The traditional way of rationally engineering enzymes to change their biocatalytic properties utilizes the modifications of their active sites. Another emerging approach is the engineering of structural features involved in the exchange of ligands between buried active sites and the surrounding solvent. However, surprisingly little is known about the effects of mutations that alter the access tunnels on the enzymes' catalytic properties, and how these tunnels should be redesigned to allow fast passage of cognate substrates and products. Thus, we have systematically studied the effects of single-point mutations in a tunnel-lining residue of a haloalkane dehalogenase on the binding kinetics and catalytic conversion of both linear and branched haloalkanes. The hotspot residue Y176 was identified using computer simulations and randomized through saturation mutagenesis, and the resulting variants were screened for shifts in binding rates. Strikingly, opposite effects of the substituted residues on the catalytic efficiency toward linear and branched substrates were observed, which was found to be due to substrate-specific requirements in the critical steps of the respective catalytic cycles. We conclude that not only the catalytic sites, but also the access pathways must be tailored specifically for each individual ligand, which is a new paradigm in protein engineering and de novo protein design. A rational approach is proposed here to address more effectively the task of designing ligand-specific tunnels using computational tools.

Molecular recognition mechanisms and kinetics of binding of ligands to buried active sites via access tunnels are not well understood. Fluorescence polarization enables rapid and non-destructive real-time quantification of the association between small fluorescent ligands and large biomolecules. In this study, we describe analysis of binding kinetics of fluorescent ligands resembling linear halogenated alkanes to haloalkane dehalogenases. Dehalogenases possess buried active sites connected to the surrounding solvent by access tunnels. Modification of these tunnels by mutagenesis has emerged as a novel strategy to tailor the enzyme properties. We demonstrate that the fluorescence polarization method can sense differences in binding kinetics originating from even single mutations introduced to the tunnels. The results show, strikingly, that the rate constant of the dehalogenase variants varied across seven orders of magnitude, and the type of ligand used strongly affected the binding kinetics of the enzyme. Furthermore, fluorescence polarization could be applied to cell-free extracts instead of purified proteins, extending the method's application to mediumthroughput screening of enzyme variant libraries generated in directed evolution experiments. The method can also provide in-depth kinetic information about the rate-determining step in binding kinetics and reveals the bottlenecks of enzyme accessibility. Assuming availability of appropriate fluorescent ligand, the method could be applied for analysis of accessibility of tunnels and buried active sites of enzymes forming a covalent alkylenzyme intermediate during their catalytic cycle, such as a/b-hydrolases containing > 100 000 protein sequences based on the Pfam database.

Immobilized cells of a recombinant Escherichia coli expressing nitrilase from Pseudomonas putida were used to catalyze the hydrolysis of mandelonitrile (2-hydroxy-2-phenylacetonitrile) to ( R )-(−)-mandelic acid. The cells had been immobilized by entrapment in an alginate matrix. Conditions for the hydrolysis reaction were optimized in shake flasks and in a packed bed reactor. In shake flasks the best conditions for the reaction were a temperature of 40 °C, pH 8, biocatalyst bead diameter of 4.3 mm, sodium alginate concentration in the gel matrix of 2 % (w/v, g/100 mL), a cell dry mass concentration in the bead matrix of 20 mg/mL, an initial substrate concentration of 50 mM and a reaction time of 60 min. Under these conditions, the conversion of mandelonitrile was nearly 95 %. In the packed bed reactor, a feed flow rate of 20 mL/h at a substrate concentration of 200 mM proved to be the best at 40 °C, pH 8, using 4.3 mm beads (2 % w/v sodium alginate in the gel matrix, 20 mg dry cell concentration per mL of gel matrix). This feed flow rate corresponded to a residence time of 0.975 h in the packed bed.