Modelling Biolog profiles' evolution for yeast growth monitoring in alcoholic fermentation

Aims: A research was undertaken to explore the possibility to express with suitable mathematical models Biolog metabolic curves obtained for oenological yeasts and to use such models for monitoring yeast growth in alcoholic fermentation. Methods and Results: Experimental curves of metabolic activity in Biolog YT microplates, obtained in a previous work for various oenological yeast strains in pure cultures and mixed populations, at various cell concentrations, have been modelled with Gompertz’s, Gompertz’s modified and Lindstrom’s mathematical equations. Lindstrom’s model proved to be the most suitable to fit the curves of the oenological yeasts under study, providing the highest correlation coefficients between experimental and calculated data. The model made it possible to recognize, in mixed yeast populations, the presence of active dry yeasts used for guided fermentations. Model’s constant parameters were used for a numerical characterization of yeast curves. Conclusions: The application of the model to the experimental data resulted to be suitable for an early prediction of the successive evolution of yeast growth. Significance and Impact of the Study: The results obtained indicate the possibility to develop protocols for monitoring yeast presence during alcoholic fermentation, with an early assessment of the correct evolution of their growth, especially when active dry yeasts are employed.     

Intracellular ethanol accumulation in yeast cells during aerobic fermentation: a Raman spectroscopic exploration

Aims: To investigate the intracellular ethanol accumulation in yeast cells by using laser tweezers Raman spectroscopy (LTRS). Methods and Results: Ethanol accumulation in individual yeast cells during aerobic fermentation triggered by excess glucose was studied using LTRS. Its amount was obtained by comparing intracellular and extracellular ethanol concentrations during initial process of ethanol production. We found that (i) yeasts start to produce ethanol within 3 min after triggering aerobic fermentation, (ii) average ratio of intracellular to extracellular ethanol is 1·54 ± 0·17 during the initial 3 h after addition of 10% (w/v) excess glucose and (iii) the accumulated intracellular ethanol is released when aerobic fermentation is stimulated with decreasing glucose concentration. Conclusions: Intracellular ethanol accumulation occurs in initial stage of a rapid aerobic fermentation and high glucose concentration may attribute to this accumulation process. Significance and Impact of the Study: This work demonstrates LTRS is a real‐time, reagent‐free, in situ technique and a powerful tool to study kinetic process of ethanol fermentation. This work also provides further information on the intracellular ethanol accumulation in yeast cells.     

Construction and evaluation of self‐cloning bottom‐fermenting yeast with high SSU1 expression

Aim: To construct a self‐cloning brewer’s yeast that can minimize the unfavourable flavours caused by oxidation and certain kinds of sulfur compounds. Methods and Results: DNA fragments of a high‐expression promoter from the TDH3 gene originating from Saccharomyces cerevisiae were integrated into the promoter regions of the S. cerevisiae‐type and Saccharomyces bayanus‐type SSU1 genes of bottom‐fermenting brewer’s yeast. PCR and sequencing confirmed the TDH3 promoter was correctly introduced into the SSU1 regions of the constructed yeasts, and no foreign DNA sequences were found. Using the constructed yeasts, the concentration of sulfite in fermenting wort was higher when compared with the parent strain. In addition, the concentrations of hydrogen sulfide, 3‐methyl‐2‐buten‐1‐thiol (MBT) and 2‐mercapto‐3‐methyl‐1‐butanol (2M3MB) were lower when compared with the parent strain. Conclusion: We successfully constructed a self‐cloning brewer’s yeast with high SSU1 expression that enhanced the sulfite‐excreting ability and diminished the production ability of hydrogen sulfide, MBT and 2M3MB. Significance and Impact of the Study: The self‐cloning brewer’s yeast with high SSU1 expression would contribute to the production of superior quality beer with a high concentration of sulfite and low concentrations of hydrogen sulfide, MBT and 2M3MB.     

Nitrogen demand of different yeast strains during alcoholic fermentation. Importance of the stationary phase

The nitrogen demand of industrial yeast strains were compared. Substantial differences were found between strains. These did not change regardless of the initial medium composition and added nitrogen source. To separately study growth and stationary phases, we ran fermentations with different nitrogen feeding profiles: a) exponentially fed fermentations with a long growth phase, and b) constant rate fermentations with nitrogen addition during the stationary phase. Differences between stains mostly appeared during the second phase. Measuring nitrogen requirements under such conditions would thus be an interesting complementary test when selecting new strains especially for enological purposes since most fermentation kinetics are nitrogen limited.     

A food‐grade site‐directed mutagenesis system for Streptococcus thermophilus LMG 18311

Aims: To develop a general method for site‐directed mutagenesis in the dairy starter strain Streptococcus thermophilus LMG 18311 which does not depend on antibiotic‐resistance genes or other selection markers for the identification of transformants. Methods and Results: In a previous study, we demonstrated that Strep. thermophilus LMG 18311 can be made competent for natural genetic transformation by overexpression of the alternative sigma factor ComX. In the present study, we wanted to investigate whether the natural transformation mechanism of Strep. thermophilus LMG 18311 is efficient enough to make it feasible to perform site‐directed mutagenesis in this strain without the use of a selection marker. Competent bacteria were mixed with a DNA fragment engineered to contain a nonsense and a frameshift mutation in the middle of the target gene (lacZ) and subsequently seeded on agar plates. By performing colony‐lift hybridization using a digoxigenin‐labelled oligonucleotide probe, we succeeded in identifying transformants containing the sought after mutation. Conclusions: By exploiting the natural transformability of Strep. thermophilus LMG 18311 and standard molecular methods, we have demonstrated that the genome of this bacterium can be altered at preselected sites without introduction of any foreign DNA. Significance and Impact of the Study: A food‐grade site‐directed mutagenesis system has been developed for Strep. thermophilus LMG 18311 that can be used by the dairy industry to construct starter strains with novel and/or improved properties.     

Performances of aseptic sampling devices for on-line monitoring of fermentation processes

Two liquid sampling systems, which are set in the bioreactor and can be sterilized in place, are described. They are composed primarily of an inorganic membrane filter which is either stationary or is set in a rotating motion. These systems have been tested during three types of fermentation processes (ethanol, lactic acid, and polysaccharide productions). The rotating system gave better filtration performances than the stationary sampler which can be used only in alcoholic fermentation. The rotating sampler was coupled with a high-pressure liquid chromatograph for the on-line quantitation of the major compounds present in the filtrate. The results are in good agreement with those obtained from off-line analysis on samples taken manually. (c) 1992 John Wiley & Sons, Inc.     

High-throughput sequencing of amplicons for monitoring yeast biodiversity in must and during alcoholic fermentation

We compared pyrosequencing technology with the PCR-ITS-RFLP analysis of yeast isolates and denaturing gradient gel electrophoresis (DGGE). These methods gave divergent findings for the yeast population. DGGE was unsuitable for the quantification of biodiversity and its use for species detection was limited by the initial abundance of each species. The isolates identified by PCR-ITS-RFLP were not fully representative of the true population. For population dynamics, high-throughput sequencing technology yielded results differing in some respects from those obtained with other approaches. This study demonstrates that 454 pyrosequencing of amplicons is more relevant than other methods for studying the yeast community on grapes and during alcoholic fermentation. Indeed, this high-throughput sequencing method detected larger numbers of species on grapes and identified species present during alcoholic fermentation that were undetectable with the other techniques.     

Real‐time monitoring of high‐gravity corn mash fermentation using in situ raman spectroscopy

In situ Raman spectroscopy was employed for real‐time monitoring of simultaneous saccharification and fermentation (SSF) of corn mash by an industrial strain of Saccharomyces cerevisiae. An accurate univariate calibration model for ethanol was developed based on the very strong 883 cm^?1 C–C stretching band. Multivariate partial least squares (PLS) calibration models for total starch, dextrins, maltotriose, maltose, glucose, and ethanol were developed using data from eight batch fermentations and validated using predictions for a separate batch. The starch, ethanol, and dextrins models showed significant prediction improvement when the calibration data were divided into separate high‐ and low‐concentration sets. Collinearity between the ethanol and starch models was avoided by excluding regions containing strong ethanol peaks from the starch model and, conversely, excluding regions containing strong saccharide peaks from the ethanol model. The two‐set calibration models for starch (R² = 0.998, percent error = 2.5%) and ethanol (R² = 0.999, percent error = 2.1%) provide more accurate predictions than any previously published spectroscopic models. Glucose, maltose, and maltotriose are modeled to accuracy comparable to previous work on less complex fermentation processes. Our results demonstrate that Raman spectroscopy is capable of real time in situ monitoring of a complex industrial biomass fermentation. To our knowledge, this is the first PLS‐based chemometric modeling of corn mash fermentation under typical industrial conditions, and the first Raman‐based monitoring of a fermentation process with glucose, oligosaccharides and polysaccharides present. Biotechnol. Bioeng. 2013; 110: 1654–1662. © 2013 Wiley Periodicals, Inc.     

Use of response surface methodology for optimizing process parameters for high inulinase production by the marine yeast <Emphasis Type="Italic">Cryptococcus aureus</Emphasis> G7a in solid-state fermentation and hydrolysis of inulin

The optimization of process parameters for high inulinase production by the marine yeast strain Cryptococcus aureus G7a in solid-state fermentation (SSF) was carried out using central composite design (CCD), one of the response surface methodologies (RSMs). We found that moisture, inoculation size, the amount ratio of wheat bran to rice husk, temperature and pH had great influence on inulinase production by strain G7a. Therefore, the CCD was used to evaluate the influence of the five factors on the inulinase production by strain G7a. Then, five levels of the five factors above were further optimized using the CCD. Finally, the optimal parameters obtained with the RSM were the initial moisture 61.5%, inoculum 2.75%, the amount ratio of wheat bran to rice husk 0.42, temperature 29 °C, pH 5.5. Under the optimized conditions, 420.9 U g⁻¹ of dry substrate of inulinase activity was reached in the solid-state fermentation culture of strain G7a within 120 h whereas the predicted maximum inulinase activity of 436.2 U g⁻¹ of inulinase activity of 436.2 U g⁻¹ of dry weight was derived from the RSM regression. This is the highest inulinase activity produced by the yeast strain reported so far. A large amount of monosaccharides and oligosaccharides were detected after inulin hydrolysis by the crude inulinase.     

Dynamic genome-scale modeling of Saccharomyces cerevisiae unravels mechanisms for ester formation during alcoholic fermentation

Fermentation employing Saccharomyces cerevisiae has produced alcoholic beverages and bread for millennia. More recently, S. cerevisiae has been used to manufacture specific metabolites for the food, pharmaceutical, and cosmetic industries. Among the most important of these metabolites are compounds associated with desirable aromas and flavors, including higher alcohols and esters. Although the physiology of yeast has been well-studied, its metabolic modulation leading to aroma production in relevant industrial scenarios such as winemaking is still unclear. Here we ask what are the underlying metabolic mechanisms that explain the conserved and varying behavior of different yeasts regarding aroma formation under enological conditions? We employed dynamic flux balance analysis (dFBA) to answer this key question using the latest genome-scale metabolic model (GEM) of S. cerevisiae. The model revealed several conserved mechanisms among wine yeasts, for example, acetate ester formation is dependent on intracellular metabolic acetyl-CoA/CoA levels, and the formation of ethyl esters facilitates the removal of toxic fatty acids from cells using CoA. Species-specific mechanisms were also found, such as a preference for the shikimate pathway leading to more 2-phenylethanol production in the Opale strain as well as strain behavior varying notably during the carbohydrate accumulation phase and carbohydrate accumulation inducing redox restrictions during a later cell growth phase for strain Uvaferm. In conclusion, our new metabolic model of yeast under enological conditions revealed key metabolic mechanisms in wine yeasts, which will aid future research strategies to optimize their behavior in industrial settings.     

Overexpression of bacterial xylose isomerase and yeast host xylulokinase improves xylose alcoholic fermentation in the thermotolerant yeast Hansenula polymorpha

The thermotolerant methylotrophic yeast Hansenula polymorpha is able to ferment xylose to ethanol. To improve characteristics of xylose fermentation, the recombinant strain Delta xyl1 Delta xyl2-ADelta xyl2-B, with deletions of genes encoding first enzymes of xylose utilization (NAD(P)H-dependent xylose reductase and NAD-dependent xylitol dehydrogenases, respectively), was constructed and used as a recipient for co-overexpression of the Escherichia coli xylA gene coding for xylose isomerase and endogenous XYL3 gene coding for xylulokinase. The expression of both genes was driven by the H. polymorpha glyceraldehyde-3-phosphate dehydrogenase promoter. Xylose isomerase activities of obtained transformants amounted to approximately 80% of that of the bacterial host strain. Xylulokinase activities of the transformants increased twofold when compared with the parental strain. The recombinant strains displayed improved ethanol production during the fermentation of xylose.