Production of ethanol from sugars in wood hydrolysate byFusarium oxysporum

Wood hydrolysate used for ethanol production by two strains ofFusarium oxysporum contained 2.3% (w/v) reducing sugars (xylose and glucose). Ethanol production at the optimum reducing sugar concentration of 54.8 g/l medium, at pH 5.5, and 30°C was 12.3 g/l and 11.7 g/l byF. oxysporum D-140 and NCIM-1072, respectively in shake flasks during 96 h fermentation. The maximum production of ethanol under optimum cultural conditions, and in the presence of yeast extract plus minerals, was 13.2 g/l medium byF. oxysporum D-140 over 108 h fermentation.

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Résumé L'hydrolysat de bois utilisé pour la production d'éthanol par deux souches deFusarium oxysporum contenait 2.3% (poids/vol.) de sucres réducteurs (xylose et glucose). La production d'éthanol, à la concentration optimum en sucres réducleurs de 54.8 g par litre de milieu à pH 5.5 et à 30°C était de 12.3 g/l et 11.7 g/l respectivement chezF. oxysporum D-140 et NCIM-1072, en flacons agités pendant 96 h de fermentation. La production maximum d'éthanol, dans les conditions optimum de culture, et en prosence d'extrait de levure et de minéraux a mit de 13.2 g par litre de milieu chezF. oxysporum D-140 en 108 h de lermentation.

     

Sugar fermentation by <Emphasis Type="Italic">Fusarium oxysporum</Emphasis> to produce ethanol

As a first step in the research on ethanol production from lignocellulose residues, sugar fermentation by Fusarium oxysporum in oxygen-limited conditions is studied in this work. As a substrate, solutions of arabinose, glucose, xylose and glucose/xylose mixtures are employed. The main kinetic and yield parameters of the process are determined according to a time-dependent model. The microorganism growth is characterized by the maximum specific growth rate and biomass productivity, the substrate consumption is studied through the specific consumption rate and biomass yield, and the product formation via the specific production rate and product yields. In conclusion, F. oxysporum can convert glucose and xylose into ethanol with product yields of 0.38 and 0.25, respectively; when using a glucose/xylose mixture as carbon source, the sugars are utilized sequentially and a maximum value of 0.28 g/g ethanol yield is determined from a 50% glucose/50% xylose mixture. Although fermentation performance by F.␣oxysporum is somewhat lower than that of other fermenting microorganisms, its ability for simultaneous lignocellulose-residue saccharification and fermentation is considered as a potential advantage.     

Co-fermentation of a mixture of glucose and xylose to ethanol by Zymomonas mobilis and Pachysolen tannophilus

This research was designed to maximize ethanol production from a glucose-xylose sugar mixture (simulating a sugar cane bagasse hydrolysate) by co-fermentation with Zymomonas mobilis and Pachysolen tannophilus. The volumetric ethanol productivity of Z. mobilis with 50 g glucose/l was 2.87 g/l/h, giving an ethanol yield of 0.50 g/g glucose, which is 98% of the theoretical. P. tannophilus when cultured on 50 g xylose/l gave a volumetric ethanol productivity of 0.10 g/l/h with an ethanol yield of 0.15 g/g xylose, which is 29% of the theoretical. On optimization of the co-fermentation with the sugar mixture (60 g glucose/l and 40 g xylose/l) a total ethanol yield of 0.33 g/g sugar mixture, which is 65% of the theoretical yield, was obtained. The co-fermentation increased the ethanol yield from xylose to 0.17 g/g. Glucose and xylose were completely utilized and no residual sugar was detected in the medium at the end of the fermentation. The pH of the medium was found to be a good indicator of the fermentation status. The optimum conditions were a temperature of 30°C, initial inoculation with Z. mobilis and incubation with no aeration, inactivation of bacterium after the utilization of glucose, followed by inoculation with P. tannophilus and incubation with limited aeration.     

Study of a single and mixed culture for the direct bio-conversion of sorghum carbohydrates to ethanol

Fusaium oxysporum F3 alone or in mixed culture with Saccharomyces cerevisiae 2541 fermented soluble and insoluble carbohydrates of sweet sorghum stalk directly to ethanol. Both microorganisms were first grown aerobically and fermented sorghum stalk to ethanol thereafter. During fermentation, insoluble carbohydrates were hydrolysed to soluble sugars by the celluloytic system of F. oxysporum. Ethanol yields as high as 24.4 and 33.5 g/100 g dry stalks were obtained by F. oxysporum and the mixed culture respectively, representing a theoretical yield enhancement of 11.6% and 53.6% respectively. The corresponding ethanol concentrations in the fermentation medium were 4.6% and 6.4% (w/v). These results clearly demonstrated that a large portion of insoluble carbohydrate from sorghum was converted by simultaneous saccharification and fermentation to ethanol, making the process promising for bioethanol production.     

High-level production of ethanol during fed-batch ethanol fermentation with a controlled aeration rate and non-sterile glucose powder feeding of Saccharomyces cerevisiae

In this study, we utilized a unique strategy for fed-batch fermentation using ethanol-tolerant Saccharomyces cerevisiae to achieve a high-level of ethanol production that could be practically applied on an industrial scale. During this study, the aeration rate was controlled at 0.0, 0.13, 0.33, and 0.8 vvm to determine the optimal aeration conditions for the production of ethanol. Additionally, non-sterile glucose powder was fed during fed-batch ethanol fermentation and corn-steep liquor (CSL) in the medium was used as an organic N-source. When aeration was conducted, the ethanol production and productivity were superior to that when aeration was not conducted. Specifically, the maximum ethanol production reached approximately 160 g/L, when the fermentor was aerated at 0.13 vvm. These findings indicate that the use of a much less expensive C-source may enable the fermentation process to be directed towards the improvement of overall ethanol production and productivity in fermentors that are aerated at 0.13 vvm. Furthermore, if a repeated fed-batch process in which the withdrawal and fill is conducted prior to 36 h can be employed, aeration at a rate of 0.33 and/or 0.8 vvm may improve the overall ethanol productivity     

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.     

Improved bioethanol production through simultaneous saccharification and fermentation of lignocellulosic agricultural wastes by <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> 6556

The combined effect of simultaneous saccharification and fermentation and separate hydrolysis and fermentation (SHF) for ethanol production by Kluyveromyces marxianus 6556 was studied using two lignocellulosic feedstocks viz., corncob and soybean cake. The ethanologenic efficiency of K. marxianus 6556 was observed as 28% (theoretical yield) in a fermentation medium containing glucose, but, there was no ethanol production by cells grown on xylose. A maximum sugar release of 888 mg/g corncob and 552 mg/g soybean cake was achieved through acid hydrolysis pretreatment. Furthermore, corncob and soybean cake treated with commercial cellulase (100 IU for 48 h) from Trichoderma reesei yielded reducing sugars of 205 and 100 mg/g, respectively. Simultaneous saccharification and fermentation resulted in highest ethanol production of 5.68 g/l on corncob and 2.14 g/l on soybean cake after 48 h of incubation. On the contrary, the presence of inhibitors decreased the overall ethanol yield in the hydrolysates obtained through SHF of corncob and soybean cake.     

Aeration alleviates ethanol inhibition and glycerol production during fed-batch ethanol fermentation

In this study, we investigated the effects of aeration on ethanol inhibition and glycerol production during fed-batch ethanol fermentation. When aeration was conducted at 0.13, 0.33, and 0.8 vvm, the ethanol productivity, specific ethanol production rate, and ethanol yield in the presence of greater than 100 g/L of ethanol were higher than when aeration was not conducted. In addition, estimation of the parameters (α and β) in a model equation of ethanol inhibition kinetics indicated that aeration alleviated ethanol inhibition against the specific growth rate and the specific ethanol production rate. Specifically, when aeration was conducted, the glycerol yield and specific glycerol production rate decreased approximately 50 and 70%, respectively. Finally, the results of this study indicated that aeration during fed-batch ethanol fermentation may improve the ethanol concentration in the final culture broth, as well as the ethanol productivity.     

Controlling accumulation of fermentation inhibitors in biorefinery recycle water using microbial fuel cells

Background  

Microbial fuel cells (MFC) and microbial electrolysis cells are electrical devices that treat water using microorganisms and convert soluble organic matter into electricity and hydrogen, respectively. Emerging cellulosic biorefineries are expected to use large amounts of water during production of ethanol. Pretreatment of cellulosic biomass results in production of fermentation inhibitors which accumulate in process water and make the water recycle process difficult. Use of MFCs to remove the inhibitory sugar and lignin degradation products from recycle water is investigated in this study.     

Insights from the Fungus Fusarium oxysporum Point to High Affinity Glucose Transporters as Targets for Enhancing Ethanol Production from Lignocellulose

Ethanol is the most-widely used biofuel in the world today. Lignocellulosic plant biomass derived from agricultural residue can be converted to ethanol via microbial bioprocessing. Fungi such as Fusarium oxysporum can simultaneously saccharify straw to sugars and ferment sugars to ethanol. But there are many bottlenecks that need to be overcome to increase the efficacy of microbial production of ethanol from straw, not least enhancement of the rate of fermentation of both hexose and pentose sugars. This research tested the hypothesis that the rate of sugar uptake by F. oxysporum would enhance the ethanol yields from lignocellulosic straw and that high affinity glucose transporters can enhance ethanol yields from this substrate. We characterized a novel hexose transporter (Hxt) from this fungus. The F. oxysporum Hxt represents a novel transporter with homology to yeast glucose signaling/transporter proteins Rgt2 and Snf3, but it lacks their C-terminal domain which is necessary for glucose signalling. Its expression level decreased with increasing glucose concentration in the medium and in a glucose uptake study the Km_(glucose) was 0.9 mM, which indicated that the protein is a high affinity glucose transporter. Post-translational gene silencing or over expression of the Hxt in F. oxysporum directly affected the glucose and xylose transport capacity and ethanol yielded by F. oxysporum from straw, glucose and xylose. Thus we conclude that this Hxt has the capacity to transport both C5 and C6 sugars and to enhance ethanol yields from lignocellulosic material. This study has confirmed that high affinity glucose transporters are ideal candidates for improving ethanol yields from lignocellulose because their activity and level of expression is high in low glucose concentrations, which is very common during the process of consolidated processing.     

Optimization of process parameters for ethanol production from sugar cane molasses by Zymomonas mobilis using response surface methodology and genetic algorithm

Ethanol is a potential energy source and its production from renewable biomass has gained lot of popularity. There has been worldwide research to produce ethanol from regional inexpensive substrates. The present study deals with the optimization of process parameters (viz. temperature, pH, initial total reducing sugar (TRS) concentration in sugar cane molasses and fermentation time) for ethanol production from sugar cane molasses by Zymomonas mobilis using Box–Behnken experimental design and genetic algorithm (GA). An empirical model was developed through response surface methodology to analyze the effects of the process parameters on ethanol production. The data obtained after performing the experiments based on statistical design was utilized for regression analysis and analysis of variance studies. The regression equation obtained after regression analysis was used as a fitness function for the genetic algorithm. The GA optimization technique predicted a maximum ethanol yield of 59.59 g/L at temperature 31 °C, pH 5.13, initial TRS concentration 216 g/L and fermentation time 44 h. The maximum experimental ethanol yield obtained after applying GA was 58.4 g/L, which was in close agreement with the predicted value.     

The effect of aeration on xylose fermentation by Candida shehatae and Pachysolen tannophilus

Summary The ability of a Candida shehatae and a Pachysolen tannophilus strain to ferment D-xylose to ethanol was evaluated in defined and complex media under different levels of aeration. Aeration enhanced the ethanol productivity of both yeasts considerably. C. shehatae maintained a higher fermentation rate and ethanol yield than P. tannophilus over a wide range of aeration levels. Ethanol production by C. shehatae commenced during the early stage of the fermentation, whereas with P. tannophilus there was a considerable lag between the initiation of growth and ethanol production. Both yeasts produced appreciable quantities of xylitol late in the fermentation. P. tannophilus failed to grow under anoxic conditions, producing a maximum of only 0.5 g · l^-1 ethanol. In comparison, C. shehatae exhibited limited growth in anoxic cultures, and produced ethanol much more rapidly. Under the condition of aeration where C. shehatae exhibited the highest ethanol productivity, the fermentation parameters were: maximum specific growth rate, 0.15 h^-1; maximum volumetric and specific rates of ethanol production, 0.7 g (l · h)^-1 and 0.34 g ethanol (g cells · h)^-1 respectively; ethanol yield, 0.36 g (g xylose)^-1. The best values obtained with P. tannophilus were: maximum specific growth rate, 0.14 h^-1; maximum volumetric and specific rates of ethanol production, 0.22 g (l · h)^-1 and 0.07 h^-1 respectively; ethanol yield coefficient, 0.28. Because of its higher ethanol productivity at various levels of aeration, C. shehatae has a greater potential for ethanol production from xylose than P. tannophilus.     

Arabinose and xylose fermentation by recombinant Saccharomyces cerevisiae expressing a fungal pentose utilization pathway

Background  

Sustainable and economically viable manufacturing of bioethanol from lignocellulose raw material is dependent on the availability of a robust ethanol producing microorganism, able to ferment all sugars present in the feedstock, including the pentose sugars L-arabinose and D-xylose. Saccharomyces cerevisiae is a robust ethanol producer, but needs to be engineered to achieve pentose sugar fermentation.     

Ethanol production from d-xylose in batch fermentations with Candida shehatae: process variables

Summary These studies examined several process variables important in scaling up the fermentation of xylose by Candida shehatae. Inoculum age and cell density were particularly influential. Young (24-h) inocula fermented xylose to ethanol two to three times as fast as older (48- or 72-h) inocula. With all three inocula ages, the initial fermentation rates were essentially linear with cell density, up to 4 g dry wt cells L^-1. Above that cell density, the ethanol production rate appeared to be oxygen limited, particularly with 24-h old cells. Aeration also played a role in xylose utilization. The fermentation proceeded under both aerobic and anaerobic conditions, but xylose was not completely utilized anaerobically. With aeration, 25% more ethanol was formed in about one third the time than without aeration. Ethanol yields were similar under the two conditions. Cell growth on xylose was observed in the absence of oxygen. Cells went through essentially one doubling in 24 h. Based on the sugar consumed, a Y _ATP of 9.9 was obtained. Slow continuous feeding of glucose significantly increased the xylose utilization rate.Maintained in cooperation with the University of Wisconsin, Madison, Wisconsin, USA     

Aeration strategy: a need for very high ethanol performance in<Emphasis Type="Italic"> Saccharomyces cerevisiae</Emphasis> fed-batch process

In order to identify an optimal aeration strategy for intensifying bio-fuel ethanol production in fermentation processes where growth and production have to be managed simultaneously, we quantified the effect of aeration conditions—oxygen limited vs non limited culture (micro-aerobic vs aerobic culture)—on the dynamic behaviour of Saccharomyces cerevisiae cultivated in very high ethanol performance fed-batch cultures. Fermentation parameters and kinetics were established within a range of ethanol concentrations (up to 147 g l^–1), which very few studies have addressed. Higher ethanol titres (147 vs 131 g l^–1 in 45 h) and average productivity (3.3 vs 2.6 g l^–1 h^–1) were obtained in cultures without oxygen limitation. Compared to micro-aerobic culture, full aeration led to a 23% increase in the viable cell mass as a result of the concomitant increase in growth rate and yield, with lower ethanol inhibition. The second beneficial effect of aeration was better management of by-product production, with production of glycerol, the main by-product, being strongly reduced from 12 to 4 g l^–1. We demonstrate that aeration strategy is as much a determining factor as vitamin feeding (Alfenore et al. 2002) in very high ethanol performance (147 g l^–1 in 45 h) in order to achieve a highly competitive dynamic process.     

The physiological characteristics of the yeast Dekkera bruxellensis in fully fermentative conditions with cell recycling and in mixed cultures with Saccharomyces cerevisiae

The yeast Dekkera bruxellensis plays an important role in industrial fermentation processes, either as a contaminant or as a fermenting yeast. In this study, an analysis has been conducted of the fermentation characteristics of several industrial D. bruxellensis strains collected from distilleries from the Southeast and Northeast of Brazil, compared with Saccharomyces cerevisiae. It was found that all the strains of D. bruxellensis showed a lower fermentative capacity as a result of inefficient sugar assimilation, especially sucrose, under anaerobiosis, which is called the Custer effect. In addition, most of the sugar consumed by D. bruxellensis seemed to be used for biomass production, as was observed by the increase of its cell population during the fermentation recycles. In mixed populations, the surplus of D. bruxellensis over S. cerevisiae population could not be attributed to organic acid production by the first yeast, as previously suggested. Moreover, both yeast species showed similar sensitivity to lactic and acetic acids and were equally resistant to ethanol, when added exogenously to the fermentation medium. Thus, the effects that lead to the employment of D. bruxellensis in an industrial process and its effects on the production of ethanol are multivariate. The difficulty of using this yeast for ethanol production is that it requires the elimination of the Custer effect to allow an increase in the assimilation of sugar under anaerobic conditions.     

Simultaneous saccharification and fermentation of cellulose by Fusarium oxysporum F3—growth characteristics and metabolite profiling

The simultaneous saccharification and fermentation (SSF) of cellulose by Fusarium oxysporum was investigated in the present study. It was found that F. oxysporum grow with a maximum specific growth rate of 0.023 h⁻¹ on cellulose at aerobic conditions and that it can produce ethanol with a volumetric productivity of 0.044 g/L/h and a yield of 0.35 g/g cellulose under anaerobic conditions. The cellulase system in F. oxysporum is well balanced as no cellobiose accumulated. The profile of the phosphorylated intermediates from Pentose Phosphate Pathway (PPP), Embden–Meyerhof–Parnas Pathway (EMP) and the key intermediates of the glycolytic pathway as well as extracellular organic and amino acids were determined during the fermentation in order to investigate the potential metabolic bottlenecks of the process. The high levels of intracellular glucose-1,6-DP a metabolic downstream of phoshoglucomutase also indicates limiting activities of this enzyme and difficulty of glucose to be channelled into biosynthetic and glycolytic pathways. The presence of high levels of γ-aminobutyrate (GABA) under anaerobic conditions suggests a functional GABA bypass and possible block in the Krebs cycle.     

Development of a fermentation method using immobilized cells under unsterile conditions. 2. Ethanol andl-lactic acid production without heat and filter sterilization

A process that was developed for protection of immobilized cells against inhibitory substances in the fermentation medium was applied for ethanol and lactic acid production with neither sterilization of the media, fermentor and other apparatus nor filtration of the aeration gas. The process involves co-immobilization of the fermentation micro-organism with castor oil and suppression of contaminant growth by addition of an anti-microbial substance to the fermentation medium. When 0.1%n-butyl,p-hydroxybenzoate (POBB) was added to the medium, ethanol and lactic acid productions were stable for 60 h and 70 h, respectively, while growth of the contaminants was completely suppressed. Longer process stability was achieved when POBB was replaced with Preventol GD, which has higher partition coefficient between castor oil and water. In this case, both glucose consumption and ethanol production were stable for 140 h. The possibilities of increasing the process stabilities were discussed.     

Production of fuel ethanol from bamboo by concentrated sulfuric acid hydrolysis followed by continuous ethanol fermentation

An efficient process for the production of fuel ethanol from bamboo that consisted of hydrolysis with concentrated sulfuric acid, removal of color compounds, separation of acid and sugar, hydrolysis of oligosaccharides and subsequent continuous ethanol fermentation was developed. The highest sugar recovery efficiency was 81.6% when concentrated sulfuric acid hydrolysis was carried out under the optimum conditions. Continuous separation of acid from the saccharified liquid after removal of color compounds with activated carbon was conducted using an improved simulated moving bed (ISMB) system, and 98.4% of sugar and 90.5% of acid were recovered. After oligosaccharide hydrolysis and pH adjustment, the unsterilized saccharified liquid was subjected to continuous ethanol fermentation using Saccharomycescerevisiae strain KF-7. The ethanol concentration, the fermentation yield based on glucose and the ethanol productivity were approximately 27.2 g/l, 92.0% and 8.2 g/l/h, respectively. These results suggest that the process is effective for production of fuel ethanol from bamboo.     

Expression of Vitreoscilla Hemoglobin Enhances Cell Growth and Dihydroxyacetone Production in Gluconobacter oxydans

Dihydroxyacetone (DHA) is an important ketose sugar, which is extensively used in the cosmetic, chemical, and pharmaceutical industries. DHA has been industrially produced by Gluconobacter oxydans with a high demand of oxygen. To improve the production of DHA, the gene vgb encoding Vitreoscilla hemoglobin (VHb) was successfully introduced into G. oxydans, where it was stably maintained, and expressed at about 76.0 nmol/g dry cell weight. Results indicated that the constitutively expressed VHb improved cell growth and DHA production in G. oxydans under different aeration conditions. Especially at low aeration rates, the VHb-expressing strain (VHb⁺) displayed 23.13% more biomass and 37.36% more DHA production than those of VHb-free strain (VHb⁻) after 32 h fermentation in bioreactors. In addition, oxygen uptake rate (OUR) was also increased in VHb⁺ strain relative to the control strain during fermentation processes.