Cellobiose Dehydrogenase, an Active Agent in Cellulose Depolymerization

The ability of cellobiose dehydrogenase purified from Phanerochaete chrysosporium to modify a Douglas fir kraft pulp was assessed. Although the addition of cellobiose dehydrogenase alone had little effect, supplementation with cellobiose and iron resulted in a substantial reduction in the degree of polymerization of the pulp cellulose. When the reaction was monitored over time, a progressive depolymerization of the cellulose was apparent with the concomitant production of cellobiono-1,5-lactone. Analysis of the reaction filtrates indicated that glucose and arabinose were the only neutral sugars generated. These sugars are derived from the degradation of the cellobiose rather than resulting from modifications of the pulp. These results suggest that the action of cellobiose dehydrogenase results in the generation of hydroxyl radicals via Fenton's chemistry which subsequently results in the depolymerization of cellulose. This appears to be the mechanism whereby a substantial reduction in the degree of polymerization of the cellulose can be achieved without a significant release of sugar.     

Kinetic models for growth and product formation on multiple substrates

Hydrolyzates from lignocellulosic biomass contain a mixture of simple sugars; the predominant ones being glucose, cellobiose and xylose. The fermentation of such mixtures to ethanol or other chemicals requires an understanding of how each of these substrates is utilized.Candida lusitaniae can efficiently produce ethanol from both glucose and cellobiose and is an attractive organism for ethanol production. Experiments were performed to obtain kinetic data for ethanol production from glucose, cellobiose and xylose. Various combinations were tested in order to determine kinetic behavior with multiple carbon sources. Glucose was shown to repress the utilization of cellobiose and xylose. However, cellobiose and xylose were simultaneously utilized after glucose depletion. Maximum volumetric ethanol production rates were 0.56, 0.33, and 0.003 g/L-h from glucose, cellobiose and xylose, respectively. A kinetic model based on cAMP mediated catabolite repression was developed. This model adequately described the growth and ethanol production from a mixture of sugars in a batch culture.     

Calorimetric versus Growth Microbial Analysis of Cellulase Enzymes Acting on Cellulose

Assay of cellulase enzymology on cellulose was investigated by two methods: (i) plate colony counting to determine microbial growth and (ii) microbial calorimetry. These methods were chosen because they accept raw samples and have the potential to be far more specific than spectrophotometric reducing sugar assays. Microbial calorimetry requires ca. 0.5 to 1 h and 10 to 100 μM concentrations of cellulolytic lower sugars (glucose and cellobiose). Growth assay (liquid culture, plating, colony counting) requires 15 to 20 h and ca. 0.5 mM sugars. Microbial calorimetry requires simply aerobic metabolism, whereas growth assay requires completion of the cell cycle. A stripping technique is described for use in conjunction with the calorimetric method to enable separate analysis of the two sugars. Mixtures of glucose and cellobiose are equilibrated with Escherichia coli and spun out to remove glucose. The supernatant is calorimetrically combusted with Klebsiella sp. to quantitate cellobiose, and the same organism combusting the nonstripped mixture gives heat proportional to the sum of the two sugars. Calorimetry of cellulolysis products from individual exo- and endocellulases, and from their reconstituted mixture, was carried out to develop a microbial calorimetric means for demonstrating enzyme synergism.     

Development and validation of a kinetic model for enzymatic saccharification of lignocellulosic biomass

A multireaction kinetic model was developed for closed-system enzymatic hydrolysis of lignocellulosic biomass such as corn stover. Three hydrolysis reactions were modeled, two heterogeneous reactions for cellulose breakdown to cellobiose and glucose and one homogeneous reaction for hydrolyzing cellobiose to glucose. Cellulase adsorption onto pretreated lignocellulose was modeled via a Langmuir-type isotherm. The sugar products of cellulose hydrolysis, cellobiose and glucose, as well as xylose, the dominant sugar prevalent in most hemicellulose hydrolyzates, were assumed to competitively inhibit the enzymatic hydrolysis reactions. Model parameters were estimated from experimental data generated using dilute acid pretreated corn stover as the substrate. The model performed well in predicting cellulose hydrolysis trends at experimental conditions both inside and outside the design space used for parameter estimation and can be used for in silico process optimization.     

Study of cellulases from a newly isolated thermophilic and cellulolytic <Emphasis Type="Italic">Brevibacillus</Emphasis> sp. strain JXL

A potentially novel aerobic, thermophilic, and cellulolytic bacterium designated as Brevibacillus sp. strain JXL was isolated from swine waste. Strain JXL can utilize a broad range of carbohydrates including: cellulose, carboxymethylcellulose (CMC), xylan, cellobiose, glucose, and xylose. In two different media supplemented with crystalline cellulose and CMC at 57°C under aeration, strain JXL produced a basal level of cellulases as FPU of 0.02 IU/ml in the crude culture supernatant. When glucose or cellobiose was used besides cellulose, cellulase activities were enhanced ten times during the first 24 h, but with no significant difference between these two simple sugars. After that time, however, culture with glucose demonstrated higher cellulase activities compared with that from cellobiose. Similar trend and effect on cellulase activities were also obtained when glucose or cellobiose served as a single substrate. The optimal doses of cellobiose and glucose for cellulase induction were 0.5 and 1%. These inducing effects were further confirmed by scanning electron microscopy (SEM) images, which indicated the presence of extracellular protuberant structures. These cellulosome-resembling structures were most abundant in culture with glucose, followed by cellobiose and without sugar addition. With respect to cellulase activity assay, crude cellulases had an optimal temperature of 50°C and a broad optimal pH range of 6–8. These cellulases also had high thermotolerance as evidenced by retaining more than 50% activity at 100°C after 1 h. In summary, this is the first study to show that the genus Brevibacillus may have strains that can degrade cellulose.     

A cellulase-free xylanase from alkali-tolerantAspergillus fischeri Fxn1

Summary An alkali-tolerant fungusAsperqillus fischeri Fxn1 isolated from xylan enrichment grew in the pH range 5–10 and secreted an extracellular cellulase-free xylanase. Arabinose, lactose, maltose, cellobiose and glucose induced low levels of xylanase (1.8–9.0 IU/ml), whereas xylose, xylan and wheat bran induced higher level (34–45 IU/ml).CMcellulose and FPcellulose did not support growth. The optimum pH of xylanase was 6.0–6.5 and it was stable in a wide range of pH 5–9.5. The optimum temperature was 60°C and it was stable upto 55°C. The half-lives at 50 and 55 °C were 240 and 40 min. respectively. This enzyme released reducing sugars from pulp at pH 9.0 and 40°C.     

Simultaneous co-fermentation of mixed sugars: a promising strategy for producing cellulosic ethanol

The lack of microbial strains capable of fermenting all sugars prevalent in plant cell wall hydrolyzates to ethanol is a major challenge. Although naturally existing or engineered microorganisms can ferment mixed sugars (glucose, xylose and galactose) in these hydrolyzates sequentially, the preferential utilization of glucose to non-glucose sugars often results in lower overall yield and productivity of ethanol. Therefore, numerous metabolic engineering approaches have been attempted to construct optimal microorganisms capable of co-fermenting mixed sugars simultaneously. Here, we present recent findings and breakthroughs in engineering yeast for improved ethanol production from mixed sugars. In particular, this review discusses new sugar transporters, various strategies for simultaneous co-fermentation of mixed sugars, and potential applications of co-fermentation for producing fuels and chemicals.     

Engineered Escherichia coli capable of co-utilization of cellobiose and xylose

Natural ability to ferment the major sugars (glucose and xylose) of plant biomass is an advantageous feature of Escherichia coli in biofuel production. However, excess glucose completely inhibits xylose utilization in E. coli and decreases yield and productivity of fermentation due to sequential utilization of xylose after glucose. As an approach to overcome this drawback, E. coli MG1655 was engineered for simultaneous glucose (in the form of cellobiose) and xylose utilization by a combination of genetic and evolutionary engineering strategies. The recombinant E. coli was capable of utilizing approximately 6 g/L of cellobiose and 2 g/L of xylose in approximately 36 h, whereas wild-type E. coli was unable to utilize xylose completely in the presence of 6 g/L of glucose even after 75 hours. The engineered strain also co-utilized cellobiose with mannose or galactose; however, it was unable to metabolize cellobiose in the presence of arabinose and glucose. Successful cellobiose and xylose co-fermentation is a vital step for simultaneous saccharification and co-fermentation process and a promising step towards consolidated bioprocessing.     

亚硫酸盐甘蔗渣浆酶解液发酵制备乙醇

以亚硫酸盐甘蔗渣浆酶解液作为原料,利用C. shehatae发酵制取燃料乙醇。结果表明：还原糖最适初始质量浓度为葡萄糖140 g/L、木糖60 g/L、酶解液总糖80 g/L。利用初始葡萄糖55.06 g/L、木糖11.18 g/L、纤维二糖4.51 g/L的亚硫酸盐甘蔗渣浆酶解液发酵,经18 h获得乙醇22.98 g/L。乙醇得率为67.23%,葡萄糖利用率为99.27%,木糖利用率为32.96%,C. shehatae适合作为蔗渣为原料的乙醇发酵菌株。     

Analysis of biomass sugars and galacturonic acid by gradient anion exchange chromatography and pulsed amperometric detection without post-column addition

While the most accurate method for analysis of sugars in biomass is based on gas chromatography of trimethylsilane or alditol acetate derivatives of sugars, the derivation method is time consuming and laborious. In comparison, sample preparation for sugar analysis of hydrolyzed biomass samples using liquid chromatography is a simple dilution procedure with water. A gradient HPLC method using a anion-exchange column and pulsed-amperometric detection modified to reduce analysis time from 75 to 40 min was further improved. The new method no longer requires post-column addition to stablilize the baseline using a pulsed-amperometric detector with the mobile phase gradient. The method provides good resolution of arabinose, rhamnose, galactose, xylose, glucose, fructose, sucrose, cellobiose, and galacturonic acid in both standards and hydrolyzed citrus waste materials. By changing the waveform used with the PAD detector, the requirement for post-column addition was eliminated while maintaining a stable baseline.     

Characterization of a recombinant mannobiose 2-epimerase from Spirochaeta thermophila that is suggested to be a cellobiose 2-epimerase

A purified recombinant enzyme from Spirochaeta thermophila, that is suggested to be a cellobiose 2-epimerase, was a 47 kDa monomer with a specific activity of 29.2 U min^?1 for mannobiose. The epimerization activity of the recombinant enzyme for mannobiose was maximal at pH 7.0 and 60 °C with a half-life of 124 h. The enzyme exhibited a higher epimerization activity for mannose or the mannose moiety at the reducing end of β- and α-1,4-glycosyl-mannose than for glucose or the glucose moiety of β- and α-1,4-glycosyl-glucose. The enzyme was identified as a mannobiose 2-epimerase by evaluating its substrate specificity with not only glucose-containing sugars but also mannose-containing sugars. The activities of the reported cellobiose 2-epimerases from Caldicellulosiruptor saccharolyticus, Dictyoglomus turgidum and Ruminococcus marinus for mannobiose were higher than those for cellobiose, strongly suggesting that these enzymes are not cellobiose 2-epimerases but are mannobiose 2-epimerases.     

Utilization of cellobiose and D-glucose by Clostridium thermocellum ATCC-27405

Cultures of Clostridium thermocellum ATCC-27405, maintained on cellulose and not adapted to grow on glucose utilize cellobiose preferentially over D-glucose, and are only able to initiate growth on D-glucose when the cellobiose has been exhausted from the growth medium. However, D-glucose is the carbon source preferentially utilized when cultures of this microorganism, previously adapted for growth on glucose, are transferred to a medium with equivalent concentrations of both sugars. One reason for the preferential utilization of glucose over that of cellobiose might be the competitive inhibition of cellobiose phosphorylase by intracellular glucose accumulation. When in the glucose-adapted cultures the pressure to grow on glucose as the sole carbon source is again released, both sugars can be simultaneously utilized.     

An improved method for analysis of biomass sugars and galacturonic acid by anion exchange chromatography

The most accurate analysis method for sugars in biomass, based on gas chromatography, requires a time consuming and laborious sample derivatation to trimethylsilanes or alditol acetates. In comparison, sample preparations for sugar analysis by liquid chromatography are simple water dilutions. However, HPLC methods either require long analysis times, use of expensive solvents, or do not give good resolution of sugars. A gradient method developed previously using a Dionex PA-1 column and pulsed-amperometric detection was modified to reduce analysis time from 75 to less than 40?min and provide good resolution of arabinose, rhamnose, galactose, xylose, glucose, fructose, sucrose, cellobiose, and galacturonic acid in both standards and hydrolyzed citrus waste biomass.     

Influence of the presence of Zymomonas anaerobia on the conversion of cellobiose, glucose, and xylose to ethanol by Clostridium saccharolyticum

To convert sugar mixtures containing cellobiose, glucose, and xylose to ethanol in a single step, the possibility of using a coculture consisting of Clostridium saccharolyticum and Zymomonas anaerobia was studied. In monoculture, C. saccharolyticum utilized all three sugars; however, it preferentially utilized glucose and produced acetic acid in addition to ethanol. The formation of acetic acid from the metabolism of glucose inhibited the growth of C. saccharolyticum and, consequently, the utilization of cellobiose and xylose. In monoculture, Z. anaerobia utilized glucose at a rate of 50 g/L day, but it did not ferment cellobiose or xylose. In coculture, Z. anaerobia converted most of the glucose to ethanol during the lag phase of growth of C. saccharolyticum, which then converted cellobiose and xylose to ethanol. The use of this coculture increased both the rate and the efficiency of the conversion of these three sugars to ethanol, and produced relatively small amounts of acetic acid.     

Utilization of glucose and cellobiose by the microflora of soil enriched with cellulose

The ability of soil microflora to utilize glucose or celloboise was found to depend on previous incubation of the soil with glucose, celloboise or cellulose. Glucose was utilized more rapidly than cellobiose in soil preincubated with glucose or cellobiose. The opposite situation was observed in soil preincubated with cellulose. In the presence of a mixture of both sugars the rate of utilization of one of them was decreased by the second and this decrease could be characterized as competitive inhibition. Glucose accumulated in the medium during utilization of cellobiose alone in soil preincubated with cellulose. This phenomenon was not observed during the utilization of cellobiose in soil preincubated with glucose or cellobiose.     

Acid hydrolysis of sunflower seed husks for production of single cell protein

Summary Sunflower seed husks were chosen as a typical lignocellulosic waste product of low value. This model substrate was hydrolyzed with sulphuric acid at 120°C. The hydrolysis was carried out in two steps: hydrolysis of the pentosan fraction and subsequent hydrolysis of the cellulose fraction. The pentosan fraction was nearly quantitatively hydrolyzed. For the cellulose hydrolysis the yield was 79% of the theoretical yield. The hydrolyzates were neutralized to pH 5 with solid calcium hydroxide and used for preparation of growth media forCandida yeasts andPaecilomyces variotii. For the pentosan hydrolyzates the yields of yeast biomass were 35–36 g per 100 g available reducing sugars (supplied to the medium). In cellulose hydrolyzates the corresponding yields were 45–48 g withCandida utilis andC. tropicalis and about 30 g withC. pseudotropicalis. P. variotii was noticeably superior to the yeasts. In pentosan hydrolyzates it produced 63 g dry mycelium from 100 g reducing sugars supplied; in cellulose hydrolyzates, 94 g. This suggests that it must be an effective utilizer of a wide range of compounds, for example, organic acids in the medium.     

Cofermentation of glucose, xylose, and cellobiose by the beetle-associated yeast Spathaspora passalidarum

Fermentation of cellulosic and hemicellulosic sugars from biomass could resolve food-versus-fuel conflicts inherent in the bioconversion of grains. However, the inability to coferment glucose and xylose is a major challenge to the economical use of lignocellulose as a feedstock. Simultaneous cofermentation of glucose, xylose, and cellobiose is problematic for most microbes because glucose represses utilization of the other saccharides. Surprisingly, the ascomycetous, beetle-associated yeast Spathaspora passalidarum, which ferments xylose and cellobiose natively, can also coferment these two sugars in the presence of 30 g/liter glucose. S. passalidarum simultaneously assimilates glucose and xylose aerobically, it simultaneously coferments glucose, cellobiose, and xylose with an ethanol yield of 0.42 g/g, and it has a specific ethanol production rate on xylose more than 3 times that of the corresponding rate on glucose. Moreover, an adapted strain of S. passalidarum produced 39 g/liter ethanol with a yield of 0.37 g/g sugars from a hardwood hydrolysate. Metabolome analysis of S. passalidarum before onset and during the fermentations of glucose and xylose showed that the flux of glycolytic intermediates is significantly higher on xylose than on glucose. The high affinity of its xylose reductase activities for NADH and xylose combined with allosteric activation of glycolysis probably accounts in part for its unusual capacities. These features make S. passalidarum very attractive for studying regulatory mechanisms enabling bioconversion of lignocellulosic materials by yeasts.     

Xylose and arabinose utilization by the rumen bacterium Butyrivibrio fibrisolvens

Abstract The rumen bacterium Butyrivibrio fibrisolvens strain D1 co-utilized xylose and glucose in batch culture, but there was a marked preference for glucose over arabinose. When both pentoses were provided, xylose was preferred over arabinose. Strain D1 co-utilized a combination of either pentose and cellobiose, but preferred pentoses over maltose. Pentose sugars were depleted less rapidly in the presence of sucrose than controls containing only pentose. In contrast, B. fibrisolvens strain A38 exhibited a strong preference for disaccharides, including maltose, over either xylose or arabinose. Theoretical maximum growth yields for strain D1v in single-substrate continuous culture were highest for sucrose and cellobiose and the maintenance energy coefficient for arabinose was at least 3.8-fold greater than for other substrates. We suggest that B. fibrisolvens may have evolved a mechanism to utilize certain sugars before arabinose in order to avoid this high maintenance energy expenditure.     

CHEMICAL COMPOSITION AND STRUCTURE OF THE CELL WALLS OF THE CONCHOCELIS AND THALLUS PHASES OF PORPHYRA TENERA (RHODOPHYCEAE)1,2

Purified cell walls were prepared from both the conchocelis and thallus phases of Porphyra tenera (Kjellm.). The nitrogen content of cell walls from the conchocelis was significantly greater than that for the thallus cell walls, being 3.35 ± 0.26% and 2.39± 0.03%, respectively. Amino acid analysis revealed important differences. The conchocelis cell wall hydrolyzates were richer in aspartic acid, glutamic acid, methionine, and basic amino acids. The thallus cell wall hydrolyzates, however, contained much more glycine and alanine than did those of the conchocelis. Hydroxyproline was not detected in cell walls of either phase. The neutral sugar content of cell wall hydrolyzates from the thallus was more than double that from the conchocelis being 83.6% and 34.5%, respectively. The former contained predominantly mannose which accounted for 72.2% of the neutral sugars while the latter was principally galactose (49.9%) and glucose (36.4%). Methylation analysis confirmed the presence of cellulose microfibrils in the conchocelis in contrast to xylan microfibrils in the thallus. The results establish that the conchocelis and thallus phases of P. tenera differ markedly in the structure and composition of the cell walls.