The GH67 α-glucuronidase of Paenibacillus curdlanolyticus B-6 removes hexenuronic acid groups and facilitates biodegradation of the model xylooligosaccharide hexenuronosyl xylotriose.

4-O-Methylglucuronic acid (MeGlcA) side groups attached to the xylan backbone through α-1,2 linkages are converted to hexenuronic acid (HexA) during alkaline pulping. α-Glucuronidase (EC 3.2.1.139) hydrolyzes 1,2-linked MeGlcA from xylooligosaccharides. To determine whether α-glucuronidase can also hydrolyze HexA-decorated xylooligosaccharides, a gene encoding α-glucuronidase (AguA) was cloned from Paenibacillus curdlanolyticus B-6. The purified protein degraded hexenuronosyl xylotriose (ΔX3), a model substrate prepared from kraft pulp. AguA released xylotriose and HexA from ΔX3, but the Vmax and kcat values for ΔX3 were lower than those for MeGlcA, indicating that HexA side groups may affect the hydrolytic activity. To explore the potential for biological bleaching, ΔX3 degradation was performed using intracellular extract from P. curdlanolyticus B-6. The intracellular extract, with synergistic α-glucuronidase and ß-xylosidase activities, degraded ΔX3 to xylose and HexA. These results indicate that α-glucuronidase can be used to remove HexA from ΔX3 derived from pulp, reducing the need for chemical treatments in the pulping process.

The C-terminal region of xylanase domain in Xyn11A from Paenibacillus curdlanolyticus B-6 plays an important role in structural stability.

Paenibacillus curdlanolyticus B-6 produces an extracellular multienzyme complex containing a major xylanase subunit, designated Xyn11A, which includes two functional domains belonging to glycosyl hydrolase family-11 (GH11) and carbohydrate binding module family-36 (CBM36) and possesses a glycine and asparagine-rich linker (linker). To clarify the roles of each functional domain, recombinant proteins XynXL and XynX (CBM36 deleted and CBM36 and linker deleted, respectively) were constructed. Their xylanase activities were similar toward soluble xylan, whereas XynXL showed decreased hydrolysis activity toward insoluble xylan while XynX had no xylanase activity. To determine the significance of the linker and its neighbor region, XynX was subjected to secondary structural alignments using circular dichroism (CD) spectroscopy and three-dimensional (3D) structural analysis. A seven amino acid (NTITIGG) neighbor linker sequence was highly conserved among GH11 xylanases of Paenibacillus species. Although XynX exhibited a typical GH11 xylanase structure, conformational gaps were observed in the ß6- and ß12-sheets and in CD spectra. Flipping of the Arg163 side chains in the subsite was also observed upon analysis of superimposed models. Docking analysis using xylohexaose indicated that flipping of the Arg163 side chains markedly affected substrate binding in the subsite. To identify the amino acids related to stabilizing the substrate binding site, XynX with an extended C-terminal region was designed. At least seven amino acids were necessary to recover substrate binding and xylanase activity. These results indicated that the seven amino acid neighbor Xyn11A linker plays an important role in the activity and conformational stability of the xylanase domain.

Direct glucose production from lignocellulose using Clostridium thermocellum cultures supplemented with a thermostable ß-glucosidase.

BACKGROUND: Cellulases continue to be one of the major costs associated with the lignocellulose hydrolysis process. Clostridium thermocellum is an anaerobic, thermophilic, cellulolytic bacterium that produces cellulosomes capable of efficiently degrading plant cell walls. The end-product cellobiose, however, inhibits degradation. To maximize the cellulolytic ability of C. thermocellum, it is important to eliminate this end-product inhibition. RESULTS: This work describes a system for biological saccharification that leads to glucose production following hydrolysis of lignocellulosic biomass. C. thermocellum cultures supplemented with thermostable beta-glucosidases make up this system. This approach does not require any supplementation with cellulases and hemicellulases. When C. thermocellum strain S14 was cultured with a Thermoanaerobacter brockii beta-glucosidase (CglT with activity 30 U/g cellulose) in medium containing 100 g/L cellulose (617 mM initial glucose equivalents), we observed not only high degradation of cellulose, but also accumulation of 426 mM glucose in the culture broth. In contrast, cultures without CglT, or with less thermostable beta-glucosidases, did not efficiently hydrolyze cellulose and accumulated high levels of glucose. Glucose production required a cellulose load of over 10 g/L. When alkali-pretreated rice straw containing 100 g/L glucan was used as the lignocellulosic biomass, approximately 72% of the glucan was saccharified, and glucose accumulated to 446 mM in the culture broth. The hydrolysate slurry containing glucose was directly fermented to 694 mM ethanol by addition of Saccharomyces cerevisiae, giving an 85% theoretical yield without any inhibition. CONCLUSIONS: Our process is the first instance of biological saccharification with exclusive production and accumulation of glucose from lignocellulosic biomass. The key to its success was the use of C. thermocellum supplemented with a thermostable beta-glucosidase and cultured under a high cellulose load. We named this approach biological simultaneous enzyme production and saccharification (BSES). BSES may resolve a significant barrier to economical production by providing a platform for production of fermentable sugars with reduced enzyme amounts.