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.     

Osmotic adjustment of Zymomonas mobilis to concentrated glucose solutions

Summary The physiological basis of the exceptionally high sugar tolerance of Zymomonas mobilis was investigated. Determinations of the internal metabolite concentrations of Z. mobilis showed that an increase in the extracellular glucose concentration was accompanied by a parallel rise in the intracellular glucose concentration, bringing about an almost complete osmotic balance between internal and external space. Studies of glucose transport confirmed that Z. mobilis has a facilitated diffusion system which enables a rapid equilibration between internal and external glucose concentrations. Studies using the non-metabolisable sugars maltose (impermeable) and xylose (permeable) revealed that these sugars were able to alter the osmotic pressure on the cytoplasmic membrane resulting in volume changes.Dedicated to Professor R. K. Finn on the occasion of his 70th birthday     

Effect of <Emphasis Type="Italic">m</Emphasis>-carbonyl cyanide 3-chlorophenylhydrazone on inorganic polyphosphates synthesis in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> under different growth conditions

The effects of different concentrations of the protonophore uncoupler m-carbonyl cyanide 3-hchlorophenylhydrazone (CCCP) on the synthesis of inorganic polyphosphates (polyP) during the first 0.5 h of hypercompensation in the yeast Saccharomyces cerevisiae VKM Y-1173 growing on media with 2% glucose under low (hypoxia) or high aeration or with 1% (vol/vol) ethanol under high aeration were studied. It was shown that the yeast growth on ethanol was completely inhibited by 5 μM CCCP, while growth on glucose was inhibited by 25 μM CCCP, independently of aeration of the medium. The maximum rate of H2 absorption was shown at 2, 5, and 25 μM CCCP for the cells grown on ethanol, on glucose under high aeration, and on glucose under hypoxia, respectively. Against the decrease of total ATP level and total polyP, CCCP had a nonuniform effect on the synthesis of individual polyP fractions. CCCP maximally inhibited synthesis of the most actively formed fractions: polyPI during growth on glucose under hypoxia, polyPIII during growth on glucose under aeration, and polyPIII and polyPV during growth on ethanol. CCCP had no substantial effect on the synthesis of polyPII and polyPIV fractions, the formation of which seems to be less related to the electrochemical potential gradient of H⁺ ions.     

Continuous production of gluconic acid by immobilized Gluconobacter oxydans cell bioreactor

Summary Living Gluconobacter oxydans cells were attached on fibrous nylon carrier. Free gluconic acid was directly continuously produced in an aerated tubular immobilized-cell bioreactor for at least 6 months, with a volumetric productivity of at least 5 g/lh at 100 g/l substrate glucose and about 80 g/l product gluconic acid concentrations. The highest volumetric productivity in respect to glucose concentration was obtained with 175 g/l glucose, with about 120 g/l product gluconic acid level. With self-directing optimization procedure in respect to maximum product gluconic acid level, productivities as high as about 12–15 g/lh were obtained at relatively high substrate feed rate of 0.166 l/lh and relatively low aeration rate of 0.5 l/lmin. The highest glucose conversion of about 96% was obtained with a long residence time, at the lowest substrate feed rate used at a relatively low aeration rate, resulting however in a significant increase in ketogluconic acid production.     

Comparative investigation of fine bubble and macrobubble aeration on gas utility and biotransformation productivity

The sufficient provision of oxygen is mandatory for enzymatic oxidations in aqueous solution, however, in process optimization this still is a bottleneck that cannot be overcome with the established methods of macrobubble aeration. Providing higher mass transfer performance through microbubble aerators, inefficient aeration can be overcome or improved. Investigating the mass transport performance in a model protein solution, the microbubble aeration results in higher k_La values related to the applied airstream in comparison with macrobubble aeration. Comparing the aerators at identical k_La of 160 and 60 1/h, the microbubble aeration is resulting in 25 and 44 times enhanced gas utility compared with aeration with macrobubbles. To prove the feasibility of microbubbles in biocatalysis, the productivity of a glucose oxidase catalyzed biotransformation is compared with macrobubble aeration as well as the gas‐saving potential. In contrast to the expectation that the same productivities are achieved at identically applied k_La, microbubble aeration increased the gluconic acid productivity by 32% and resulted in 41.6 times higher oxygen utilization. The observed advantages of microbubble aeration are based on the large volume‐specific interfacial area combined with a prolonged residence time, which results in a high mass transfer performance, less enzyme deactivation by foam formation, and reduced gas consumption. This makes microbubble aerators favorable for application in biocatalysis.     

New Bacillus thuringiensis strain isolated from the gut of Malabari goat is effective against Tetranychus macfarlanei

This study illustrates a novel strain (designated as BPU5) of Bacillus thuringiensis (Bt) isolated from the rumen of Malabari goat, capable of producing polymorphic δ‐endotoxin crystals concomitantly with sporulation in Luria–Bertani medium (LB), and the δ‐endotoxin was efficient to combat Tetranychus macfarlanei, a devastating mite. Polymorphic δ‐endotoxin crystals produced were assessed by scanning electron microscopy and monitored its production concomitantly with sporulation in LB with or without sugar supplements. Toxicity of the δ‐endotoxin was assessed on T. macfarlanei using leaf disc bioassay method. Mortality rate was determined by comparing the survival of mites on the diet (prepared in 10% sucrose and powdered rice husk) containing different concentrations (1–10 mg/ml) of 72‐h‐old crude pellet (dried mixture of δ‐endotoxin (17 mg/g pellet), endospores and a few vegetative cells) or control diet with autoclaved pellet. The maximum production (1.39 mg/ml) of δ‐endotoxin was observed at 72 h in LB. Among the sugars (glucose, sucrose, maltose or lactose) tested as additional carbon source, glucose (8 g/l) enhanced (1.82 mg/ml) the production of δ‐endotoxin by 30%. The lethal concentration (LC₅₀) required to kill 50% mites was estimated as 8.024 mg/ml. The δ‐endotoxin produced by B. thuringiensis BPU5 is shown to efficiently combat T. macfarlanei, a devastating mite infesting agricultural fields.     

Induction of microcin B17 formation in Escherichia coli ZK650 by limitation of oxygen and glucose is independent of glucose consumption rate

We examined the consumption of glucose from the media in which Escherichia coli ZK650 was grown. This organism, which produces the polypeptide antibiotic microcin B17 best under conditions of limiting supplies of glucose and air, was grown with a low level of glucose (0.5 mg/ml) as well as a high level (5.0 mg/ml) under both high and low aeration. Glucose consumption rates were virtually identical under both high and low aeration. Thus, glucose consumption rate is not a regulating factor in microcin B17 formation. Journal of Industrial Microbiology & Biotechnology (2001) 26, 341–344. Received 25 September 2000/ Accepted in revised form 16 April 2001     

The role of malic acid in the metabolism of Schizosaccharomyces pombe: substrate consumption and cell growth

Summary The effect of initial concentrations of malate varying from 0 to 28.6 g/l was studied. The acid was found to be inhibitory for growth of Schizosaccharomyces pombe but not for its deacidification activity. Malate was never integrated into biomass but partly transformed into ethanol if the aeration rate was weak (oxygen limitation). In the absence of glucose, resting cells of S. pombe were able to degrade malic acid if their concentration was sufficient, but their viability gradually decreased. However, for 0.15 g/l of growing cells (inoculum) 6 g/l of glucose was necessary to consume 8 g/l of malate. When the medium did not contain sugar no growth was observed despite the partial consumption of malate, showing that the acid was neither a carbon source nor an energy source. Offprint requests to: P. Strehaiano     

The amino‐terminal tail of Hxt11 confers membrane stability to the Hxt2 sugar transporter and improves xylose fermentation in the presence of acetic acid

Hxt2 is a glucose repressed, high affinity glucose transporter of the yeast Saccharomyces cerevisiae and is subjected to high glucose induced degradation. Hxt11 is a sugar transporter that is stably expressed at the membrane irrespective the sugar concentration. To transfer this property to Hxt2, the N‐terminal tail of Hxt2 was replaced by the corresponding region of Hxt11 yielding a chimeric Hxt11/2 transporter. This resulted in the stable expression of Hxt2 at the membrane and improved the growth on 8% d ‐glucose and 4% d ‐xylose. Mutation of N361 of Hxt11/2 into threonine reversed the specificity for d ‐xylose over d ‐glucose with high d ‐xylose transport rates. This mutant supported efficient sugar fermentation of both d ‐glucose and d ‐xylose at industrially relevant sugar concentrations even in the presence of the inhibitor acetic acid which is normally present in lignocellulosic hydrolysates. Biotechnol. Bioeng. 2017;114: 1937–1945. © 2017 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.     

Polyalcohol Production by Pichia miso in a Jar Fermentor

Cultural conditions for polyalcohol production by Pichia miso were examined in Waldhof type 20 liter-fermentor scale. The best result was obtained under conditions where the aeration rate was 1 volume per volume of the medium per minute with the stirring rate of 500r.p.m., (Kd=5×l0^-6 [g-mol of O₂/atm. min. ml.]); in 5 days incubation, Pichia miso completely dissimilated the glucose of a high concentration, 30%, and produced glycerol, D-arabitol and erythritol in a very high yield, 50% of sugar consumed. The greatest advantage compared with the shake flask culture is that the required fermentation time is shortened to half.     

Root Respiration and Carbohydrate Status of Two Wheat Genotypes in Response to Hypoxia

To investigate root respiration and carbohydrate status in relationto waterlogging or hypoxia tolerance, root respiration rateand concentrations of soluble sugars in leaves and roots weredetermined for two wheat (Triticum aestivum L.) genotypes differingin waterlogging-tolerance under hypoxia (5% O₂) and subsequentresumption of full aeration. Root and shoot growth were reducedby hypoxia to a larger extent for waterlogging-sensitive Coker9835. Root respiration or oxygen consumption rate declined withhypoxia, but recovered after 7 d of resumption of aeration.Respiration rate was greater for sensitive Coker 9835 than fortolerant Jackson within 8 d after hypoxia. The concentrationsof sucrose, glucose and fructose decreased in leaves for bothgenotypes under hypoxia. The concentration of these sugars inroots, however, increased under hypoxia, to a greater degreefor Jackson. An increase in the ratio of root sugar concentrationto shoot sugar concentration was found for Jackson under hypoxicconditions, suggesting that a large amount of carbohydrate waspartitioned to roots under hypoxia. The results indicated thatroot carbohydrate supply was not a limiting factor for rootgrowth and respiration under hypoxia. Plant tolerance to waterloggingof hypoxia appeared to be associated with low root respirationor oxygen consumption rate and high sugar accumulation underhypoxic conditions.Copyright 1995, 1999 Academic Press Oxygen consumption rate, sugar accumulation, Triticum aestivum L., waterlogging tolerance     

Studies on the growth, modelling and pigment production by the yeast Phaffia rhodozyma during fed-batch cultivation

Summary As Phaffia rhodozyma is a Crabtree positive yeast, its cell yield and pigment production are reduced at high sugar concentrations. A method for maintaining low growth medium sugar concentrations is fed-batch culture. Using a mass balance approach and Monod growth kinetics a model is presented which describes the fed-batch culture of Phaffia rhodozyma and enables the calculation of a feed regime to obtain the maximum yield of cells and pigment. Although developed on a glucose medium, the model was also applied successfully to a molasses-based medium.     

Evidence for trehalose-6-phosphate-dependent and -independent mechanisms in the control of sugar influx into yeast glycolysis

In the yeast Saccharomyces cerevisíae, trehalose-6-phosphate (tre-6-P) synthase encoded by GGS1/TPS1, is not only involved in the production of trehalose but also in restriction of sugar influx into glycolysis in an unknown fashion; it is therefore essential for growth on glucose or fructose. In this work, we have deleted the TPS2 gene encoding tre-6-P phosphatase in a strain which displays very low levels of Ggs1/Tps1, as a result of the presence of the byp1-3 allele of GGS1/TPS1. The byp1-3 tps2Δ double mutant showed elevated tre-6-P levels along with improved growth and ethanol production, although the estimated concentrations of glycolytic metabolites indicated excessive sugar influx. In the wild-type strain, the addition of glucose caused a rapid transient increase of tre-6-P. In tps2^Δ mutant cells, which showed a high tre-6-P level before glucose addition, sugar influx into glycolysis appeared to be diminished. Furthermore, we have confirmed that tre-6-P inhibits the hexokinases in vitro. These data are consistent with restriction of sugar influx into glycolysis through inhibition of the hexokinases by tre-6-P during the switch to fermentative metabolism. During logarithmic growth on glucose the tre-6-P level in wild-type cells was lower than that of the byp1-3 tps2Δ. mutant. However, the latter strain arrested growth and ethanol production on glucose after about four generations. Hence, other mechanisms, which also depend on Ggs1/Tps1, appear to control sugar influx during growth on glucose. In addition, we provide evidence that the requirement for Ggs1/Tps1 for sporulation may be unrelated to its involvement in trehalose metabolism or in the system controlling glycolysis.     

The role of aeration and agitation in the production of glucose oxidase in submerged culture. II

The main purpose of the work reported here was to establish the effectiveness of aeration and agitation, and to determine the best conditions of aeration for the growth and production of glucose oxidase of Aspergillus niger, on a semi-industrial scale. Concentration of dissolved O₂, O₂ consumption and CO₂ production were measured. It was found that the rate of growth and the activity of glucose oxidase per gram mycelium increased with the increase of speed of agitation. The concentration of dissolved oxygen of the fermentation broth, as well as the rate of respiration (O₂ consumption and CO₂ production) increased in direct proportion to the increase of speed of agitation, while assimilation of sugars was accelerated. The values of the respiratory ratio showed a fluctuation according to the presence or absence of sugar in the medium.     

Heterologous expression of the apple hexose transporter MdHT2.2 altered sugar concentration with increasing cell wall invertase activity in tomato fruit

Sugar transporters are necessary to transfer hexose from cell wall spaces into parenchyma cells to boost hexose accumulation to high concentrations in fruit. Here, we have identified an apple hexose transporter (HTs), MdHT2.2, located in the plasma membrane, which is highly expressed in mature fruit. In a yeast system, the MdHT2.2 protein exhibited high ¹⁴C‐fructose and ¹⁴C‐glucose transport activity. In transgenic tomato heterologously expressing MdHT2.2, the levels of both fructose and glucose increased significantly in mature fruit, with sugar being unloaded via the apoplastic pathway, but the level of sucrose decreased significantly. Analysis of enzyme activity and the expression of genes related to sugar metabolism and transport revealed greatly up‐regulated expression of SlLIN5, a key gene encoding cell wall invertase (CWINV), as well as increased CWINV activity in tomatoes transformed with MdHT2.2. Moreover, the levels of fructose, glucose and sucrose recovered nearly to those of the wild type in the sllin5‐edited mutant of the MdHT2.2‐expressing lines. However, the overexpression of MdHT2.2 decreased hexose levels and increased sucrose levels in mature leaves and young fruit, suggesting that the response pathway for the apoplastic hexose signal differs among tomato tissues. The present study identifies a new HTs in apple that is able to take up fructose and glucose into cells and confirms that the apoplastic hexose levels regulated by HT controls CWINV activity to alter carbohydrate partitioning and sugar content.     

The influence of type and concentration of the carbon source on production of citric acid by Aspergillus niger

Summary The influence of various carbon sources and their concentration on the production of citrate by Aspergillus niger has been investigated. The sugars maltose, sucrose, glucose, mannose and fructose (in the given order) were carbon sources giving high yields of citric acid. Optimal yields were observed at sugar concentrations of 10% (w/v), with the exception of glucose (7.5%). No citric acid was produced on media containing less than 2.5% sugar. Precultivation of A. niger on 1% sucrose and transference to a 14% concentration of various other sugars induced citrate accumulation. This could be blocked by the addition of cycloheximide, an inhibitor of de novo protein synthesis. This induction was achieved using maltose, sucrose, glucose, mannose and fructose, and also by some other carbon sources (e.g. glycerol) that gave no citric acid accumulation in direct fermentation. Precultivation of A. niger at high (14%) sucrose concentrations and subsequent transfer to the same concentrations of various other carbohydrates, normally not leading to citric acid production, led to formation of citrate. Endogenous carbon sources were also converted to citrate under these conditions. A 14%-sucrose precultivated mycelium continued producing some citrate upon transfer to 1% sugar. These results indicate that high concentrations of certain carbon sources are required for high citrate yields, because they induce the appropriate metabolic imbalance required for acidogenesis.     

Derepression of a baker's yeast strain for maltose utilization is associated with severe deregulation of HXT gene expression

Aims: We undertook to improve an industrial Saccharomyces cerevisiae strain by derepressing it for maltose utilization in the presence of high glucose concentrations. Methods and Results: A mutant was obtained from an industrial S. cerevisiae strain following random UV mutagenesis and selection on maltose/5‐thioglucose medium. The mutant acquired the ability to utilize glucose simultaneously with maltose and possibly also sucrose and galactose. Aerobic sugar metabolism was still largely fermentative, but an enhanced respirative metabolism resulted in a 31% higher biomass yield on glucose. Kinetic characterization of glucose transport in the mutant revealed the predominance of the high‐affinity component. Northern blot analysis showed that the mutant strain expresses only the HXT6/7 gene irrespective of the glucose concentration in the medium, indicating a severe deregulation in the induction/repression pathways modulating HXT gene expression. Interestingly, maltose‐grown cells of the mutant display inverse diauxy in a glucose/maltose mixture, preferring maltose to glucose. Conclusion: In the mutant here reported, the glucose transport step seems to be uncoupled from downstream regulation, because it seems to be unable to sense abundant glucose, via both repression and induction pathways. Significance and Impact of the Study: We report here the isolation of a S. cerevisiae mutant with a novel derepressed phenotype, potentially interesting for the industrial fermentation of mixed sugar substrates.     

1,3-Propanediol production in a two-step process fermentation from renewable feedstock

In this work, the production of 1,3-propanediol from glucose and molasses was studied in a two-step process using two recombinant microorganisms. The first step of the process is the conversion of glucose or other sugar into glycerol by the metabolic engineered Saccharomyces cerevisiae strain HC42 adapted to high (>200 g l⁻¹) glucose concentrations. The second step, carried out in the same bioreactor, was performed by the engineered strain Clostridium acetobutylicum DG1 (pSPD5) that converts glycerol to 1,3-propanediol. This two-step strategy led to a flexible process, resulting in a 1,3-propanediol production and yield that depended on the initial sugar concentration. Below 56.2 g l⁻¹ of sugar concentration, cultivation on molasses or glucose showed no significant differences. However, at higher molasses concentrations, glycerol initially produced by yeast could not be totally converted into 1,3-propanediol by C. acetobutylicum and a lower 1,3-propanediol overall yield was observed. In our hand, the best results were obtained with an initial glucose concentration of 103 g l⁻¹, leading to a final 1,3-propanediol concentration of 25.5 g l⁻¹, a productivity of 0.16 g l⁻¹ h⁻¹ and 1,3-propanediol yields of 0.56 g g⁻¹ glycerol and 0.24 g g⁻¹ sugar, which is the highest value reported for a two-step process. For an initial sugar concentration (from molasses) of 56.2 g l⁻¹, 27.4 g l⁻¹ of glycerol were produced, leading to 14.6 g l⁻¹ of 1.3-propanediol and similar values of productivity, 0.15 g l⁻¹ h⁻¹, and overall yield, 0.26 g g⁻¹ sugar.     

Influence of sugar source (lactose,glucose, galactose) on 2,3-butanediol production by Klebsiella oxytoca NRRL-B199

The ability of Klebsiella oxytoca NRRL-B199 to use either lactose or the mixture of glucose and galactose as substrate for the production of 2,3-butanediol was studied in batch fermentations with different conditions of aeration and pH. 2,3-butanediol was undetected, or present in minute concentration in the fermentation broths with lactose, while it was the main product from glucose+galactose with final concentrations of up to 18.8 g/l in media at pH 6.0. Under conditions optimal for 2,3-butanediol synthesis, when aeration limited growth, the rate of biomass growth was more tightly related to the aeration rate in lactose medium than in glucose+galactose medium. These relations suggest that the growth rate is very low on lactose but still considerable on glucose+galactose when aeration rate tends toward zero. Correspondingly, the metabolism is more oxidative in the former medium, yielding mainly acetate as product.Abbreviations CDW cell dry weight     

Improvement of <Emphasis Type="Italic">Escherichia coli</Emphasis> production strains by modification of the phosphoenolpyruvate:sugar phosphotransferase system

The application of metabolic engineering in Escherichia coli has resulted in the generation of strains with the capacity to produce metabolites of commercial interest. Biotechnological processes with these engineered strains frequently employ culture media containing glucose as the carbon and energy source. In E. coli, the phosphoenolpyruvate:sugar phosphotransferase system (PTS) transports glucose when this sugar is present at concentrations like those used in production fermentations. This protein system is involved in phosphoenolpyruvate-dependent sugar transport, therefore, its activity has an important impact on carbon flux distribution in the phosphoenolpyruvate and pyruvate nodes. Furthermore, PTS has a very important role in carbon catabolite repression. The properties of PTS impose metabolic and regulatory constraints that can hinder strain productivity. For this reason, PTS has been a target for modification with the purpose of strain improvement. In this review, PTS characteristics most relevant to strain performance and the different strategies of PTS modification for strain improvement are discussed. Functional replacement of PTS by alternative phosphoenolpyruvate-independent uptake and phosphorylation activities has resulted in significant improvements in product yield from glucose and productivity for several classes of metabolites. In addition, inactivation of PTS components has been applied successfully as a strategy to abolish carbon catabolite repression, resulting in E. coli strains that use more efficiently sugar mixtures, such as those obtained from lignocellulosic hydrolysates.