Biorefining of wood: combined production of ethanol and xylanase from waste fiber sludge

The possibility to utilize fiber sludge, waste fibers from pulp mills and lignocellulose-based biorefineries, for combined production of liquid biofuel and biocatalysts was investigated. Without pretreatment, fiber sludge was hydrolyzed enzymatically to monosaccharides, mainly glucose and xylose. In the first of two sequential fermentation steps, the fiber sludge hydrolysate was fermented to cellulosic ethanol with the yeast Saccharomyces cerevisiae. Although the final ethanol yields were similar, the ethanol productivity after 9.5?h was 3.3?g/l/h for the fiber sludge hydrolysate compared with only 2.2?g/l/h for a reference fermentation with similar sugar content. In the second fermentation step, the spent fiber sludge hydrolysate (the stillage obtained after distillation) was used as growth medium for recombinant Aspergillus niger expressing the xylanase-encoding Trichoderma reesei (Hypocrea jecorina) xyn2 gene. The xylanase activity obtained with the spent fiber sludge hydrolysate (8,500?nkat/ml) was higher than that obtained in a standard medium with similar monosaccharide content (1,400?nkat/ml). Analyses based on deglycosylation with N-glycosidase?F suggest that the main part of the recombinant xylanase was unglycosylated and had molecular mass of 20.7?kDa, while a minor part had N-linked glycosylation and molecular mass of 23.6?kDa. Chemical analyses of the growth medium showed that important carbon sources in the spent fiber sludge hydrolysate included xylose, small aliphatic acids, and oligosaccharides. The results show the potential of converting waste fiber sludge to liquid biofuel and enzymes as coproducts in lignocellulose-based biorefineries.     

Production of cellulosic ethanol and enzyme from waste fiber sludge using SSF,recycling of hydrolytic enzymes and yeast,and recombinant cellulase-producing Aspergillus niger

Bioethanol and enzymes were produced from fiber sludges through sequential microbial cultivations. After a first simultaneous saccharification and fermentation (SSF) with yeast, the bioethanol concentrations of sulfate and sulfite fiber sludges were 45.6 and 64.7 g/L, respectively. The second SSF, which included fresh fiber sludges and recycled yeast and enzymes from the first SSF, resulted in ethanol concentrations of 38.3 g/L for sulfate fiber sludge and 24.4 g/L for sulfite fiber sludge. Aspergillus niger carrying the endoglucanase-encoding Cel7B gene of Trichoderma reesei was grown in the spent fiber sludge hydrolysates. The cellulase activities obtained with spent hydrolysates of sulfate and sulfite fiber sludges were 2,700 and 2,900 nkat/mL, respectively. The high cellulase activities produced by using stillage and the significant ethanol concentrations produced in the second SSF suggest that onsite enzyme production and recycling of enzyme are realistic concepts that warrant further attention.     

Reducing agents improve enzymatic hydrolysis of cellulosic substrates in the presence of pretreatment liquid

Enzymatic hydrolysis of pretreated lignocellulosic substrates has emerged as an interesting option to produce sugars that can be converted to liquid biofuels and other commodities using microbial biocatalysts. Lignocellulosic substrates are pretreated to make them more accessible to cellulolytic enzymes, but the pretreatment liquid partially inhibits subsequent enzymatic hydrolysis. The presence of pretreatment liquid from Norway spruce resulted in a 63% decrease in the enzymatic saccharification of Avicel compared to when the reaction was performed in a buffered aqueous solution. The addition of 15 mM of a reducing agent (hydrogen sulfite, dithionite, or dithiothreitol) to reaction mixtures with the pretreatment liquid resulted in up to 54% improvement of the saccharification efficiency. When the reducing agents were added to reaction mixtures without pretreatment liquid, there was a 13-39% decrease in saccharification efficiency. In the presence of pretreatment liquid, the addition of 15 mM dithionite to Avicel, α-cellulose or filter cake of pretreated spruce wood resulted in improvements between 25 and 33%. Positive effects (6-17%) of reducing agents were also observed in experiments with carboxymethyl cellulose and 2-hydroxyethyl cellulose. The approach to add reducing agents appears useful for facilitating the utilization of enzymes to convert cellulosic substrates in industrial processes.     

Effect of sulfur oxyanions on lignocellulose-derived fermentation inhibitors

Recent results show that treatments with reducing agents, including the sulfur oxyanions dithionite and hydrogen sulfite, efficiently improve the fermentability of inhibitory lignocellulose hydrolysates, and that the treatments are effective when the reducing agents are added in situ into the fermentation vessel at low temperature. In the present investigation, dithionite was added to medium with model inhibitors (coniferyl aldehyde, furfural, 5-hydroxymethylfurfural, or acetic acid) and the effects on the fermentability with yeast were studied. Addition of 10 mM dithionite to medium containing 2.5 mM coniferyl aldehyde resulted in a nine-fold increase in the glucose consumption rate and a three-fold increase in the ethanol yield. To investigate the mechanism behind the positive effects of adding sulfur oxyanions, mixtures containing 2.5 mM of a model inhibitor (an aromatic compound, a furan aldehyde, or an aliphatic acid) and 15 mM dithionite or hydrogen sulfite were analyzed using mass spectrometry (MS). The results of the analyses, which were performed by using UHPLC-ESI-TOF-MS and UHPLC-LTQ/Orbitrap-MS/MS, indicate that the positive effects of sulfur oxyanions are primarily due to their capability to react with and sulfonate inhibitory aromatic compounds and furan aldehydes at low temperature and slightly acidic pH (such as 25°C and pH 5.5).     

Interaction of the cysteine proteinase inhibitor chicken cystatin with papain

The two forms of chicken cystatin, with different isoelectric points, that have been described previously were indistinguishable in analyses of amino- and carboxy-terminal residues, amino acid composition, and peptide maps. The two forms thus are highly similar and most likely differ only in an amide group or in a small charged substituent. The binding of either cystatin form to highly purified, active papain was accompanied by the same pronounced changes in near-ultraviolet circular dichroism, ultraviolet absorption, and fluorescence emission. These changes were compatible with perturbations of the environment of aromatic residues in one or both proteins of the complex, arising from local interactions or from a conformational change. Modification of the single tryptophan residue of cystatin, at position 104, with N-bromosuccinimide resulted in considerably smaller spectroscopic changes on binding of the inhibitor to papain, indicating that the environment of this residue is affected by the binding. Analogous modification of Trp-69 and Trp-177 of papain markedly affected the fluorescence changes observed on binding of cystatin to the enzyme, similarly suggesting that these two residues of papain are involved in the interaction. The fluorescence increase of papain at alkaline pH, arising from Trp-177 and due to deprotonization of the adjacent His-159, was abolished on binding of cystatin to the enzyme, further supporting the proposal that this region of papain participates in the interaction with the inhibitor. A stoichiometry of binding of either cystatin form to papain of 1:1 and a lower limit for the binding constant of 10(9) M-1 were determined by titrations monitored by either the ultraviolet absorption or fluorescence changes induced by the interaction.     

Soil changes in different age classes of Norway spruce (Picea abies (L.) Karst.) on afforested farmland

The aim of this study was to test the hypothesis that afforestation changes the content and distribution of soil organic carbon, nutrients and pH in the A-horizon of land previously used in agriculture, and that such soil changes depend on stand development. The investigation was evaluated as a completely randomised design with three treatments representing different age classes of trees: 20 years (Y20), 40 years (Y40) and 55 years (Y55). Eighteen trial plots, six per treatment, were established in plantations of Picea abies (L.) Karst. on soils of similar texture and mineralogy. Tree volume was 220 m³ ha^-1 in Y20, 400 in Y40 and 440 m³ ha^-1 in Y55.Concentrations of carbon (C) and nitrogen (N) were significantly higher in the uppermost part of the soil in the older stands Y40 and Y55 than in Y20. The total amount of organic C in the litter layer plus the top 15 cm of the soil differed between age classes, with Y40 and Y55 having the largest amounts. A reference layer (15–20 cm) was used in calculating the amount of soil C that had accumulated in the horizon since afforestation, being about 10 tonnes ha^-1 of C in Y20 and 19 tonnes ha^-1 in Y40 and Y55.Cation exchange capacity (CEC) and base saturation (BS) was higher in the older stands. Carbon contents and CEC were strongly correlated. In Y40 and Y55, pH was significantly lower than in Y20 in the lower part of the soil horizon. There was a general decrease with depth of C, N, CEC, K⁺ and Mg²⁺ in the soil horizon. BS, Ca²⁺, Na⁺ and pH showed a somewhat different pattern of distribution, with deceasing values in the upper part of the soil horizon and increasing values in the lower part of the soil horizon.Abbreviations BD Bulk density - CEC cation exchange capacity - BS base saturation - Ca²⁺ calcium ion - Mg²⁺ magnesium ion - K⁺ potassium ion - Na⁺ sodium ion - C carbon - Ca _a accumulated carbon content - C _t total carbon content - N nitrogen - Y20 age class 20 years - Y40 age class 40 years - Y55 age class 55 years     

Cellulase Production from Spent Lignocellulose Hydrolysates by Recombinant Aspergillus niger

A recombinant Aspergillus niger strain expressing the Hypocrea jecorina endoglucanase Cel7B was grown on spent hydrolysates (stillage) from sugarcane bagasse and spruce wood. The spent hydrolysates served as excellent growth media for the Cel7B-producing strain, A. niger D15[egI], which displayed higher endoglucanase activities in the spent hydrolysates than in standard medium with a comparable monosaccharide content (e.g., 2,100 nkat/ml in spent bagasse hydrolysate compared to 480 nkat/ml in standard glucose-based medium). In addition, A. niger D15[egI] was also able to consume or convert other lignocellulose-derived compounds, such as acetic acid, furan aldehydes, and phenolic compounds, which are recognized as inhibitors of yeast during ethanolic fermentation. The results indicate that enzymes can be produced from the stillage stream as a high-value coproduct in second-generation bioethanol plants in a way that also facilitates recirculation of process water.Energy security, petroleum depletion, and global warming have been the main driving forces for the development of renewable fuels that can replace petroleum-derived fuels, such as gasoline and diesel. Bioethanol is currently the most commonly used renewable automobile fuel. It is largely produced by fermentation of sugar- or starch-containing feedstocks, such as cane sugar, corn, and wheat. However, the supply of these crops is relatively limited and many of them can be considered human food resources. Lignocellulose is a more-abundant and less-expensive raw material with the potential to give a high net energy gain (11, 17).In the production of bioethanol from lignocellulosic materials, hydrolytic enzymes, such as cellulases and cellobiases, can be used to convert the lignocellulosic polysaccharides to monosaccharides. Microorganisms can be used to ferment the monosaccharides to ethanol. The yeast Saccharomyces cerevisiae is one of the most suitable microorganisms for ethanol production and is favored in industrial processes. However, S. cerevisiae only metabolizes hexose sugars. Many lignocellulosic materials consist of a significant proportion of xylan and arabinan, which give rise to pentose sugars. The cost of enzymes for the hydrolysis of polysaccharides and the inability of S. cerevisiae to utilize pentose sugars have been pointed out as two bottlenecks for commercialization of cellulosic ethanol production (9, 25). Considerable research efforts have therefore been focused on reducing the enzyme cost by producing more-efficient enzymes from cheaper growth media (25). Other efforts have been focused on different approaches to convert pentose sugars to ethanol by using recombinant microorganisms (3, 10).A novel approach to reduce the enzyme cost and to optimally utilize all sugars generated from lignocellulose would be to produce hydrolytic enzymes, such as cellulases, from the pentose fraction remaining after consumption of hexoses by S. cerevisiae (Fig. ​(Fig.1).1). The cellulases produced can then be used on site in the next round of hydrolysis of the lignocellulosic feedstock and thereby reduce the dependence on externally produced enzymes.Open in a separate windowFIG. 1.Schematic representation of the experimental approach and on-site enzyme production in a cellulose-to-ethanol process.Furthermore, it is desirable to recycle the process water in an ethanol production plant to minimize the production costs. However, lignocellulose hydrolysates are very complex and contain a wide range of different compounds. Some of these compounds, such as furan aldehydes, aliphatic acids, and phenolic compounds, inhibit the yeast S. cerevisiae, which results in lower ethanol yield and productivity. Recycling of the process water can lead to a buildup in the concentration of inhibitors, which is a phenomenon that has been pointed out as an obstacle to reusing the stillage stream (1, 35). There are several methods to avoid inhibitor-related problems, but they are often associated with additional process cost (40). However, A. niger is an organism that can utilize a broad range of compounds as nutrients, possibly including compounds that inhibit S. cerevisiae. It would be convenient if the A. niger cells could metabolize such compounds and thereby, due to the removal of inhibitors, make it more feasible to reuse the process water.In this study, we explored the possibility of utilizing sugarcane bagasse and spruce wood for ethanol production and using the spent hydrolysates (stillage) for production of the Hypocrea jecorina cellulase Cel7B (formerly called endoglucanase I) by a recombinant strain of Aspergillus niger. Simultaneously, the Cel7B-producing recombinant A. niger strain also removed inhibitory lignocellulose-derived products, thus facilitating recycling of process water.     

Kinetics of binding of chicken cystatin to papain

The kinetics of binding of chicken cystatin to papain were studied by stopped-flow fluorometry under pseudo-first-order conditions, i.e., with an excess of inhibitor. All reactions showed first-order behavior, and the observed pseudo-first-order rate constant increased linearly with the cystatin concentration up to the highest concentration that could be studied, 35 microM. The analyses thus provided no evidence for a limiting rate resulting from a conformational change stabilizing an initial encounter complex, in contrast with previous studies of reactions between serine proteinases and their protein inhibitors. The second-order association rate constant for complex formation was 9.9 X 10(6) M-1 s-1 at 25 degrees C, pH 7.4, I = 0.15, for both forms of cystatin, 1 and 2. This value approaches that expected for a diffusion-controlled rate. The temperature dependence of the association rate constant gave an enthalpy of activation at 25 degrees C of 31.5 kJ mol-1 and an entropy of activation at 25 degrees C of -7 J K-1 mol-1, compatible with no appreciable conformational change during the reaction. The association rate constant was independent of pH between pH 6 and 8 but decreased at lower and higher pH in a manner consistent with involvement of an unprotonated acid group with a pKa of 4-4.5 and a protonated basic group with a pKa of 9-9.5 in the interaction. The association rate constant was unaffected by ionic strengths between 0.15 and 1.0 but decreased somewhat at lower ionic strengths. Incubation of the complex between cystatin 2 and papain with an excess of cystatin 1 resulted in slow displacement of cystatin 2 from the complex.(ABSTRACT TRUNCATED AT 250 WORDS)     

Why Aren't Advanced High–Strength Steels More Widely Used?: Stakeholder Preferences and Perceived Barriers to New Materials

Advanced high‐strength steels may reduce the use of nonrenewable resources and energy given that the amount of material needed is smaller, compared to traditional steel grades. Still, advanced steel grades are not utilized to the extent that could be expected. This study examines stakeholders’ preferences of steel characteristics and perceived barriers to the introduction of new materials. Focus group interviews were used to identify steel characteristics and perceived barriers. Stakeholder preferences of steel characteristics were evaluated through a conjoint analysis; the results showed that low weight was given the highest priority, followed by high impact strength and low price. Low chromium content was the steel characteristic of least interest. Perceived barriers to the introduction of high‐strength steel were categorized as technical barriers, knowledge barriers, scrap management barriers, suitability barriers, and cost barriers.     

Field testing of transgenic aspen from large greenhouse screening identifies unexpected winners

Trees constitute promising renewable feedstocks for biorefinery using biochemical conversion, but their recalcitrance restricts their attractiveness for the industry. To obtain trees with reduced recalcitrance, large-scale genetic engineering experiments were performed in hybrid aspen blindly targeting genes expressed during wood formation and 32 lines representing seven constructs were selected for characterization in the field. Here we report phenotypes of five-year old trees considering 49 traits related to growth and wood properties. The best performing construct considering growth and glucose yield in saccharification with acid pretreatment had suppressed expression of the gene encoding an uncharacterized 2-oxoglutarate-dependent dioxygenase (2OGD). It showed minor changes in wood chemistry but increased nanoporosity and glucose conversion. Suppressed levels of SUCROSE SYNTHASE, (SuSy), CINNAMATE 4-HYDROXYLASE (C4H) and increased levels of GTPase activating protein for ADP-ribosylation factor ZAC led to significant growth reductions and anatomical abnormalities. However, C4H and SuSy constructs greatly improved glucose yields in saccharification without and with pretreatment, respectively. Traits associated with high glucose yields were different for saccharification with and without pretreatment. While carbohydrates, phenolics and tension wood contents positively impacted the yields without pretreatment and growth, lignin content and S/G ratio were negative factors, the yields with pretreatment positively correlated with S lignin and negatively with carbohydrate contents. The genotypes with high glucose yields had increased nanoporosity and mGlcA/Xyl ratio, and some had shorter polymers extractable with subcritical water compared to wild-type. The pilot-scale industrial-like pretreatment of best-performing 2OGD construct confirmed its superior sugar yields, supporting our strategy.