Characterization and immobilization of liposome-bound cellulase for hydrolysis of insoluble cellulose

The liposome-bound cellulase was prepared by covalently coupling cellulase with the enzyme-free liposomes bearing aldehyde groups so that cellulase was located solely on the outer membrane of liposomes. The modified cellulase possessed the higher activity efficiency and lipid-based specific activity than the cellulase-containing liposomes reported previously. The enzyme-free liposomes bearing aldehyde groups were covalently immobilized with the chitosan gel beads and the free cellulase was coupled with the treated gel beads to prepare the immobilized liposome-bound cellulase. The activity efficiency of the immobilized liposome-bound cellulase was much higher than that of the conventionally immobilized cellulase. The results on reusability of the immobilized liposome-bound cellulase in the hydrolysis of either soluble or insoluble cellulose showed that the immobilized liposome-bound cellulase had the higher remaining cellulase activity and reusability than the conventionally immobilized cellulase for the hydrolysis of either type of cellulose. The liposomal membrane was suggested to be efficient in maintaining the cellulase activity during the hydrolysis.     

固定化纤维素酶对预处理纤维素原料水解效果的影响

以壳聚糖为载体用交联法制备固定化纤维素酶,考察固定化纤维素酶对蒸爆、球磨、超声波、喷淋、高温预处理玉米秸秆纤维素原料的酶解效果.结果表明:物料经蒸爆预处理后酶水解效率最高可以达到95%,球磨预处理水解效率次之,达到60%.用电镜和FT-IR对处理前后秸秆结构进行表征分析,证明预处理对物料的物理结构及化学组成有一定的影响.蒸爆法和球磨法可以使物料致密的天然结构彻底破坏,从而增加物料的比表面积;蒸爆预处理可以使纤维素内部氢键和官能团改变,使物料更易于酶解.     

Performance of an external loop air-lift bioreactor for the production of monoclonal antibodies by immobilized hybridoma cells

Summary The performance of an external loop air-lift bioreactor was investigated by assessing the inter-relationships between various hydrodynamic properties and mass transfer. The feasibility of using this bioreactor for the production of monoclonal antibodies by mouse hybridoma cells immobilized in calcium alginate gel beads and alginate/poly-l-lysine microcapsules was also examined. When the superficial gas velocity, V _g , in the 300 ml reactor was varied from 2 to 36 cm/min, the average liquid velocity increased from 3 to 14 cm/sec, the gas hold-up rose from 0.2 to 3.0%, and the oxygen mass transfer coefficient, k _L a, increased from 2.5 to 18.1 h^-1. A minimum liquid velocity of 4 cm/s was required to maintain alginate gel beads (1000 m diameter, occupying 3% of reactor volume) in suspension. Batch culture of hybridoma cells immobilized in alginate beads followed logarithmic growth, reaching a concentration of 4×10⁷ cells/ml beads after 11 days. Significant antibody production did not occur until day 9 into the culture, reaching a value of 100 g/ml of medium at day 11. On the other hand, bioreactor studies with encapsulated hybridoma cells gave monoclonal antibody concentrations of up to 800 g/ml capsules (the antibody being retained within the semipermeable capsule) and maximum cell densities of 2×10⁸ cells/ml capsule at day 11. The volumetric productivities of the alginate gel immobilized cell system and the encapsulated cell system were 9 and 3 g antibody per ml of reactor volume per day, respectively. The main advantage of the bioreactor system is its simple design, since no mechanical input is required to vary the hydrodynamic properties.     

Optimal operating policy of the ultrafiltration membrane bioreactor for enzymatic hydrolysis of cellulose

The dilution rate of an ultrafiltration membrane bioreactor in the enzymatic hydrolysis of cellulose was optimized using the kinetic model developed by Fan and Lee.(4) The sequence of optimal dilution rates was found to generally consist of an initial period of a minimal value (batch period), a subsequent period of maximum dilution rate, a period of a second batch, and a final period of a singular dilution rate. The effects of operating conditions, such as beta-glucosidase activity, operating time, maximum dilution rate, substrate feeding rate, and enzyme-to-substrate ratio on both the conversion yield and the sequence of optimal dilution rates were investigated. To evaluate the validity of kinetic model employed in this work, enzymatic hydrolysis was carried out using alpha-cellulose as a substrate in the ultrafiltration membrane bioreactor. The experimental data were well consistent with the simulation results. (c) 1993 John Wiley & Sons, Inc.     

Development of effective modified cellulase for cellulose hydrolysis process

Cellulase was modified with amphilic copolymers made of alpha-allyl-omega-methoxy polyoxyalkylene (POA) and maleic acid anhydride (MAA) to improve the cellulose hydrolytic reactivity and cellulase separation. Amino groups of the cellulase molecule are covalently coupled with the MAA functional groups of the copolymer. At the maximum degree of modification (DM) of 55%, the modified cellulase activity retained more than 80% of the unmodified native cellulase activity. The modified cellulase shows greater stability against temperature, pH, and organic solvents, and demonstrated greater conversion of substrate than native cellulase does. Cellulase modification is also useful for controlling strong adsorption of cellulase onto substrate. Moreover, cellulase modified with the amphiphilic copolymer displays different separation characteristics which are new. One is a reactive two-phase partition and another is solubility in organic solvents. It appears that these characteristics of modified cellulase work very effectively in the hydrolysis of cellulose as a total system, which constitutes the purification of cellulase from culture broth, hydrolysis of cellulose, and recovery of cellulase from the reaction mixture. (c) 1995 John Wiley & Sons, Inc.     

Size-modulated synergy of cellulase clustering for enhanced cellulose hydrolysis

Immobilization of enzymes onto nanoparticles for enhanced biocatalytic activity via enzyme clustering is a growing field. In this paper, the effect of nanoparticle size on the hydrolytic activity of artificial cellulosomes was investigated. A simple method based on metal affinity coordination was employed to directly conjugate two enzymes, an endoglucanase CelA and an exoglucanase CelE, onto CdSe–ZnS core–shell quantum dots (QDs) without the use of any chemical modification or linker molecules such as streptavidin. Artificial cellulosomes were created by clustering the enzymes onto two different QDs (5 and 10 nm) to systematically study the influence of particle size and QD to enzyme ratio on the enhancement in cellulose hydrolysis. Our results indicate that enzyme proximity is the most important factor for activity enhancement while the influence of particle size is relatively modest. This detailed understanding will provide insights for the design of other artificial cellulosomes based on nanoclustering of multiple catalytic domains with significantly enhanced activities, and may be applicable for designing improved nanobiocatalysts for biofuel production, bioremediation, and drug design.     

Detrimental effect of cellulose oxidation on cellulose hydrolysis by cellulase

To effectively convert complex and recalcitrant biomass carbohydrates to simple platform sugars useful for fuel and chemicals production, mechanical or chemical pre-treatments are often required to make the carbohydrates more accessible for enzymatic hydrolysis. Due to their harsh conditions, some pre-treatments might negatively affect enzymatic hydrolysis because of events such as cellulose oxidation. To study how oxidative modification may impact cellulose's reactivity toward hydrolysis by cellulases, we prepared three cellulose substrates by cupric ion and hypochlorite oxidations, and subjected the derived celluloses to hydrolysis by various cellobiohydrolases from glycoside hydrolase families 6 and 7, and one cellulolytic Hypocrea jecorina extracellular enzyme mixture. We observed a profound decrease of enzymatic hydrolysis on the oxidized celluloses. The effect was attributed to the interference, from oxidized functional groups in cellulose, on its binding/activation in the active pocket/tunnel of cellobiohydrolases. Potential implication of the observed effect from cellulose oxidation on pre-treatment optimization and cellulase improvement was discussed.     

Continuous neomycin production by immobilized cells of Streptomyces marinensis NUV-5 in an airlift bioreactor

Neomycin production by free and calcium alginate immobilized cells was investigated in an airlift reactor. The average volumetric productivity with continuous fermentation (72.97 mg/l/h) was greater than with free cells (45.05 mg/l/h). The total neomycin produced with continuous fermentation was 62% greater than with that of free cells. Immobilized Streptomyces particles showed a half-life of 42 days during continuous fermentation under airlift conditions.     

Enzymatic cellulose hydrolysis in an attrition bioreactor combined with an aqueous two-phase system

Cellulose was hydrolyzed in the attrition bioreactor (ABR) with enzyme recycling by employing an aqueous two-phase system (composed of dextran and polyethylene glycol) and an ultrafiltration unit. The ABR combines wet ball milling and enzymatic hydrolysis in one process step. The cellulase enzymes were more stable in the two-phase system than in the normal buffer solution. With the initial substrate concentration (Solka Floe BW200) of 40 g/L and intermittent addition of cellulose, sugar was semicontinuously produced at dilution rates of 0.06 h(-1) and productivities of 2.1 g/L h, which is approximately a 10-fold increase of the previously reported values performed in a regular stirred reactor with an aqueous two-phase system. The conversion of the substrate was 86%.     

Importance of cellulase cocktails favoring hydrolysis of cellulose

Depolymerization of lignocellulosic biomass is catalyzed by groups of enzymes whose action is influenced by substrate features and the composition of cellulase preparation. Cellulases contain a mixture of variety of enzymes, whose proportions dictate the saccharification of biomass. In the current study, four cellulase preparation varying in their composition were used to hydrolyze two types of alkali-treated biomass (aqueous ammonia-treated rice straw and sodium hydroxide-treated rice straw) to study the effect on catalytic rate, saccharification yields, and sugar release profile. We found that substrate features affected the extent of saccharification but had minimal effect on the sugar release pattern. In addition, complete hydrolysis to glucose was observed with enzyme preparation having at least a cellobiase units (CBU)/carboxymethyl cellulose (CMC) ratio (>0.15), while a modified enzyme ratio can be used for oligosaccharide synthesis. Thus, cellulase preparation with defined ratios of the three main enzymes can improve the saccharification which is of utmost importance in defining the success of lignocellulose-based economies.     

An airlift loop reactor for the transformation of steroids by immobilized cells

Summary The flow behaviour of calcium alginate beads in an airlift reactor (ALR) with external loop was dependent on the airflow rate into and the amount of beads in the reactor. The performance of immobilizedArthrobacter simplex for the ¹-dehydrogenation of hydrocortisone in the ALR compared favourably to that in a stirred tank reactor. The physical stability of the calcium alginate beads was significantly greater in the ALR.     

Design of highly efficient cellulase mixtures for enzymatic hydrolysis of cellulose

An extremely highly active cellobiohydrolase (CBH IIb or Cel6B) was isolated from Chrysosporium lucknowense UV18-25 culture filtrate. The CBH IIb demonstrated the highest ability for a deep degradation of crystalline cellulose amongst a few cellobiohydrolases tested, including C. lucknowense CBH Ia, Ib, IIa, and Trichoderma reesei CBH I and II. Using purified C. lucknowense enzymes (CBH Ia, Ib, and IIb; endoglucanases II and V; beta-glucosidase, xylanase II), artificial multienzyme mixtures were reconstituted, displaying an extremely high performance in a conversion of different cellulosic substrates (Avicel, cotton, pretreated Douglas fir wood) to glucose. These mixtures were much or notably more effective in hydrolysis of the cellulosic substrates than the crude multienzyme C. lucknowense preparation and other crude cellulase samples produced by T. reesei and Penicillium verruculosum. Highly active cellulases are a key factor in bioconversion of plant lignocellulosic biomass to ethanol as an alternative to fossil fuels.     

Toward an aggregated understanding of enzymatic hydrolysis of cellulose: noncomplexed cellulase systems

Information pertaining to enzymatic hydrolysis of cellulose by noncomplexed cellulase enzyme systems is reviewed with a particular emphasis on development of aggregated understanding incorporating substrate features in addition to concentration and multiple cellulase components. Topics considered include properties of cellulose, adsorption, cellulose hydrolysis, and quantitative models. A classification scheme is proposed for quantitative models for enzymatic hydrolysis of cellulose based on the number of solubilizing activities and substrate state variables included. We suggest that it is timely to revisit and reinvigorate functional modeling of cellulose hydrolysis, and that this would be highly beneficial if not necessary in order to bring to bear the large volume of information available on cellulase components on the primary applications that motivate interest in the subject.     

Synergistic proteins for the enhanced enzymatic hydrolysis of cellulose by cellulase

Reducing the enzyme loadings for enzymatic saccharification of lignocellulose is required for economically feasible production of biofuels and biochemicals. One strategy is addition of small amounts of synergistic proteins to cellulase mixtures. Synergistic proteins increase the activity of cellulase without causing significant hydrolysis of cellulose. Synergistic proteins exert their activity by inducing structural modifications in cellulose. Recently, synergistic proteins from various biological sources, including bacteria, fungi, and plants, were identified based on genomic data, and their synergistic activities were investigated. Currently, an up-to-date overview of several aspects of synergistic proteins, such as their functions, action mechanisms and synergistic activity, are important for future industrial application. In this review, we summarize the current state of research on four synergistic proteins: carbohydrate-binding modules, plant expansins, expansin-like proteins, and Auxiliary Activity family 9 (formerly GH61) proteins. This review provides critical information to aid in promoting research on the development of efficient and industrially feasible synergistic proteins.     

Modeling of continuous L(+)-lactic acid production with immobilized R. oryzae in an airlift bioreactor

Continuous L(+)-lactic acid production was carried out in an airlift bioreactor with immobilized R. oryzae in polyurethane foam cubes. In a pseudo-steady state, the productivity of lactic acid increased with increasing dilution rate or feeding glucose concentration. A double-layer reaction-diffusion model for the pseudo-steady state process was developed to describe the bioreaction system. Using independently determined model parameters, the model prediction agreed well with the experimental results. Therefore, the model can be employed to understand the fermentation behavior, and for the process design and optimization.     

A functionally based model for hydrolysis of cellulose by fungal cellulase

A new functionally based kinetic model for enzymatic hydrolysis of pure cellulose by the Trichoderma cellulase system is presented. The model represents the actions of cellobiohydrolases I, cellobiohydrolase II, and endoglucanase I; and incorporates two measurable and physically interpretable substrate parameters: the degree of polymerization (DP) and the fraction of beta-glucosidic bonds accessible to cellulase, F(a) (Zhang and Lynd, 2004). Initial enzyme-limited reaction rates simulated by the model are consistent with several important behaviors reported in the literature, including the effects of substrate characteristics on exoglucanase and endoglucanase activities; the degree of endo/exoglucanase synergy; the endoglucanase partition coefficient on hydrolysis rates; and enzyme loading on relative reaction rates for different substrates. This is the first cellulase kinetic model involving a single set of kinetic parameters that is successfully applied to a variety of cellulosic substrates, and the first that describes more than one behavior associated with enzymatic hydrolysis. The model has potential utility for data accommodation and design of industrial processes, structuring, testing, and extending understanding of cellulase enzyme systems when experimental date are available, and providing guidance for functional design of cellulase systems at a molecular scale. Opportunities to further refine cellulase kinetic models are discussed, including parameters that would benefit from further study.     

Continuous enzymatic cellulose hydrolysis in a tubular membrane bioreactor

Cellulose hydrolysis by Celluclast 1.5L (Novozymes A/S, Denmark) enzyme preparation was studied in a special tubular membrane reactor, where a porous stainless steel filter was covered by a non-woven technical textile layer providing a fine, hairy surface for simultaneous adsorption of both the cellulose particles and the biocatalyst. Solka Floc BW 200 powder and Mavicell pellets were used as substrates in the process. Beyond the adsorption studies, the composite membrane was characterized, having 30 l/m² bar h hydraulic permeability and an ability to retain both cellulose and enzyme, while glucose (product) permeated easily across the membrane. Using Solka Floc substrate experiments were carried out in both the hairy tubular and a “normal” flat sheet membrane bioreactor. It was found that 10% higher average conversion was possible to achieve in the special layered tubular unit compared to the “traditional” ultrafiltration membrane reactors. Finally, milled and sieved Mavicell pellets were applied as substrates, and 70% conversion was reached with the pretreated fraction.     

Effect of air flow rate on scleroglucan synthesis by Sclerotium glucanicum in an airlift bioreactor with an internal loop

The effects of several plant cell wall polysaccharides degrading enzymes on sugar beet pulps pressing were studied. Study was carried out using three two level fractional factorial experiment designs. With only 36 experiments, the effects of the presence of pectin methylesterase, pectin lyase, polygalacturonase, cellulase, arabinase, xylanase and two rhamnogalacturonases on pressing were examined. Pectin lyase, pectin methylesterase and cellulase had a negative effect and caused the decrease of sugar beet pulp pressability. On the contrary, the presence of polygalacturonase, arabinase and xylanase increased pressing efficiency. When increasing enzymes concentrations, these effects varied and positive interactions between xylanase and polygalacturonase appeared. The presence of each of the two rhamnogalacturonases improved pressability despite their antagonistic effects. These enzymes had a complex effect and strongly interacted with polygalacturonase, arabinase and xylanase.