that de novo protein synthesis is not required for induced tolerance in this organism. This revised version was published online in November 2006 with corrections to the Cover Date.