Properties and applications of microbial β-D-xylosidases featuring the catalytically efficient enzyme from Selenomonas ruminantium

Activation of a GH43 β-xylosidase by divalent metal cations: slow binding of divalent metal and high substrate specificity

RS223-BX of glycoside hydrolase family 43 is a β-d-xylosidase that is strongly activated (k(cat)/K(m) as much as 116-fold) by the addition of divalent metal cations, Ca(2+), Co(2+), Fe(2+), Mg(2+), Mn(2+) and Ni(2+). Slow activation by Mg(2+) was demonstrated (k(on) 0.013 s(-1) mM(-1), k(off) 0.008 s(-1)) at pH 7.0 and 25 °C. k(off) and k(on) values are independent of Mg(2+) concentration, but k(off) and k(on) are slower in the presence of increasing levels of substrate 4-nitrophenyl-β-D-xylopyranoside. The kinetics strongly suggest that M(2+) binds to the enzyme rapidly, forming E M(2+), followed by slow isomerization to the activated enzyme, E* M(2+). Moderately high values of kcat (7-30 s(-1)) were found for M(2+)-activated RS223-BX acting on xylobiose (natural substrate) at pH 7.0 and 25 °C. Certain M(2+)-activated RS223-BX exhibit the highest reported values of k(cat)/K(m) of any β-xylosidase acting on natural substrates: for example, at pH 7.0 and 25°C, xylobiose (Mn(2+), 190 s(-1) mM(-1)), xylotriose (Ca(2+), 150 s(-1) mM(-1)) and xylotetraose (Ca(2+), 260 s(-1) mM(-1)). There is potential for the enzyme to add value to industrial saccharification operations at low substrate and high d-glucose and high d-xylose concentrations.

The substrate/product-binding modes of a novel GH120 β-xylosidase (XylC) from Thermoanaerobacterium saccharolyticum JW/SL-YS485

Xylan-1,4-β-xylosidase (β-xylosidase) hydrolyses xylo-oligomers at their non-reducing ends into individual xylose units. Recently, XylC, a β-xylosidase from Thermoanaerobacterium saccharolyticum JW/SL-YS485, was found to be structurally different from corresponding glycosyl hydrolases in the CAZy database (http://www.cazy.org/), and was subsequently classified as the first member of a novel family of glycoside hydrolases (GH120). In the present paper, we report three crystal structures of XylC in complex with Tris, xylobiose and xylose at 1.48-2.05 Å (1 Å=0.1 nm) resolution. XylC assembles into a tetramer, and each monomer comprises two distinct domains. The core domain is a right-handed parallel β-helix (residues 1-75 and 201-638) and the flanking region (residues 76-200) folds into a β-sandwich domain. The enzyme contains an open carbohydrate-binding cleft, allowing accommodation of longer xylo-oligosaccharides. On the basis of the crystal structures and in agreement with previous kinetic data, we propose that XylC cleaves the glycosidic bond by the retaining mechanism using two acidic residues Asp382 (nucleophile) and Glu405 (general acid/base). In addition to the active site, nine other xylose-binding sites were consistently observed in each of the four monomers, providing a possible reason for the high tolerance of product inhibition.

Divalent metal activation of a GH43 β-xylosidase

Depolymerization of xylan, a major fraction of lignocellulosic biomass, releases xylose which can be converted into transportation fuels and chemical feedstocks. A requisite enzyme for the breakdown of xylan is β-xylosidase. A gene encoding the 324-amino acid β-xylosidase, RS223-BX, was cloned from an anaerobic mixed microbial culture. This glycoside hydrolase belongs to family 43. Unlike other GH43 enzymes, RS223-BX can be strongly activated by exogenously supplied Ca(2+), Co(2+), Fe(2+), Mg(2+), Mn(2+) and Ni(2+) (e.g., 28-fold by Mg(2+)) and it is inhibited by Cu(2+) or Zn(2+). Sedimentation equilibrium centrifugation experiments indicated that the divalent metal cations mediate multimerization of the enzyme from a dimeric to a tetrameric state, which have equal catalytic activity on an active-site basis. Compared to the determined active sites of other GH43 β-xylosidases, the predicted active site of RS223-BX contains two additional amino acids with carboxylated side chains that provide potential sites for divalent metal cations to reside. Thus, the divalent metal cations likely occupy the active site and participate in the catalytic mechanism. RS223-BX accepts as substrate xylobiose, arabinobiose, 4-nitrophenyl-β-D-xylopyranoside, and 4-nitrophenyl-α-L-arabinofuranoside. Additionally, the enzyme has good pH and temperature stabilities and a large K(i) for D-glucose (1.3 M), favorable properties for performance in saccharification reactors.

Highly active β-xylosidases of glycoside hydrolase family 43 operating on natural and artificial substrates

The hemicellulose xylan constitutes a major portion of plant biomass, a renewable feedstock available for conversion to biofuels and other bioproducts. β-xylosidase operates in the deconstruction of the polysaccharide to fermentable sugars. Glycoside hydrolase family 43 is recognized as a source of highly active β-xylosidases, some of which could have practical applications. The biochemical details of four GH43 β-xylosidases (those from Alkaliphilus metalliredigens QYMF, Bacillus pumilus, Bacillus subtilis subsp. subtilis str. 168, and Lactobacillus brevis ATCC 367) are examined here. Sedimentation equilibrium experiments indicate that the quaternary states of three of the enzymes are mixtures of monomers and homodimers (B. pumilus) or mixtures of homodimers and homotetramers (B. subtilis and L. brevis). k cat and k cat/K m values of the four enzymes are higher for xylobiose than for xylotriose, suggesting that the enzyme active sites comprise two subsites, as has been demonstrated by the X-ray structures of other GH43 β-xylosidases. The K i values for D-glucose (83.3-357 mM) and D-xylose (15.6-70.0 mM) of the four enzymes are moderately high. The four enzymes display good temperature (K t (0.5) ∼ 45 °C) and pH stabilities (>4.6 to <10.3). At pH 6.0 and 25 °C, the enzyme from L. brevis ATCC 367 displays the highest reported k cat and k cat/K m on natural substrates xylobiose (407 s(-1), 138 s(-1) mM(-1)), xylotriose (235 s(-1), 80.8 s(-1) mM(-1)), and xylotetraose (146 s(-1), 32.6 s(-1) mM(-1)).

Plant cell walls to ethanol

Conversion of plant cell walls to ethanol constitutes second generation bioethanol production. The process consists of several steps: biomass selection/genetic modification, physiochemical pretreatment, enzymatic saccharification, fermentation and separation. Ultimately, it is desirable to combine as many of the biochemical steps as possible in a single organism to achieve CBP (consolidated bioprocessing). A commercially ready CBP organism is currently unreported. Production of second generation bioethanol is hindered by economics, particularly in the cost of pretreatment (including waste management and solvent recovery), the cost of saccharification enzymes (particularly exocellulases and endocellulases displaying kcat ~1 s−1 on crystalline cellulose), and the inefficiency of co-fermentation of 5- and 6-carbon monosaccharides (owing in part to redox cofactor imbalances in Saccharomyces cerevisiae).