Recycling cellulases during the hydrolysis of steam exploded and ethanol pretreated Lodgepole pine

Recycling of cellulases is one way of reducing the high cost of enzymes during the bioconversion process. The effects of surfactant addition on enzymatic hydrolysis and the potential recycling of cellulases were studied during the hydrolysis of steam exploded Lodgepole pine (SELP) and ethanol pretreated Lodgepole pine (EPLP). Three cellulase preparations (Celluclast, Spezyme CP, and MSUBC) were evaluated to determine their hydrolysis efficiencies over multiple rounds of recycling. The surfactant, Tween 80, significantly increased the yield from 63% to 86% during the hydrolysis of the SELP substrate. The addition of surfactant to the hydrolysis of the EPLP substrate increased the free enzymes in the supernatant from 71% of the initial protein to 96%. Based on the Langmuir adsorption constants, cellulases (Celluclast and Spezyme CP) from Trichoderma reesei showed a higher affinity (3.48 mL/mg and 3.17 mL/mg) for the EPLP substrate than did the Penicillium enzyme (0.62 mg/mg). The Trichoderma reesei enzyme was used in four successive rounds of enzyme recycling using surfactant addition and readsorption onto fresh substrates during the hydrolysis of EPLP. In contrast, the Penicillium-derived enzyme preparation (MSUBC) could only be recycled once. When the same recycling strategy was carried out using the SELP substrate, the hydrolysis yield declined during each enzyme recycling round. These results suggested that the higher lignin content of the SELP substrate, and the low affinity of cellulases for the SELP substrate limited enzyme recycling by readsorption onto fresh substrates.     

An approach to cellulase recovery from enzymatic hydrolysis of pretreated sugarcane bagasse with high lignin content

The possibility of recovering the cellulases used for enzymatic hydrolysis of sugarcane bagasse was evaluated. A strategy was adopted to maximize the enzyme recovery: desorption of the enzymes adsorbed in the solid residue after hydrolysis, and re-adsorption of the enzymes from the liquid medium onto a fresh substrate. The use of surfactant during the enzymatic hydrolysis was important to improve the glucose release from the material structure and also to facilitate the enzyme desorption from the solid residue after hydrolysis. The temperature and pH used during desorption influenced the enzymes recovery, with the best results (90% adsorbed cellulase) being achieved at 45?°C and pH 5.5. The enzymes present in the liquid medium after enzymatic hydrolysis were partially recovered (77%) by adsorption onto the fresh substrate and used in new enzymatic hydrolysis batches. It was concluded that it is possible to recycle cellulases from an enzymatic medium for use in subsequent hydrolysis processes.     

Benefits from tween during enzymic hydrolysis of corn stover

Corn stover is a potential substrate for fermentation processes. Previous work with corn stover demonstrated that lime pretreatment rendered it digestible by cellulase; however, high sugar yields required very high enzyme loadings. Because cellulase is a significant cost in biomass conversion processes, the present study focused on improving the enzyme efficiency using Tween 20 and Tween 80; Tween 20 is slightly more effective than Tween 80. The recommended pretreatment conditions for the biomass remained unchanged regardless of whether Tween was added during the hydrolysis. The recommended Tween loading was 0.15 g Tween/g dry biomass. (The critical relationship was the Tween loading on the biomass, not the Tween concentration in solution.) The 72-h enzymic conversion of pretreated corn stover using 5 FPU cellulase/g dry biomass at 50 degrees C with Tween 20 as part of the medium was 0.85 g/g for cellulose, 0.66 g/g for xylan, and 0.75 for total polysaccharide; addition of Tween improved the cellulose, xylan, and total polysaccharide conversions by 42, 40, and 42%, respectively. Kinetic analyses showed that Tween improved the enzymic absorption constants, which increased the effective hydrolysis rate compared to hydrolysis without Tween. Furthermore, Tween prevented thermal deactivation of the enzymes, which allows for the kinetic advantage of higher temperature hydrolysis. Ultimate digestion studies showed higher conversions for samples containing Tween, indicating a substrate effect. It appears that Tween improves corn stover hydrolysis through three effects: enzyme stabilizer, lignocellulose disrupter, and enzyme effector. Copyright 1998 John Wiley & Sons, Inc.     

Evaluating the distribution of cellulases and the recycling of free cellulases during the hydrolysis of lignocellulosic substrates

The recycling of cellulase enzymes is one potential strategy for reducing the cost of the enzymatic hydrolysis step during the bioconversion of lignocellulosics to ethanol. To determine the influence of lignin on the post-hydrolysis distribution of cellulase enzymes between the liquid and solid phases, the hydrolysis of Avicel was compared to an organosolv-pretreated Douglas fir substrate with a lignin content of 3.0%. After a 12 h hydrolysis reaction on Avicel, 90% of the added cellulases (including beta-glucosidases) remained "free" in the liquid phase compared to only 65% in the case of the hydrolysis of the organosolv-pretreated Douglas fir substrate. The readsorption of free cellulases by supplementing the hydrolysis reaction with fresh substrate was explored as a potential means of recovering the free cellulases that remain in the liquid phase after hydrolysis. The Langmuir adsorption isotherm was used to develop a model predicting that 82% of the free cellulases could be recovered via readsorption onto fresh substrates during the hydrolysis of an ethanol-pretreated mixed softwood substrate with a lignin content of 6%. Recoverable free cellulase values of 85% and 88% based on cellulase activity and protein content, respectively, were obtained after experimental verification of the model. The readsorption of free cellulases onto fresh lignocellulosic substrates was shown to be an effective method for free enzyme recovery.     

The cellulase complex of Neurospora crassa: activity, stability and release

The temperature and pH optima, and the temperature and pH stability, of crude and purified enzymes of the cellulase complex of the cellulolytic ascomycete fungus Neurospora crassa were investigated. The effects of some non-ionic surfactants and fatty acids on the production/release of enzymes of cellulase complex were also examined. For the different enzymes of the complex, activity maxima occurred between pH 4.0 and 7.0, with pH 5.0 being close to optimal for stability of all. Temperature optima for activity ranged between 45 and 65 degrees C, with the stability optimum between 45 and 50 degrees C. The presence of C18 fatty acids and surfactants resulted in increased production of both endoglucanase and exoglucanase in the medium. Oleic acid was the most effective fatty acid tested, and Tween 80 the most effective surfactant. Oleic acid had no detectable effect on production of beta-glucosidase, and Tween 80 actually reduced its production.     

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     

Enzyme regeneration during hydrolysis of steam-pretreated willow and requirement for cellulase complex composition

In order to reduce the total enzyme consumption in high-solids static hydrolysis of nonwashed steam-exploded willow Salix caprea by mixed cellulase of Trichoderma 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 permanent 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 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 identified T. reesei cellobiohydrolase II as the predominant component, whereas clear domination of T. reesei cellobiohydrolase I was found by electrophoresis of proteins tightly bound to hydrolysis residual solids.     

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.

     

Characterization of the interaction between surfactants and enzymes by fluorescence probe

In order to investigate the mechanism of the different stimulatory effects of the biosurfactant rhamnolipid and the chemical surfactant Tween 80 on enzymatic hydrolysis of lignocellulose, the interaction between surfactants and enzymes was analyzed by the fluorescence probe method using pyrene as probe. Based on the evolution law of pyrene fluorescence spectroscopy in the “surfactants-enzymes” systems, the interaction relationship between surfactants and enzymes was analyzed and discussed in this paper. The results show that enzyme molecules bind with rhamnolipid molecules, participate in the formation of rhamnolipid micelles, and increase the inner hydrophobic polarity of micelles, but do not change the properties of rhamnolipid micelles above the CMC (Critical Micelle Concentration). Nevertheless, for Tween 80, enzyme molecules also participate in the forming of micelles, however, they exhibit a stronger interaction with enzymes above the CMC. Both rhamnolipid and Tween 80 bind more strongly with xylanase than cellulase. Considering also previous experimental results, it can be concluded that the interaction between surfactants and enzymes improve enzyme stability and activity, and, therefore, the efficiency of enzymatic hydrolysis of lignocellulose is enhanced. The findings further provide theoretical knowledge about the mechanism of the stimulative effects of surfactants on enzymatic hydrolysis of lignocellulose.     

Effect of surfactants on separate hydrolysis fermentation and simultaneous saccharification fermentation of pretreated lodgepole pine

The effects of surfactants addition on enzymatic hydrolysis and subsequent fermentation of steam exploded lodgepole pine (SELP) and ethanol pretreated lodgepole pine (EPLP) were investigated in this study. Supplementing Tween 80 during cellulase hydrolysis of SELP resulted in a 32% increase in the cellulose‐to‐glucose yield. However, little improvement was obtained from hydrolyzing EPLP in the presence of the same amount of surfactant. The positive effect of surfactants on SELP hydrolysis led to an increase in final ethanol yield after the fermentation. It was found that the addition of surfactant led to a substantial increase in the amount of free enzymes in the 48 h hydrolysates derived from both substrates. The effect of surfactant addition on final ethanol yield of simultaneous saccharification and fermentation (SSF) was also investigated by using SELP in the presence of additional furfural and hydroxymethylfurfural (HMF). The results showed that the surfactants slightly increased the conversion rates of furfural and HMF during SSF process by Saccharomyces cerevisiae. The presence of furfural and HMF at the experimental concentrations did not affect the final ethanol concentration either. The strategy of applying surfactants in cellulase recycling to reduce enzyme cost is presented. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Factors affecting cellulose hydrolysis and the potential of enzyme recycle to enhance the efficiency of an integrated wood to ethanol process

Past technoeconomic modeling work has identified the relatively large contribution that enzymatic hydrolysis adds to the total cost of producing ethanol from lignocellulosic substrates. This cost was primarily due to the high concentration of enzyme and long incubation time that was required to obtain complete hydrolysis. Although enzyme and substrate concentration and end-product inhibition influenced the rate of hydrolysis, the effect was less pronounced during the initial stages of hydrolysis. During this time most of the cellulases were adsorbed onto the unhydrolyzed residue. By recycling the cellulases adsorbed to the residual substrate remaining after an initial 24 h, a high rate of hydrolysis, with low overall residence time and minimal cellulase input, could be achieved for several rounds of enzyme recycle. A comparison of the front end (pretreatment, fractionation, and hydrolysis) of a softwood/hardwood to ethanol process indicated that the lignin associated with the softwood-derived cellulose stream limited the number of times the cellulose containing residue could be recycled. (c) 1996 John Wiley & Sons, Inc.     

Effects of the surfactant tween 80 on enzymatic hydrolysis of newspaper

The effects of Tween 80 on the enzymatic hydrolysis of newspaper were tested. By monitoring sugar production it was found that the surfactant (0.1%) increased the rate and extent of cellulose saccharification. Consequently, the rate of enzyme usage in the hydrolysis reactor was improved by 33%. In addition, in the presence of surfactant the recovery of enzymes was higher. Analysis of the enzyme solution showed that with Tween 80 present larger fractions of enzyme remained in solution throughout hydrolysis. Thus, it appears that the surfactant hindered the immobilization of the enzymes on the substrates by reducing the strength of adsorption.     

Utility of enzymes from <Emphasis Type="Italic">Fibrobacter succinogenes</Emphasis> and <Emphasis Type="Italic">Prevotella ruminicola</Emphasis> as detergent additives

In this study, we investigated the application of cellulase and protease purified from rumen bacteria as detergent additives. Cellulase and protease were purified from the rumen cellulytic bacteria Fibrobacter succinogenes S85, and Prevotella ruminicola 23, respectively. An inhibitor test indicated that the purified protease belongs to the category of serine proteases and metalloproteases. Both the enzymes were effective at a high temperature (50 degrees C) and neutral pH (pH 7-8), but the protease activity increased with the increase in temperature and pH. The purified protease was treated with ten types of surfactants/detergents; it was found to retain over 60% of its activity in the presence of anionic and nonionic detergents. The cellulose plus protease combination was still effective after treatment with Triton X-100 and Tween 80, but the residual activity was low after treatment with Tween 20 than that after treatment with other nonionic detergents. Washing tests indicated that enzyme addition produced no significant improvement in the removal of grass stains, but individual enzyme addition in surfactants/detergents, especially in nonionic detergents, could improve the washing performance of the detergents by improving its ability to remove blood stains. This suggested that the surfactant/detergent class, enzyme properties, and the mixing ratio of ingredients should be considered simultaneously to enhance the washing performance.     

Characterization of direct cellulase immobilization with superparamagnetic nanoparticles

Abstract

Methods of cellulase immobilization on magnetic particles via glutaraldehyde binding were studied. The binding was confirmed by transmission electronic microscopy (TEM), X-ray diffraction (XRD), Fourier-transform infrared spectroscopy (FTIR) and vibrating sample magnetometry (VSM). Samples analyzed by TEM and XRD showed that the magnetic particles with or without bound cellulase were all nanosized particles with a mean diameter of 11.5 nm, and the binding process did not cause significant changes in particle size and structure. Analysis by FTIR showed that the binding of cellulase to the magnetic nanoparticles might be via covalent bonding between residual amine groups on Fe₃O₄ nanoparticles and amine groups of the cellulase. The VSM analysis showed that magnetic nanoparticles with or without bound cellulase were all superparamagnetic. The immobilized cellulase had a wider pH and temperature range and improved storage stability compared with the free enzyme. Determination of the Michaelis constants revealed that the immobilized cellulase had a greater affinity for the cellulosic substrate than the free enzyme. The immobilized cellulase showed better performance on hydrolysis of steam-exploded corn stalks than of bleached sulfite bagasse pulp.     

Erucic acid production using porcine pancreas lipase: Enhancement by mixed surfactants

Application of mixed surfactants coupled with statistical optimization in lipase catalyzed oil hydrolysis is presented for the first time in this study. Selective hydrolysis of brown mustard oil to erucic acid by porcine pancreas lipase was enhanced by mixed surfactants comprising of an oil-soluble nonionic surfactant (Span 80) and a watersoluble nonionic surfactant (Tween 80). The production of erucic acid was maximized using statistically designed experiments and subsequent analysis of their result by response surface methodology. The most significant variables were enzyme concentration and concentration of Tween 80. Small changes in pH and concentration of Span 80 also produced a significant change in the production of erucic acid. Temperature and speed of agitation were insignificant variables and were fixed at 35oC and 900 rpm, respectively. Under these conditions, the optimal combination of other variables were pH 9.65, 2.13 mg/g enzyme in oil, 9.8 × 10⁻³ M Span 80 (in oil), and 4 × 10⁻³ M Tween 80 (in buffer). These conditions led to formation of 99.69% of the total erucic acid in 1.25 h. Interaction of enzyme concentration with pH significantly affected erucic acid production.     

Inhibition of enzymatic hydrolysis by residual lignins from softwood--study of enzyme binding and inactivation on lignin-rich surface

Lignin-derived inhibition is a major obstacle restricting the enzymatic hydrolysis of cell wall polysaccharides especially with softwood lignocellulosics. Enzyme adsorption on lignin is suggested to contribute to the inhibitory effect of lignin. The interaction of cellulases with softwood lignin was studied in the present work with commercial Trichoderma reesei cellulases (Celluclast) and lignin-rich residues isolated from steam pretreated softwood (SPS) by enzymatic and acid hydrolysis. Both lignin preparations inhibited the hydrolysis of microcrystalline cellulose (Avicel) and adsorbed the major cellulases present in the commercial cellulase mixture. The adsorption phenomenon was studied at low temperature (4°C) and at the typical hydrolysis temperature (45°C) by following activities of free and lignin-bound enzymes. Severe inactivation of the lignin-bound enzymes was observed at 45°C, however at 4°C the enzymes retained well their activity. Furthermore, SDS-PAGE analysis of the lignin-bound enzymes indicated that very strong interactions form between the residue and the enzymes at 45°C, because the enzymes were not released from the residue in the electrophoresis. These results suggest that heat-induced denaturation may take place on the surface of softwood lignin at the hydrolysis temperature.     

The stimulatory effects of surfactants on composting of waste rich in cellulose

The chemical surfactant Tween 80 and biosurfactant rhamnolipid were respectively added to the composting substrate, a mixture of rice straw and bran, and their effects on the composting process were investigated. Samples were analysed for microbial communities of bacteria, actinomycetes and fungi, carboxymethylcellulose hydrolysis (CMCase) and xylanase activities, cellulose and hemicellulose fractions, water-soluble carbon (WSC) contents in the substrates, organic matter contents and pH values during the composting process. The results showed that both Tween 80 and rhamnolipid had slight stimulatory effects on the microbial populations of bacteria, actinomycetes and fungi. In addition, rhamnolipid increased the peak xylanase activity 15% higher than that of the control, while Tween 80 increased the maximum CMCase activity 35% higher than that of the control. As a result of the increased enzyme activities, treatments with Tween 80 and rhamnolipid were of higher WSC contents than the control during the whole composting process. Accordingly, the composting process was accelerated by the surfactants, since the organic matter was decomposed more quickly and the breakdown of cellulose and hemicellulose was better in the treatments with Tween 80 and rhamnolipid.     

Fermentation of cassava peels for the production of cellulolytic enzymes

Cassava peels were used as a substrate for the production of cellulolytic enzymes. Under solid substrate fermentation conditions and a Rhizopus sp., thermostable cellulolytic enzymes were produced. Optimal production temperature and pH were 45°C and 5.6 respectively. Kinetic studies of the enzymes showed that the cellulase C₁ activity was optimal at pH 5.0 and 50°C, whereas that of cellulase C_x was optimal at pH 7.0 and 60°C. The enzymes degraded ca 44% of sorghum grains in 6 h, thus suggesting a possible use in saccharification processes. The results also showed the possibility of re-cycling cassava peels as a cheap substrate for the enzyme industry. and accepted 6 June 1989     

纤维素降解菌L-06的筛选、鉴定及其产酶条件的分析

从用于堆肥的水稻秸秆中初筛出一株高效纤维素降解菌L-06, 根据18S rRNA基因序列和菌株形态分析, 初步鉴定该菌为斜卧青霉(Penicillium decumbens)。研究了液体发酵培养基中氮源、碳源、表面活性剂、培养温度、起始pH以及接种量对该菌株各纤维素酶活力的影响。在最适条件下, 该菌的b-葡萄糖苷酶(BGL)、外切纤维素酶(CBH)于培养第3天酶活力分别达到1662 u/mL和2770 u/mL; 内切纤维素酶(EG)、滤纸糖化力(FPase)于培养第4天酶活力分别达到18064 u/mL和4035 u/mL。在产酶优化实验中, 该菌的EG和CBH在pH10的培养条件下分别保持了70%和43%的酶活性; 在50oC培养条件下EG和CBH分别保持了68%和59%的酶活性。表现出了耐热, 耐碱的特性。     

纤维素降解菌L-06的筛选、鉴定及其产酶条件的分析

从用于堆肥的水稻秸秆中初筛出一株高效纤维素降解菌L-06, 根据18S rRNA基因序列和菌株形态分析, 初步鉴定该菌为斜卧青霉(Penicillium decumbens)。研究了液体发酵培养基中氮源、碳源、表面活性剂、培养温度、起始pH以及接种量对该菌株各纤维素酶活力的影响。在最适条件下, 该菌的b-葡萄糖苷酶(BGL)、外切纤维素酶(CBH)于培养第3天酶活力分别达到1662 u/mL和2770 u/mL; 内切纤维素酶(EG)、滤纸糖化力(FPase)于培养第4天酶活力分别达到18064 u/mL和4035 u/mL。在产酶优化实验中, 该菌的EG和CBH在pH10的培养条件下分别保持了70%和43%的酶活性; 在50oC培养条件下EG和CBH分别保持了68%和59%的酶活性。表现出了耐热, 耐碱的特性。