One of the primary sources of enzyme instability is protein oxidative modification triggering activity loss or denaturation. We show here that the side chain of Cys108 is the main site undergoing stress-induced oxidation in Trigonopsis variabilis D-amino acid oxidase, a flavoenzyme employed industrially for the conversion of cephalosporin C. High-resolution anion-exchange chromatography was used to separate the reduced and oxidized protein forms, which constitute, in a molar ratio of about 3:1, the active biocatalyst isolated from the yeast. Comparative analysis of their tryptic peptides by electrospray tandem mass spectrometry allowed unequivocal assignment of the modification as the oxidation of Cys108 into cysteine sulfinic acid. Cys108 is likely located on a surface-exposed protein region within the flavin adenine dinucleotide (FAD) binding domain, but remote from the active center. Its oxidized side chain was remarkably stable in solution, thus enabling the relative biochemical characterization of native and modified enzyme forms. The oxidation of Cys108 causes a global conformational response that affects the protein environment of the FAD cofactor. In comparison with the native enzyme, it results in a fourfold-decreased specific activity, reflecting a catalytic efficiency for reduction of dioxygen lowered by about the same factor, and a markedly decreased propensity to aggregate under conditions of thermal denaturation. These results open up unprecedented routes for stabilization of the oxidase and underscore the possible significance of protein chemical heterogeneity for biocatalyst function and stability.

Trigonopsis variabilis D-amino acid oxidase (TvDAO) is a long-known flavoenzyme whose most important biocatalytic application is currently the industrial production of 7-amino-cephalosporanic acid (7-ACA) from cephalosporin C. Lacking mechanistic foundation, rational stabilization of TvDAO for improved process performance remains a problem. We report on results of thermal denaturation studies at 50 degrees C in which two purified TvDAO forms were compared: the native enzyme, and a site-specifically oxidized protein variant that had the side chain of cysteine108 converted into a sulfinic acid and lost 75% of original specific activity. Although inactivation time courses for both enzymes are fairly well described by simple single-exponential decays, the underlying denaturation mechanisms are shown by experiments and modeling to be complex. One main path leading to inactivation is FAD release, a process whose net rate is determined by the reverse association rate constant (k), which is 25-fold lower in the oxidized form of TvDAO. Cofactor dissociation is kinetically coupled to aggregation and can be blocked completely by the addition of free FAD. Aggregation is markedly attenuated in the less stable Cys108-SO(2)H-containing enzyme, suggesting that it is a step accompanying but not causing the inactivation. A second parallel path, characterized by a k-value of 0.26/h that is not dependent on protein concentration and identical for both enzymes, likely reflects thermal unfolding reactions. A third, however, slow process is the conversion of the native enzyme into the oxidized form (k < 0.03/h). The results fully explain the different stabilities of native and oxidized TvDAO and provide an inactivation mechanism-based tool for the stabilization of the soluble oxidase.

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The aim of this work was to investigate the possibility of conducting a continuous aerobic bioprocess in a horizontal rotating tubular bioreactor (HRTB). Aerobic oxidation of acetate by the action of a mixed microbial culture was chosen as a model process. The microbial culture was not only grown in a suspension but also in the form of a biofilm on the interior surface of HRTB. Efficiency of the bioprocess was monitored by determination of the acetate concentration and chemical oxygen demand (COD). While acetate inlet concentration and feeding rate influenced efficiency of acetate oxidation, the bioreactor rotation speed did not influence the bioprocess dynamics significantly. Gradients of acetate concentration and pH along HRTB were more pronounced at lower feeding rates. Volumetric load of acetate was proved to be the most significant parameter. High volumetric loads (above 2 g acetate l-1 h-1) gave poor acetate oxidation efficiency (only 17 to 50%). When the volumetric load was in the range of 0.60-1.75 g acetate l-1 h-1, acetate oxidation efficiency was 50-75%. At lower volumetric loads (0.14-0.58 g acetate l-1 h-1), complete acetate consumption was achieved. On the basis of the obtained results, it can be concluded that HRTB is suitable for conducting aerobic continuous bioprocesses.