Anodic reactions in microbial fuel cells

Potentiometric and amperometric measurements were made with microbial fuel cells containing E. coli or yeast as the anodic reducing agent and glucose as the oxidizable substrate. The catalytic effects of thionine and resorufin on the anode reaction were investigated. Results on the potentiometry, polarization, and coulombic output of the cells support a mediator-coupled mechanism for the transfer of electrons from the organism to the electrode in preference to a mechanism of "direct" electrochemical oxidation of glucose or its degradation products. Experiments with (14)C-labeled glucose show that when a microbial fuel cell produces a current under load, exogenous glucose is metabolized to produce (14)CO(2). The Coulombic yields of the cells indicate a high degree of energy conversion in these systems.     

Mediator-free glucose/O<Subscript>2</Subscript> biofuel cell based on a 3-dimensional glucose oxidase/SWNT/polypyrrole composite electrode

In this study, a mediator-free glucose/O₂ bio-fuel cell was developed based on a 3-dimensional carbon nanomaterial/polypyrrole composite with glucose oxidase and tyrosinase as the anodic and cathodic catalysts, respectively. This mediator-free biofuel cell has the following merits: (1) the biocatalyst was unaffected by toxic mediators and (2) current generation is independent, because there is no problem associated with mediator leakage from the electrode. The carbon nanomaterial in this 3-dimensional composite was used not only as immobilization support for the biocatalyst, but also as an electron carrier. This would be advantageous for glucose oxidation on the bioanode and O₂ reduction on the biocathode in the glucose/O₂ biofuel cell. This biofuel cell showed enhanced power density and half-life compared to other glucose/O₂ biofuel cells previously reported, producing 157.4 μW/cm³ with 1 mM glucose as fuel and 0.5 M NaCl as the electrolyte, at a cell voltage of +85 mV over 29 h with continuous 1 mM glucose feeding.     

Dihydroorotate dehydrogenase B of Enterococcus faecalis. Characterization and insights into chemical mechanism.

Enterococcus faecalis dihydroorotate dehydrogenase B is a heterodimer of 28 and 33 kDa encoded by the pyrK and pyrDb genes. Both subunits copurify during all chromatographic steps, and, as determined by HPLC, one FMN and one FAD are bound per heterodimer. The enzyme catalyzes efficient oxidation of 4-S-NADH by orotate. Isotope effect and pH data suggest that reduction of flavin by NADH at the PyrK site is only partially rate limiting with no kinetically significant proton transfer occurring in the reductive half-reaction; therefore, a group exhibiting a pK of 5.7 +/- 0.2 represents a residue involved in binding of NADH rather than in catalysis. The reducing equivalents are shuttled between the NADH-oxidizing flavin in PyrK and the orotate-reacting flavin in PyrDb, by iron-sulfur centers through flavin semiquinones as intermediates. A solvent kinetic isotope effect of 2.5 +/- 0.2 on V is indicative of rate-limiting protonation in the oxidative half-reaction and most likely reflects the interaction between the isoalloxazine N1 of the orotate-reducing flavin and Lys 168 (by analogy with L. lactis DHODase A). The oxidative half-reaction is facilitated by deprotonation of the group(s) with pK(s) of 5.8-6.3 and reflects either deprotonation of the reduced flavin or binding of orotate; this step is followed by hydride transfer to C6 and general acid-assisted protonation (pK of 9.1 +/- 0.2) at C5 of the product.     

Regioselective control of β-d-glucose oxidation by pyranose 2-oxidase is intimately coupled to conformational degeneracy

Trametes multicolor pyranose 2-oxidase (P2O) is a flavoprotein oxidase that oxidizes d-glucose at C2 to 2-keto-d-glucose by a highly regioselective mechanism. In this work, fluorinated sugar substrates were used as mechanistic probes to investigate the basis of regioselectivity in P2O. Although frequently used to study the mechanisms of glycoside hydrolases, our work provides the first example of applying these probes to sugar oxidoreductases. Our previous structure of the P2O mutant H167A in complex with the slow substrate 2-deoxy-2-fluoro-d-glucose showed a substrate-binding mode compatible with oxidation at C3. To accommodate the sugar, a gating segment, ⁴⁵⁴FSY⁴⁵⁶, in the substrate recognition loop partly unfolded to create a spacious and more polar active site that is distinct from the closed state of P2O. The crystal structure presented here shows that the preferred C2 oxidation where an ordered complex of P2O H167A with 3-deoxy-3-fluoro-d-glucose at 1.35 Å resolution was successfully trapped. In this semi-open C2-oxidation complex, the substrate recognition loop tightens to form an optimized substrate complex stabilized by interactions between Asp452 and glucose O4, as well as Tyr456 and the glucose O6 group, interactions that are not possible when glucose is positioned for oxidation at C3. The different conformations of the ⁴⁵⁴FSY⁴⁵⁶ gating segment in the semi-open and closed states induce backbone and side-chain movements of Thr169 and Asp452 that add further differential stabilization to the individual states. We expect the semi-open state (C2-oxidation state) and closed state to be good approximations of the active-site structure during the reductive half-reaction (sugar oxidation) and oxidative half-reaction (O₂ reduction).     

Development of Enterobacter aerogenes fuel cells: From in situ biohydrogen oxidization to direct electroactive biofilm

This study described an Enterobacter aerogenes-catalyzed microbial fuel cell (MFC) with a carbon-based anode that exhibited a maximum power density of 2.51 W/m³ in the absence of artificial electron mediators. The MFC was started up rapidly, within hours, and the current generation in the early stage was demonstrated to result from in situ oxidation of biohydrogen produced by E. aerogenes during glucose fermentation. Over periodic replacement of substrate, both planktonic biomass in the culture liquid and hydrogen productivity decreased, while increased power density and coulombic efficiency and decreased internal resistance were unexpectedly observed. Using scanning electron microscopy and cyclic voltammetry, it was found that the enhanced MFC performance was associated with the development of electroactive biofilm on the anodic surface, proposed to involve an acclimation and selection process of E. aerogenes cells under electrochemical tension. The significant advantage of rapid start-up and the ability to develop an electroactive biofilm identifies E. aerogenes as a suitable biocatalyst for MFC applications.     

Kinetic methods for the study of the enzyme systems of β-oxidation

Kinetic methods for studying the reactions of the “general” fatty acyl CoA dehydrogenase under three sets of substrate and enzyme concentration conditions have been developed. The reaction of butyryl-CoA and electron transfer flavoprotein (ETF) can be studied either under steady-state conditions with enzyme at catalytic concentration or under single-turnover conditions with enzyme in excess. Under the latter conditions, acyl-CoA dehydrogenase acts both as a catalyst and an ultimate electron-transfer acceptor. The reductive half-reaction of butyryl-CoA and enzyme can also be studied in a separate kinetic experiment. Comparison of the pH dependences of the rate constants and isotope effects of the steady-state reaction of butyryl-CoA and ETF with the same parameters for the reductive half-reaction is consistent with a mechanism involving transfer of electrons from butyryl-CoA to ETF within a ternary complex. An alternative mechanism in which the reductive half-reaction takes place prior to the binding and reaction of ETF seems unlikely because the pH 8.5 isotope effect on the reductive half-reaction is much larger than that on the complete reaction in spite of the fact that the rates of the reactions are comparable. The pH dependence of the K_m for substrate and K_I for inhibitor is consistent with a mechanism for transfer of electrons within the ternary complex which involves protonation of the C group of substrates. The protonation labilizes the C-2 proton and base catalysis of the removal of the C-2 proton results in the production of the active enzyme-substrate species, namely the C-2 anion of substrate.     

Preferential use of an anode as an electron acceptor by an acidophilic bacterium in the presence of oxygen

Several anaerobic metal-reducing bacteria have been shown to be able to donate electrons directly to an electrode. This property is of great interest for microbial fuel cell development. To date, microbial fuel cell design requires avoiding O(2) diffusion from the cathodic compartment to the sensitive anodic compartment. Here, we show that Acidiphilium sp. strain 3.2 Sup 5 cells that were isolated from an extreme acidic environment are able to colonize graphite felt electrodes. These bacterial electrodes were able to produce high-density electrocatalytic currents, up to 3 A/m(2) at a poised potential of +0.15 V (compared to the value for the reference standard calomel electrode) in the absence of redox mediators, by oxidizing glucose even at saturating air concentrations and very low pHs.     

Understanding the Anodic Mechanism of a Seafloor Fuel Cell: Interactions Between Geochemistry and Microbial Activity

Seafloor fuel cells made with graphite electrodes generate electricity by promoting electron transfer in response to a natural voltage difference (−0.7 to −0.8 V) between anoxic sediments and overlying oxic seawater. Geochemical impacts of a seafloor fuel cell on sediment solids and porewaters were examined to identify the anodic mechanisms and substrates available for current production. In an estuarine environment with little dissolved sulfide, solid-phase acid volatile sulfide and Cr²⁺-reducible sulfur minerals decreased significantly toward the anode after 7 months of nearly continuous energy harvesting. Porewater iron and sulfate increased by millimolar amounts. Scanning electron microscope images showed a biofilm overcoating the anode, and electron microprobe analyses revealed accumulations of sulfur, iron, silicon and phosphorus at the electrode surface. Sulfur deposition was also observed on a laboratory fuel cell anode used to generate electricity with only dissolved sulfide as an electron donor. Moreover, current densities and voltages displayed by these purely chemical cells were similar to the values measured with field devices. These results indicate that electron transfer to seafloor fuel cells can readily result in the oxidation of dissolved and solid-phase forms of reduced sulfur producing mainly S⁰ which deposits at the electrode surface. This oxidation product is consistent with the observed enrichment of bacteria most closely related to Desulfobulbus/Desulfocapsa genera within the anode biofilm, and its presence is proposed to promote a localized biogeochemical cycle whereby biofilm bacteria regenerate sulfate and sulfide. This electron-shuttling mechanism may co-occur while these or other bacteria use the anode directly as a terminal electron acceptor.     

Comparison of Electrode Reduction Activities of Geobacter sulfurreducens and an Enriched Consortium in an Air-Cathode Microbial Fuel Cell

An electricity-generating bacterium, Geobacter sulfurreducens PCA, was inoculated into a single-chamber, air-cathode microbial fuel cell (MFC) in order to determine the maximum electron transfer rate from bacteria to the anode. To create anodic reaction-limiting conditions, where electron transfer from bacteria to the anode is the rate-limiting step, anodes with electrogenic biofilms were reduced in size and tests were conducted using anodes of six different sizes. The smallest anode (7 cm², or 1.5 times larger than the cathode) achieved an anodic reaction-limiting condition as a result of a limited mass of bacteria on the electrode. Under these conditions, the limiting current density reached a maximum of 1,530 mA/m², and power density reached a maximum of 461 mW/m². Per-biomass efficiency of the electron transfer rate was constant at 32 fmol cell⁻¹ day⁻¹ (178 μmol g of protein⁻¹ min⁻¹), a rate comparable to that with solid iron as the electron acceptor but lower than rates achieved with fumarate or soluble iron. In comparison, an enriched electricity-generating consortium reached 374 μmol g of protein⁻¹ min⁻¹ under the same conditions, suggesting that the consortium had a much greater capacity for electrode reduction. These results demonstrate that per-biomass electrode reduction rates (calculated by current density and biomass density on the anode) can be used to help make better comparisons of electrogenic activity in MFCs.     

A novel wireless glucose sensor employing direct electron transfer principle based enzyme fuel cell

In this paper we present a novel wireless glucose biosensing system employing direct electron transfer principle based enzyme fuel cell. Using the glucose dehydrogenase complex, which is composed of a catalytic subunit containing FAD, the cytochrome c subunit that harbors heme c as the electron transfer subunit, and chaperone-like subunit, a direct electron transfer-type glucose enzyme fuel cell was constructed. The enzyme glucose fuel cell generated electric power, and the open-circuit voltage showed glucose concentration dependence, which suggests potential applications for this glucose-sensing system. We constructed a miniaturized "all-in-one" glucose enzyme fuel cell, which represents a compartmentless fuel that is based on the direct electron transfer principle. This involved the combination of a wireless transmitter system and a simple and miniaturized continuous glucose monitoring system, which operated continuously for about 3 days with stable response. This is the first demonstration of an enzyme-based direct electron transfer-type enzyme fuel cell and fuel cell-type glucose sensor which can be utilized as a subcutaneously implantable system for continuous glucose monitoring.     

Power overshoot in two-chambered microbial fuel cell (MFC)

A two-chamber microbial fuel cell was started using iron-reducing strains as inoculum and acetate as carbon sources. The tested microbial fuel cell had an open-circuit voltage of 0.67 V, and reached 1045 mA m⁻² and a power density of 486 mW m⁻² at 0.46 V before power overshoot occurred. Anodic reactions were identified as the rate-determining steps. Stirring the anolyte insignificantly increased cell performance, suggesting a minimal external mass transfer resistance from the anolyte to the anodic biofilm. Data regression analysis indicates that charge transfer resistance at the biofilm-anode junction was negligible. The order of magnitude estimation of electrical conductance indicates that electron transfer resistance had an insignificant effect on microbial fuel cell performance. Resistance in electrogens for substrate utilization is proposed to induce microbial fuel cell power overshoot.     

Monitoring the Reductive and Oxidative Half-Reactions of a Flavin-Dependent Monooxygenase using Stopped-Flow Spectrophotometry

Aspergillus fumigatus siderophore A (SidA) is an FAD-containing monooxygenase that catalyzes the hydroxylation of ornithine in the biosynthesis of hydroxamate siderophores that are essential for virulence (e.g. ferricrocin or N'',N",N''''''-triacetylfusarinine C)¹. The reaction catalyzed by SidA can be divided into reductive and oxidative half-reactions (Scheme 1). In the reductive half-reaction, the oxidized FAD bound to Af SidA, is reduced by NADPH^2,3. In the oxidative half-reaction, the reduced cofactor reacts with molecular oxygen to form a C4a-hydroperoxyflavin intermediate, which transfers an oxygen atom to ornithine. Here, we describe a procedure to measure the rates and detect the different spectral forms of SidA using a stopped-flow instrument installed in an anaerobic glove box. In the stopped-flow instrument, small volumes of reactants are rapidly mixed, and after the flow is stopped by the stop syringe (Figure 1), the spectral changes of the solution placed in the observation cell are recorded over time. In the first part of the experiment, we show how we can use the stopped-flow instrument in single mode, where the anaerobic reduction of the flavin in Af SidA by NADPH is directly measured. We then use double mixing settings where Af SidA is first anaerobically reduced by NADPH for a designated period of time in an aging loop, and then reacted with molecular oxygen in the observation cell (Figure 1). In order to perform this experiment, anaerobic buffers are necessary because when only the reductive half-reaction is monitored, any oxygen in the solutions will react with the reduced flavin cofactor and form a C4a-hydroperoxyflavin intermediate that will ultimately decay back into the oxidized flavin. This would not allow the user to accurately measure rates of reduction since there would be complete turnover of the enzyme. When the oxidative half-reaction is being studied the enzyme must be reduced in the absence of oxygen so that just the steps between reduction and oxidation are observed. One of the buffers used in this experiment is oxygen saturated so that we can study the oxidative half-reaction at higher concentrations of oxygen. These are often the procedures carried out when studying either the reductive or oxidative half-reactions with flavin-containing monooxygenases. The time scale of the pre-steady-state experiments performed with the stopped-flow is milliseconds to seconds, which allow the determination of intrinsic rate constants and the detection and identification of intermediates in the reaction⁴. The procedures described here can be applied to other flavin-dependent monooxygenases.^5,6     

Electricity Generation in Microbial Fuel Cells Using Neutral Red as an Electronophore

Neutral red (NR) was utilized as an electron mediator in microbial fuel cells consuming glucose to study both its efficiency during electricity generation and its role in altering anaerobic growth and metabolism of Escherichia coli and Actinobacillus succinogenes. A study of chemical fuel cells in which NADH, NR, and ferricyanide were the electron donor, the electronophore, and the electron acceptor, respectively, showed that electrical current produced from NADH was proportional to the concentration of NADH. Fourfold more current was produced from NADH in chemical fuel cells when NR was the electron mediator than when thionin was the electron mediator. In microbial fuel cells in which E. coli resting cells were used the amount of current produced from glucose when NR was the electron mediator (3.5 mA) was 10-fold more than the amount produced when thionin was the electron mediator (0.4 mA). The amount of electrical energy generated (expressed in joules per mole of substrate) and the amount of current produced from glucose (expressed in milliamperes) in NR-mediated microbial fuel cells containing either E. coli or A. succinogenes were about 10- and 2-fold greater, respectively, when resting cells were used than when growing cells were used. Cell growth was inhibited substantially when these microbial fuel cells were making current, and more oxidized end products were formed under these conditions. When sewage sludge (i.e., a mixed culture of anaerobic bacteria) was used in the fuel cell, stable (for 120 h) and equivalent levels of current were obtained with glucose, as observed in the pure-culture experiments. These results suggest that NR is better than other electron mediators used in microbial fuel cells and that sludge production can be decreased while electricity is produced in fuel cells. Our results are discussed in relation to factors that may improve the relatively low electrical efficiencies (1.2 kJ/mol) obtained with microbial fuel cells.     

Evidence for an inducible glucose transport system in Kluyveromyces lactis

To find the cause of delayed glucose oxidation in succinate-grown Kluyveromyces lactis, glucose transport was studied in glucose- and in succinate-grown cells. The initial rate of 2-deoxyglucose (2-dGlc) accumulation, as well as the appearance of 2-deoxyglucose 6-phosphate, was higher in the glucose-grown cells. In both cell types, 2-dGlc was apparently transported in the free form to be phosphorylated intracellularly . In glucose-grown cells the level of free 2-dGlc in the pool was always less than the external concentration. Exchange transport in starved, poisoned cells loaded with unlabeled 2-dGlc was 140-fold greater in glucose- than in succinate-grown cells, probably because of the presence of an inducible transport component. The development of the increased rate of transport in a succinate-grown uracil-requiring auxotroph after transfer to glucose depends on the presence of uracil.     

Generation of electric potential difference across the electrodes of the microbial fuel cell in the anaerobic oxidation of substrates by microbial associations

Several microbial associations were obtained from natural and anthropogenic sources. All of the associations grow well on glucose and significantly worse on acetate. We observed 80–95% glucose consumption during 3–5 days of growth. The oxidation of substrates by the cultures generates an electric potential difference between anode and cathode electrodes of a microbial fuel cell (MFC). The value of the potential difference depends on the nature of the association and the substrate and reaches 400–500 mV. The potential difference generation accompanied by a shift to the negative region of the medium redox potential (E _h ) to — (400–500) mV. This indicates H₂ evolution by the association cultures during oxidation of carbohydrates. Artificial redox mediators, such as tetramethyl-p-phenylenediamine, phenazine methosulfate, and benzyl viologen, were able to increase up to 15% the difference in electrical potential across the electrodes of the MFC. It is assumed that an increase in the potential difference across the electrodes induced by the redox mediators is due to their direct involvement in the transfer of electrons from the bacteria in the incubation medium to the MFC anode electrode. The direct measurement of current and potential difference on the electrodes in a short-circuit mode shows that the internal resistance of the MFC is equal to 1 kΩ and the power reaches 5 μW. Undoubtedly, this testifies to the low efficiency developed by the MFE.     

Microbial fuel cell energy from an ocean cold seep

Benthic microbial fuel cells are devices that generate modest levels of electrical power in seafloor environments by a mechanism analogous to the coupled biogeochemical reactions that transfer electrons from organic carbon through redox intermediates to oxygen. Two benthic microbial fuel cells were deployed at a deep-ocean cold seep within Monterey Canyon, California, and were monitored for 125 days. Their anodes consisted of single graphite rods that were placed within microbial mat patches of the seep, while the cathodes consisted of carbon-fibre/titanium wire brushes attached to graphite plates suspended ∼0.5 m above the sediment. Power records demonstrated a maximal sustained power density of 34 mW·m⁻² of anode surface area, equating to 1100 mW m⁻² of seafloor. Molecular phylogenetic analyses of microbial biofilms that formed on the electrode surfaces revealed changes in microbial community composition along the anode as a function of sediment depth and surrounding geochemistry. Near the sediment surface (20–29 cm depth), the anodic biofilm was dominated by micro-organisms closely related to Desulfuromonas acetoxidans. At horizons 46–55 and 70–76 cm below the sediment–water interface, clone libraries showed more diverse populations, with increasing representation of δ-proteobacteria such as Desulfocapsa and Syntrophus, as well as ɛ-proteobacteria. Genes from phylotypes related to Pseudomonas dominated the cathode clone library. These results confound ascribing a single electron transport role performed by only a few members of the microbial community to explain energy harvesting from marine sediments. In addition, the microbial fuel cells exhibited slowly decreasing current attributable to a combination of anode passivation and sulfide mass transport limitation. Electron micrographs of fuel cell anodes and laboratory experiments confirmed that sulfide oxidation products can build up on anode surfaces and impede electron transfer. Thus, while cold seeps have the potential to provide more power than neighbouring ocean sediments, the limits of mass transport as well as the proclivity for passivation must be considered when developing new benthic microbial fuel cell designs to meet specific power requirements.     

Effect of vitamins and cell constructions on the activity of microbial fuel cell battery

Construction of efficient performance of microbial fuel cells (MFCs) requires certain practical considerations. In the single chamber microbial fuel cell, there is no border between the anode and the cathode, thus the diffusion of the dissolved oxygen has a contrary effect on the anodic respiration and this leads to the inhibition of the direct electron transfer from the biofilm to the anodic surface. Here, a fed-batch single chambered microbial fuel cells are constructed with different distances 3 and 6?cm (anode- cathode spacing), while keeping the working volume is constant. The performance of each MFC is individually evaluated under the effects of vitamins & minerals with acetate as a fed load. The maximum open circuit potential during testing the 3 and 6?cm microbial fuel cells is about 946 and 791?mV respectively. By decreasing the distance between the anode and the cathode from 6 to 3?cm, the power density is decreased from 108.3?mW?m^?2 to 24.5?mW?m^?2. Thus, the short distance in membrane-less MFC weakened the cathode and inhibited the anodic respiration which affects the overall performance of the MFC efficiency. The system is displayed a maximum potential of 564 and 791?mV in absence & presence of vitamins respectively. Eventually, the overall functions of the acetate single chamber microbial fuel cell can be improved by the addition of vitamins & minerals and increasing the distance between the cathode and the anode.     

Role of active site histidines in the two half-reactions of the aryl-alcohol oxidase catalytic cycle

The crystal structure of aryl-alcohol oxidase (AAO), a flavoenzyme involved in lignin degradation, reveals two active-site histidines, whose role in the two enzyme half-reactions was investigated. The redox state of flavin during turnover of the variants obtained show a stronger histidine involvement in the reductive than in the oxidative half-reaction. This was confirmed by the k(cat)/K(m(Al)) and reduction constants that are 2-3 orders of magnitude decreased for the His546 variants and up to 5 orders for the His502 variants, while the corresponding O(2) constants only decreased up to 1 order of magnitude. These results confirm His502 as the catalytic base in the AAO reductive half-reaction. The solvent kinetic isotope effect (KIE) revealed that hydroxyl proton abstraction is partially limiting the reaction, while the α-deuterated alcohol KIE showed a stereoselective hydride transfer. Concerning the oxidative half-reaction, directed mutagenesis and computational simulations indicate that only His502 is involved. Quantum mechanical/molecular mechanical (QM/MM) reveals an initial partial electron transfer from the reduced FADH(-) to O(2), without formation of a flavin-hydroperoxide intermediate. Reaction follows with a nearly barrierless His502H(+) proton transfer that decreases the triplet/singlet gap. Spin inversion and second electron transfer, concomitant with a slower proton transfer from flavin N5, yields H(2)O(2). No solvent KIE was found for O(2) reduction confirming that the His502 proton transfer does not limit the oxidative half-reaction. However, the small KIE on k(cat)/K(m(Ox)), during steady-state oxidation of α-deuterated alcohol, suggests that the second proton transfer from N5H is partially limiting, as predicted by the QM/MM simulations.     

The mechanism of end product inhibition of serine biosynthesis. V. Mechanism of serim inhibition of phosphoglycerate dehydrogenases.

The reduction of enzyme-bound DPN constitutes a half-reaction of phosphoglycerate dehydrogenase and has been investigated fluorometrically. Serine was found to inhibit the half-reaction to the same extent and with the same degree of cooperation as the steady state reaction. This finding identifies the ternary complex conversion as the point in the reaction sequence at which serine inhibition occurs. Delta H determinations for the half-reaction showed no difference whether serine was or was not present and led to the conclusion that the inhibitory effect of serine could only manifest itself through the delta S term in the expression for the formation of the activated transition state complex. DL-3-P[2-2H]glyceric acid showed no primary isotope effect in the half-reaction. This result excludes hydrogen transfer as the rate-limiting step in the half-reaction and confirms that an isomerization step, affected by serine, exists in the ternary complex conversion scheme. The deuterated 3-P-glyceric acid shows an isotope effect of 2 in the steady state reaction.     

Atomic level insight into the oxidative half-reaction of aromatic amine dehydrogenase

The quinoprotein aromatic amine dehydrogenase (AADH) uses a covalently bound tryptophan tryptophylquinone (TTQ) cofactor to oxidatively deaminate primary aromatic amines. Recent crystal structures have provided insight into the reductive half-reaction. In contrast, no atomic details are available for the oxidative half-reaction. The TTQ O7 hydroxyl group is protonated during reduction, but it is unclear how this proton can be removed during the oxidative half-reaction. Furthermore, compared with the electron transfer from the N-quinol form, electron transfer from the non-physiological O-quinol form to azurin is significantly slower. Here we report crystal structures of the O-quinol, N-quinol, and N-semiquinone forms of AADH. A comparison of oxidized and substrate reduced AADH species reveals changes in the TTQ-containing subunit, extending from residues in the immediate vicinity of the N-quinol to the putative azurin docking site, suggesting a mechanism whereby TTQ redox state influences interprotein electron transfer. In contrast, chemical reduction of the TTQ center has no significant effect on protein conformation. Furthermore, structural reorganization upon substrate reduction places a water molecule near TTQ O7 where it can act as proton acceptor. The structure of the N-semiquinone, however, is essentially similar to oxidized AADH. Surprisingly, in the presence of substrate a covalent N-semiquinone substrate adduct is observed. To our knowledge this is the first detailed insight into a complex, branching mechanism of quinone oxidation where significant structural reorganization upon reduction of the quinone center directly influences formation of the electron transfer complex and nature of the electron transfer process.