Enhanced cellulase production through random mutagenesis of Talaromyces pinophilus OPC4-1 and fermentation optimization

Reducing cellulase cost remains a major challenge for lignocellulose to fuel and chemical industries. In this study, mutants of a novel wild-type cellulolytic fungal strain Talaromyces pinophilus OPC4-1 were developed by consecutive UV irradiation, N-methyl-N`-nitro-N-nitrosoguanidine (NTG) and ethylmethane sulfonate (EMS) treatment. A potential mutant EMM was obtained and displayed enhanced cellulase production. Using Solka Floc cellulose as the substrate, through fed-batch fermentation, mutant strain T. pinophilus EMM generated crude enzymes with an FPase activity of 27.0 IU/mL and yield of 900 IU/g substrate. When corncob powder was used, strain EMM produced crude enzymes with an FPase activity of 7.3 IU/mL and yield of 243.3 IU/g substrate. In addition, EMM crude enzymes contained 29.2 and 16.3 IU/mL β-glucosidase on Solka Floc cellulose and corncob power, respectively. The crude enzymes consequently displayed strong biomass hydrolysis performance. For corncob hydrolysis, without supplement of any commercial enzymes, glucose yields of 591.7 and 548.6 mg/g biomass were obtained using enzymes produced from Solka Floc cellulose and corncob powder, respectively. It was 553.9 mg/g biomass using the commercial enzyme mixture of Celluclast 1.5 L and Novozyme 188. Strain T. pinophilus EMM was therefore a potential fungus for on-site enzyme production in biorefinery processes.     

Effect of xylanase supplementation of cellulase on digestion of corn stover solids prepared by leading pretreatment technologies

Solids resulting from pretreatment of corn stover by ammonia fiber expansion (AFEX), ammonia recycled percolation (ARP), controlled pH, dilute acid, lime, and sulfur dioxide (SO₂) technologies were hydrolyzed by enzyme cocktails based on cellulase supplemented with β-glucosidase at an activity ratio of 1:2, respectively, and augmented with up to 11.0 g xylanase protein/g cellulase protein for combined cellulase and β-glucosidase mass loadings of 14.5 and 29.0 mg protein (about 7.5 and 15 FPU, respectively)/g of original potential glucose. It was found that glucose release increased nearly linearly with residual xylose removal by enzymes for all pretreatments despite substantial differences in their relative yields. The ratio of the fraction of glucan removed by enzymes to that for xylose was defined as leverage and correlated statistically at two combined cellulase and β-glucosidase mass loadings with pretreatment type. However, no direct relationship was found between leverage and solid features following different pretreatments such as residual xylan or acetyl content. However, acetyl content not only affected how xylanase impacted cellulase action but also enhanced accessibility of cellulose and/or cellulase effectiveness, as determined by hydrolysis with purified CBHI (Cel7A). Statistical modeling showed that cellulose crystallinity, among the main substrate features, played a vital role in cellulase–xylanase interactions, and a mechanism is suggested to explain the incremental increase in glucose release with xylanase supplementation.     

Expression and characterization of Pichia etchellsii β-glucosidase in Escherichia coli

The β-glucosidase enzyme is important as the terminal enzyme involved in hydrolysis of cellobiose and short-chain cellodextrins generated during enzymatic cellulose degradation. Under controlled reaction conditions the enzyme also displays cello-oligosaccharide synthesizing ability (based on either the thermodynamic or kinetic approach). We present here the purification of the enzyme β-glucosidase (BGL) of Pichia etchellsii from recombinant pBG55 Escherichia coli clone. The kinetic parameters, substrate specificity and oligosaccharide synthesizing ability of the purified enzyme are also reported. The purified 200-kDa protein (tetramer of 50 kDa) was identified as a broad-substrate-specificity enzyme exhibiting increased temperature and glucose tolerance compared to the native yeast enzyme. Temperature directed substrate specificity for aryl β,1–4 linkage, and β(1–2), β(1–4), β(1–6) and β(2-1) linkages in various natural disaccharides was observed. Glycosylation of the enzyme was found to be unimportant for enzyme activity. With both cellobiose and glucose, oligosaccharide synthesis was detected. The implications of this information with regard to cellulose hydrolysis and oligosaccharide synthesis are discussed.     

Enzymatic hydrolysis of cellulose to glucose lung immobilized β-glucosidase

The production of sugars by enzymatic hydrolysis of cellulose is a multistep process which includes conversion of the intermediate cellobiose to glucose by β-glucosidase. Aside from its role as an intermediate, cellobiose inhibits the endoglucanase components of typical cellulase enzyme systems. Because these enzyme systems often contain insufficient concentrations of β-glucosidase to prevent accumulation of inhibitory cellobiose, this research investigated the use of supplemental immobilized β-glucosidase to increase yield of glucose. Immobilized β-glucosidase from Aspergillus phoenicis was produced by sorption at controlled-pore alumina with about 90% activity retention. The product lost only about 10% of the original activity during an on-stream reaction period of 500 hr with cellobiose as substrate; maximum activity occurred near pH 3.5 and the apparent activation energy was about 11 kcal/mol. The immobilized β-glucosidase was used together with Trichoderma reesei cellulase to hydrolyze cellulosic materials, such as Solka Floc, corn stove and exploded wood. Increased yields of glucose and greater conversions of cellobiose of glucose were observed when the reaction systems contained supplemental immobilized β-glucosidase.     

Biodegradation of cellulose by β-glucosidase and cellulase immobilized on a pH-responsive copolymer

Biodegradation of cellulose involves synergistic action of the endoglucanases, exoglucanases and β-glucosidases in cellulase. However, the yield of glucose is limited by the lack of β-glucosidase to hydrolyze cellobiose into glucose. In this study, β-glucosidase as a supplemental enzyme along with cellulase are co-immobilized on a pHresponsive copolymer, poly (MAA-co-DMAEMA-co-BMA) (abbreviated P_MDB, where MAA is α-methacrylic acid, DMAEMA is 2-dimethylaminoethyl methacrylate and BMA is butyl methacrylate). The thermal and storage stabilities of PMDB with immobilized enzymes are improved greatly, compared with those of free cellulase. Biodegradation of cellulose is carried out in a pH-responsive recyclable aqueous two-phase system composed of poly (AA-co- DMAEMA-co-BMA) (abbreviated P_{ADB 3.8}, where AA is acrylic acid) and P_MDB. Insoluble substrate and P_MDB with immobilized cellulase and β-glucosidase (Celluclast 1.5L FG and Novozyme 188, respectively) were biased to the bottom phase, while the product was partitioned to the top phase in the presence of 40 mM (NH₄)₂SO₄. When the degradation reaction of cellulose is carried out with PMDB containing immobilized cellulase and β-glucosidase, the concentration of glucose reaches 4.331 mg/mL after 108 h. The yield of glucose is 50.25% after P_MDB containing the immobilized enzymes is recycled five times.     

Conversion of cellobiose to glucose using immobilized β-glucosidase reactors

Cellobiose is an intermediate in the enzymatic hydrolysis of cellulose to glucose and acts as an inhibitor for the cellulase enzymes. The conversion of cellobiose to glucose was studied with β-glucosidase adsorbed on Amberlite DP-1, a cation-exchange resin. The best overall pH for adsorption and reactor operation was near 5.0. The K_m values increased with increasing enzyme loading due to competitive inhibition. The maximum practical enzyme loading was about 28 units/g resin. The immobilized enzyme was operated continously in both packed bed and fluidized bed reactors, giving half-lives between 200 and 375 h.     

Cellobiose metabolism and cellobiohydrolase I biosynthesis by Trichoderma reesei

The relationship between β-linked disaccharide (cellobiose, sophorose) utilization and cellulase, particularly cellobiohydrolase I (CBH I) synthesis by Trichoderma reesei, was investigated. During growth on cellobiose and sophorose as carbon sources in batch as well as resting-cell culture, only sophorose induced cellulase formation. In the latter experiments, sophorose was utilized at a much lower rate than cellobiose, and the more cellulase produced, the lower its rate of utilization. Cellobiose and sophorose were utilized by the fungus mainly via hydrolysis by the cell wall- and cell membrane-bound β-glucosidase. Addition of sophorose to T. reesei growing on cellulose did not further stimulate cellulase synthesis, and addition of cellobiose was inhibitory. Cellobiose, however, promoted cellulase formation in both batch and resting cell cultures, when its hydrolysis by β-glucosidase was inhibited by nojirimycin. No cellulase formation was observed when the uptake of glucose (produced from cellobiose by β-glucosidase) was inhibited by 3-O-methylglucoside. Cellodextrins (C₂ to C₆) promoted formation of low levels of cellobiohydrolase I in indirect proportion to their rate of hydrolysis by β-glucosidase. Studies on the uptake of [³H]cellobiose, [³H]sophorose, and [¹⁴C]glucose in the presence of inhibitors of β-glucosidase (nojirimycin) and glucose transport (3-O-methylglucoside) show that glucose transport occurs at a much higher rate than disaccharide hydrolysis. Extracellular disaccharide hydrolysis accounts for at least 95% of their metabolism. The presence of an uptake system for cellobiose was established by demonstrating the presence of intracellular labeled [³H]cellobiose in T. reesei after its extracellular supply. The data are consistent with induction of cellulase and particularly CBH I formation in T. reesei by β-linked disaccharides under conditions where their uptake is favored at the expense of extracellular hydrolysis.     

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.     

Conversion of cellulose to glucose with cellulase of Trichoderma viride ITCC-1433

Trichoderma viride ITCC-1433 secretes a cellulase complex that is rich in β-glucosidase and therefore well suited for the saccharification of cellulosic materials. The cellulase was investigated with respect to optimum conditions of reaction and enzyme stability. Avicelase, CMCase, and β-glucosidase differed considerably in their physicochemical properties. At temperatures above 50°C, β-glucosidase is not very stable. Therefore, as a compromise the conditions of hydrolysis were chosen to be 50°C and pH 4.5. With the crude culture filtrate of T. viride ITCC-1433 a nearly pure glucose solution of 4% is reached from a 10% cellulose suspension. Wood pulp and newsprint are hydrolyzed to a much smaller extent. With an enzyme concentrate up to 8% glucose accumulated in the reaction fluid within 48 hr. At this time the glucose-cellobiose ratio was 75:1. Glucose was demonstrated to be the most potent inhibitor of total hydrolysis. The addition of glucose to the enzyme-substrate solution at zero time completely stopped its own formation and cellobiose and reducing groups (oligosaccharides) accumulated. By removing glucose through an ultrafilter device about 90% saccharification of cellulose to glucose was achieved in 48 hr without any accumulation of cellobiose.     

Isolation and properties of mutants of the fungus Penicillium pinophilum with enhanced cellulase and β-glucosidase production

A number of mutant strains overproducing cellulase, β-glucosidase and xylanase enzyme were isolated from the cellulolytic fungus Penicillium pinophilum 87160iii after mutagenesis by u.v. irradiation and/or chemical treatment. Selection was carried out using either an agar-plate or an enrichment technique. Cellulase (filter paper-hydrolysing activity) production by some of the mutants in shake flask cultures was approximately four-fold higher than the wild-type strain; improvements in β-glucosidase production were of the order of eight- to-ninefold. The morphology of the mycelium of the mutants was quite different from that of the wild type. The mutants, for example, produced mycelium which was highly branched and thicker in cross section. In several of the mutants synthesis of xylanase and β-glucosidase was completely derepressed in the presence of glycerol, which was a known repressor of the synthesis of these enzymes. Several of the mutants produced β-glucosidase enzyme which showed altered kinetics of hydrolysis in the presence of inhibitors.     

Assessment of methods to determine minimal cellulase concentrations for efficient hydrolysis of cellulose

Summary The enzyme loading needed to achieve substrate saturation appeared to be the most economical enzyme concentration to use for hydrolysis, based on percentage hydrolysis. Saturation was reached at 25 filter paper units per gram substrate on Solka Floc BW300, as determined by studying (a) initial adsorption of the cellulase preparation onto the substrate, (b) an actual hydrolysis or (c) a combined hydrolysis and fermentation (CHF) process. Initial adsorption of the cellulases onto the substrate can be used to determine the minimal cellulase requirements for efficient hydrolysis since enzymes initially adsorbed to the substrate have a strong role in governing the overall reaction. Trichoderma harzianum E58 produces high levels of -glucosidase and is able to cause high conversion of Solka Floc BW300 to glucose without the need for exogenous -glucosidase. End-product inhibition of the cellulase and -glucosidase can be more effectively reduced by employing a CHF process than by supplemental -glucosidase.Offprint requests to: C. M. Hogan     

Comparative production of cellulases by mutants of Penicillium janthinellum NCIM 1171 and its application in hydrolysis of Avicel and cellulose

Mutants of Penicillium janthinellum NCIM 1171 were evaluated for cellulase production using both submerged fermentation (SmF) and solid state fermentation (SSF). Mutant EU2D-21 gave highest yields of cellulases in both SmF and SSF. Hydrolysis of Avicel and cellulose were compared using SmF and SSF derived enzyme preparations obtained from EU2D-21. Surprisingly, the use of SSF derived preparation gave less hydrolysis compared to SmF derived enzymes. This may be due to inactivation of β-glucosidase at 50 °C in SSF derived enzyme preparations. SmF derived enzyme preparations contained both thermostable and thermosensitive β-glucosidases where as SSF derived enzyme preparations contained predominantly thermosensitive β-glucosidase. This is the first report on less thermostability of SSF derived β-glucosidase which is the main reason for getting less hydrolysis.     

Influence of solid loading on enzymatic hydrolysis of steam exploded or liquid hot water pretreated olive tree biomass

Olive tree pruning biomass, pretreated by either liquid hot water or steam explosion under selected conditions, was used as a substrate for enzymatic hydrolysis. The pretreated material was further submitted to alkaline delignification, the objective being to improve hydrolysis yields as well as increasing cellulose content in the pretreated feedstock. The enzymatic hydrolysis of pretreated residues was performed using a commercial cellulase mixture supplemented with β-glucosidase, using a solid loading range from 2 to 30% (w/v). The influence of substrate concentration on the enzymatic hydrolysis yield and on glucose concentration was studied. Comparative results with and without a delignification step are presented. Enzymatic hydrolysis at high substrate concentration (≥20%) is possible, yielding a concentrated glucose solution (>50 g/L). Nevertheless, a cellulose fraction of the pretreated residue remains unaltered.     

Comprehensive Enzymatic Analysis of the Cellulolytic System in Digestive Fluid of the Sea Hare Aplysia kurodai. Efficient Glucose Release from Sea Lettuce by Synergistic Action of 45 kDa Endoglucanase and 210 kDa ?-Glucosidase

Although many endo-ß-1,4-glucanases have been isolated in invertebrates, their cellulolytic systems are not fully understood. In particular, gastropod feeding on seaweed is considered an excellent model system for production of bioethanol and renewable bioenergy from third-generation feedstocks (microalgae and seaweeds). In this study, enzymes involved in the conversion of cellulose and other polysaccharides to glucose in digestive fluids of the sea hare (Aplysia kurodai) were screened and characterized to determine how the sea hare obtains glucose from sea lettuce (Ulva pertusa). Four endo-ß-1,4-glucanases (21K, 45K, 65K, and 95K cellulase) and 2 ß-glucosidases (110K and 210K) were purified to a homogeneous state, and the synergistic action of these enzymes during cellulose digestion was analyzed. All cellulases exhibited cellulase and lichenase activities and showed distinct cleavage specificities against cellooligosaccharides and filter paper. Filter paper was digested to cellobiose, cellotriose, and cellotetraose by 21K cellulase, whereas 45K and 65K enzymes hydrolyzed the filter paper to cellobiose and glucose. 210K ß-glucosidase showed unique substrate specificity against synthetic and natural substrates, and 4-methylumbelliferyl (4MU)-ß-glucoside, 4MU–ß-galactoside, cello-oligosaccharides, laminarin, and lichenan were suitable substrates. Furthermore, 210K ß-glucosidase possesses lactase activity. Although ß-glucosidase and cellulase are necessary for efficient hydrolysis of carboxymethylcellulose to glucose, laminarin is hydrolyzed to glucose only by 210K ß-glucosidase. Kinetic analysis of the inhibition of 210K ß-glucosidase by D-glucono-1,5-lactone suggested the presence of 2 active sites similar to those of mammalian lactase-phlorizin hydrolase. Saccharification of sea lettuce was considerably stimulated by the synergistic action of 45K cellulase and 210K ß-glucosidase. Our results indicate that 45K cellulase and 210K ß-glucosidase are the core components of the sea hare digestive system for efficient production of glucose from sea lettuce. These findings contribute important new insights into the development of biofuel processing biotechnologies from seaweed.     

Hydrolysis of different chain length xylooliogmers by cellulase and hemicellulase

Commercial cellulase complexes produced by cellulolytic fungi contain enzyme activities that are capable of hydrolyzing non-cellulosic polysaccharides in biomass, primarily hemicellulose and pectins, in addition to cellulose. However, xylanase activities detected in most commercial enzyme preparations have been shown to be insufficient to completely hydrolyze xylan, resulting in high xylooligomer concentrations remaining in the hydrolysis broth. Our recent research showed that these xylooligomers are stronger inhibitors of cellulase activity than others have previously established for glucose and cellobiose, making their removal of great importance. In this study, a HPLC system that can measure xylooligomers with degrees of polymerization (DP) up to 30 was applied to assess how Spezyme CP cellulase, Novozyme 188 β-glucosidase, Multifect xylanase, and non-commercial β-xylosidase enzymes hydrolyze different chain length xylooligomers derived from birchwood xylan. Spezyme CP cellulase and Multifect xylanase partially hydrolyzed high DP xylooligomers to lower DP species and monomeric xylose, while β-xylosidase showed the strongest ability to degrade both high and low DP xylooligomers. However, about 10-30% of the higher DP xylooligomers were difficult to be breakdown by cellulase or xylanase and about 5% of low DP xylooligomers (mainly xylobiose) proved resistant to hydrolysis by cellulase or β-glucosidase, possibly due to low β-xylosidase activity in these enzymes and/or the precipitation of high DP xylooligomers.     

Directed evolution of an exoglucanase facilitated by a co-expressed β-glucosidase and construction of a whole engineered cellulase system in Escherichia coli

A novel high-throughput screening method is proposed for the directed evolution of exoglucanase facilitated by the co-expression of β-glucosidase, using the glucose released from filter paper as the screening indicator. Three transformants (B1, D6 and G10) with improved activity were selected from 4,000 colonies. The specific activities of B1, D6 and G10 for releasing glucose were, respectively, 1.4-, 1.3- and 1.6-fold higher than that of the wild type. The engineered exoglucanase gene was inserted into an expression vector carrying the previously engineered endoglucanase and β-glucosidase genes, and transformed into Escherichia coli to form a completely engineered cellulase system that showed 8.2-fold increase in glucose production (relative activity) compared to the cells equipped with wild-type enzymes. To our knowledge, this is the first report for directed evolution of an exoglucanase using insoluble cellulose as the screening substrate.     

Functional cello-oligosaccharides production from the corncob residues of xylo-oligosaccharides manufacture

An integrated process has been developed, consisting of the “adsorption–separation” of cellulase enzymes to selectively remove β-glucosidase, and multi-stage enzymatic hydrolysis of corncob residues from xylo-oligosaccharides manufacture with the β-glucosidase deficient cellulase, aiming to obtain a high yield of cello-oligosaccharides production. After the “adsorption–separation” process, 79.50% of the endo-glucanase was retained in substrate, whereas 90.67% of β-glucosidase was removed with the separated liquid fraction, utilizing the different adsorbability of these enzymes to the substrate. A three-stage enzymatic hydrolysis of corncob residues with the β-glucosidase deficient cellulase was proposed in which the first, the second and the third stage were conducted for 6, 6 h and 12 h, respectively. Analysis indicated that the removal of hydrolysis products (glucose and cello-oligosaccharides) at each stage improved cello-oligosaccharides productivity and enzymatic hydrolysis yield. The cello-oligosaccharides yield and enzymatic hydrolysis yield in three-stage enzymatic hydrolysis were significantly improved to 51.78% and 75.56%, respectively, which were 36.00% and 25.10% higher than single-stage hydrolysis with original cellulase enzymes.     

Ethanol production from sunflower meal biomass by simultaneous saccharification and fermentation (SSF) with Kluyveromyces marxianus ATCC 36907

The lignocellulosic materials are considered promising renewable resources for ethanol production, but improvements in the processes should be studied to reduce operating costs. Thus, the appropriate enzyme loading for cellulose saccharification is critical for process economics. This study aimed at evaluating the concentration of cellulase and β-glucosidase in the production of bioethanol by simultaneous saccharification and fermentation (SSF) of sunflower meal biomass. The sunflower biomass was pretreated with 6 % H₂SO₄ (w/v), at 121 °C, for 20 min, for hemicellulose removal and delignificated with 1 % NaOH. SSF was performed with Kluyveromyces marxianus ATCC 36907, at 38 °C, 150 rpm, for 72 h, with different enzyme concentrations (Cellulase Complex NS22086-10, 15 and 20 FPU/g_substrate and β-Glucosidase NS22118, with a cellulase to β-glucosidase ratio of 1.5:1; 2:1 and 3:1). The best condition for ethanol production was cellulase 20 FPU/g_substrate and β-glucosidase 13.3 CBU/g_substrate, resulting in 27.88 g/L ethanol, yield of 0.47 g/g and productivity of 0.38 g/L h. Under this condition the highest enzymatic conversion of cellulose to glucose was attained (87.06 %).     

The heterologous expression potential of an acid-tolerant <Emphasis Type="Italic">Talaromyces pinophilus</Emphasis> β-glucosidase in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

A filamentous fungus displaying high cellulase activity was isolated from a compost heap with triticale (a wheat-rye hybrid) as the main constituent. It was preliminarily identified as a Talaromyces pinophilus species. A 2577 base pair β-glucosidase gene was cloned from complementary DNA and heterologously expressed in Saccharomyces cerevisiae. The recombinant β-glucosidase production profile was assessed and compared to that of the Saccharomycopsis fibuligera β-glucosidase which served as a benchmark. The enzyme was also characterised in terms of pH and temperature tolerance as well as response to inhibitors. Maximal extracellular β-glucosidase activity of 0.56 nkat/mg total protein was measured using p-nitrophenyl-β-D-glucopyranoside as substrate. The recombinant protein displayed a pH optimum of 4.0, and good thermostability as 70% of maximal enzyme activity was retained after 1 h at 60 °C. Activity of the recombinant β-glucosidase was adversely affected by the presence of glucose and ethanol at higher concentrations while xylose had no effect. The expression of the T. pinophilus β-glucosidase did not reach the same titres as for the benchmark; however, in the context of constructing a yeast strain for bioethanol production in a consolidated bioprocess, the enzyme may still show good potential.