p-Aminophenyl 1-thio-β-d-cellobioside: Synthesis and application in affinity chromatography of exo-type cellulases

Rhamnolipids as affinity foaming agent for selective collection of β-glucosidase from cellulase enzyme mixture

Selective and effective separation can potentially be achieved with affinity foam fractionation using simple foaming setup and operation. In this study the use of affinity foam fractionation for selective collection and enrichment of β-glucosidase from a cellulase enzyme mixture was evaluated. Rhamnolipids, a group of glycolipids produced most commonly by Pseudomonas aeruginosa, were used as the affinity foaming agent, because of their foaming property and the presence of dirhamnose moiety (a potential substrate analog for β-glucosidase) in some rhamnolipids. The effects of aeration rate, medium pH, cellulase concentration and rhamnolipid concentration on the foam fractionation performance were examined. Among the pH studied (3.1, 5.0, 7.0 and 9.0), pH 5 was clearly the optimal for selective enrichment of β-glucosidase, presumably corresponding to the high binding affinity between the enzyme and the substrate analog (dirhamnose). With adequate rhamnolipid concentrations (≥0.1 g/L), the aeration rate of 0.1L/min (i.e., 2VVM) for 50 ml test samples was found to give the highest enrichment; higher aeration rates produced wetter foam and, thus, lower (diluted) enzyme activity in the foamate. The enrichment increased with the increasing rhamnolipids-to-cellulase ratio, in the range of 0-2 (w/w) investigated in this study. The finding indicated that rhamnolipids were the limiting compounds in these systems so that the amount of surfactant-enzyme complexes formed and removed into the foam phase would increase when more rhamnolipids were added. At the rhamnolipids-to-cellulase ratio of 2, the β-glucosidase activity in the foamate was about 9 times as high as the activity in the original sample of cellulase mixture and about 17 times the activity in the remaining solution (after foaming). The overall FPU (filter paper unit, a measurement of total cellulase activity) and the activities of endo- and exo-glucanases were only enriched 70-150%. The feasibility of affinity foam fractionation was demonstrated.

Beta-glycosylamidine as a ligand for affinity chromatography tailored to the glycon substrate specificity of beta-glycosidases

An affinity adsorbent for beta-glycosidases has been prepared by using beta-glycosylamidine as a ligand. beta-Glucosylamidine and beta-galactosylamidine, highly potent and selective inhibitors of beta-glucosidases and beta-galactosidases, respectively, were immobilized by a novel one-pot procedure involving the addition of a beta-glycosylamine and 2-iminothiolane.HCl simultaneously to a matrix modified with maleimido groups via an appropriate spacer to give an affinity adsorbent for beta-glucosidases and beta-galactosidases, respectively. This one-pot procedure enables various beta-glycosylamidine ligands to be formed and immobilized conveniently according to the glycon substrate specificities of the enzymes. A crude enzyme extract from tea leaves (Camellia sinensis) and a beta-galactosidase from Penicillium multicolor were chromatographed directly on each affinity adsorbent to give a beta-glucosidase and a beta-galactosidase to apparent homogeneity in one step by eluting the column with glucose or by a gradient NaCl elution, respectively. The beta-glucosidase and beta-galactosidase were inhibited competitively by a soluble form of the corresponding beta-glycosylamidine ligand with an inhibition constant (K(i)) of 2.1 and 0.80 microM, respectively. Neither enzyme was bound to the adsorbent with a mismatched ligand, indicating that the binding of the glycosidases was of specific nature that corresponds to the glycon substrate specificity of the enzymes. The ease of preparation and the selective nature of the affinity adsorbent should promise a large-scale preparation of the affinity adsorbent for the purification and removal of specific glycosidases according to their glycon substrate specificities.

Adsorption of Trichoderma reesei CBHI cellulase on silanized silica

Adsorption kinetics and surfactant-mediated elution of Trichoderma reesei CBHI cellulase were recorded in situ, at hydrophobic, silanized silica. Experiments were performed at different solution concentrations, ranging from 0.001 to 0.98 mg/mL. Adsorbed enzyme was partially elutable upon rinsing, with the amount of adsorbed mass remaining being highest at intermediate concentrations. In addition, the resistance to elution with buffer was generally lower at higher concentrations, and the resistance to elution with surfactant was generally lower at intermediate concentrations. These observations are tentatively explained with reference to a mechanism allowing for adsorption of associated monomers of CBHI as well as free monomers.

Aryl thioglycoside-based affinity purification of exo-acting cellulases

The influence of ligand-coupling chemistry and mobile-phase composition on the interaction of exo-acting cellulases with an immobilized complementary ligand was investigated. p-Aminophenyl 1-thio-beta-D-cellobioside (APTC) was used as a representative affinity ligand to which exo-acting cellulases (cellobiohydrolases, CBHs) preferentially bind. A "crude" cellulase preparation from the fungus Trichoderma reesei served as an enzyme source. The adsorption properties of the two principal exo-acting CBHs in this preparation, CBH I and CBH II, are shown to be distinctly different under several scenarios. Their relative affinities, based on column elution behavior and partition equilibrium experiments, are shown to be highly dependent on the functional groups employed for ligand coupling, the extent of functional group hydrolysis, the composition of the mobile phase, and the inherent nature of the enzymes. The dependency on the chemistry of the supporting matrix was illustrated using agarose supports containing cyanate ester, N-hydroxy-succinimide, and epoxy functional groups. When compared under apparent optimal conditions, the affinity of CBH II for immobilized APTC was approximately 10-fold that of CBH I. However, selective adsorption of CBH I or CBH II can be achieved by adjusting experimental parameters.