Ethanol production from starch by a coimmobilized mixed culture system of Aspergillus awamori and Zymomonas mobilis

The production of ethanol from starch by a coimmobilized mixed culture system of aerobic and anaerobic microorganisms in Ca-alginate gel beads was investigated. The mold Aspergillus awamori was used as an aerobic amylolytic microorganism and an anaerobic bacterium, Zymomonas mobilis, as an ethanol producer. By controlling the mixing ratio of the microorganisms in the inoculum size, a desirable coimmobilized mixed culture system, in which the aerobic mycelia grew on and near the oxygen-rich surface of the gel beads while the anaerobic bacterial cells mainly grew in the oxygen-deficient central part of the gel beads, was naturally established under the aerobic culture conditions, and ethanol could be directly produced from starch by the system. The ethanol productivity by the system in flask culture was particularly affected by the shear stress (dependent on the shaking speed) which controlled the mycelial growth on the surface of the gel beads. Under optimum culture conditions in the flask culture, the glucose produced was instantly consumed, and was not observed in the culture broth; the final concentration of ethanol produced from 100 g/L starch was 25 g/L and the yield coefficient for ethanol, Y(pls), was 0.38. The ethanol productivity by the coimmobilized mixed culture system was compared with those by other various culture systems and the advantages of the system were clarified.     

Changes in ethanol concentration during incubation in multiwell tissue culture trays

Ethanol can have direct effects in tissue culture and is often used as a solvent. Analysis of these effects will require a precise knowledge of the concentration over time in the particular system employed. We measured the disappearance rate of ethanol from multiwell culture trays (open system) containing single or multiple concentrations of ethanol over a 48-hr time period. The ethanol concentration was also measured at 72 hr in stoppered Erlenmeyer flasks (closed system). In multiwell culture trays, 1 and 0.3% ethanol (V/V) evaporated with a t1/2 of 6 to 12 hr. Media containing no ethanol but adjacent to wells with 1% ethanol accumulated ethanol with a peak of 0.2% at 12 hr. The evaporation of 0.3% ethanol was slower from wells adjacent to those containing 1% ethanol. At 72 hr, stoppered Erlenmeyer flasks, which originally contained 1% ethanol, still had a concentration of 0.85%. Since both evaporation and transfer can occur in an open system, it is necessary to specify precise conditions or measure concentrations in such systems. Alternatively, a closed system in which the concentration of ethanol is maintained can be employed.     

Regulation of Product Formation in Bacteroides xylanolyticus X5-1 by Interspecies Electron Transfer

Bacteroides xylanolyticus X5-1 was grown in pure culture and in mixed culture with Methanospirillum hungatei JF-1 under xylose limitation in the chemostat. In the pure culture, ethanol, acetate, CO(2), and hydrogen were the products. In the mixed culture, acetate, CO(2), and presumably hydrogen were the only products formed by B. xylanolyticus X5-1. The biomass yield of B. xylanolyticus X5-1 increased because of cocultivation. In cell extracts of the pure culture, both NAD- and NADP-dependent acetaldehyde dehydrogenase and ethanol dehydrogenase activities were found. In cell extracts of the mixed culture, activities of these enzymes were not detected. Inhibition of methanogenesis in the mixed culture by the addition of bromoethanosulfonic acid (BES) resulted in an accumulation of H(2), ethanol, and formate. Immediately after the addition of BES, NAD-dependent acetaldehyde dehydrogenase and ethanol dehydrogenase activities were detected. After a short lag phase, a NADP-dependent ethanol dehydrogenase was also detectable. The induction of acetaldehyde dehydrogenase and ethanol dehydrogenase was inhibited by chloramphenicol, suggesting de novo synthesis of these enzymes. These results are consistent with a model in which the shift in product formation caused by interspecies electron transfer is regulated at the level of enzyme synthesis.     

Selection of Ethanol-Tolerant Yeast Hybrids in pH-Regulated Continuous Culture

Hybrids between naturally occurring wine yeast strains and laboratory strains were formed as a method of increasing genetic variability to improve the ethanol tolerance of yeast strains. The hybrids were subjected to competition experiments under continuous culture controlled by pH with increasing ethanol concentrations over a wide range to select the fastest-growing strain at any concentration of ethanol. The continuous culture system was obtained by controlling the dilution rate of a chemostat connected to a pH-meter. The nutrient pump of the chemostat was switched on and off in response to the pH of the culture, which was thereby kept near a critical value (pH_c). Under these conditions, when the medium was supplemented with ethanol, the ethanol concentration of the culture increased with each pulse of dilution. A hybrid strain was selected by this procedure that was more tolerant than any of the highly ethanol-tolerant wine yeast strains at any concentration of ethanol and was able to grow at up to 16% (vol/vol) ethanol. This improvement in ethanol tolerance led to an increase in both the ethanol production rate and the total amount of ethanol produced.     

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.     

Rational optimization of culture conditions for the most efficient ethanol production in Scheffersomyces stipitis using design of experiments

Optimization of culture parameters for achieving the most efficient ethanol fermentation is challenging due to multiple variables involved. Here we presented a rationalized methodology for multi‐variables optimization through the design of experiments DoE approach. Three critical parameters, pH, temperature, and agitation speed, affecting ethanol fermentation in S. stipitis was investigated. A predictive model showed that agitation speed significantly affected ethanol synthesis. Reducing pH and temperature also improved ethanol production. The model identified the optimum culture conditions for the most efficient ethanol production with the yield and productivity of 0.46 g/g and 0.28 g/l h, respectively, which is consistent with experimental observation. The results also indicated the scalability of the model from shake flask to bioreactor. Thus, DoE is a promising tool permitting the rapid establishment of culture conditions for the most efficient ethanol fermentation in S. stipitis. The approach could be useful to reduce process development time in lignocellulosic ethanol industry. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Ethanol production from xylose by Thermoanaerobacter ethanolicus in batch and continuous culture

The fermentation of xylose by Thermoanaerobacter ethanolicus ATCC 31938 was studied in pH-controlled batch and continuous cultures. In batch culture, a dependency of growth rate, product yield, and product distribution upon xylose concentration was observed. With 27 mM xylose media, an ethanol yield of 1.3 mol ethanol/mol xylose (78% of maximum theoretical yield) was typically obtained. With the same media, xylose-limited growth in continuous culture could be achieved with a volumetric productivity of 0.50 g ethanol/liter h and a yield of 0.42 g ethanol/g xylose (1.37 mol ethanol/mol xylose). With extended operation of the chemostat, variation in xylose uptake and a decline in ethanol yield was seen. Instability with respect to fermentation performance was attributed to a selection for mutant populations with different metabolic characteristics. Ethanol production in these T. ethanolicus systems was compared with xylose-to-ethanol conversions of other organisms. Relative to the other systems, T. ethanolicus offers the advantages of a high ethanol yield at low xylose concentrations in batch culture and of a rapid growth rate. Its disadvantages include a lower ethanol yield at higher xylose concentrations in batch culture and an instability of fermentation characteristics in continuous culture.     

Involvement of a cell size control mechanism in the induction and maintenance of oscillations in continuous cultures of budding yeast

Spontaneous oscillations occur in glucose-limited continuous cultures of Saccharomyces cerevisiae under aerobic conditions. The oscillatory behavior is detectable as a periodic change of many bioparameters such as dissolved oxygen, ethanol production, biomass concentration, as well as cellular content of storage carbohydrates and is associated to a marked synchronization of the yeast population. These oscillations may be related to a periodic accumulation of ethanol produced by yeast in the culture medium.The addition of ethanol to oscillating yeast cultures supports this hypothesis: indeed, no effect was observed if ethanol was added when already present in the medium, while a marked phase oscillation shift was obtained when ethanol was added at any other time. Moreover, the addition of ethanol to a nonoscillating culture triggers new oscillations. An accurate analysis performed at the level of nonoscillating yeast populations perturbed by addition of ethanol showed that both the growth rate and the protein content required for cell division increased in the presence of mixed substrate (i.e., ethanol plus limiting glucose). A marked synchronization of the yeast population occurred when the added ethanol was exhausted and the culture resumed growth only on limiting glucose. A decrease of protein content required for cell division was also apparent. These experimental findings support a new model for spontaneous oscillations in yeast cultures in which the alternative growth on limiting glucose and limiting glucose plus ethanol modifies the critical protein content required for cell division.     

Kinetics of ethanol production by yeast in continuous culture

Summary The rate of fermentation of glucose by Saccharomyces uvarum in steadystate continuous culture in excess of substrates showed non-competitive inhibition kinetics with respect to ethanol. A model is presented which predicts that growth stops at a finite ethanol concentration, which was calculated to be 95 gl^-1 for the system used here. The observed maximum ethanol concentration in a single stage continuous culture was 92 gl^-1.     

Effect of acute ethanol on beta-endorphin secretion from rat fetal hypothalamic neurons in primary cultures

To characterize the effect of ethanol on the hypothalamic beta-endorphin-containing neurons, rat fetal hypothalamic neurons were maintained in primary culture, and the secretion of beta-endorphin (beta-EP) was determined after ethanol challenges. Constant exposure to ethanol at doses of 6-50 mM produced a dose-dependent increase in basal secretion of beta-EP from these cultured cells. These doses of ethanol did not produce any significant effect on cell viability, DNA or protein content. The stimulated secretion of beta-EP following constant ethanol exposure is short-lasting. However, intermittent ethanol exposures maintained the ethanol stimulatory action on beta-EP secretion for a longer time. The magnitude of the beta-EP response to 50 mM ethanol is similar to that of the beta-EP response to 56 mM of potassium. Ethanol-stimulated beta-EP secretion required extracellular calcium and was blocked by a calcium channel blocker; a sodium channel blocker did not affect ethanol-stimulated secretion. These results suggest that the neuron culture system is a useful model for studying the cellular mechanisms involved in the ethanol-regulated hypothalamic opioid secretion.     

Production of ethanol by Clostridium thermosaccharolyticum: I. Effect of cell recycle and environmental parameters

The direct microbial conversion (DMC) process for the production of ethanol from lignocellulosic biomass is limited by low volumetric ethanol production rates due to the low cell densities of Clostridium thermosaccharolyticum which is a key organism for ethanol production in this process. Hence, this study focuses on the use of a continuous- culture cell recycle system to improve the volumetric ethanol productivity and yield of the fermentation of xylose by C. thermosaccharolyticum. Early experiments with the continuous-culture cell recycle system showed a two-fold improvement in volumetric ethanol productivity. However, the ethanol yield at the higher dilution rates suffered because of the large amount of lactate produced. The manipulation of two environmental parameters-iron concentration in the nutrient medium and the N(2) purge rate of the fermentor headspace-allowed a dramatic reduction in the lactate production and a simultaneous improvement in the ethanol titer and yield. Under the improved conditions of increased iron concentration (12.5 mg/L FeSO(4) . 7H(2)O) and decreased N(2) purge rate (0.1 L/min), a continuous culture of C. thermosaccharolyticum operating at a dilution rate of 0.24 h(-1) and 50% cell recycle produced 8.6 g/L ethanol and less than 1 g/L each of acetate and lactate. The volumetric ethanol productivity was 2.2 g/L/h, which is 8 times larger than obtained for a continuous culture operated with no cell recycle and the same specific growth rate.     

Alcohol fermentation of starch by a genetic recombinant yeast having glucoamylase activity

Alcohol fermentation of starch was investigated using a direct starch fermenting yeast, Saccharomyces cerevisiae SR93, constructed by integrating a glucoamylase-producing gene (STA1) into the chromosome of Saccharomyces cerevisiae SH1089. The glucoamylase was constitutively produced by the recombinant yeast. The ethanol concentration produced by the recombinant yeast was 14.3 g/L which was about 1.5-fold higher than by the conventional mixed culture using an amylolytic microorganism and a fermenting microorganism. About 60% of the starch was converted into ethanol by the recombinant yeast, and the ethanol yield reached its maximum value of 0.48 at the initial starch concentration of 50 g/L. The fed-batch culture, which maintains the starch concentration in the range of 30 to 50 g/L, was used to produce a large amount of ethanol from starch. The amount of ethanol produced in the fed-batch culture increased about 20% compared to the batch culture. (c) 1997 John Wiley & Sons, Inc.     

Kinetics of biphasic growth of yeast in continuous and fed-batch cultures

The influence of dilution rate on the production of biomass, ethanol, and invertase in an aerobic culture of Saccharomyces carlsbergensis was studied in a glucose-limited chemostat culture. A kinetic model was developed to analyze the biphasic growth of yeast on both the glucose remaining and the ethanol produced in the culture. The model assumes a double effect where glucose regulates the flux of glucose catabolism (respiration and aerobic fermentation) and the ethanol utilization in yeast cells. The model could successfully demonstrate the experimental results of a chemostat culture featuring the monotonic decrease of biomass concentration with an increase of dilution rate higher than 0.2 hr^?1 as well as the maximum ethanol concentration at a particular dilution rate around 0.5 hr^?1. Some supplementary data were collected from an ethanol-limited aerobic chemostat culture and a glucose-limited anaerobic chemostat culture to use in the model calculation. Some parametric constants of cell growth, ethanol production, and invertase formation were determined in batch cultures under aerobic and anaerobic states as summarized in a table in comparison with the chemostat data. Using the constants, a prediction of the optimal control of a glucose fed-batch yeast culture was conducted in connection with an experiment for harvesting a high yield of yeast cells with high invertase activity.     

Ethanol sensitivity of sporulation in Bacillus subtilis: a new tool for the analysis of the sporulation process.

The growth rate of Bacillus subtilis is lowered but the final cell yield is unchanged when certain concentrations of ethanol are present in the culture medium. At the concentration allowing growth at half-maximal rate, practically no spores are formed. Blockage of spore formation generally occurs at stage 0-I. Sensitivity to ethanol of the capacity to form spores is limited, in a nonsynchronized culture, to a period of at most 45 min around t1. Postexponential events such as excretion of certain enzymes and modification of ribonucleic acid polymerase are altered or suppressed in the presence of ethanol, possibly as the results of a physical change upon the cell membrane. In effect, ethanol is turning wild-type cells into phenocopies of spoO mutants.     

Ethanol metabolism in suspension cultured carrot cells

Ethanol production in plant tissues deprived of oxygen is a well known process. Nevertheless, little information is available on the toxic effects of ethanol on plant cells and tissues, or on the possible role of acetaldehyde, the first oxidative product of ethanol, in inducing toxic effects in plants. Data on the metabolism of ethanol in suspension cultured cells of carrot ( Daucus carola L. cv. S. Valery, cell line T22), a system highly sensitive to the presence of ethanol in the culture medium, indicate that carrot cells oxidize only small amounts of ethanol to CO₂. Instead, they convert ethanol mainly to acetaldehyde, which accumulates in the culture medium. This suggests a possible role of acetaldehyde in causing ethanol-induced injury to carrot cells.     

Ethanol increases cytochromes P450IIE, IIB1/2, and IIIA in cultured rat hepatocytes

In intact rats, ethanol treatment has been associated with increases in hepatic levels of both P450IIB1/2 and P450IIE. When rat hepatocytes were cultured on an extracellular tumor matrix (Matrigel), exposure to ethanol from 48 to 96 h in culture resulted in increases in cytochromes P450IIE, IIB1/2, and IIIA. Cytochrome P450IIE was detected immunologically and enzymatically, using two activities associated with cytochrome P450IIE, p-nitrophenol hydroxylation, and acetaminophen activation to a metabolite that binds to glutathione. The content of cytochrome P450IIE in freshly isolated cells decreased when the cells were placed in culture. Exposure of the cultured hepatocytes to ethanol from 48 to 96 h after inoculation resulted in an increase in cytochrome P450IIE compared to untreated cultured cells. In addition, in culture, the amount of enzymatically active protein after ethanol treatment was equal to that in hepatocytes freshly isolated from intact animals. Ethanol treatment resulted in increases in cytochrome P450IIB1/2 compared to untreated cells, as shown immunologically and by increased benzyloxyresorufin dealkylase activity. However, phenobarbital induced cytochrome P450IIB1/2 to higher levels, compared to ethanol. Ethanol and phenobarbital treatments both increased P450IIIA, as determined immunologically and by the amount of propoxycoumarin depropylase activity that is inhibited by triacetyloleandomycin. However, the amount of P450IIIA increased after ethanol treatment was less than that increased after treatment with dexamethasone in these cells. The ethanol-mediated increases in all four forms of cytochrome P450 in culture suggest that these increases in the intact animal result from direct effects of ethanol on the liver.     

A comparison of carbon/energy and complex nitrogen sources for bacterial sulphate-reduction: potential applications to bioprecipitation of toxic metals as sulphides

Detailed nutrient requirements were determined to maximise efficacy of a sulphate-reducing bacterial mixed culture for biotechnological removal of sulphate, acidity and toxic metals from waste waters. In batch culture, lactate produced the greatest biomass, while ethanol was more effective in stimulating sulphide production and acetate was less effective. The presence of additional bicarbonate and H₂ only marginally stimulated sulphide production. The sulphide output per unit of biomass was greatest using ethanol as substrate. In continuous culture, ethanol and lactate were used directly as efficient substrates for sulphate reduction while acetate yielded only slow growth. Glucose was utilised following fermentation to organic acids and therefore had a deleterious effect on pH. Ethanol was selected as the most efficient substrate due to cost and efficient yield of sulphide. On ethanol, the presence of additional carbon sources had no effect on growth or sulphate reduction in batch culture but the presence of complex nitrogen sources (yeast extract or cornsteep) stimulated both. Cornsteep showed the strongest effect and was also preferred on cost grounds. In continuous culture, cornsteep significantly improved the yield of sulphate reduced per unit of ethanol consumed. These results suggest that the most efficient nutrient regime for bioremediation using sulphate-reducing bacteria required both ethanol as carbon source and cornsteep as a complex nitrogen source.     

On-line measurement of ethanol with a gas-sensor-dip-electrode

Biotechnology Letters - A simple gas-sensor-dip-electrode (GSDE) for the direct measurement of ethanol in the culture broth is described. The GSDE was used for the online ethanol determination for...     

A new process for red pigment production by submerged culture of Monascus purpureus

Formation of red pigment by Monascus purpureus via diauxic growth on glucose and ethanol in submerged culture was optimized based on inoculum preparation and culture medium. A vegetative inoculum was prepared from spores grown on ethanol. The optimized culture medium was low in phosphates, and had an initial pH?of 5.5. The characteristics of Monascus purpureus grown on glucose and on ethanol were compared: the specific consumption rate of glucose (q_G) was higher than the specific consumption rate of ethanol (q_E), whereas the specific growth rate was greatest with ethanol. The specific production rate of red pigment (p_OD) and pigment yield (Y_OD/s) with glucose was twice that with ethanol. A novel fermentation process was developed with M. purpureus initially grown with controlled ethanol formation, and consumption of the latter during pigment formation.     

Isolation of ethanol-tolerant mutants of yeast by continuous selection

Summary Mutants of Saccharomyces uvarum, 5D-cyc with increased tolerance to ethanol have been isolated by a continuous selection technique which allows the culture itself to determine the intensity of selection via a feedback control circuit. The output of CO₂ from a continuous culture of the yeast was monitored using an infrared analyser and the signal from that analyser fed to a potentiometric controller which regulated the introduction of a concentrated ethanol solution into the culture vessel. The frequency of ethanol addition to the culture thus increased as the tolerance of the organisms improved.The use of this system permitted the selection of mutants of yeast which were viable in the presence of 12% w/v ethanol and which showed higher fermentation rates (as measured by CO₂ production) than the wild-type in the presence of 10% w/v ethanol and above. The technique of continuous selection with feedback should be generally applicable to the isolation of mutants of any microorganism to improved tolerance to any inhibitory condition of either its physical or chemical environment.