Compositional analysis of polysaccharides via solvolysis with liquid hydrogen fluoride

A simple procedure is described for solvolysis of the glycosidic linkages of polysaccharides and related compounds in and by liquid hydrogen fluoride (HF), which does so without destruction of acid-sensitive sugars or formation of reversion products from the released monosaccharides. Following solvolysis, water is added to effect hydrolysis of the resulting glycosyl fluorides. Liberated reducing sugars are determined qualitatively and quantitatively, without derivatization, by high-performance liquid chromatography.     

川西高海拔增温和加氮对红杉凋落物有机组分释放的影响

对川西高山树线红杉新鲜凋落物中有机组分于11月进行自然条件(对照)、加氮(2 g N·m^-2)、增温(顶开式培养室)、加氮+增温4个处理的原位培养,并监测凋落物中有机组分的分解动态.结果表明: 在试验开始后4个月内,增温、加氮以及加氮+增温处理比对照显著促进了红杉凋落物中水溶性糖、水溶性酚和多酚的分解,但随着培养时间的延长,累积分解量的差异逐渐缩小.与对照相比,增温、加氮和增温+加氮处理均抑制红杉凋落物中CH₂Cl₂提取组分、酸溶碳水化合物、酸溶木质素和非酸溶木质素分解,其中增温处理抑制作用最强,加氮处理抑制效果最弱,增温+加氮处理介于二者之间;增温处理对非酸溶木质素和CH₂Cl₂提取组分的半分解周期延长1倍以上,热水溶组分的半分解周期延长50%以上.在原位培养条件下,红杉新鲜凋落物中水溶性糖、水溶性酚、多酚、酸溶碳水化合物、酸溶木质素是较容易分解的有机组分,半分解周期分别为182、159、127、154和190 d;热水溶组分、CH₂Cl₂提取组分和非酸溶木质素是较难分解的有机组分,半分解周期分别是209、302和318 d;尽管低温季节(11月至次年3月)极其寒冷,气温均低于0 ℃,常被认为是微生物活性最弱、有机物分解最慢的时期,但结果显示低温季节期间红杉凋落物各有机组分却分解最快.因此,氮沉降和升温将迟滞该区域高寒红杉林凋落物的分解.这将有利于高寒森林生态系统的土壤碳固持.     

Improved pretreatment of lignocellulosic biomass using enzymatically-generated peracetic acid

Release of sugars from lignocellulosic biomass is inefficient because lignin, an aromatic polymer, blocks access of enzymes to the sugar polymers. Pretreatments remove lignin and disrupt its structure, thereby enhancing sugar release. In previous work, enzymatically generated peracetic acid was used to pretreat aspen wood. This pretreatment removed 45% of the lignin and the subsequent saccharification released 97% of the sugars remaining after pretreatment. In this paper, the amount of enzyme needed is reduced tenfold using first, an improved enzyme variant that makes twice as much peracetic acid and second, a two-phase reaction to generate the peracetic acid, which allows enzyme reuse. In addition, the eight pretreatment cycles are reduced to only one by increasing the volume of peracetic acid solution and increasing the temperature to 60 °C and the reaction time to 6 h. For the pretreatment step, the weight ratio of peracetic acid to wood determines the amount of lignin removed.     

Fast and efficient alkaline peroxide treatment to enhance the enzymatic digestibility of steam-exploded softwood substrates.

The enzymatic digestibility of steam-exploded Douglas-fir wood chips (steam exploded at 195 degrees C, 4.5 min, and 4.5% (w/w) SO(2)) was significantly improved using an optimized alkaline peroxide treatment. Best hydrolysis yields were attained when the steam-exploded material was post-treated with 1% hydrogen peroxide at pH 11.5 and 80 degrees C for 45 min. This alkaline peroxide treatment was applied directly to the water-washed, steam-exploded material eliminating the need for independent alkali treatment with 0.4% NaOH, which has been traditionally used to post-treat wood samples to try to remove residual lignin. Approximately 90% of the lignin in the original wood was solubilized by this novel procedure, leaving a cellulose-rich residue that was completely hydrolyzed within 48 h, using an enzyme loading of 10 FPU/g cellulose. About 82% of the originally available polysaccharide components of the wood could be recovered. The 18% of the carbohydrate that was not recovered was lost primarily to sugar degradation during steam explosion.     

Valorization of cashew apple bagasse using acetic acid pretreatment: Production of cellulosic ethanol and lignin for their use as sunscreen ingredients

The present study focuses on the fractionation of cashew apple bagasse via a pretreatment using acetic acid as a delignifying agent and sulfuric acid as an external catalyst. As expected, the concentrations of both acids and the incubation time dramatically affected delignification and hemicellulose solubilization. Under the optimal pretreatment conditions, recycling of the spent liquor had no apparent impact on the chemical composition of the pretreated material, yield of sugar produced via enzymatic hydrolysis (∼37 g/L reducing sugars at 7.5% (w/v) solid loading), or yield of ethanol obtained via fermentation with Saccharomyces cerevisiae (∼16 g/L at 10% (w/v) solid loading). The lignin recovered from the spent liquor showed a good ultraviolet protective effect; the addition of 5% (w/w) of the biopolymer increased the sun protection factor of a commercial sunscreen lotion from 21.62 to 40.71. The combined use of hydrogen peroxide and ultraviolet radiation reduced the organosolv lignin color (absorbance at 450 nm was four times lower) owing to aromatic ring cleavage, but cosmetics containing whitened organosolv lignin had low sun protection factor values. In summary, the results obtained in this study demonstrate the utility of organic acid pretreatment in the valorization of lignocellulosic materials.     

Preparation and use of α-maltosyl fluoride as a substrate by beta amylase

The preparation of pure (amorphous) α-maltosyl fluoride is described. A modification of the procedure of Brauns was used to obtain analytically pure, crystalline hepta-O-acetyl-α-maltosyl fluoride, the structure of which was assigned by¹⁹F-and¹H-n.m.r. spectroscopy. α-Maltosyl fluoride was obtained by deacetylating the heptaacetate. It behaved as a single compound on thin-layer and paper chromatography, and was essentially completely hydrolyzed to maltose and hydrogen fluoride by 0.01M sulfuric acid in 10 min at 100°. Crystalline beta amylase, likewise, catalyzed essentially complete hydrolysis of α-maltosyl fluoride to give maltose and hydrogen fluoride. The rates of hydrolysis catalyzed by beta amylase preparations from sweet potatoes and soybeans acting on a range of concentrations of the substrate produced linear curves for the relationship, 1/v vs 1/S; reaction constants for crystalline, sweet-potato enzyme were K_m 3.6 mM and V_max ~ 2 μ mol/min/mg. The finding that α-maltosyl fluoride is hydrolyzed 30–60 times faster than maltotriose demonstrates for the first time that beta amylase is capable of effecting hydrolysis at an appreciable rate of a substrate having only two d-glucose residues.     

Isolation and characterisation of cellulose obtained by a two-stage treatment with organosolv and cyanamide activated hydrogen peroxide from wheat straw

Seven wheat straw cellulose preparations were isolated by a two-stage acidic organosolv treatment followed by cyanamide activated hydrogen peroxide bleaching. The effects of concentration of acetic and formic acids on the yield of cellulose and degradation of lignin and non-cellulose polysaccharides were investigated. Organic acids were more effective than alcohols on the degradation of lignin and hemicelluloses. Formic acid/acetic acid/water (30/60/10, v/v/v) system was found to be the most effective in delignification and removal of non-cellulose polysaccharides from the straw and did not have any undesirable effects on cellulose properties such as its intrinsic viscosity. In this case, the treatment removed 94.1% of the original lignin and 76.5% of the original hemicelluloses using 0.1% HCl as a catalyst at 85 °C for 4 h. Cyanamide activated hydrogen peroxide bleaching degraded substantial amounts of residual hemicelluloses and lignin, produced the cellulose samples having a relatively high purity. Under a best condition, a cellulose relatively free of lignin (0.7%) and with intrinsic viscosity of 393 ml g⁻¹ and favourable molar mass (213,940 g mol⁻¹) was obtained. Both unbleached and bleached cellulose preparations were further characterised by FT-IR and CP/MAS ¹³C NMR spectroscopy, and thermal stability.     

Dilute sulfuric acid cycle spray flow-through pretreatment of corn stover for enhancement of sugar recovery

A cycle spray flow-through reactor was designed and used to pretreat corn stover in dilute sulfuric acid medium. The dilute sulfuric acid cycle spray flow-through (DCF) process enhanced xylose sugar yields and cellulose digestibility while increasing the removal of lignin. Within the DCF system, the xylose sugar yields of 90–93% could be achieved for corn stover pretreated with 2% (w/v) dilute sulfuric acid at 95 °C during the optimal reaction time (90 min). The remaining solid residue exhibited enzymatic digestibility of 90–95% with cellulase loading of 60 FPU/g glucan that was due to the effective lignin removal (70–75%) in this process. Compared with flow-through and compress-hot water pretreatment process, the DCF method produces a higher sugar concentration and higher xylose monomer yield. The novel DCF process provides a feasible approach for lignocellulosic material pretreatment.     

Preparation,characterization, biological activity and metabolism of all-trans retinoyl fluoride

All-trans retinoyl fluoride was prepared by treating all-trans retinoic acid with diethylaminosulfurtrifluoride. The crystalline product, which was characterized by melting point, infrared, ¹H-NMR, ¹⁹F-NMR and elementary analysis, showed λ_max at 382 nm in hexane (ε = 4.98·10⁴ M^?1·cm^?1) and at 392 nm in methanol (ε = 4.60·10⁴ M^?1·cm^?1). Its biological activity in the rat growth assay, relative to all-trans retinyl acetate, was 22% ± 10%. Upon oral administration for 5 days to vitamin A-depleted rats, retinoyl fluoride (1020 μg) was rapidly metabolized to a polar metabolite fraction and, in the intestine, to an unstable retinol-like metabolite, purpotedly 15-fluororetinol. Upon administering intraperitoneally smaller doses (47–94 μg) of [11-³H]retinoyl fluoride, which was synthesized from [11-³H] retinoic acid, radioactive retinoic acid was noted in the liver and plasma but not in the intestine. As expected, a radioactive polar fraction appeared in the intestine and liver, but radioactive retinol, retinyl ester and some common oxidation products were not detected. Of the administered radioactivity, 72% was excreted in the urine, and only 4% was found in the feces over a 7-day period. Hydrolysis of the urine gave a radioactive fraction with a polarity similar to that of retinoic acid. Retinoyl fluoride also reacts readily with glycine to yield N-retinoyl glycine. Thus, the biological activity of retinoyl fluoride can be attributed to the formation of retinoic acid, probably by way of N-retinoyl derivatives. A possible pathway for its metabolism is presented.     

Characterization of lignin-rich residues remaining after continuous super-critical water hydrolysis of poplar wood (Populus albaglandulosa) for conversion to fermentable sugars

Poplar wood flour (Populous albaglandulosa) was treated with sub- and super-critical water (subcritical: 325, 350 °C; super-critical: 380, 400, 425 °C) for 60 s at 220 ± 10 atm. Hydrochloric acid (0.05% v/v) was added to samples as acidic catalyst. The final products were separated into water soluble fraction and undegraded solids. The yields of undegraded solids were thoroughly dependent on temperature severity and mainly composed of lignin fragments. Average molecular weights of the lignins were between 1500 and 4400 Da, which was only 1/3-1/8-fold of poplar milled wood lignin (13,250 Da). DFRC (Derivatization Followed by Reductive Cleavage) analysis revealed that C6C3 phenols (coniferyl and sinapyl alcohol) were rarely detected in the lignins, indicating occurrence of two probable lignin reactions during SCW hydrolysis: lignin fragmentation via splitting of β-O-4 linkage and loss of propane side chains. These results were also confirmed by ¹H and ¹³C NMR spectroscopic analysis.     

Qualitative analysis of products formed during the acid catalyzed liquefaction of bagasse in ethylene glycol

Bagasse was liquefied in ethylene glycol (EG) catalyzed by sulfuric acid at 190 degrees C under atmospheric pressure. The compositions of the crude products obtained were analyzed after separating them into three fractions: a water-soluble fraction, an acetone-soluble fraction and a residue. With infrared, gel permeation chromatography and elemental analyses, the residue mainly included undissolved cellulose and lignin derivatives and the acetone-soluble fraction mainly contained lignin degradation products with high molecular weights. The water-soluble fraction, after further analyzed by GC-MS and HPLC, showed EG, diethylene glycol, EG derivatives, saccharides, alcohols, aldehydes, ketones, phenols, especially some acids such as formic acid, levulinic acid, acetic acid, oxalic acid and 2-hydroxy-butyric acid and their esters. The Higher Heating Value (HHV) of the residue and the acetone-soluble fractions were higher than that of bagasse. The results showed that some useful chemicals and biofuels could be obtained by this process.     

Incorporation of p-cresol into lignins via peroxidase-catalysed copolymerization in nonaqueous media

Lignin, the second most abundant biopolymer after cellulose, is a low value by-product of agricultural and wood conversion processes, including wood pulp manufacture. Copolymerization with phenols has the potential to convert by-product lignins to higher-value phenolic resins. In this initial investigation, we have studied the use of horseradish peroxidase (HRP) in aqueous dioxane to catalyse the grafting of p-cresol (p-methylphenol) onto milled wood lignin, kraft lignin, and a lignin selectively o-demethylated by a brown-rot fungus. Advantages of this system are (1) the mild reaction conditions employed and (2) the ability of HRP to function in the dioxane: water solutions which solubilize lignin. The reaction is monitored by gel permeation chromatography using a reaction system of [¹⁴C]-p-cresol with unlabeled lignins. We have found that optimal incorporation of cresol into high-molecular-weight polymer occurs at 50–70% dioxane in water under the conditions used; a maximum incorporation of ca. 4 mol% (e.g., p-cresol incorporated per C₉ lignin unit) was obtained. Blocking the phenolic hydroxyl groups of the lignin inhibits copolymerization, consistent with the proposed mechanism of phenoxy radical copolymerization for this reaction.     

Modification of corn cob meal with quarternary ammonium groups

Corn cob meal was modified with quarternary ammonium groups and subsequently extracted with 80% ethanol, water, and 5% NaOH. The fractions obtained had lower polydispersities, values, and yields than unmodified material. The yields are lower than those obtained on bagasse under the same conditions. The modification caused the drastic degradation of the ethanol-lignin (EL) fraction. The one-step extraction with NaOH/H₂O₂ gave 28·8% yield of material (calculated on the starting material) which contained 12·0% Klason lignin, and had the highest polydispersity (4·3, ). The water-soluble fractions consisted of arabinoglucuronoxylan and alkali-soluble fractions of xylan without other sugar moieties. The water-soluble fraction from NaOH/H₂O₂ extraction contained arabinoglucuronoxylan with modified arabinose and acid units. By this method higher yields could be obtained than on bagasse treated by the sequential extraction.     

Biorefining of softwoods using ethanol organosolv pulping: preliminary evaluation of process streams for manufacture of fuel-grade ethanol and co-products

Pulps with residual lignin ranging from 6.4-27.4% (w/w) were prepared from mixed softwoods using a proprietary biorefining technology (the Lignol process) based on aqueous ethanol organosolv extraction. The pulps were evaluated for bioconversion using enzymatic hydrolysis of the cellulose fraction to glucose and subsequent fermentation to ethanol. All pulps were readily hydrolyzed without further delignification. More than 90% of the cellulose in low lignin pulps (< or =18.4% residual lignin) was hydrolyzed to glucose in 48 h using an enzyme loading of 20 filter paper units/g cellulose. Cellulose in a high lignin pulp (27.4% residual lignin) was hydrolyzed to >90% conversion within 48 h using 40 filter paper units/g. The pulps performed well in both sequential and simultaneous saccharification and fermentation trials indicating an absence of metabolic inhibitors. Chemical and physical analyses showed that lignin extracted during organosolv pulping of softwood is a suitable feedstock for production of lignin-based adhesives and other products due to its high purity, low molecular weight, and abundance of reactive groups. Additional co-products may be derived from the hemicellulose sugars and furfural recovered from the water-soluble stream.     

Covalent linkages between cellulose and lignin in cell walls of coniferous and nonconiferous woods

Covalent linkages between wall polysaccharides and lignin, especially linkage between cellulose and lignin were discussed by carboxymethylation technique of whole cell walls of coniferous and nonconiferous woods. Hydroxyl groups of plant cell walls polysaccharides were highly substituted, but not those of lignin by carboxymethyl groups under the used conditions, and separated into water-soluble and insoluble fractions by water extraction. Carboxymethylated wall polysaccharides linked covalently with lignin were distributed into the water-insoluble fractions. Composition of carboxymethylated sugar residues in the both fractions was analyzed quantitatively by 1H NMR spectroscopy after hydrolyzation with D2SO4 in D2O. More than half of cellulose linked covalently with lignin in coniferous wood, but only one-sixth of cellulose was involved in the linkage in nonconiferous wood. The major noncellulosic wall polysaccharides of coniferous wood also linked significantly with lignin. On the other hand, noncellulosic wall polysaccharides of nonconiferous wood were involved slightly in the covalent linkage with lignin. The situation of linkage between wall polysaccharides containing cellulose and lignin was visualized by scanning electron micrographs.     

Enzymatic modification of kraft lignin through oxidative coupling with water-soluble phenols

The aromatic polymer lignin can be modified through promotion of oxidative coupling between phenolic groups on lignin and various phenols. The reaction is initiated by an oxidation of both components, e.g., by using the oxidoreductases laccase or peroxidase. Coupling between phenolic monomers and lignin has previously been studied by the use of radio-labeled phenols. In this study, incorporation of water-soluble phenols into kraft lignin, using laccase as catalyst, was investigated. Several phenols with carboxylic or sulfonic acid groups were used as markers for the incorporation. The modified lignin was isolated and the amount of phenol incorporated was characterized by means of titration, quantitative 1H-NMR, and quantitative 31P-NMR after modification with 2-chloro-4,4,5,5-tetramethyl-1,2,3-dioxaphospholane. Only a few of the phenols studied were found to be incorporated into lignin. When the phenol guaiacol sulfonate was incorporated into kraft lignin, the lignin became water-soluble at pH 2.4 and a low ionic strength due to the introduction of sulfonic acid groups. The content of sulfonic acid groups in the product was 0.5-0.6 mmol/g lignin. A lower amount of 4-hydroxyphenylacetic acid was incorporated under similar conditions.     

Bioethanol production from ammonia percolated wheat straw

This study examined the effectiveness of ammonia percolation pretreatment of wheat straw for ethanol production. Ground wheat straw at a 10% (w/v) loading was pretreated with a 15% (v/v) ammonia solution. The experiments were performed at treatment temperature of 50∼170°C and residence time of 10∼150 min. The solids treated with the ammonia solution showed high lignin degradation and sugar availability. The pretreated wheat straw was hydrolyzed by a cellulase complex (NS50013) and β-glucosidase (NS50010) at 45°C. After saccharification, Saccharomyces cerevisiae was added for fermentation. The incubator was rotated at 120 rpm at 35°C. As a result of the pretreatment, the delignification efficiency was > 70% (170°C, 30 min) and temperature was found to be a significant factor in the removal of lignin than the reaction time. In addition, the saccharification results showed an enzymatic digestibility of > 90% when 40 FPU/g cellulose was used. The ethanol concentration reached 24.15 g/L in 24 h. This paper reports a total process for bioethanol production from agricultural biomass and an efficient pretreatment of lignocellulosic material.     

Biodegradation of lignin-carbohydrate complexes

Covalent lignin-carbohydrate (LC) linkages exist in lignocellulose from wood and groups herbaceous plants. In wood, they consist of ester and ether linkages through sugar hydroxyl to the -carbanol of phenylpropane subunits in lignin. In grasses, ferulic and p-coumaric acids are esterified to hemicelluloses and lignin, respectively. Hemicelluloses also contain substitutents and side groups that restrict enzymatic attack. Watersoluble lignin-carbohydrate complexes (LCCs) often precipitate during digestion with polysaccharidases, and the residual sugars are more diverse than the bulk hemicellulose. A number of microbial esterases and hemicellulose polysaccharidases including acetyl xylan esterase, ferulic acid esterase, and p-coumaric esterase attack hemicellulose side chains. Accessory hemicellulases include -l-arabinofuranosidase and -methyl-glucuranosidase. Both of these side chains are involved in LC bonds. -Glucosidase will attach sugar residues to lignin degradation products and when carbohydrate is attached to lignin, lignin peroxidase will depolymerize the lignin more readily.Abbreviations APPL acid precipitable polymeric lignin - CBQase cellobioquinone oxidoreductase - LC lignincarbohydrate - LCC(s) lignin-carbohydrate complex - DHP Dehydrogenative polymerisate - DMSO dimethylsulfoxide - DP degree of polymerisation - MWEL milled wood enzyme lignin - MWL milled wood lignin (not digested with carbohydrases)     

Characterization of degradation products from alkaline wet oxidation of wheat straw

Alkaline wet oxidation pre-treatment (water, sodium carbonate, oxygen, high temperature and pressure) of wheat straw was performed as a 2(4-1) fractional factorial design with the process parameters: temperature, reaction time, sodium carbonate and oxygen. Alkaline wet oxidation was an efficient pre-treatment of wheat straw that resulted in solid fractions with high cellulose recovery (96%) and high enzymatic convertibility to glucose (67%). Carbonate and temperature were the most important factors for fractionation of wheat straw by wet oxidation. Optimal conditions were 10 min at 195 degrees C with addition of 12 bar oxygen and 6.5 g l(-1) Na2CO3. At these conditions the hemicellulose fraction from 100 g straw consisted of soluble hemicellulose (16 g), low molecular weight carboxylic acids (11 g), monomeric phenols (0.48 g) and 2-furoic acid (0.01 g). Formic acid and acetic acid constituted the majority of degradation products (8.5 g). The main phenol monomers were 4-hydroxybenzaldehyde, vanillin, syringaldehyde. acetosyringone (4-hydroxy-3,5-dimethoxy-acetophenone), vanillic acid and syringic acid, occurring in 0.04-0.12 g per 100 g straw concentrations. High lignin removal from the solid fraction (62%) did not provide a corresponding increase in the phenol monomer content but was correlated to high carboxylic acid concentrations. The degradation products in the hemicellulose fractions co-varied with the pre-treatment conditions in the principal component analysis according to their chemical structure, e.g. diacids (oxalic and succinic acids), furan aldehydes, phenol aldehydes, phenol ketones and phenol acids. Aromatic aldehyde formation was correlated to severe conditions with high temperatures and low pH. Apart from CO2 and water, carboxylic acids were the main degradation products from hemicellulose and lignin.     

Preparation of retinamides by use of retinoyl fluoride

Retinoyl fluoride (2) prepared from retinoic acid (1) by reaction with diethylaminosulfurtrifluoride is a stable crystalline compound not easily hydrolyzed by water. By reacting retinoyl fluoride with water-soluble amines in the presence of sodium bicarbonate, retinamide (4), N-retinoyl glycine (6), N-retinoyl DL-phenylalanine (7), alpha-N-retinoyl-L-lysine (11), N-retinoyl 4-aminophenol (4-hydroxyphenylretinamide) (8), and N-retinoyl-2-amino-2-deoxy-D-glucose (2-deoxy-D-glucose-2-retinamide) (9) have been prepared in good yields and characterized by UV absorption, 1H NMR, IR spectra, mass spectrometry, and elemental analysis.