Fungal metabolism of fermentation inhibitors present in corn stover dilute acid hydrolysate

Use of agricultural residues for ethanol production requires pretreatment of the material to facilitate release of sugars. Physical–chemical pretreatment of lignocellulosic biomass can, however, give rise to side-products that may be toxic to fermenting microorganisms and hinder utilization of sugars obtained from biomass. Potentially problematic compounds include furan aldehydes formed by degradation of sugars, organic acids released from hemicellulose side-groups, and aldehydes and phenolics released from lignin. A fungal isolate, Coniochaeta ligniaria NRRL30616, metabolizes furfural and 5-hydroxymethylfurfural (HMF) as well as aromatic and aliphatic acids and aldehydes. NRRL30616 grew in corn stover dilute-acid hydrolysate, and converted furfural to both furfuryl alcohol and furoic acid. Hydrolysate was inoculated with NRRL30616, and the fate of pretreatment side-products was followed in a time-course study. A number of aromatic and aliphatic acids, aldehydes, and phenolic compounds were quantitated by analytical extraction of corn stover hydrolysate, followed by HPLC–UV–MS/MS analysis. Compounds representing all of the classes of inhibitory side-products were removed during the course of fungal growth. Biological abatement of hydrolysates using C. ligniaria improved xylose utilization in subsequent ethanol fermentations.     

大肠杆菌AFP111利用玉米粉全水解液厌氧发酵合成丁二酸

利用双酶法制得的玉米粉糖液及制糖过程中玉米糖渣酶解后含氮水解液作为发酵培养基,考察在不添加其他营养物质条件下大肠杆菌(E.coli)AFP111专一厌氧发酵产丁二酸的可能性。结果表明:E.coli AFP111厌氧发酵48 h后,丁二酸质量浓度达到15.24 g/L,丁二酸的得率为0.76 g/g。与在LB培养基中发酵相比,产量提高了14.41%。对关键酶酶活和辅因子NAD(H)含量的测定结果显示,能利用玉米粉全水解液的苹果酸脱氢酶(MDH)、磷酸烯醇式丙酮酸(PEP)羧化酶(PPC)、PEP羧化激酶(PCK)酶活及辅因子NAD(H)含量分别为0.88 U、0.29 U、0.31 U和15.09μmol/g,均比LB培养基中关键酶酶活和辅因子NAD(H)含量高。由此推测,玉米粉全水解液中关键生长因子(D-生物素、VB1和烟酸)的含量影响了关键酶酶活和辅因子NAD(H)的含量,从而影响丁二酸的产量。在5 L罐中厌氧发酵120 h,利用玉米粉全水解液,丁二酸的得率为0.84 g/g,比利用LB培养基发酵得到的丁二酸得率提高了21.74%。     

Acetic acid removal from corn stover hydrolysate using ethyl acetate and the impact on Saccharomyces cerevisiae bioethanol fermentation

Acetic acid is introduced into cellulose conversion processes as a consequence of composition of lignocellulose feedstocks, causing significant inhibition of adapted, genetically modified and wild‐type S. cerevisiae in bioethanol fermentation. While adaptation or modification of yeast may reduce inhibition, the most effective approach is to remove the acetic acid prior to fermentation. This work addresses liquid–liquid extraction of acetic acid from biomass hydrolysate through a pathway that mitigates acetic acid inhibition while avoiding the negative effects of the extractant, which itself may exhibit inhibition. Candidate solvents were selected using simulation results from Aspen Plus?, based on their ability to extract acetic acid which was confirmed by experimentation. All solvents showed varying degrees of toxicity toward yeast, but the relative volatility of ethyl acetate enabled its use as simple vacuum evaporation could reduce small concentrations of aqueous ethyl acetate to minimally inhibitory levels. The toxicity threshold of ethyl acetate, in the presence of acetic acid, was found to be 10 g L^?1. The fermentation was enhanced by extracting 90% of the acetic acid using ethyl acetate, followed by vacuum evaporation to remove 88% removal of residual ethyl acetate along with 10% of the broth. NRRL Y‐1546 yeast was used to demonstrate a 13% increase in concentration, 14% in ethanol specific production rate, and 11% ethanol yield. This study demonstrated that extraction of acetic acid with ethyl acetate followed by evaporative removal of ethyl acetate from the raffinate phase has potential to significantly enhance ethanol fermentation in a corn stover bioethanol facility. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:929–937, 2016     

Mannose fermentation by an ethanologenic recombinant Escherichia coli

Summary Recombinant E. coli B (pLOI297) grows in Luria broth with mannose at a rate that is only about one-half of the rate with xylose and about one-quarter of the rate with glucose as carbon source. For a sugar concentration of about 2 % (w/v), the corresponding specific ethanol productivities (q_p) are 0.22, 0.45 and 0.70 g ethanol/g cell/h for mannose, xylose and glucose. At higher sugar concentrations (8–11 %), the sp. productivities are 0.12, 0.33 and 0.35 g ethanol/g cell/h for mannose, xylose and glucose. Using a synthetic softwood prehydrolysate medium, in which the mass ratio of mannose:xylose:glucose was approx. 1.0:0.6:0.4 (total sugar conc'n 4.5 %), the sp. productivities associated with glucose and xylose metabolism were decreased by about 50 % and 75 % respectively, whereas mannose metabolism appeared unaffected by the presence of the other sugars. In all cases, the sugar-to-ethanol conversion efficiency was >90 % of theoretical maximum     

Biological removal of inhibitors leads to the improved lipid production in the lipid fermentation of corn stover hydrolysate by Trichosporon cutaneum

Corn stover (CS) hydrolysate was used as the fermentation feedstock of Trichosporon cutaneum CX1 for production of microbial lipid as the potential raw material of biodiesel. Two major technical barriers of the lipid fermentation were investigated: one was the strong inhibition of lignocellulose degradation compounds generated in the CS pretreatment; the other was the low carbon-to-nitrogen molar ratio (C/N ratio) of the CS hydrolysate. The newly established biodetoxification method was applied to remove the inhibitors in the pretreated CS. The enhancement of the pretreatment severity and the biodetoxification intensity on the lipid fermentation was investigated. The results show that the biodetoxification not only efficiently removed the inhibitor substances, but also led to the reduction of nitrogen content and the increase of C/N ratio. The cell lipid content of T. cutaneum CX1 using the biodetoxified CS hydrolysate reached 23.5%, which was doubled than that using the non-detoxified value.     

Coproduction of acetaldehyde and hydrogen during glucose fermentation by Escherichia coli

Escherichia coli K-12 strain MG1655 was engineered to coproduce acetaldehyde and hydrogen during glucose fermentation by the use of exogenous acetyl-coenzyme A (acetyl-CoA) reductase (for the conversion of acetyl-CoA to acetaldehyde) and the native formate hydrogen lyase. A putative acetaldehyde dehydrogenase/acetyl-CoA reductase from Salmonella enterica (SeEutE) was cloned, produced at high levels, and purified by nickel affinity chromatography. In vitro assays showed that this enzyme had both acetaldehyde dehydrogenase activity (68.07 ± 1.63 μmol min(-1) mg(-1)) and the desired acetyl-CoA reductase activity (49.23 ± 2.88 μmol min(-1) mg(-1)). The eutE gene was engineered into an E. coli mutant lacking native glucose fermentation pathways (ΔadhE, ΔackA-pta, ΔldhA, and ΔfrdC). The engineered strain (ZH88) produced 4.91 ± 0.29 mM acetaldehyde while consuming 11.05 mM glucose but also produced 6.44 ± 0.26 mM ethanol. Studies showed that ethanol was produced by an unknown alcohol dehydrogenase(s) that converted the acetaldehyde produced by SeEutE to ethanol. Allyl alcohol was used to select for mutants with reduced alcohol dehydrogenase activity. Three allyl alcohol-resistant mutants were isolated; all produced more acetaldehyde and less ethanol than ZH88. It was also found that modifying the growth medium by adding 1 g of yeast extract/liter and lowering the pH to 6.0 further increased the coproduction of acetaldehyde and hydrogen. Under optimal conditions, strain ZH136 converted glucose to acetaldehyde and hydrogen in a 1:1 ratio with a specific acetaldehyde production rate of 0.68 ± 0.20 g h(-1) g(-1) dry cell weight and at 86% of the maximum theoretical yield. This specific production rate is the highest reported thus far and is promising for industrial application. The possibility of a more efficient "no-distill" ethanol fermentation procedure based on the coproduction of acetaldehyde and hydrogen is discussed.     

玉米秸秆酸解副产物对重组酿酒酵母6508-127发酵的影响

将木质纤维素类生物质如玉米秸秆等用稀酸水解预处理,在半纤维素水解为单糖的同时,水解液中还会产生一些可能对后续发酵有影响的副产物。本实验分别考查了在玉米秸秆稀酸水解液中检测出的乙酸、甲酸、香草醛、糠醛和羟甲基糠醛对重组木糖发酵菌株S. cerevisiae 6508-127生长和发酵的影响。结果表明,甲酸和乙酸对菌体生长的抑制强于乙醇生成,且甲酸的抑制程度远大于乙酸;2g/L香草醛可使菌体生长延滞期明显延长,而在较低浓度（≤1.2g/L）此现象不明显。糠醛在0.5-1.5g/L范围内对菌体生长有抑制作用,但使乙醇得率提高;羟甲基糠醛在0.2g/L浓度存在就使乙醇得率有明显降低,但使生物量得率提高;研究中还发现,糠醛、羟甲基糠醛和香草醛可被S. cerevisiae 6508-127代谢。     

Mutagenesis and stress responses induced in Escherichia coli by hydrogen peroxide

Killing of Escherichia coli by hydrogen peroxide proceeds by two modes. Mode one killing appears to be due to DNA damage, has a maximum near 1 to 3 mM H2O2, and requires active metabolism during exposure. Mode two killing is due to uncharacterized damage, occurs in the absence of metabolism, and exhibits a classical multiple-order dose-response curve up to at least 50 mM H2O2 (J. A. Imlay and S. Linn, J. Bacteriol. 166:519-527, 1986). H2O2 induces the SOS response in proportion to the degree of killing by the mode one pathway, i.e., induction is maximal after exposure to 1 to 3 mM H2O2. Mutant strains that cannot induce the SOS regulon are hypersensitive to peroxide. Analysis of the sensitivities of mutants that are deficient in individual SOS-regulated functions suggested that the SOS-mediated protection is due to the enhanced synthesis of recA protein, which is rate limiting for recombinational DNA repair. Specifically, strains wholly blocked in both SOS induction and DNA recombination were no more sensitive than mutants that are blocked in only one of these two functions, and strains carrying mutations in uvrA, -B, -C, or -D, sfiA, umuC or -D, ssb, or dinA, -B, -D, -F, -G, -H, -I, or -J were not abnormally sensitive to killing by H2O2. After exposure to H2O2, mutagenesis and filamentation also occurred with the dose response characteristic of SOS induction and mode one killing, but these responses were not dependent on the lexA-regulated umuC mutagenesis or sfiA filamentation functions, respectively. Exposure of E. coli to H2O2 also resulted in the induction of functions under control of the oxyR regulon that enhance the scavenging of active oxygen species, thereby reducing the sensitivity to H2O2. Catalase levels increased 10-fold during this induction, and katE katG mutants, which totally lack catalase, while not abnormally sensitive to killing by H2O2 in the naive state, did not exhibit the induced protective response. Protection equal to that observed during oxyR induction could be achieved by the addition of catalase to cultures of naive cells in an amount equivalent to that induced by the oxyR response. Thus, the induction of catalase is necessary and sufficient for the observed oxyR-directed resistance to killing by H2O2. Although superoxide dismutase appeared to be uninvolved in this enhanced protective response, sodA sodB mutants, which totally lack superoxide dismutase, were especially sensitive to mode one killing by H2O2 in the naive state. gshB mutants, which lack glutathione, were not abnormally sensitive to killing by H2O2.     

Fate of Escherichia coli during ensiling of wheat and corn

A recombinant Escherichia coli strain carrying a plasmid with an antibiotic resistance marker and expressing the green fluorescent protein was inoculated at a concentration of 3.8 x 10(8) CFU/g into direct-cut wheat (348 g of dry matter kg(-1)), wilted wheat (450 g of dry matter kg(-1)), and corn (375 g of dry matter kg(-1)). The forages were ensiled in mini-silos. The treatments included control (no E. coli added), application of tagged E. coli, and delayed sealing of the inoculated wheat. Three silos per treatment were sampled on predetermined dates, and the numbers of E. coli were determined on Chromocult TBX medium with or without kanamycin. Colonies presumptively identified as E. coli were also tested for fluorescence activity. Addition of E. coli at the time of ensiling resulted in a more rapid decrease in the pH but had almost no effect on the chemical composition of the final silages or their aerobic stability. E. coli disappeared from the silages when the pH decreased below 5.0. It persisted longer in silages of wilted wheat, in which the pH declined more slowly. Control silages of all crops also contained bacteria, presumptively identified as E. coli, that were resistant to the antibiotic, which suggests that some epiphytic strains are naturally resistant to antibiotics.     

Chemical and enzymic pretreatment of corn stover to produce soluble fermentation substrates

Corn stover was pretreated with various chemical agents, including sodium hydroxide, sulfuric acid, ethylenediamine, n-butylamine (either alone or in solution with methanol), and acetonitrile or ethanol containing hydrochloric acid. Of these chemicals, n-butylamine was the best reagent for pretreatment of corn stover, considering the degree of loss of total carbohydrate, delignification, cumulative weight loss, cumulative yield of reducing sugars per original total carbohydrate, and the potential ease of recovery and reuse of reagent. In comparison to the other reagents tested, n-butylamine (n-BA) selectively delignified corn stover. The best conditions were as follows: a 12-h presoak of about a 155 g dry wt/L slurry (1 mm average particle size) in 100% n-BA at room temperature, followed by 30 min of refluxing (86.5 degrees C) with 40% (w/w) n-BA-distilled water solution. The cumulative yield of reducing sugars after enzymic hydrolysis was 44.5% of the original total carbohydrate and the cumulative total weight loss (dry basis) was 59%. Degradative loss of total carbohydrate during pretreatment was not detected.     

Hydrogenase activity and proton-motive force generation by Escherichia coli during glycerol fermentation

Proton motive force (Δp) generation by Escherichia coli wild type cells during glycerol fermentation was first studied. Its two components, electrical—the membrane potential (?φ) and chemical—the pH transmembrane gradient (ΔpH), were established and the effects of external pH (pH_ex) were determined. Intracellular pH was 7.0 and 6.0 and lower than pH_ex at pH 7.5 and 6.5, respectively; and it was higher than pH_ex at pH 5.5. At high pH_ex, the increase of ?φ (?130 mV) was only partially compensated by a reversed ΔpH, resulting in a low Δp. At low pH_ex ?φ and consequently Δp were decreased. The generation of Δp during glycerol fermentation was compared with glucose fermentation, and the difference in Δp might be due to distinguished mechanisms for H⁺ transport through the membrane, especially to hydrogenase (Hyd) enzymes besides the F₀F₁-ATPase. H⁺ efflux was determined to depend on pH_ex; overall and N,N’-dicyclohexylcarbodiimide (DCCD)-inhibitory H⁺ efflux was maximal at pH 6.5. Moreover, ΔpH was changed at pH 6.5 and Δp was different at pH 6.5 and 5.5 with the hypF mutant lacking all Hyd enzymes. DCCD-inhibited ATPase activity of membrane vesicles was maximal at pH 7.5 and decreased with the hypF mutant. Thus, Δp generation by E. coli during glycerol fermentation is different than that during glucose fermentation. Δp is dependent on pH_ex, and a role of Hyd enzymes in its generation is suggested.     

Escherichia coli and Lactobacillus plantarum responses to osmotic stress

Escherichia coli and Lactobacillus plantarum were subjected to final water potentials of −5.6 MPa and −11.5 MPa with three solutes: glycerol, sorbitol and NaCl. The water potential decrease was realized either rapidly (osmotic shock) or slowly (20 min) and a difference in cell viability between these conditions was only observed when the solute was NaCl. The cell mortality during osmotic shocks induced by NaCl cannot be explained by a critical volume decrease or by the intensity of the water flow across the cell membrane. When the osmotic stress is realized with NaCl as the solute, in a medium in which osmoregulation cannot take place, the application of a slow decrease in water potential resulted in the significant maintenance of cell viability (about 70–90%) with regard to the corresponding viability observed after a sudden step change to same final water potential (14–40%). This viability difference can be explained by the existence of a critical internal free Na⁺ concentration. Received: 20 May 1998 / Received revision: 31 July 1998 / Accepted: 31 July 1998     

Global metabolomic responses of Escherichia coli to heat stress

Microbial metabolomic analysis is essential for understanding responses of microorganisms to heat stress. To understand the comprehensive metabolic responses of Escherichia coli to continuous heat stress, we characterized the metabolomic variations induced by heat stress using NMR spectroscopy in combination with multivariate data analysis. We detected 15 amino acids, 10 nucleotides, 9 aliphatic organic acids, 7 amines, glucose and its derivative glucosylglyceric acid, and methanol in the E. coli extracts. Glucosylglyceric acid was reported for the first time in E. coli. We found that heat stress was an important factor influencing the metabolic state and growth process, mainly via suppressing energy associated metabolism, reducing nucleotide biosynthesis, altering amino acid metabolism and promoting osmotic regulation. Moreover, metabolic perturbation was aggravated during heat stress. However, a sign of recovery to control levels was observed after the removal of heat stress. These findings enhanced our understanding of the metabolic responses of E. coli to heat stress and demonstrated the effectiveness of the NMR-based metabolomics approach to study such a complex system.     

High solid simultaneous saccharification and fermentation of wet oxidized corn stover to ethanol

In this study ethanol was produced from corn stover pretreated by alkaline and acidic wet oxidation (WO) (195 degrees C, 15 min, 12 bar oxygen) followed by nonisothermal simultaneous saccharification and fermentation (SSF). In the first step of the SSF, small amounts of cellulases were added at 50 degrees C, the optimal temperature of enzymes, in order to obtain better mixing condition due to some liquefaction. In the second step more cellulases were added in combination with dried baker's yeast (Saccharomyces cerevisiae) at 30 degrees C. The phenols (0.4-0.5 g/L) and carboxylic acids (4.6-5.9 g/L) were present in the hemicellulose rich hydrolyzate at subinhibitory levels, thus no detoxification was needed prior to SSF of the whole slurry. Based on the cellulose available in the WO corn stover 83% of the theoretical ethanol yield was obtained under optimized SSF conditions. This was achieved with a substrate concentration of 12% dry matter (DM) acidic WO corn stover at 30 FPU/g DM (43.5 FPU/g cellulose) enzyme loading. Even with 20 and 15 FPU/g DM (corresponding to 29 and 22 FPU/g cellulose) enzyme loading, ethanol yields of 76 and 73%, respectively, were obtained. After 120 h of SSF the highest ethanol concentration of 52 g/L (6 vol.%) was achieved, which exceeds the technical and economical limit of the industrial-scale alcohol distillation. The SSF results showed that the cellulose in pretreated corn stover can be efficiently fermented to ethanol with up to 15% DM concentration. A further increase of substrate concentration reduced the ethanol yield significant as a result of insufficient mass transfer. It was also shown that the fermentation could be followed with an easy monitoring system based on the weight loss of the produced CO2.     

Aerobic fermentation of D-glucose by an evolved cytochrome oxidase-deficient Escherichia coli strain

Fermentation of glucose to D-lactic acid under aerobic growth conditions by an evolved Escherichia coli mutant deficient in three terminal oxidases is reported in this work. Cytochrome oxidases (cydAB, cyoABCD, and cbdAB) were removed from the E. coli K12 MG1655 genome, resulting in the ECOM3 (E. coli cytochrome oxidase mutant) strain. Removal of cytochrome oxidases reduced the oxygen uptake rate of the knockout strain by nearly 85%. Moreover, the knockout strain was initially incapable of growing on M9 minimal medium. After the ECOM3 strain was subjected to adaptive evolution on glucose M9 medium for 60 days, a growth rate equivalent to that of anaerobic wild-type E. coli was achieved. Our findings demonstrate that three independently adaptively evolved ECOM3 populations acquired different phenotypes: one produced lactate as a sole fermentation product, while the other two strains exhibited a mixed-acid fermentation under oxic growth conditions with lactate remaining as the major product. The homofermenting strain showed a D-lactate yield of 0.8 g/g from glucose. Gene expression and in silico model-based analyses were employed to identify perturbed pathways and explain phenotypic behavior. Significant upregulation of ygiN and sodAB explains the remaining oxygen uptake that was observed in evolved ECOM3 strains. E. coli strains produced in this study showed the ability to produce lactate as a fermentation product from glucose and to undergo mixed-acid fermentation during aerobic growth.     

Effect of alcohol compounds found in hemicellulose hydrolysate on the growth and fermentation of ethanologenic Escherichia coli

Lignocellulose can be readily hydrolyzed into a mixture of sugars using dilute mineral acids. During hydrolysis, a variety of inhibitors are also produced which include aromatic alcohols from lignin and furfuryl alcohol from pentose destruction. Seven compounds were investigated individually and in binary combinations (catechol, coniferyl alcohol, furfuryl alcohol, guaiacol, hydroquinone, methylcatechol, and vanillyl alcohol). Aromatic alcohols and furfuryl alcohol inhibited ethanol production from xylose in batch fermentations primarily by inhibiting the growth of Escherichia coli LY01, the biocatalyst. The toxicities of these compounds were directly related to their hydrophobicity. Methylcatechol was the most toxic compound tested (MIC = 1.5 g/L). In binary combination, the extent of growth inhibition was roughly additive for most compounds tested. However, combinations with furfuryl alcohol and furfural (furaldehyde) appear synergistic in toxicity. When compared individually, alcohol components which are formed during hemicellulose hydrolysis are less toxic for growth than the aldehydes and organic acids either on a weight basis or a molar basis.     

Oxidative stress responses in Escherichia coli and Salmonella typhimurium.

Oxidative stress is strongly implicated in a number of diseases, such as rheumatoid arthritis, inflammatory bowel disorders, and atherosclerosis, and its emerging as one of the most important causative agents of mutagenesis, tumorigenesis, and aging. Recent progress on the genetics and molecular biology of the cellular responses to oxidative stress, primarily in Escherichia coli and Salmonella typhimurium, is summarized. Bacteria respond to oxidative stress by invoking two distinct stress responses, the peroxide stimulon and the superoxide stimulon, depending on whether the stress is mediated by peroxides or the superoxide anion. The two stimulons each contain a set of more than 30 genes. The expression of a subset of genes in each stimulon is under the control of a positive regulatory element; these genes constitute the OxyR and SoxRS regulons. The schemes of regulation of the two regulons by their respective regulators are reviewed in detail, and the overlaps of these regulons with other stress responses such as the heat shock and SOS responses are discussed. The products of Oxy-R- and SoxRS-regulated genes, such as catalases and superoxide dismutases, are involved in the prevention of oxidative damage, whereas others, such as endonuclease IV, play a role in the repair of oxidative damage. The potential roles of these and other gene products in the defense against oxidative damage in DNA, proteins, and membranes are discussed in detail. A brief discussion of the similarities and differences between oxidative stress responses in bacteria and eukaryotic organisms concludes this review.     

玉米秸秆水解液发酵联产氢气与2,3-丁二醇的初步研究

选用实验室自行筛选的Klebsiella pneumoniae ECU-15,进行了玉米秸秆水解液发酵联产氢气和2,3-丁二醇的初步研究。结果表明:以葡萄糖为碳源时,两目标产物随培养条件的改变呈现相同的变化趋势,且最佳发酵温度为37℃,最佳pH为6.0,最佳初始糖浓度为30 g/L;不同比例葡萄糖/木糖为混合碳源时,均能实现氢气和2,3-丁二醇的联产过程,但随着木糖含量的增加,细胞产量、氢气产量和2,3-丁二醇的产量都有所下降,并且木糖的存在会降低葡萄糖的消耗速率;实验最后以玉米秸秆水解液和同比例模拟合成培养基为底物,初步探明了该菌株利用水解液发酵联产氢气和2,3-丁二醇的可行性,最终氢气产量为0.65 v/v,产氢得率为0.43 mol/mol sugar;2,3-丁二醇产量为5.05 g/L,得率为0.82 mol/mol sugar。