Chemical structure of kenaf xylan

Methylation and partial acid hydrolysis of xylans from the bast and core of kenaf (Hibiscus cannabinus) showed that the main chain of these xylans consists of (1 → 4)-linked β-d-xylopyranosyl (Xylp) residues, some of which carry a -1,2-linked 4-O-methyl-glucopyranosyluronic acid (Me-GlcAp) and glucopyranosyluronic acid (GlcAp) residues as side chains. Partial hydrolysis of kenaf xylans afforded two series of aldouronic acids from aldobio- to aldotetraouronic acids. The acids of the first series composed of 4-O-Me-d-GlcAp and d-Xylp residues: 4-O-Me-GlcA-Xyl₃, 4-O-Me-GlcA-Xyl₂ and 4-O-Me-GlcA-Xyl. The second series composed of d-GlcAp and d-Xylp: GlcA-Xyl₃, GlcA-Xyl₂ and GlcA-Xyl.

In addition to these acids, another aldobiouronic acid, 4-O-(-d-GalAp)-d-Xyl was found to be present in the partial hydrolysate.

The molar ratio of GalA, GlcA, 4-O-Me-GlcA, and Xyl residues was calculated to be 1.0:2.0:9.4:119 for the bast xylan and 1.0:1.3:7.9:99.4 for the core xylan.     

Citric acid production from cellobiose by 2-deoxyglucose-resistant mutant strains of Aspergillus niger in semi-solid culture

Citric acid production from cellobiose by Aspergillus niger was studied by a semi-solid culture method using bagasse as a carrier. From the parental strain Yang no. 2, mutant strains showing resistance to 2-deoxy-d-glucose (DG) on minimal medium containing glucose as a carbon source were induced. The representative mutant strain M155 was selected and subjected to further mutation. The new series of mutant strains showing resistance to DG on minimal medium containing cellobiose as a carbon source was induced, and among them the best mutant strain C192 showed higher citric acid productivity than Yang no. 2 in semi-solid culture when glucose was used as a carbon source. Moreover, in semi-solid culture, the strain C192 produced 49.6 g/l of citric acid, 1.6 times as much citric acid as Yang no. 2 produced, from 100 g cellobiose/l and showed enhanced -glucosidase production. In shake culture, the extracellular -glucosidase activity of C192 was higher than that of Yang no. 2 when not only cellobiose but also glucose and glycerol, catabolite repressors, were used as a carbon source. These results indicate that mutant strains such as C192 are insensitive to catabolite repression. Correspondence to: S. Usami     

Enhancement of citric acid production with ram horn hydrolysate by Aspergillus niger

The potential use of ram horn hydrolysate (RHH) as a supplement for improvement of citric acid production by Aspergillus niger NRRL 330 was studied. For this purpose, first RHH was produced. Ram horns were hydrolyzed by treating with acid (6 N-H2SO4) and the RHH was obtained. With the addition of RHH to the fermentation medium with a final concentration of 4% (optimal concentration), citric acid value reached a maximum value (94 g/l), which is 52% higher than that of the control experiment. The addition of 4% (v/v) RHH enhanced citric acid accumulation, reduced residual sugar concentration and stimulated mycelial growth. Adding 4% RHH had no adverse effects on A. niger. As a result, RHH was found to be suitable as a valuable supplement for citric acid production in the submerged fermentation.     

Amylose-like polysaccharide accumulation and hyphal cell-surface structure in relation to citric acid production by Aspergillus niger in shake culture

When 120 mg glucose/ml was used as a carbon source, in shake culture Aspergillus niger Yang no. 2 maximally produced only 15.4 mg citric acid/ml but accumulated 3.0 mg extracellular polysaccharide/ml. The polysaccharide secreted by mycelia of Yang no. 2 in shake culture was confirmed to be an amylose-like alpha-1,4-glucan by hydrolysis analysis with acid, amylase and glucoamylase. However, in static cultures, such as semisolid and surface cultures free from physical stresses caused by shaking damage, Yang no. 2 produced more citric acid but did not accumulate the polysaccharide. With cultivation time in shake culture, the amount of extracellular polysaccharide and the viscosity of the culture broth increased. The increase of shaking speed caused a remarkable increase in the accumulation of extracellular polysaccharide, e.g. 11.2 mg extracellular polysaccharide/ml was accumulated in the medium at a shaking speed of 200 rpm. The addition of 2.0 mg carboxymethylcellulose (CMC)/ml as a viscous additive to the medium reduced drastically the amount of extracellular polysaccharide accumulated to 1.5 mg/ml, but increased the citric acid produced to 52.0 mg/ml. However, intracellular polysaccharide accumulation kept up a steady rate of 0.26 microgram/mg dried mycelium through the entire period of cultivation. The addition of 3.0 mg polysaccharide/ml purified from the culture broth to the medium at the start of a culture resulted in a decrease of extracellular polysaccharide accumulation but an increase of citric acid accumulation. From electronmicroscopic observation, cell surfaces of hyphae cultivated with CMC were smooth, while hyphae cultivated without CMC had fibrous and granular polysaccharide on the cell surface. These results suggested that Yang no. 2 secreted the polysaccharide on the cell surface as a viscous substance and/or a shock absorber to protect itself from physical stresses caused by shaking damage in shake culture.     

Bioconversion of waste office paper to L(+)-lactic acid by the filamentous fungus Rhizopus oryzae

L(+)-lactic acid production was investigated using an enzymatic hydrolysate of waste office automation (OA) paper in a culture of the filamentous fungus Rhizopus oryzae. In 4 d culture, 82.8 g/l glucose, 7 g/l xylose, and 3.4 g/l cellobiose contained in the hydrolysate were consumed to produce 49.1 g/l of lactic acid. The lactic acid yield and production rate were only 0.59 g/g and 16.3 g/l/d, respectively, only 75% and 61% of the results from the glucose medium. The low production rate from waste OA hydrolysate was elucidated by trials using xylose as the sole carbon source; in those trials, the lactic acid production rate was 7.3 g/l/d, only 28% that of glucose or cellobiose. The low lactic acid yield from waste OA hydrolysate was clarified by trials using artificial hydrolysates comprised of 7:2:1 or 7:1:2 ratios of glucose:cellobiose:xylose. For both, the lactic acid production rate of 17.4 g/l/d matched that of waste OA paper, while the lactic acid yield was similar to that of the glucose medium. This indicates that the production rate may be inhibited by xylose derived from hemicellulose, and the yield may be inhibited by unknown compounds derived from paper pulp.     

Thermostable xylanolytic enzymes from Rhodothermus marinus grown on xylan

The thermophilic eubacterium Rhodothermus marinus was cultivated in a fermentor and studied with respect to activities of induced xylanolytic enzymes. Growth in the fermentor on xylan occurred with a maximum specific growth rate of 0.43 h^–1 for a batch culture. The final cell concentration was 4 g cell dry weight (CDW)/l for cells grown on xylan compared to 2 g CDW/l for cells grown without xylan in the cultivation medium. At least two xylanolytic enzymes, endo-1,4--xylanase and xylan 1,4--xylosidase, were secreted into the culture medium when cells were cultivated on xylan. Of the three cellulolytic enzymes tested for activity, -glucosidase activity was in the range of the xylanolytic enzyme activities whereas cellulose-1,4--cellobiosidase and cellulase activities were hardly detectable. The expression of endo-1,4--xylanase activities during cultivation indicates the existance of more than one xylanase in R. marinus. This is also observed in fractions from gel filtration. The xylanolytic enzymes are heat-stable. At 90°C and at pH 7.0 the half-life of the endo-1,4--xylanase was about 14 h and that of xylan 1,4--xylosidase was 45 min. Correspondence to: L. Dahlberg     

Optimization of a culture medium for xylanase production by Bacillus sp. using statistical experimental designs

The concentrations of oat spelt xylan, casein hydrolysate and NH4Cl in the culture medium for production of xylanase from Bacillus sp. I-1018 were optimized by means of response surface methods. The path of steepest ascent was used to approach the optimal region of the medium composition. The optimum composition of the nutrient medium was then easily determined by using a central composite design and was found to be 3.16g/l of xylan, 1.94g/l casein hydrolysate, 0.8g/l of NH4Cl. The xylanase production was increased by 135% when the strain was grown in the optimized medium compared to initial medium.     

Optimization of a culture medium for xylanase production by Bacillus sp. using statistical experimental designs

The concentrations of oat spelt xylan, casein hydrolysate and NH4Cl in the culture medium for production of xylanase from Bacillus sp. I-1018 were optimized by means of response surface methods. The path of steepest ascent was used to approach the optimal region of the medium composition. The optimum composition of the nutrient medium was then easily determined by using a central composite design and was found to be 3.16g/l of xylan, 1.94g/l casein hydrolysate, 0.8g/l of NH4Cl. The xylanase production was increased by 135% when the strain was grown in the optimized medium compared to initial medium.     

Citric acid production by selected mutants of Aspergillus niger from cane molasses

The present investigation deals with citric acid production by some selected mutant strains of Aspergillus niger from cane molasses in 250 ml Erlenmeyer flasks. For this purpose, a conidial suspension of A. niger GCB-75, which produced 31.1 g/l citric acid from 15% (w/v) molasses sugar, was subjected to UV-induced mutagenesis. Among the 3 variants, GCM-45 was found to be a better producer of citric acid (50.0 +/- 2a) and it was further improved by chemical mutagenesis using N-methyl, N-nitro-N-nitroso-guanidine (MNNG). Out of 3,2-deoxy-D-glucose resistant variants, GCMC-7 was selected as the best mutant, which produced 96.1 +/- 1.5 g/l citric acid 168 h after fermentation of potassium ferrocyanide and H2SO4 pre-treated blackstrap molasses in Vogel's medium. On the basis of kinetic parameters such as volumetric substrate uptake rate (Qs), and specific substrate uptake rate (qs), the volumetric productivity, theoretical yield and specific product formation rate, it was observed that the mutants were faster growing organisms and produced more citric acid. The mutant GCMC-7 has greater commercial potential than the parental strain with regard to citrate synthase activity. The addition of 2.0 x 10(-5) M MgSO4 x 5H2O into the fermentation medium reduced the Fe2+ ion concentration by counter-acting its deleterious effect on mycelial growth. The magnesium ions also induced a loose-pelleted form of growth (0.6 mm, diameter), reduced the biomass concentration (12.5 g/l) and increased the volumetric productivity of citric acid monohydrate (113.6 +/- 5 g/l).     

Acetone, butanol and ethanol production from domestic organic waste by solventogenic clostridia

Domestic organic waste (DOW) was washed and dried to 85 % dryness by VAM (The Netherlands). This material contained 25.1 g glucose, 8.4 g xylose and 5.8 g other monosaccharides/100 g dry matter. Using Mansonite steam explosion and enzymatic hydrolysis, a hydrolysate containing 15.4 g glucose, 2.2 g xylose and 0.8 g other monosaccharides per l was made. Clostridium acetobutylicum DSM 1731 produced 1.5 and C. beijerinckii B-592 0.9 g/l ABE and Clostridium LMD 84.48 1.9 g/l IBE, respectively, from this hydrolysate without further supplementation. Incubation with 2 fold concentrated hydrolysate completely impaired ABE production. After removal of unspecific inhibiting components, the yield of ABE production by Clostridium acetobutylicum DSM 1731 increased about 3 fold as compared to the nontreated hydrolysate. From 4 fold concentrated, partially purified, hydrolysate containing 34.2 g glucose/l, ABE production was 9.3 g/l after 120 h as compared to 3.2 g ABE/I from non-concentrated hydrolysate which contained 12.0 g glucose/l after elution over the same column. The concentration of butyric acid in the fermented hydrolysates was 2.2 and 0.4 g/l, respectively. This reasonably low amount of butyric acid showed that the fermentation had proceeded quite well.     

Citric Acid Production from Hydrolysate of Pretreated Straw Cellulose by Yarrowia lipolytica SWJ-1b Using Batch and Fed-Batch Cultivation

In this study, crude cellulase produced by Trichoderma reesei Rut-30 was used to hydrolyze pretreated straw. After the compositions of the hydrolysate of pretreated straw were optimized, the study showed that natural components of pretreated straw without addition of any other components such as (NH₄)₂SO₄, KH₂PO₄, or Mg²⁺ were suitable for citric acid production by Yarrowia lipolytica SWJ-1b, and the optimal ventilatory capacity was 10.0 L/min/L medium. Batch and fed-batch production of citric acid from the hydrolysate of pretreated straw by Yarrowia lipolytica SWJ-1b has been investigated. In the batch cultivation, 25.4 g/L and 26.7 g/L citric acid were yields from glucose and hydrolysate of straw cellulose, respectively, while the cultivation time was 120 hr. In the three-cycle fed-batch cultivation, citric acid (CA) production was increased to 42.4 g/L and the cultivation time was extended to 240 hr. However, iso-citric acid (ICA) yield in fed-batch cultivation (4.0 g/L) was similar to that during the batch cultivation (3.9 g/L), and only 1.6 g/L of reducing sugar was left in the medium at the end of fed-batch cultivation, suggesting that most of the added carbon was used in the cultivation.     

Optimization of cellulase-free xylanase production by a novel yeast strain

Summary A novel yeast strain, NCIM 3574, isolated from a decaying wood produced up to 570 IU ml^–1 of xylanolytic enzymes when grown on medium containing 4% xylan. The yeast strain also produced xylanase activity (40–50 IU ml^–1) in the presence of soluble carbon sources like xylose or arabinose. No xylanase activity was detected when the organism was grown on glucose. The crude xylanase preparation showed no activity towards cellulolytic substrates but low levels of -xylosidase (0.1 IU ml^–1) and -l-arabinofuranosidase (0.05 IU ml^–1) were detected. The temperature and pH optima for the crude xylanase preparation were 55°C and 4.5 respectively. The crude xylanase produced mainly xylose from xylan within 5 min. Prolonged hydrolysis of xylan produced xylobiose and arabinose, in addition to xylose, as the end products. The presence of arabinose as one of the end products in xylan hydrolysate could be due to the low levels of arabinofuranosidase enzyme present in the crude fermentation broth.     

Enzymatic synthesis of alkyl xylobioside and xyloside from xylan and alcohol

Summary Alkyl -D-xylobioside and alkyl -D-xyloside were prepared by the one-pot reaction of xylan and a fatty alcohol, such as 1-octanol, 1-decanol, 2-octanol and 2-ethylhexanol using the cell-free culture filtrate of the xylan-assimilating strain, Aureobasidium pullulans KK415. Using this strain, a novel surfactant, alkyl -D-xylobioside, was produced as the main product when the alcohol and xylan was incubated at a temperature of 65 °C and pH 4.5.     

Direct conversion of xylan to ethanol by recombinant Saccharomyces cerevisiae strains displaying an engineered minihemicellulosome

Arabinoxylan is a heteropolymeric chain of a β-1,4-linked xylose backbone substituted with arabinose residues, representing a principal component of plant cell walls. Here we developed recombinant Saccharomyces cerevisiae strains as whole-cell biocatalysts capable of combining hemicellulase production, xylan hydrolysis, and hydrolysate fermentation into a single step. These strains displayed a series of uni-, bi-, and trifunctional minihemicellulosomes that consisted of a miniscaffoldin (CipA3/CipA1) and up to three chimeric enzymes. The miniscaffoldin derived from Clostridium thermocellum contained one or three cohesin modules and was tethered to the cell surface through the S. cerevisiae a-agglutinin adhesion receptor. Up to three types of hemicellulases, an endoxylanase (XynII), an arabinofuranosidase (AbfB), and a β-xylosidase (XlnD), each bearing a C-terminal dockerin, were assembled onto the miniscaffoldin by high-affinity cohesin-dockerin interactions. Compared to uni- and bifunctional minihemicellulosomes, the resulting quaternary trifunctional complexes exhibited an enhanced rate of hydrolysis of arabinoxylan. Furthermore, with an integrated d-xylose-utilizing pathway, the recombinant yeast displaying the bifunctional minihemicellulosome CipA3-XynII-XlnD could simultaneously hydrolyze and ferment birchwood xylan to ethanol with a yield of 0.31 g per g of sugar consumed.     

Preparation and application of sulfated xylan as a flocculant for dye solution

The main purpose of this study is to explore the sulfation of xylan to produce an anionic flocculant, sulfated xylan, for removing ethyl violet dye from simulated dye solutions. In this work, xylan was sulfated with chlorosulfonic acid in N, N‐dimethylformamide solvent and the reaction conditions were optimized using a response surface methodology. It was observed that the maximum degree of substitution of 1.1 was obtained for sulfated xylan under the conditions of 3.71 chlorosulfonic acid/xylan molar ratio, 70°C and 7 h reaction time. The resulting sulfated xylan had a charge density of ?3.12 mmol/g and molecular weight (M_w) of 22,300 g/mol. Furthermore, elemental and thermogravimetric analyses, Fourier transform infrared spectroscopy and proton nuclear magnetic resonance (¹H‐NMR) confirmed the sulfation of xylan. The application of sulfated xylan as a flocculant for decolorizing the simulated ethyl violet dye wastewater was studied. The results indicated that 97% of dye was removed from 50 mg/L dye solution at the sulfated concentration of 175 mg/L and pH 9, but unmodified xylan was ineffective in flocculating and removing dye segments. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:529–536, 2018     

Potential inhibitors from wet oxidation of wheat straw and their effect on growth and ethanol production by Thermoanaerobacter mathranii

Alkaline wet oxidation (WO) (using water, 6.5 g/l sodium carbonate, and 12 bar oxygen at 195 degrees C) was used for pre-treating wheat straw (60 g/l), resulting in a hemicellulose-rich hydrolysate and a cellulose-rich solid fraction. The hydrolysate consisted of soluble hemicellulose (9 g/l), aliphatic carboxylic acids (6 g/l), phenols (0.27 g/l or 1.7 mM), and 2-furoic acid (0.007 g/l). The wet-oxidized wheat straw hydrolysate caused no inhibition of ethanol yield by the anaerobic thermophilic bacterium Thermoanaerobacter mathranii. Nine phenols and 2-furoic acid, identified to be present in the hydrolysate, were each tested in concentrations of 10-100x the concentration found in the hydrolysate for their effect on fermentation by T. mathranii. At 2 mM, these aromatic compounds were not inhibitory to growth or ethanol yield in T. mathranii. When the concentration of aromatics was increased to 10 mM, the fermentation was severely inhibited by the phenol aldehydes and to a lesser extent by the phenol ketones. By adding the same aromatic compounds to WO hydrolysate (10 mM), synergistic inhibitory effects of all tested compounds with hydrolysate components were shown. When the hydrolysate was concentrated three- and six-fold, growth and fermentation with T. mathranii were inhibited. At a six-fold hydrolysate concentration, the total concentration of phenolic monomers was 17 mM; hence aromatic monomers are an important co-factor in hydrolysate inhibition.     

Selection of mutants of Aspergillus niger showing enhanced productivity of citric acid from starch in shaking culture

Mutants with enhanced citric acid production from soluble starch were induced from Aspergillus niger WU-2223L. After UV-irradiation of a conidial suspension of strain WU-2223L, mutants were selected on modified starch-methyl red agar plates on the basis of higher amylolytic activity and acid productivity. The 8 mutants selected showed enhanced citric acid production from soluble starch in shaking culture. Among them, a representative mutant strain, 2M-43, produced 48.0gg/l of citric acid from 120 g/l of soluble starch in 9 d of cultivation in shaking culture, whereas strain WU-2223L produced 35.1 g/l. Glucoamylase activities in the culture filtrates of strains 2M-43 and WU-2223L reached maximum levels of 3.62 U/ml and 2.11 U/ml, respectively, both at 3 d of cultivation, and thereafter decreased.     

Mutation of Aspergillus niger for hyperproduction of citric acid from black strap molasses

Spore suspensions of Aspergillus niger GCB 75, which produced 31.1 g/l citric acid from 15% sugars in molasses, were subjected to u.v.-induced mutagenesis. Among three variants, GCM 45 was found to be the best citric acid producer and was further improved by chemical mutagenesis using NTG. Out of 3 deoxy-D-glucose-resistant variants, GCM 7 was selected as the best mutant which produced 86.1 ± 1.5 g/l citric acid after 168 h of fermentation of potassium ferricyanide + H₂SO₄-pretreated black strap molasses (containing 150 g sugars/l) in Vogel's medium. On the basis of comparison of kinetic parameters, namely the volumetric substrate uptake rate (Q _s), and specific substrate uptake rate (q _s), the volumetric productivity, theoretical yield and specific product formation rate, it was observed that the mutants were faster growing organisms and had the ability to overproduce citric acid.     

An Aspergillus oryzae acetyl xylan esterase: molecular cloning and characteristics of recombinant enzyme expressed in Pichia pastoris

We screened 20,000 clones of an expressed sequence tag (EST) library from Aspergillus oryzae (http://www.nrib.go.jp/ken/EST/db/index.html) and obtained one cDNA clone encoding a protein with similarity to fungal acetyl xylan esterase. We also cloned the corresponding gene, designated as Aoaxe, from the genomic DNA. The deduced amino acid sequence consisted of a putative signal peptide of 31-amino acids and a mature protein of 276-amino acids. We engineered Aoaxe for heterologous expression in P. pastoris. Recombinant AoAXE (rAoAXE) was secreted by the aid of fused alpha-factor secretion signal peptide and accumulated as an active enzyme in the culture medium to a final level of 190 mg/l after 5 days. Purified rAoAXEA before and after treatment with endoglycosidase H migrated by SDS-PAGE with a molecular mass of 31 and 30 kDa, respectively. Purified rAoAXE displayed the greatest hydrolytic activity toward alpha-naphthylacetate (C2), lower activity toward alpha-naphthylpropionate (C3) and no detectable activity toward acyl-chain substrates containing four or more carbon atoms. The recombinant enzyme catalyzed the release of acetic acid from birchwood xylan. No activity was detectable using methyl esters of ferulic, caffeic or sinapic acids. rAoAXE was thermolabile in comparison to other AXEs from Aspergillus.