Comparative stability of ethanol production by Escherichia coliKO11 in batch and chemostat culture

Differing claims regarding the stability of the recombinant ethanologen E. coli KO11 are addressed here in batch and chemostat culture. In repeat batch culture, the organism was stable on glucose, mannose, xylose and galactose for at least three serial transfers, even in the absence of a selective antibiotic. Chemostat cultures on glucose were remarkably stable, but on mannose, xylose and a xylose/glucose mixture, they progressively lost their hyperethanologenicity. On xylose, the loss was irreversible, indicating genetic instability. The loss of hyperethanologenicity was accompanied by the production of high concentrations of acetic acid and by increasing biomass yields, suggesting that the higher ATP yield associated with acetate production may foster the growth of acetate-producing revertant strains. Plate counts on high chloramphenicol-containing medium, whether directly, or following preliminary growth on non-selective medium, were not a reliable indicator of high ethanologenicity during chemostat culture. In batch culture, the organism appeared to retain its promise for ethanol production from lignocellulosics and concerns that antibiotics may need to be included in all media appear unfounded. Received 13 January 1999/ Accepted in revised form 23 April 1999     

Kinetics of ethanol production by recombinant Escherichia coli KO11

The fermentation kinetics for separate as well as simultaneous glucose and xylose fermentation with recombinant ethanologenic Escherichia coli KO11 are presented. Glucose and xylose were consumed simultaneously and exhibited mutual inhibition. The glucose exhibited 15 times stronger inhibition in xyclose fermentation than vice versa. The fermentation of condensate from steampretreated willow (Salix) was investigated. The kinetics were studied in detoxified as well as in nondetoxified condensate. The fermentation of the condensate followed two phases: First the glucose and some of the pentoses (xylose in addition to small amounts of arabinose) were fermented simultaneously, and then the remaining part of the pentoses were fermented. The rate of the first phase was independent of the detoxification method used, whereas the rate of the second phase was found to be strongly dependent. When the condensate was detoxified with overliming in combination with sulfite, which was the best detoxification method investigated, the sugars in the condensate, 9 g/L, were fermented in 11 h. The same fermentation took 150 h in nondetoxified condensate. The experimental data were used to develop an empirical model, describing the batch fermentation of recombinant E. coli KO11 in the condensate. The model is based on Monod kinetics including substrate and product inhibition and the sum of the inhibition exerted by the rest of the inhibitors, lumped together. (c) 1995 John Wiley & Sons, Inc.     

Genetic changes to optimize carbon partitioning between ethanol and biosynthesis in ethanologenic Escherichia coli

The production of ethanol from xylose by ethanologenic Escherichia coli strain KO11 was improved by adding various medium supplements (acetate, pyruvate, and acetaldehyde) that prolonged the growth phase by increasing cell yield and volumetric productivity (approximately twofold). Although added pyruvate and acetaldehyde were rapidly metabolized, the benefit of these additives continued throughout fermentation. Both additives increased the levels of extracellular acetate through different mechanisms. Since acetate can be reversibly converted to acetyl coenzyme A (acetyl-CoA) by acetate kinase and phosphotransacetylase, the increase in cell yield caused by each of the three supplements is proposed to result from an increase in the pool of acetyl-CoA. A similar benefit was obtained by inactivation of acetate kinase (ackA), reducing the production of acetate (and ATP) and sparing acetyl-CoA for biosynthetic needs. Inactivation of native E. coli alcohol-aldehyde dehydrogenase (adhE), which uses acetyl-CoA as an electron acceptor, had no beneficial effect on growth, which was consistent with a minor role for this enzyme during ethanol production. Growth of KO11 on xylose appears to be limited by the partitioning of carbon skeletons into biosynthesis rather than the level of ATP. Changes in acetyl-CoA production and consumption provide a useful approach to modulate carbon partitioning. Together, these results demonstrate that xylose fermentation to ethanol can be improved in KO11 by redirecting small amounts of pyruvate away from fermentation products and into biosynthesis. Though negligible with respect to ethanol yield, these small changes in carbon partitioning reduced the time required to complete the fermentation of 9.1% xylose in 1% corn steep liquor medium from over 96 h to less than 72 h.     

Engineering a homo-ethanol pathway in Escherichia coli: increased glycolytic flux and levels of expression of glycolytic genes during xylose fermentation

Replacement of the native fermentation pathway in Escherichia coli B with a homo-ethanol pathway from Zymomonas mobilis (pdc and adhB genes) resulted in a 30 to 50% increase in growth rate and glycolytic flux during the anaerobic fermentation of xylose. Gene array analysis was used as a tool to investigate differences in expression levels for the 30 genes involved in xylose catabolism in the parent (strain B) and the engineered strain (KO11). Of the 4,290 total open reading frames, only 8% were expressed at a significantly higher level in KO11 (P < 0.05). In contrast, over half of the 30 genes involved in the catabolism of xylose to pyruvate were expressed at 1.5-fold- to 8-fold-higher levels in KO11. For 14 of the 30 genes, higher expression was statistically significant at the 95% confidence level (xylAB, xylE, xylFG, xylR, rpiA, rpiB, pfkA, fbaA, tpiA, gapA, pgk, and pykA) during active fermentation (6, 12, and 24 h). Values at single time points for only four of these genes (eno, fbaA, fbaB, and talA) were higher in strain B than in KO11. The relationship between changes in mRNA (cDNA) levels and changes in specific activities was verified for two genes (xylA and xylB) with good agreement. In KO11, expression levels and activities were threefold higher than in strain B for xylose isomerase (xylA) and twofold higher for xylulokinase (xylB). Increased expression of genes involved in xylose catabolism is proposed as the basis for the increase in growth rate and glycolytic flux in ethanologenic KO11.     

Carbohydrate utilization patterns and substrate preferences in Bacteroides thetaiotaomicron

Specific growth rates of Bacteroides thetaiotaomicron NCTC 10582 with either glucose, arabinose, mannose, galactose or xylose as sole carbon sources were 0.42/h, 0.10/h, 0.38/h, 0.38/h and 0.16/h respectively, suggesting that hexose metabolism was energetically more efficient than pentose fermentation in this bacterium. Batch culture experiments to determine whether carbohydrate utilization was controlled by substrate-induced regulatory mechanisms demonstrated that mannose inhibited uptake of glucose, galactose and arabinose, but had less effect on xylose. Arabinose and xylose were preferentially utilized at high dilution rates (D > 0.26/h) in carbon-limited continuous cultures grown on mixtures of arabinose, xylose, galactose and glucose. When mannose was also present, xylose was co-assimilated at all dilution rates. Under nitrogen-limited conditions, however, mannose repressed uptake of all sugars, showing that its effect on xylose utilization was strongly concentration dependent. Studies with individual D-ZU-14C]-labelled substrates showed that transport systems for glucose, galactose, xylose and mannose were inducible. Measurements to determine incorporation of these sugars into trichloroacetic acid-precipitable material indicated that glucose and mannose were the principal precursor monosaccharides. Xylose was only incorporated into intracellular macromolecules when it served as growth substrate. Phosphoenolpyruvate:phosphotransferase systems were not detected in preliminary experiments to elucidate the mechanisms of sugar uptake, and studies with inhibitors of carbohydrate transport showed no consistent pattern of inhibition with glucose, galactose, xylose and mannose. These results indicate the existence of a variety of different systems involved in sugar transport in B. thetaiotaomicron.     

宿主遗传背景对重组酿酒酵母木糖共发酵影响的研究进展

木糖是纤维素原料水解液中最主要的五碳糖成分,由于野生的酿酒酵母缺乏有效的木糖利用途径,将外源木糖代谢途径整合至酿酒酵母中使其具有发酵木糖生产乙醇的能力是构建纤维素乙醇发酵菌株的关键。国内外学者的研究表明,同一木糖代谢途径导入不同酿酒酵母菌株中,所得到的重组菌发酵性能存在明显差异,表明宿主的遗传背景对菌株利用木糖能力和发酵性能具有重要的影响。就酿酒酵母宿主对重组菌株的木糖发酵性能的影响进行了综述,分析了产生宿主差异的内在机理,为进一步选育高效木糖共发酵菌种提供借鉴。     

Isolation and characterization of ethanol-tolerant mutants of Escherichia coli KO11 for fuel ethanol production

Genetically engineered Escherichia coli KO11 is capable of efficiently producing ethanol from all sugar constituents of lignocellulose but lacks the high ethanol tolerance of yeasts currently used for commercial starch-based ethanol processes. Using an enrichment method which selects alternatively for ethanol tolerance during growth in broth and for ethanol production on solid medium, mutants of KO11 with increased ethanol tolerance were isolated which can produce more than 60 g ethanol L⁻¹ from xylose in 72 h. Ethanol concentrations and yields achieved by the LY01 mutant with xylose exceed those reported for recombinant strains of Saccharomyces and Zymomonas mobilis, both of which have a high native ethanol tolerance. Received 18 September 1997/ Accepted in revised form 07 January 1998     

Ethanol production from corn cob hydrolysates by <Emphasis Type="Italic">Escherichia coli</Emphasis> KO11

Corn cob hydrolysates, with xylose as the dominant sugar, were fermented to ethanol by recombinant Escherichia coli KO11. When inoculum was grown on LB medium containing glucose, fermentation of the hydrolysate was completed in 163 h and ethanol yield was 0.50 g ethanol/g sugar. When inoculum was grown on xylose, ethanol yield dropped, but fermentation was faster (113 h). Hydrolysate containing 72.0 g/l xylose and supplemented with 20.0 g/l rice bran was readily fermented, producing 36.0 g/l ethanol within 70 h. Maximum ethanol concentrations were not higher for fermentations using higher cellular concentration inocula. A simulation of an industrial process integrating pentose fermentation by E. coli and hexose fermentation by yeast was carried out. At the first step, E. coli fermented the hydrolysate containing 85.0 g/l xylose, producing 40.0 g/l ethanol in 94 h. Baker's yeast and sucrose (150.0 g/l) were then added to the spent fermentation broth. After 8 h of yeast fermentation, the ethanol concentration reached 104.0 g/l. This two-stage fermentation can render the bioconversion of lignocellulose to ethanol more attractive due to increased final alcohol concentration. Journal of Industrial Microbiology & Biotechnology (2002) 29, 124–128 doi:10.1038/sj.jim.7000287 Received 20 February 2002/ Accepted in revised form 04 June 2002     

Proteomics analysis of Bifidobacterium longum NCC2705 growing on glucose, fructose, mannose, xylose, ribose, and galactose

To investigate the molecular mechanisms underlying carbohydrate uptake and connected metabolic pathways of Bifidobacterium longum NCC2705, the proteomic profiles of bacteria grown on different carbon sources including glucose, fructose, mannose, xylose, ribose, and galactose were analyzed. Our results show that all sugars tested were catabolized via the bifid shunt. Sixty-eight proteins that exhibited changes in abundance of threefold or greater were identified by MS. A striking observation was the differential expression of proteins related to the pyruvate metabolism. Further analysis of acetic acid and lactic acid in the culture supernatants by HPLC at the end of fermentation showed that more lactic acid was produced during growth on fructose, ribose, xylose, galactose and more acetic acid was produced during the fermentation of glucose and mannose. Growth experiments revealed that B. longum NCC2705 preferentially used fructose, ribose, xylose, and galactose with higher growth rates over glucose and mannose. Furthermore, five proteins (GroEL, Eno, Tal, Pgm, and BL0033) exhibited clear phosphorylation modifications at serine and/or tyrosine residues. BL0033, a component of an ATP-binding cassette (ABC) transporter, was significantly more abundant in bacteria grown on fructose and, to a lesser extent, ribose and xylose. RT-PCR analysis revealed that all genes of the ABC transporter are induced in the presence of these sugars suggesting that BL0033, BL0034, BL0035, and BL0036 constitute an ABC transporter with fructose as preferred substrate.     

Lack of protective osmolytes limits final cell density and volumetric productivity of ethanologenic Escherichia coli KO11 during xylose fermentation

Limited cell growth and the resulting low volumetric productivity of ethanologenic Escherichia coli KO11 in mineral salts medium containing xylose have been attributed to inadequate partitioning of carbon skeletons into the synthesis of glutamate and other products derived from the citrate arm of the anaerobic tricarboxylic acid pathway. The results of nuclear magnetic resonance investigations of intracellular osmolytes under different growth conditions coupled with those of studies using genetically modified strains have confirmed and extended this hypothesis. During anaerobic growth in mineral salts medium containing 9% xylose (600 mM) and 1% corn steep liquor, proline was the only abundant osmolyte (71.9 nmol x ml(-1) optical density at 550 nm [OD(550)] unit(-1)), and growth was limited. Under aerobic conditions in the same medium, twice the cell mass was produced, and cells contained a mixture of osmolytes: glutamate (17.0 nmol x ml(-1) OD(550) unit(-1)), trehalose (9.9 nmol x ml(-1) OD(550) unit(-1)), and betaine (19.8 nmol x ml(-1) OD(550) unit(-1)). Two independent genetic modifications of E. coli KO11 (functional expression of Bacillus subtilis citZ encoding NADH-insensitive citrate synthase; deletion of ackA encoding acetate kinase) and the addition of a metabolite, such as glutamate (11 mM) or acetate (24 mM), as a supplement each increased the intracellular glutamate pool during fermentation, doubled cell growth, and increased volumetric productivity. This apparent requirement for a larger glutamate pool for increased growth and volumetric productivity was completely eliminated by the addition of a protective osmolyte (2 mM betaine or 0.25 mM dimethylsulfoniopropionate), consistent with adaptation to osmotic stress rather than relief of a specific biosynthetic requirement.     

An interlaboratory comparison of the performance of ethanol-producing micro-organisms in a xylose-rich acid hydroysate

A xylose-rich, dilute-acid-pretreated corncob hydrolase was fermented by Escherichia coli ATCC 11303, recombinant (rec) E. coli (pLOI 297 and KO11), Pichia stipitis (CBS 5773, 6054 adn R), Saccharomyces cerevisiae siolate 3 in combination with xylose isomerase, rec S. cerevisiae (TJ1, H550 and H477), and Fusraium oxysporum VIT-D-80134 in an interlaboratory comparison. The micro-organisms were studied according to three different options: (A) fermentation under consistent conditions, (B) fermentation under optimal conditions for the organisms, and (C) fermentation under optimal conditions for the organism with detoxification if the hydrolysate. The highest yields of tehanol, 0.24 g/g (A), 0.36 g/g (B) and 0.54 g/g (C), were obtained from rec E. coli B, KO11. P. stipitis and F. oxysporum were sensitive to the inhibitors present in the hydrolysate and produced a minimum yields of 0.34 g/g (C) and 0.04 g/g (B), respectively. The analysis of the corn-cob hydrolysate and aspects of process economy of the different fermentation options (pH, sterilization, nutrient supplementation, adaptation, detoxification) are discussed.Correspondece to: B. Hahn-Hägerdal     

Fermentation of carbohydrates and yield of microbial protein in mixed cultures of rabbitcaecal microorganisms

Fermentation pattern and yields of microbial protein were investigated in cultures of the rabbit caecal contents supplied with glucose, xylose, starch, pectin and xylan. Rabbits at the age of 4 weeks (before weaning) and 3 months were slaughtered, their caecal contents added at 1.1% to growth media and incubated anaerobically at 39°C for 18 h. Caecal microorganisms of 4‐week‐old rabbits produced no methane and caproate, less butyrate, but more propionate than microorganisms of 3‐month‐old rabbits. In both groups of rabbits, fermentation of xylose produced significantly more propionate and less butyrate than fermentation of glucose. More propionate and less acetate was formed from starch than from pectin. In caecal cultures from 4‐week‐old rabbits with pectin, the molar percentages of acetate was significantly higher and percentages of other short‐chain fatty acids (SCFA) lower than in cultures with starch or xylan. In cultures from 3‐month‐old rabbits, fermentation of pectin and xylan produced similar SCFA profiles, different from SCFA molar composition in cultures with starch. Average production of microbial protein was 129mg per lg of carbohydrate digested (range 110 to 141mg/g). Protein yields were the same on glucose and xylose, but nonsignificantly higher on starch than on pectin and xylan. It can be concluded that the characteristics of substrate affected fermentation pattern in mixed cultures of rabbit caecal microorganisms. Substrate effects on protein yields were not statistically significant, due to high variation.     

Encapsulation enhances protoplast fusant stability

A barrier to cost-efficient biomanufacturing is the instability of engineered genetic elements, such as plasmids. Instability can also manifest at the whole-genome level, when fungal dikaryons revert to parental species due to nuclear segregation during cell division. Here, we show that by encapsulating Saccharomyces cerevisiae-Pichia stipitis dikaryons in an alginate matrix, we can limit cell division and preserve their expanded metabolic capabilities. As a proxy to cellulosic ethanol production, we tested the capacity of such cells to carry out ethanologenic fermentation of glucose and xylose, examining substrate use, ploidy, and cell viability in relation to planktonic fusants, as well as in relation to planktonic and encapsulated cell cultures consisting of mixtures of these species. Glucose and xylose consumption and ethanol production by encapsulated dikaryons were greater than planktonic controls. Simultaneous co-fermentation did not occur; rather the order and kinetics of glucose and xylose catabolism by encapsulated dikaryons were similar to cultures where the two species were encapsulated together. Over repeated cycles of fed-batch culture, encapsulated S. cerevisiae-P. stipitis fusants exhibited a dramatic increase in genomic stability, relative to planktonic fusants. Encapsulation also increased the stability of antibiotic-resistance plasmids used to mark each species and preserved a fixed ratio of S. cerevisiae to P. stipitis cells in mixed cultures. Our data demonstrate how encapsulating cells in an extracellular matrix restricts cell division and, thereby, preserves the stability and biological activity of entities ranging from genomes to plasmids to mixed populations, each of which can be essential to cost-efficient biomanufacturing.     

Establishment of l-arabinose fermentation in glucose/xylose co-fermenting recombinant Saccharomyces cerevisiae 424A(LNH-ST) by genetic engineering

Cost-effective and efficient ethanol production from lignocellulosic materials requires the fermentation of all sugars recovered from such materials including glucose, xylose, mannose, galactose, and l-arabinose. Wild-type strains of Saccharomyces cerevisiae used in industrial ethanol production cannot ferment d-xylose and l-arabinose. Our genetically engineered recombinant S. cerevisiae yeast 424A(LNH-ST) has been made able to efficiently ferment xylose to ethanol, which was achieved by integrating multiple copies of three xylose-metabolizing genes. This study reports the efficient anaerobic fermentation of l-arabinose by the derivative of 424A(LNH-ST). The new strain was constructed by over-expression of two additional genes from fungi l-arabinose utilization pathways. The resulting new 424A(LNH-ST) strain exhibited production of ethanol from l-arabinose, and the yield was more than 40%. An efficient ethanol production, about 72.5% yield from five-sugar mixtures containing glucose, galactose, mannose, xylose, and arabinose was also achieved. This co-fermentation of five-sugar mixture is important and crucial for application in industrial economical ethanol production using lignocellulosic biomass as the feedstock.     

一株厌氧嗜热杆菌生长及发酵特性的初步研究

论文对筛选并鉴定为Thermoanaerobacterium saccharolyticum菌株的生长、底物利用情况、产物生成以及酒精耐受性进行了研究。结果表明,该菌在以甘露糖、葡萄糖和木糖为碳源时生长较好,同时能够较好的利用木聚糖和木薯淀粉;最适底物浓度为15g/L;不同的葡萄糖:木糖比例对其生长无显著影响;能耐受的培养基最高初始酒精浓度为3%(V/V)。在5g/L的木聚糖、木糖和木薯淀粉培养基中发酵60h后,产物主要有乙醇、乳酸和乙酸,乙醇产量分别为0.824、0.867和0.916g/L。     

Improved strains of recombinant Escherichia coli for ethanol production from sugar mixtures

Hemicellulose hydrolysates of agricultural residues often contain mixtures of hexose and pentose sugars. Ethanologenic Escherichia coli that have been previously investigated preferentially ferment hexose sugars. In some cases, xylose fermentation was slow or incomplete. The purpose of this study was to develop improved ethanologenic E. coli strains for the fermentation of pentoses in sugar mixtures. Using fosfomycin as a selective agent, glucose-negative mutants of E. coli KO11 (containing chromosomally integrated genes encoding the ethanol pathway from Zymomonas mobilis) were isolated that were unable to ferment sugars transported by the phosphoenolpyruvate-dependent phosphotransferase system. These strains (SL31 and SL142) retained the ability to ferment sugars with independent transport systems such as arabinose and xylose and were used to ferment pentose sugars to ethanol selectively in the presence of high concentrations of glucose. Additional fosfomycin-resistant mutants were isolated that were superior to strain KO11 for ethanol production from hexose and pentose sugars. These hyperproductive strains (SL28 and SL40) retained the ability to metabolize all sugars tested, completed fermentations more rapidly, and achieved higher ethanol yields than the parent. Both SL28 and SL40 produced 60 gl^–1 ethanol from 120 gl^–1 xylose in 60 h, 20% more ethanol than KO11 under identical conditions. Further studies illustrated the feasibility of sequential fermentation. A mixture of hexose and pentose sugars was fermented with near theoretical yield by SL40 in the first step followed by a second fermentation in which yeast and glucose were added. Such a two-step approach can combine the attributes of ethanologenic E. coli for pentoses with the high ethanol tolerance of conventional yeasts in a single vessel.     

Comparison of the xylose reductase-xylitol dehydrogenase and the xylose isomerase pathways for xylose fermentation by recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Background  

Two heterologous pathways have been used to construct recombinant xylose-fermenting Saccharomyces cerevisiae strains: i) the xylose reductase (XR) and xylitol dehydrogenase (XDH) pathway and ii) the xylose isomerase (XI) pathway. In the present study, the Pichia stipitis XR-XDH pathway and the Piromyces XI pathway were compared in an isogenic strain background, using a laboratory host strain with genetic modifications known to improve xylose fermentation (overexpressed xylulokinase, overexpressed non-oxidative pentose phosphate pathway and deletion of the aldose reductase gene GRE3). The two isogenic strains and the industrial xylose-fermenting strain TMB 3400 were studied regarding their xylose fermentation capacity in defined mineral medium and in undetoxified lignocellulosic hydrolysate.     

Kinetic modeling of Candida shehatae ATCC 22984 on xylose and glucose for ethanol production

Candida shehatae ATCC 22984, a xylose-fermenting yeast, showed an ability to produce ethanol in both glucose and xylose medium. Maximum ethanol produced by the yeast was 48.8?g/L in xylose and 52.6?g/L in glucose medium with ethanol yields that varied between 0.3 and 0.4?g/g depended on initial sugar concentrations. Xylitol was a coproduct of ethanol production using xylose as substrate, and glycerol was detected in both glucose and xylose media. Kinetic model equations indicated that growth, substrate consumption, and product formation of C. shehatae were governed by substrate limitation and inhibition by ethanol. The model suggested that cell growth was totally inhibited at 40?g/L of ethanol and ethanol production capacity of the yeast was 52?g/L, which were in good agreement with experimental results. The developed model could be used to explain C. shehatae fermentation in glucose and xylose media from 20 to 170?g/L sugar concentrations.     

A model of xylitol production by the yeast Candida mogii

Production of xylitol from xylose in batch fermentations of Candida mogii ATCC 18364 is discussed in the presence of glucose as the cosubstrate. Various initial ratios of glucose and xylose concentrations are assessed for their impact on yield and rate of production of xylitol. Supplementation with glucose at the beginning of the fermentation increased the specific growth rate, biomass yield and volumetric productivity of xylitol compared with fermentation that used xylose as the sole carbon source. A mathematical model is developed for eventual use in predicting the product formation rate and yield. The model parameters were estimated from experimental observations, using a genetic algorithm. Batch fermentations, which were carried out with xylose alone and a mixture of xylose and glucose, were used to validate the model. The model fitted well with the experimental data of cell growth, substrate consumption and xylitol production.