Activating transhydrogenase and NAD kinase in combination for improving isobutanol production

Isobutanol is an excellent alternative biofuel. Fermentative production of isobutanol had been realized in several microorganisms by combining branched-chain amino acids synthetic pathway and Ehrlich pathway. In contrast to using plasmid overexpression and inducible promoters, genetically stable Escherichia coli strains for isobutanol production were constructed in this work by integrating essential genes into chromosome. A chromosome-based markerless gene modulation method was then developed for fine-tuning gene expression with multiple regulatory parts to improve isobutanol production. There was also a cofactor imbalance problem for anaerobic isobutanol synthesis. NADPH is the reducing equivalent required for isobutanol production, while the common reducing equivalent under anaerobic condition is NADH. Two strategies were used to modulate expression of transhydrogenase (pntAB) and NAD kinase (yfjB) genes to increase NADPH supply for improving isobutanol production. Plasmid overexpression of pntAB and yfjB genes either individually or in combination had little effect on isobutanol production. In contrast, modulating pntAB and yfjB gene expression in chromosome with multiple regulatory parts identified optimal modulators under aerobic and anaerobic conditions, respectively, and improved isobutanol production. Modulating pntAB gene alone led to 20% and 8% increase of anaerobic isobutanol titer and yield. Although modulating yfjB gene alone had nearly no effect, modulating pntAB and yfjB genes in combination led to 50% and 30% increase of isobutanol titer and yield in comparison with modulating pntAB gene alone. It was also found that increasing pntAB gene expression alone had a threshold for improving anaerobic isobutanol production, while activating NAD kinase could break through this threshold, leading to a yield of 0.92 mol/mol. Our results suggested that transhydrogenase and NAD kinase had a synergistic effect on increasing NADPH supply and improving anaerobic isobutanol production. This strategy will be useful for improving production of target compounds using NADPH as reducing equivalent within their synthetic pathways. In addition, combined activation of PntAB and YfjB led to 28% and 22% increase of aerobic isobutanol titer and yield, resulting in production of 10.8 g/L isobutanol in 24 h with a yield of 0.62 mol/mol.     

Direct ethanol production from N-acetylglucosamine and chitin substrates by Mucor species

Chitin, which is a polymer of β-(1–4) linked N-acetyl-d-glucosamine (GlcNAc) residues, is one of the most abundant renewable resources in nature, after cellulose. In this study, we found some native Mucor strains, which can use GlcNAc and chitin substrates as carbon sources for growth and ethanol production. One of these strains, M. circinelloides NBRC 6746 produced 18.6 ± 0.6 g/l of ethanol from 50 g/l of GlcNAc after 72 h and the maximum ethanol production rate was 0.75 ± 0.1 g/l/h. Furthermore, M. circinelloides NBRC 4572 produced 6.00 ± 0.22 and 0.46 ± 0.04 g/l of ethanol from 50 g/l of colloidal chitin and chitin powder after 16 and 12 days, respectively. We also found an extracellular chitinolytic enzyme producing strain M. ambiguus NBRC 8092, and successfully improved ethanol productivity of NBRC 4572 from colloidal chitin using crude chitinolytic enzyme derived from NBRC 8092. The ethanol titer reached 9.44 ± 0.10 g/l after 16 days. These results were the first bioethanol production from GlcNAc and chitin substrates by native organisms, and also suggest that these Mucor strains have great potential for the simultaneous saccharification and fermentation (SSF) of chitin biomass.     

Transformation of maltose into prebiotic isomaltooligosaccharides by a novel α-glucosidase from Xantophyllomyces dendrorhous

The transglycosylation activity of a novel α-glucosidase from the basidiomycetous yeast Xanthophyllomyces dendrorhous (formerly Phaffia rhodozyma) was studied using maltose as glucosyl donor. The enzyme synthesized oligosaccharides with α-(1 → 2), α-(1 → 4) and α-(1 → 6) bonds. Using 200 g/l maltose, the yield of oligosaccharides was 53.8 g/l, with prebiotic oligosaccharides containing at least one α-(1 → 6) linkage (panose, 6-O-α-glucosyl-maltotriose and 6-O-α-isomaltosyl-maltose) being the major products (47.1 g/l). The transglycosylatying yield was 3.6 times higher than the observed with the α-glucosidase from Saccharomyces cerevisiae (53.8 vs. 14.7 g/l). Moreover, when increasing the maltose concentration up to 525 g/l, the maximum production of tri- and tetrasaccharides reached 167.1 g/l, without altering the percentage of oligosaccharides in the mixture. Compared with other microbial α-glucosidases in which the main transglycosylation product is a disaccharide, the enzyme from X. dendrorhous yields a final product enriched in trisaccharides and tetrasaccharides.     

Milk-clotting enzymes produced by culture of Bacillus subtilis natto

Factors affecting the production of milk-clotting enzyme (MCE) by Bacillus subtilis (natto) Takahashi, a ready available commercial natto starter, were studied. Remarkable milk-clotting activity (MCA), 685.7 SU/ml or 12,000 SU/g, was obtained when the bacteria were cultivated in the medium containing sucrose (50 g/L) and basal salts at pH 6, 37 °C with shaking at 175 rpm for 1 day. The MCA and MCA/PA ratio of the crude enzyme obtained are comparable with those of Pfizer microbial rennin and Mucor rennin. The crude enzyme showed excellent pH and thermal stability; it retained 96% of MCA after incubation for 40 min at 40 °C and retained more than 80% of its activity between pH 4 and pH 7 for more than 30 min at 30 °C. The MCE of B. subtilis (natto) Takahashi has potential as calf rennet substitutes.     

High titer production of tetracenomycins by heterologous expression of the pathway in a Streptomyces cinnamonensis industrial monensin producer strain

Streptomyces cinnamonensis C730.1 and C730.7, are industrially mutagenized strains that produce moderate and high levels of the polyketide polyether antibiotic monensin A, respectively, in an oil-based fermentation medium. The possibility that these strains could be used for high titer production of a heterologous polyketide product was investigated by expression of the entire tetracenomycin (TCM) biosynthetic pathway using an integrative plasmid, pSET154. Expression in C730.1 led to stable production of ~0.44 g/l TCM C (the final biosynthetic product) and ~2.69 g/l TCM A2 (the penultimate biosynthetic product), and resulted in a 40% decrease in monensin production. Expression in the C730.7 led to higher levels of TCMs, ~0.6 g/l TCM C and ~4.35 g/l TCM A2, without any detectable decrease in the higher titer monensin production. Abrogation of monensin production in this strain through deletion of the corresponding biosynthetic genes did not lead to higher levels of TCM products. In the case of the C730.7 host, 85% of the TCM C and virtually all of the TCM A2 were intracellular, suggesting feedback inhibition leads to the accumulation of the final pathway intermediate. These observations contrast those made for the native producer Streptomyces glaucescens where the predominant product is TCM C and TCM titers are significantly lower levels (~0.3 g/l), and demonstrate the potential utility of S. cinnamonensis strains as heterologous hosts for high level expression of a variety of polyketide synthase derived products.     

Purification and characterization of cellulase from a marine Bacillus sp. H1666: A potential agent for single step saccharification of seaweed biomass

In this study, 115 marine bacterial isolates were screened for cellulase enzymatic activity and enzyme with a molecular mass of 40 kDa was purified from culture supernatant of the marine bacterium Bacillus sp. H1666 using ion exchange and size exclusion chromatography method. Growth of bacterial strain H1666 with efficient cellulase enzyme production was observed on untreated wheat straw and rice bran. The biochemical properties of the extracted cellulase were studied and enzyme was found active over a range of pH 3–9. The optimum cellulase activity was observed at pH 7 and temperature 50 °C. The enzyme was also shown to be slightly thermo-stable with 40% residual activity at 60 °C for 4 h. The potential applicability of enzyme was tested on dried green seaweed (Ulva lactuca) and 450 mg/g increase in glucose yield was obtained after saccharification. MALDI TOF–TOF analysis of cellulase peptide fingerprint showed similarity to the sequence of the glycoside hydrolase family protein.     

Microbial levan from Brachybacterium phenoliresistens: Characterization and enhancement of production

Levan producing bacteria was isolated from rhizosphere soil. The molecular identification of this isolate was conducted using 16S rRNA, which resulted in a sequenced region of 1298 base pairs. The sequence alignment in the gene bank indicated that this isolate has a high percentage of similarity (99%) to the retrieved consensus sequence of Brachybacterium phenoliresistens strain phenol-A. The produced levan was characterized using TLC, FTIR, 1H NMR and 13C NMR spectroscopy techniques. The effects of nutritional and physical factors on this isolate’s levan production were investigated. The results demonstrated that the optimal sources for carbon and casein during levan production were sucrose and casein, yielding 7.88 g/land 8.12 g/l of levan, respectively. The highest levan yield (7.97 g/l) was obtained at a sucrose concentration of 300 g/l. At an initial pH of 7.8, this bacterium yielded their highest levan production of 7.88 g/l. The optimal incubation period was 72 h with a yield of 8.58 g/l, the optimal temperature was 30 °C and resulted in 7.87 g/l, and the highest levan production yield was obtained at 150 rpm and yielded 8.12 g/l.     

Comparative biochemical characterization of soluble and chitosan immobilized β-galactosidase from Kluyveromyces lactis NRRL Y1564

An investigation was conducted on the production of β-galactosidase (β-gal) by different strains of Kluyveromyces, using lactose as a carbon source. The maximum enzymatic activity of 3.8 ± 0.2 U/mL was achieved by using Kluyveromyces lactis strain NRRL Y1564 after 28 h of fermentation at 180 rpm and 30 °C. β-gal was then immobilized onto chitosan and characterized based on its optimal operation pH and temperature, its thermal stability and its kinetic parameters (K_m and V_max) using o-nitrophenyl β-d-galactopyranoside as substrate. The optimal pH for soluble β-gal activity was found to be 6.5 while the optimal pH for immobilized β-gal activity was found to be 7.0, while the optimal operating temperatures were 50 °C and 37 °C, respectively. At 50 °C, the immobilized enzyme showed an increased thermal stability, being 8 times more stable than the soluble enzyme. The immobilized enzyme was reused for 10 cycles, showing stability since it retained more than 70% of its initial activity. The immobilized enzyme retained 100% of its initial activity when it was stored at 4 °C and pH 7.0 for 93 days. The soluble β-gal lost 9.4% of its initial activity when it was stored at the same conditions.     

A novel low-temperature-active exo-inulinase identified based on Molecular-Activity strategy from Sphingobacterium sp. GN25 isolated from feces of Grus nigricollis

A novel glycosyl hydrolase family 32 exo-inulinase (InuAGN25) gene was cloned from Sphingobacterium sp. GN25 isolated from feces of Grus nigricollis. InuAGN25 showed the highest identity of 54.3% with a putative levanase recorded in GenBank. Molecular-Activity strategy was proposed to predict InuAGN25 to be a low-temperature-active exo-inulinase before experiments performance. Molecular analyses included progressive sequential, phylogenetic and structural analyses. InuAGN25 was effectively expressed in Escherichia coli. The purified recombinant InuAGN25 showed characteristics of low-temperature-active enzymes: (1) the enzyme retained 55.8% of the maximum activity at 20 °C, 35.8% at 10 °C, and even 8.2% at 0 °C; (2) the enzyme exhibited 75.8, 30.5 and 10.8% of the initial activity after preincubation for 60 min at 45, 50 and 55 °C, respectively; (3) K_m values of the enzyme toward inulin were 2.8, 3.0, 3.2 and 5.8 mg ml⁻¹ at 0, 10, 20 and 40 °C, respectively. Fructose was the main product of inulin and Jerusalem artichoke tubers hydrolyzed by the purified recombinant InuAGN25 at room temperature, 10 °C and 0 °C. These results suggested the Molecular-Activity strategy worked efficiently and made InuAGN25 promising for the production of fructose at low temperatures.     

Cell-associated acid β-xylosidase production by Penicillium sclerotiorum

In recent decades, β-xylosidases have been used in many processing industries. In this work, the study of xylosidase production by Penicillium sclerotiorum and its characterization are reported. Optimal production was obtained in medium supplemented with oat spelts xylan, pH 5.0, at 30 °C, under stationary condition for six days. The optimum activity temperature was 60 °C and unusual optimum pH 2.5. The enzyme was stable at 50 and 55 °C, with half-life of 240 and 232 min, respectively. High pH stability was verified from pH 2.0 to 4.0 and 7.5. The β-xylosidase was strongly inhibited by divalent cations, sensitive to denaturing agents SDS, EDTA and activated by thiol-containing reducing agents. The apparent V_max and K_m values was 0.48 μmol PNXP min^?1 mg^?1 protein and 0.75 mM, respectively. The enzyme was xylose tolerant with a K_i of 28.7. This enzyme presented interesting characteristics for biotechnological process such as animal feed, juice and wine industries.     

Inulinase biosynthesis using immobilized mycelium of Aspergillus niger

Conidia of Aspergillus niger 20 Osm producing extracellular inulinase were immobilized on pumice stones or polyurethane sponge and used in repeated-batch processes. Some factors affecting inulinase biosynthesis by the mycelium A. niger immobilized on pumice stones were investigated. Maximal inulinase production occurred in 50 ml of medium containing 0.5 g of carrier at 30 °C, pH 6.0 and at an agitation speed of 200 rpm. This procedure enabled repeated-batch enzyme production and as many as six subsequent 24 h batches could be fermented by using the same carrier. This is the first report on inulinase biosynthesis by mycelium of A. niger immobilized on polyurethane sponge using unconventional oxygenation of culture which ensures that the dissolved oxygen concentration remains constant.     

Cellulose ethanol production from waste newsprint by simultaneous saccharification and fermentation using Saccharomyces cerevisiae KNU5377

A thermotolerant ethanol-fermenting yeast, Saccharomyces cerevisiae KNU5377, isolated from a sludge of a local industrial complex stream in Korea, was evaluated for its capability for lignocellulosic ethanol production from waste newsprint in high temperature. In this fermentation, most of dry-defibrated waste newspaper was first saccharified at 50 °C for 108 h using a commercial cellulase and, then with the last addition of dry-defibrated newsprints to the pre-saccharified broth, simultaneous saccharification and fermentation (SSF) of 1.0 L of reaction mixture was carried out at 40 °C, slowly being dropped from 50 °C, for further 72 h in a 5 L fermentor by inoculating the overnight culture of KNU5377. The maximum production of 8.4% (v/v) ethanol was obtained when 250 g (w/v)/L of dry-defibrated waste newspaper was used for ethanol production by SSF. These results suggest that S. cerevisiae KNU5377 is very useful for cellulose ethanol production by the SSF system.     

Optimization of fermentation conditions for the production of ethanol from sago starch by co-immobilized amyloglucosidase and cells of Zymomonas mobilis using response surface methodology

Statistical experimental design was used to optimize the conditions of simultaneous saccharification and fermentation (SSF), viz. temperature, pH and time of fermentation of ethanol from sago starch with co-immobilized amyloglucosidase (AMG) and Zymomonas mobilis MTCC 92 by submerged fermentation. Maximum ethanol concentration of 55.3 g/l was obtained using a starch concentration of 150 g/l. The optimum conditions were found to be a temperature of 32.4 °C, pH of 4.93 and time of fermentation of 17.24 h. Thus, by using SSF process with co-immobilized AMG and Z. mobilis cells MTCC 92, the central composite design (CCD) was found to be the most favourable strategy investigated with respect to ethanol production and enzyme recovery.     

Lipolytic enzyme production by Thermus thermophilus HB27 in a stirred tank bioreactor

In this study, lipolytic enzyme production by Thermus thermophilus HB27 at bioreactor scale has been investigated. Cultivation was performed in a 5-L stirred tank bioreactor in discontinuous mode, at an agitation speed of 200 rpm. Different variables affecting intra- and extra-cellular lipolytic enzyme production such as culture temperature and aeration rate have been analysed. The bacterium was able to grow within the temperature range tested (from 60 to 70 °C) with an optimum value of 70 °C for intra- and extra-cellular lipolytic enzyme production.On the other hand, various aeration levels (from 0 to 2.5 L/min) were employed. A continuous supply of air was necessary, but no significant improvement in biomass or enzyme production was detected when air flow rates were increased above 1 L/min. Total lipolytic enzyme production reached a maximum of 167 U/L after 3 days, and a relatively high concentration of extra-cellular activity was detected (40% of the total amount). Enzyme yield was around 158 U/g cells. Moreover, it is noteworthy that the lipolytic activity obtained operating at optimal conditions (70 °C and air flow of 1 L/min) was about five-fold higher than that attained in shake flask cultures     

Use of different carbon sources in cultivation of recombinant Pichia pastoris for angiostatin production

To improve the growth of recombinant Pichia pastoris with a phenotype of Mut^S and expression of angiostatin, the effects of glycerol, sorbitol, acetate and lactic acid which were, respectively, added together with methanol in the expression phase, were studied in a 5-l fermentor. Methanol concentration was automatically controlled at 5 g/l by a methanol monitor and control system, while the feeding of the other carbon source was manually adjusted. The angiostatin production level was 108 mg/l when glycerol was added at an initial rate of 2.3 g/h and gradually increased to 9.9 g/h within an induction period of 96 h. The angiostatin concentration was 141 mg/l as sorbitol was used, while only 52 mg/l were obtained on acetate. The highest angiostatin production of 191 mg/l was achieved as lactic acid was used; whose feeding rate was gradually increased from 2.6 to 11.3 g/h. Lactic acid accumulated during the induction phase and reached 6.3 g/l at the end of fermentation. However, the accumulation of lactic acid did not interfere with angiostatin production, indicating that lactic acid to be a non-repressive carbon source. The average productivity and specific productivity of angiostatin obtained on lactic acid and methanol were, respectively, 2.96 and 0.044 mg/(g h), 1.7- and 2.5-fold of those obtained in the fermentation fed with glycerol and methanol.     

Continuous degradation of maltose by enzyme entrapment technology using calcium alginate beads as a matrix

Maltase from Bacillus licheniformis KIBGE-IB4 was immobilized within calcium alginate beads using entrapment technique. Immobilized maltase showed maximum immobilization yield with 4% sodium alginate and 0.2 M calcium chloride within 90.0 min of curing time. Entrapment increases the enzyme–substrate reaction time and temperature from 5.0 to 10.0 min and 45 °C to 50 °C, respectively as compared to its free counterpart. However, pH optima remained same for maltose hydrolysis. Diffusional limitation of substrate (maltose) caused a declined in V_max of immobilized enzyme from 8411.0 to 4919.0 U ml^?1 min^?1 whereas, K_m apparently increased from 1.71 to 3.17 mM ml^?1. Immobilization also increased the stability of free maltase against a broad temperature range and enzyme retained 45% and 32% activity at 55 °C and 60 °C, respectively after 90.0 min. Immobilized enzyme also exhibited recycling efficiency more than six cycles and retained 17% of its initial activity even after 6th cycles. Immobilized enzyme showed relatively better storage stability at 4 °C and 30 °C after 60.0 days as compared to free enzyme.     

Cloning,expression and characterization of highly thermo- and pH-stable maltogenic amylase from a thermophilic bacterium Geobacillus caldoxylosilyticus TK4

Maltogenic amylases (MAases), a subclass of cyclodextrin (CD)-hydrolyzing enzymes, belong to glycoside hydrolase family 13. A gene corresponding to MA in Geobacillus caldoxylosilyticus TK4 (GcaTK4MA) was cloned into pET28a(+) vector and expressed in Escherichia coli with 6xHis-tag at the N-terminus. Herein, we report on the biochemical properties of a new thermo- and pH-stable MA. GcaTK4MA has similar properties those of other MAases in terms of the primary structure, preference for CD over starch and having an extra domain at its N- and C-terminals. The recombinant protein was purified efficiently by using one-step nickel affinity chromatography. The purified enzyme exhibited optimal activity for β-CD hydrolysis at 50 °C and pH 7.0. When the enzyme was separately incubated at 4 °C and 50 °C in the buffer solutions (pH 3.0–9.0) up to 7 days, it was seen that the enzyme had the higher stability at 50 °C than 4 °C. The enzyme retained about 80% of its original activity when it was incubated at 50 °C for 7 days. The enzyme activity was significantly inhibited by SDS and EDTA at the final concentration of 1%. These results suggest that this is the first reported MA having an extremely pH- and thermal stabilities.     

Yeast cell-free enzyme system for bio-ethanol production at elevated temperatures

A yeast cell-free enzyme system containing an intact fermentation assembly and that is capable of bio-ethanol production at elevated temperatures in the absence of living cells was developed to address the limitations associated with conventional fermentation processes. The presence of both yeast glycolytic and fermentation enzymes in the system was verified by SDS-PAGE and LC–MS/MS Q-TOF analyses. Quantitative measurements verified sufficient quantities of the co-factors ATP (1.8 mM) and NAD⁺ (0.11 mM) to initiate the fermentation process. Bio-ethanol was produced at a broad temperature range of 30–60 °C but was highly specific to a pH range of 6.0–7.0. The final bio-ethanol production at 30, 40, 50, and 60 °C was 3.37, 3.83, 1.94, and 1.60 g/L, respectively, when a 1% glucose solution was used, and the yield increased significantly with increasing cell-free enzyme concentrations. A comparative study revealed better results for the conventional fermentation system (4.46 g/L) at 30 °C than the cell-free system (3.37 g/L); however, the efficacy of the cell-free system increased with temperature, reaching a maximum (3.83 g/L) at 40 °C, at which the conventional system could only produce 0.48 g/L bio-ethanol. Successful bio-ethanol production using a single yeast cell-based enzyme system at higher temperatures will lead to the development of novel strategies for efficient bio-ethanol production through SSF.     

A new strategy for strain improvement of Aurantiochytrium sp. based on heavy-ions mutagenesis and synergistic effects of cold stress and inhibitors of enoyl-ACP reductase

Developing a strain with high docosahexaenoic acid (DHA) yield and stable fermenting-performance is an imperative way to improve DHA production using Aurantiochytrium sp., a microorganism with two fatty acid synthesis pathways: polyketide synthase (PKS) pathway and Type I fatty acid synthase (FAS) pathway. This study investigated the growth and metabolism response of Aurantiochytrium sp. CGMCC 6208 to two inhibitors of enoyl-ACP reductase of Type II FAS pathway (isoniazid and triclosan), and proposed a method of screening high DHA yield Aurantiochytrium sp. strains with heavy ion mutagenesis and pre-selection by synergistic usage of cold stress (4 °C) and FAS inhibitors (triclosan and isoniazid). Results showed that (1) isoniazid and triclosan have positive effects on improving DHA level of cells; (2) mutants from irradiation dosage of 120 Gy yielded more DHA compared with cells from 40 Gy, 80 Gy treatment and wild type; (3) DHA contents of mutants pre-selected by inhibitors of enoyl-ACP reductase of Type II FAS pathway (isoniazid and triclosan)at 4 °C, were significantly higher than that of wild type; (4) compared to the wild type, the DHA productivity and yield of a mutant (T-99) obtained from Aurantiochytrium sp. CGMCC 6208 by the proposed method increased by 50% from 0.18 to 0.27 g/Lh and 30% from 21 to 27 g/L, respectively. In conclusion, this study developed a feasible method to screen Aurantiochytrium sp. with high DHA yield by a combination of heavy-ion mutagenesis and mutant-preselection by FAS inhibitors and cold stress.     

Efficiencies of designed enzyme combinations in releasing arabinose and xylose from wheat arabinoxylan in an industrial ethanol fermentation residue

The generation of a fermentable hydrolysate from arabinoxylan is an important prerequisite for utilization of wheat hemicellulose in production of ethanol or other value added products. This study examined the individual and combined efficiencies of four selected, commercial, multicomponent enzyme preparations Celluclast 1.5 L (from Trichoderma reesei), Finizym (from Aspergillus niger), Ultraflo L (from Humicola insolens), and Viscozyme L (from Aspergillus aculeatus) in catalyzing arabinose and xylose release from water-soluble wheat arabinoxylan in an industrial fermentation residue (still bottoms) in lab scale experiments. Different reaction conditions, i.e. enzyme dosage, reaction time, pH, and temperature, were evaluated in response surface and ternary mixture designs. Ultraflo L treatment gave optimal arabinose release: treatment (6 h, 60 °C, pH 6) with this enzyme preparation liberated up to 46% by weight (wt.%) of the theoretically maximal arabinose yield from the substrate. Celluclast 1.5 L was superior to the other enzyme preparations in releasing xylose and catalyzed release of up to 25 wt.% of the theoretical maximum xylose yield (6 h, 60 °C, pH 4). Prolonged treatment for 24 h with a 50:50 mixture of Celluclast 1.5 L and Ultraflo L at 50 °C, pH 5 exhibited a synergistic effect in xylose release and 62 wt.% of the theoretically maximal xylose yield was achieved. Addition of pure β-xylosidase from T. reesei to the Ultraflo L preparation released the same amounts of xylose from the substrate as the 50:50 mixture of Celluclast 1.5 L and Ultraflo L. The data thus signified that the synergistic effect in xylose release between Celluclast 1.5 L and Ultraflo L is the result of a three-step interaction mechanism involving α-l-arabinofuranosidase and different xylan degrading enzyme activities in the two enzyme preparations.