Applicability of an empirical rate expression to enzymatic hydrolysis of cellulosic materials

Summary The empirical rate expression previously proposed for the hydrolysis of avicel and tissue paper by Meicelase from Trichoderma viride also held for the hydrolysis of dewaxing cotton, Whatmann CF-11, Solka Floc SW-40, tissue paper and 1% NaOH-pretreated sawdust by Meicelase, Trichoderma reesei QM9414 or Cellulosin from Aspergillus nigar.     

Biological pretreatment of rice straw with Streptomyces griseorubens JSD-1 and its optimized production of cellulase and xylanase for improved enzymatic saccharification efficiency

Biological pretreatment of rice straw and production of reducing sugars by hydrolysis of bio-pretreated material with Streptomyces griseorubens JSD-1 was investigated. After 10 days of incubation, various chemical compositions of inoculated rice straw were degraded and used for further enzymatic hydrolysis studies. The production of cellulolytic enzyme by S. griseorubens JSD-1 favored the conversion of cellulose to reducing sugars. The culture medium for cellulolytic enzyme production by using agro-industrial wastes was optimized through response surface methodology. According to the response surface analysis, the concentrations of 11.13, 20.34, 4.61, and 2.85 g L^?1 for rice straw, wheat bran, peptone, and CaCO₃, respectively, were found to be optimum for cellulase and xylanase production. Then the hydrolyzed spent Streptomyces cells were used as a nitrogen source and the maximum filter paper cellulase, carboxymethylcellulase, and xylanase activities of 25.79, 78.91, and 269.53 U mL^?1 were achieved. The crude cellulase produced by S. griseorubens JSD-1 was subsequently used for the hydrolysis of bio-pretreated rice straw, and the optimum saccharification efficiency of 88.13% was obtained, indicating that the crude enzyme might be used instead of commercial cellulase during a saccharification process. These results give a basis for further study of bioethanol production from agricultural cellulosic waste.     

Enzyme recovery in high-solids enzymatic hydrolysis of steam-pretreated willow: Requirements for the enzyme composition

In order to reduce the total enzyme consumption in high-solids static hydrolysis of nonwashed steam-exploded willowSalix caprea by mixed cellulase ofTrichoderma reesei + Aspergillus foetidus, two different approaches were proposed. In the first case, the enzyme activity adsorbed on residual solids after extended hydrolysis was used for hydrolysis of the newly added substrate. The initial mixing of fresh and hydrolyzed substrates was sufficient for the adsorbed enzyme redistribution and conversion of the new substrate portion, and constant mechanical stirring was not required. Feeding of two additional portions of the exploded hardwood adjusted to pH 4 with dry caustic into the reactor with simultaneous replacement of accumulated sugars with fresh buffer (pH 4.5) resulted, on average, in a 90% conversion of cellulose at the final enzyme loading of 8 IFPU per g ODM substrate, an average sugar concentration of 12%, and a glucose/xylose ratio of 5 : 1. In the second approach, weakly adsorbed cellulase fractions were used for static high-solids hydrolysis followed by their ultrafiltration recovery from the resultant sugar syrup. In contrast to the initial cellulase mixture whose residual activity in a syrup did not exceed 5–10% at the end of hydrolysis (48 h), up to 60% of weakly adsorbed enzyme fraction could be separated from sugar syrups by ultrafiltration and then reused. Weakly adsorbed enzymes displayed a hydrolysis efficiency of not less than 80% per IFPU enzyme consumed in extended hydrolysis of pretreated willow as compared to the original enzyme mixture. An electrophoretic study of the weakly adsorbed enzyme fraction identifiedT. reesei cellobiohydrolase II as the predominant component, whereas clear domination ofT. reesei cellobiohydrolase I was found by electrophoresis of proteins tightly bound to residual hydrolysis solids. Deceased     

Enzymatic production of N-acetyl- -glucosamine from chitin. Degradation study of N-acetylchitooligosaccharide and the effect of mixing of crude enzymes

N-Acetyl- -glucosamine (GlcNAc) was produced from chitin by use of crude enzyme preparations. The efficient production of GlcNAc by cellulases derived from Trichoderma viride (T) and Acremonium cellulolyticus (A) was observed by HPLC analysis compared to lipase, hemicellulase, and pectinase. β-Chitin showed higher degradability than α-chitin when using cellulase T. The optimum pH of cellulase T was 4.0 on the hydrolysis of β-chitin. The yield of GlcNAc was enhanced by mixing of cellulase T and A.     

Bioethanol Production from Horticultural Waste Using Crude Fungal Enzyme Mixtures Produced by Solid State Fermentation

It was desired to study efficient and simplified methods to convert organosolv-pretreated horticultural waste (HW) to ethanol fuel using cellulase produced under solid-state fermentation (SSF). The unprocessed cellulase crude (72.2 %) showed better reducing sugar yield using filter paper than the commercial enzyme blend (68.7 %). Enzymatic hydrolysis of organosolv-pretreated HW using the crude cellulase with 20 % solid content, enzyme loading of 15 FPU/g HW at 50 °C, and pH 5.5 resulted in a HW hydrolysate containing 25.06 g/L glucose after 72 h. Fermentation of the hydrolysate medium produced 12.39 g/L ethanol with 0.49 g/g yield from glucose and 0.062 g/g yield from HW at 8 h using Saccharomyces cerevisiae. This study proved that crude cellulase complex produced under SSF and organosolv pretreatment can efficiently convert woody biomass to ethanol without any commercial cellulase usage.     

Efficient cellulase production by the filamentous fungus Acremonium cellulolyticus

Cellulase production was investigated in a culture of a strain of Acremonium cellulolyticus. The medium components were optimized for the improvement of cellulase production. The maximum production of cellulolytic enzymes was obtained in a medium containing (grams per liter) 50 Solka Floc, 5 (NH4)2SO4, 24 KH2PO4, 4.7 potassium tartrate hemihydrate, 1.2 MgSO4.7H2O, 1 Tween 80, 4 urea, 0.01 ZnSO4.7H2O, 0.01 MnSO4.6H2O, and 0.01 CuSO4.7H2O, with a pH of 4.0. In the flask culture, 15.5 filter paper units (FPU)/mL of maximum cellulase activity was obtained, 17.42 FPU/mL in a 7-L bioreactor, and 13.08 FPU/mL in a 50-L scale bioreactor for 4-8 d at 30 degrees C. Average production rates were 1.94 FPU/mL.d in flasks, 2.86 FPU/mL.d in the 7-L bioreactor, and 2.56 FPU/mL.d in the 50-L bioreactor. Cellulase production on a small scale was successfully reproduced in the 50-L pilot scale bioreactor. Saccharification activity from A. cellulolyticus was compared with cellulolytic enzymes produced by other strains. The A. cellulolyticus culture broth had a comparable saccharification yield in comparison with those of other Trichoderma enzymes (GC220 or Cellulosin T2) under the same total cellulase activity. Its saccharification yield (percent of released reducing sugar to used dried substrate) was 60%, and its glucose content was 83%.     

Conversion of paper sludge to ethanol. I: Impact of feeding frequency and mixing energy characterization

In this paper, conversion of paper sludge to ethanol was investigated with the objective of optimization of the overall operation costs. Experimental work was undertaken to optimize cellulase loading, and to determine mixing energy requirements. It was found that decreasing feeding frequency (feed additions per residence time) allows the cellulase loading to be decreased at least two fold with no decrease in cellulose conversion but also entails mixing a slurry of higher solids content and lower conversion at the beginning of the operating cycle. The viscosity of paper sludge slurries was found to increase exponentially with decreasing conversion and increasing solid content. In particular, the viscosity (V) was described well by equation V = e^(kX−X ₀^)(S−S ₀^)+C (V viscosity (cp), X conversion, S solid content (g/L), k, X ₀, S ₀, C are empirical parameters). Added costs associated with operating at low feeding frequencies (including higher mixing energy and higher capital costs for the motor and for sludge hold tasks) were found to be small compared to the economic benefits resulting from reduced cellulase loading.     

Paddy straw as substrate for ethanol production

Pretreatment of paddy straw with 2% sodium hydroxide at 15 psi for 1 h resulted in 83% delignification. The hydrolysis of alkali treated paddy straw with a commercial preparation of cellulase for 2 h at 50°C resulted in release of 65% total reducing sugars. Maximum sugars were released at enzyme loading of 1.5% (v/v). The fermentation of hydrolysate supplemented with nutrients by S. cerevisiae resulted in the production of 20–30 g L⁻¹ ethanol after 48 h incubation which was further improved with addition of yeast nitrogen base and inoculated with 1% (w/v) yeast cells.     

The enzymatic hydrolysis and fermentation of pretreated wheat straw to ethanol

Autohydrolysis and ethanol-alkali pulping were used as pretreatment methods of wheat straw for its subsequent saccharification by Trichoderma reesei cellulase. The basic hydrolysis parameters, i.e., reaction time, pH, temperature, and enzyme and substrate concentration, were optimized to maximize sugar yields from ethanol-alkali modified straw. Thus, a 93% conversion of 2.5% straw material to sugar syrup containing 73% glucose was reached in 48 h using 40 filter paper units/g hydrolyzed substrate. The pretreated wheat straw was then fermented to ethanol at 43 degrees C in the simultaneous saccharification and fermentation (SSF) process using T. reesei cellulase and Kluyveromyces fragilis cells. From 10% (w/v) of chemically treated straw (dry matter), 2.4% (w/v) ethanol was obtained after 48 h. When the T. reesei cellulase system was supplemented with beta-glucosidase from Aspergillus niger, the ethanol yield in the SSF process increased to 3% (w/v) and the reaction time was shortened to 24 h.     

Differential responses of wood-rot fungi cellulases towards polyclonal antibodies against Trichoderma viride cellobiohydrolase I

Cellobiohydrolase (CBH) I, a main component of Trichoderma extracellular protein, was purified to an electrophoretically homogeneous state from a commercial cellulase preparation (Meicelase from T. viride) by column chromatography on anion and cation exchangers. The difference in the cross-reactivity of cellulolytic enzyme systems of brown-rot and white-rot fungi with the polyclonal antibodies to the CBH I was studied by enzyme-linked immunosorbent assay (ELISA). The antibodies were observed to react quantitatively and with great sensitivity with the antigen (CBH I), and at the same time to cross-react to some extent with T. viride cellulase components other than the CBH I. Nevertheless, the intensity of cross-reactivity of wood-rot fungi cellulases with the antibodies was parallel to the activity of exo-1,4-ß-glucanase. The cellulase system from brown-rot fungi, believed to lack exo-1,4-ß-glucanases, gave a negative response towards the antibodies. These results suggested the presence of some homologous sequences and structures with the T. viride CBH I in the enzymes of white-rot fungi and their absence in those of brown-rot fungi. Correspondence to: M. Ishihara     

Mechanisms of the inhibition of enzymatic hydrolysis of waste pulp fibers by calcium carbonate and the influence of nonionic surfactant for mitigation

Recycled paper mills produce large quantities of fibrous rejects and fines which are usually sent to landfills as solid waste. These cellulosic materials can be enzymatically hydrolyzed into sugars for the production of biofuels and biomaterials. Paper mill wastes also contain large amounts of calcium carbonate which inhibits cellulase activity. The calcium carbonate (30%, w/w) decreased 40–60% of sugar yield of unbleached softwood kraft pulp. The prime mechanisms for this are by pH variation, competitive and non-productive binding, and aggregation effect. Addition of acetic acid (pH adjustment) increased the sugar production from 19 to 22 g/L of paper mill waste fibers. Strong affinity of enzyme—calcium carbonate decreased free enzyme in solution and hindered sugar production. Electrostatic and hydrogen bond interactions are mainly possible mechanism of enzyme—calcium carbonate adsorption. The application of the nonionic surfactant Tween 80 alleviated the non-productive binding of enzyme with the higher affinity on calcium carbonate. Dissociated calcium ion also inhibited the hydrolysis by aggregation of enzyme.

     

Biodegradation of microcrystalline cellulose in pH–pH recyclable aqueous two-phase systems with water-soluble immobilized cellulase

Product inhibition is a barrier for enzymatic conversion of cellulose into reducing sugar in single aqueous phase. In addition, the difficulty in the recovery of cellulase also leads to high cost for the enzymatic hydrolysis of cellulose. In this study, enzymatic degradation of cellulose was carried out in pH–pH recyclable aqueous two-phase systems (ATPS) composed by copolymers poly (AA-co-DMAEMA-co-BMA) (abbreviated P_ADB3.8) and poly (MAA-co-DMAEMA-co-BMA) (abbreviated P_MDB). In the systems, cellulase was immobilized on pH-response copolymer P_MDB by using 1-Ethyl-3-(3-dimethyllaminopropyl)-carbodiimide hydrochloride (EDC) as cross-linker. Optimized partition coefficient of product in the systems was 2.45, in the presence of 40 mM (NH₄)₂SO₄. Insoluble substrate and immobilized enzyme were biased to bottom phase, while the product was partitioned to top phase. Microcrystalline cellulose was hydrolyzed into reducing sugar, and the product entered into top phase. The yield of saccharification in ATPS could reach 70.57% at the initial substrate concentration of 0.5% (w/v), and the value was 9.3% higher than that in the single aqueous phase. Saccharification yield could reach 66.15% after immobilized cellulase was recycled five times in ATPS.     

Use of a combined Cellulomonas and Trichoderma cellulase preparation for cellulose saccharification

Summary An enzyme preparation from a mutant strain of Cellulomonas CS1-17 acts synergistically with low levels of Trichoderma reesei cellulase in saccharification of alkali-pretreated sugar cane bagasse and in assays of Filter Paper activity. Supplementation of the Cellulomonas preparation with 0.1 or 0.25 FPU.ml^- of T. reesei cellulase provides a preparation approximately equivalent to one using T. reesei alone at 1 FPU.ml^-1.     

The Use of Cellulase in Inhibiting Biofilm Formation from Organisms Commonly Found on Medical Implants

A study was made of the use of cellulase to inhibit biofilm formation by a pathogenic bacterium commonly found in medical implants. A Pseudomonas aeruginosa biofilm was grown on glass slides in a parallel flow chamber for 4 d with glucose as the nutrient source. Biofilm development was assessed by measuring the colony forming units (CFU) and biomass areal density. Biofilm was grown at pH 5 and 7 in the presence of three different cellulase concentrations, 9.4, 37.6 and 75.2 units ml^{m 1}. In addition, a control study using deactivated cellulase was performed. The results show that cellulase is effective in partially inhibiting biomass and CFU formation by P. aeruginosa on glass surfaces. The effect of cellulase depended on concentration and was more effective at pH 5 than pH 7. The experiment was further extended by investigating the effect of cellulase on the apparent molecular weight of purified P. aeruginosa exopolysaccharides (EPS). The observation of EPS using size exclusion chromatography showed a decrease in apparent molecular weight when incubated with enzyme. An increase in the amount of reducing sugar with time when the purified EPS were incubated with enzyme also supports the hypothesis that cellulase degrades the EPS of P. aeruginosa. While cellulase does not provide total inhibition of biofilm formation, it is possible that the enzyme could be used in combination with other treatments or in combinations with other enzymes to increase effectiveness.     

Recycle of cellulases and the use of lignocellulosic residue for enzyme production after hydrolysis of steam-pretreated aspenwood

Summary Various modes of substrate and enzyme addition were used to hydrolyze a 10% concentration (w/v) of steam-exploded, water-and-alkali extracted aspenwood withTrichoderma harzianum E58 cellulases. Although cellulose conversion was high (94–100%), enzyme recovery was low in all cases. Low enzyme recovery was due to a combination of thermal inactivation and adsorption of the cellulases onto the lignocellulosic residue. Enzyme recycle was not feasible as the activity of the recovered cellulases towards crystalline cellulose was low. However, the residual material from enzyme hydrolysis was a suitable carbon source for cellulase enzyme production byT. harzianum based on enzyme yield and hydrolytic potential. These residues could only be used up to a 1% substrate concentration, since at higher substrate loadings cellulase production was reduced, likely because of lignin inhibitors.     

Pretreatment Of Hardwood (Eucalyptus Regnans) Sawdust By Autohydrolysis Explosion And Its Saccharification By Trichodermal Cellulases

Autohydrolysis explosion pretreatment of hardwood (Eucalyptus regnans) sawdust at 200°C and 6.9 MPa gas pressure (steam + nitrogen) for 5 min solubilized 85% of the total hemicellulose components and produced a pulp that was highly accessible to attack by cellulases from Trichoderma reesei C-30 and by a commercial preparation, Meicelase. The autohydrolysis liquor, representing 15% of the original weight of the sawdust on a solids basis, consisted mainly of xylose, xylose oligomers and minor amounts of galactose, mannose, arabinose, glucose and uronic acids. Enzymic hydrolysis of pretreated E. regnans pulps using Trichodermal cellulases resulted in saccharification yields of <50% within 24 h from 10% (w/v) substrate slurries and 20 cellulase (FPU) units per g of pretreated pulp. The cellulose-to-glucose conversions were lower and this was attributable to the production of a compound(s) during enzymic hydrolysis that was inhibitory to the β-glucosidase component, but not the cellulases, in the Trichodermal cellulase preparations. Enzymic digests supplemented with Novozym 188 β-glucosidase showed >70% cellulose-to-glucose conversion within 24 h under similar conditions of hydrolysis. The inhibitor compound was not inhibitory to the Novozym 188 β-glucosidases. Alkali-extracted autohydrolysis-exploded pulps were less susceptible to hydrolysis than unextracted pulps. Factors that influenced the extent of cellulose conversion into glucose such as enzyme-substrate and cellulase-to-β-glucosidase ratios are also discussed.     

Saccharification of used paper with different cellulases

Various used paper materials have been exposed to the action of cellulases from Penicillium funiculosum, Trichoderma reesei, Trichoderma viride and Aspergillus niger. A 2 h incubation period showed cellulase from T. viride the most active except for office paper that was maximally degraded by A. niger cellulase. Cellulase mixtures increased saccharification while sequential treatment with cellulases from T. reesei and P. funiculosum increased biodegradation at values between 15% and 190%. The maximum increase of saccharification (190%) was obtained when T. reesei cellulase initiated the sequential treatment of newspaper relative to the sole action of P. funiculosum cellulase on this non-pretreated and pretreated material.     

A statistical approach for optimization of R-phycoerythrin extraction from the red algae Gracilaria verrucosa by enzymatic hydrolysis using central composite design and desirability function

The aim of this research is to statistically optimize enzymatic hydrolysis parameters for the production of R-phycoerythrin (RPE) from red algae Gracilaria verrucosa. Six independent variables, incubation temperature, incubation time, ratio of buffer to raw material, cellulase loading, xylanase loading, and pH, were selected for response surface methodology studies. A central composite design was employed to maximize RPE production. A mathematical model with high determination coefficient (R ²?=?0.86) was developed and could be employed to optimize RPE extraction. The optimal extraction conditions of RPE were determined as follows: incubation temperature (48°C), incubation time (6?h), ratio of buffer to raw material (20 w/v), cellulase loading (15%), xylanase loading (5%), and pH (6.5). Under this optimal condition, the experimental yield of RPE was 6.25?mg?g^?1. Based on the result of response surface methodology and desirability function approach study, total sugar, the main by-product in RPE extraction was considered as another response. A new optimal condition was predicted as follows: incubation temperature (30°C), incubation time (12?h), ratio of buffer to raw material (20, w/v), cellulase loading (15%), xylanase loading (5%), and pH (6). Under this condition, similar RPE levels were obtained while the concentration of total sugar decreased by 40%.     

Biodegradation of lignocellulosic waste by Aspergillus terreus

Biodegradation of lignocellulosic waste by Aspergillus terreus is reported for the first time. This isolate produced 250 CMCase (carboxymethyl cellulase or endoglucanase) U.ml^-1 and biodegraded hay and straw during 3 days and the biomass production on straw was 5g.L^-1dry weight from 0.25 cm² inoculated mycellium. This strain secreted endocellulases and exocellulases in the culture medium, but some of the enzymes produced, remained cell membrane bound. Cell bound enzymes were released by various treatments. The highest amount of endoglucanase and exoglucanase was released when the cells were treated with sonication. Aspergillus terreus was added to two tanks containing sugar wastewater and pulp manufacturing waste, as a seed for COD removal. This fungus reduced the COD by 40–80 percent, also, ammonia was reduced from 14.5 mM to 5.6 mM in sugar beet wastewater. The effects of crude enzyme of this fungus for COD removal was studied.     

Preparation and properties of an immobilized cellulase on the reversibly soluble matrix Eudragit L-100

Abstract

To prepare a smart biocatalyst, cellulase was immobilized on the reversibly soluble matrix Eudragit L-100 by non-covalent and covalent methods. Covalent immobilization using carbodiimide coupling exhibited superior enzyme loading and reusability compared with non-covalent immobilization, and the covalent loading was increased by almost 20% through the addition of N-hydroxysuccinimide. The temperature optimum of the cellulase was not improved apparently by immobilization but the pH optimum increased from 4.75 to 5.25. Immobilized cellulase was more active than free cellulase above pH 5.0. Immobilized cellulase was more stable than free cellulase during storage at 4°C, room temperature and 50°C. K_m values of immobilized and free cellulase were 85.55 and 73.84 g L^?1, respectively. About 50% productivity was retained after five cycles for hydrolysis of steam-exploded straw.