Team:Bielefeld-Germany/Modelling/Oxidation

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<h1>Modelling - Mediator Oxidation</h1>
<h1>Modelling - Mediator Oxidation</h1>
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<p><a href="https://2013.igem.org/Team:Bielefeld-Germany/Modelling/Optimal">Optimal<br> conditions</a></p></div>
<p><a href="https://2013.igem.org/Team:Bielefeld-Germany/Modelling/Optimal">Optimal<br> conditions</a></p></div>
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<p><a href="https://2013.igem.org/Team:Bielefeld-Germany/Modelling#Two_Reactions">Two<br> Reactions</a></p></div>
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<p><a href="https://2013.igem.org/Team:Bielefeld-Germany/Modelling/Two_Reactions">Two<br> Reactions</a></p></div>
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=='''Mediator Reduction'''==
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==Mediator Oxidation==
<p align="justify">
<p align="justify">
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In Microbial Fuel Cell microorganisms provide the electrons for the anode from the oxidation of the substrate(s) in the intracellular metabolic pathways.
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In a third electrochemical reaction the reduced mediator is regenerated at the electrode.This electrochemical oxidation at the anode surface occurs as shown in equation: <br><br>
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The transfer of the electrons to electrodes has been demonstrated for several species, though this process is inefficient as far as Coulombic yield and current generation are concerned [A].
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Hence, the application of the electrochemical mediators is essential for the construction of Microbial Fuel Cell.
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[[File:Bielefeld-germany-model-oxid-reaction-1.PNG|300px|center]]
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Mediators are usually small water-soluble molecules, which are capable of undergoing the redox transformations. The mediator acts as an electron shuttle, enhancing the kinetics of the electron transfer. This approach has been proven to be generally quite successful and many substances were tested for their potential as electron shuttle.<br>
 
<br>
<br>
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There are two classes of mediators, the endogenous and the exogenous mediator. The endogenous mediators are generated by the bacteria and can be secreted to the medium and then be reduced at the electrode. The exogenous mediators are the redox molecules that are chemically synthesized and must be added into the anode chamber of the Microbial Fuel Cell, in order to enable electron transfer from bacterial metabolic pathways to the anode. <br>
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 +
,where M<sub>red</sub> is the reduced mediator and <br>
 +
M<sub>ox</sub> the oxidized mediator.
<br>
<br>
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Therefore, the anodic performance dependents not only on the nature and the rate of the metabolism, but on the nature and the rate of electron transfer from the mediator to the anode as well.
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Then the current output can be calculated based on formula according to the Faraday's law:<br>
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Several exogenous mediators have been already studied in regard to their effect on electron transfer and so their impact on the electricity generation. Among those mediators are methylene blue (MB),  neutral red (NR), thionin, ferricyanide, humic acid or methyl viologen.
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In our model we modelled the influence of the three of the mediators: <br><br>
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* N-methyl phenazine (NMP)methosulfate,
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* 1-methoxy-5-methyl phenazine (MNMP) methosulfate and
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* Meldola Blue (MB )
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</p>
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<br><br><br><br>
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== '''Reaction Kinetics''' ==
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In contrast to the first bottle neck reaction of our model, which has been described as the Michaelis-Menten reaction, the redox reaction between the bacterial metabolites and the oxidized mediator can be considered as a first order reaction:
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[[File:Bielefeld-germany-model-oxid-reaction-2.PNG|250px|center]]
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[[File:Bielefeld-germany-model-reduction-1.PNG|300px|center]]
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<br><br>
 +
,where I is the current density [A]<br>
 +
[M<sub>red</sub>] is the concentration of reduced mediator in the chamber<br>
 +
''n'' is the number of electrons taking part in the electrode reaction,<br>
 +
F is the Faradays constant (96 500 C) and <br>
 +
k<sub>3</sub> is the reaction rate of the mediator oxidation at the anode.<br>
 +
</p>
 +
<br>
 +
==Simulation==
 +
<p align="justify">
 +
The value ''k<sub>3</sub>'' obtained as mentioned above was applied in the simulation of the current output in the final reaction of the three-reaction model. The start concentrations of the NAD<sup>+</sup> and oxidized mediator were set as in the simulations preformed for the proceeding reactions at 100 µM. The simulation time span was set for 60 sec.
 +
The resulting plot for the mediator '''MB''' is shown in the Figure 1, below:
 +
<br><br>
 +
[[File:Bielefeld-germany-model-oxid-diagramm-MB-01.png|600px|center|thumb|'''Figure 1''': Curves for the current output, fluxes of concentration of the intermediates. Simulation performed for the start concentration of both NAD<sup>+</sup> and oxidized mediator '''MB''' at 100 µM.]]
 +
<br><br>
 +
Further simulation has been performed for four different start concentrations of the oxidized mediator in order to investigate how varying start concentration influence the current output. The concentrations were set at 10 µM, 50 µM, 100 µM and 500 µM. The time span was set at 30 sec. The curves of the current outputs are presented in the Figure 2.
 +
<br><br>
 +
[[File:Bielefeld-germany-model-oxid-diagramm-MB-02.png|600px|center|thumb|'''Figure 2''': Curves for the current output and fluxes of concentration of the intermediates. Simulation performed for the varying start concentration of the oxidized mediator '''MB''' [M<sub>ox</sub>] .]]
 +
<br><br>
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The kinetic properties of the electrocatalytic oxidation of NADH and reduction of the soluble mediator, regarding rate constants were studied by cyclic voltammetry and chronoamperometry [B].
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The MATLAB source code for both simulations can be obtained [https://static.igem.org/mediawiki/2013/2/27/Bielefeld-germany-model-oxid-matlab-code-1.m here] and [https://static.igem.org/mediawiki/2013/3/36/Bielefeld-germany-model-oxid-matlab-code-2.m here].<br>
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The measured rates are shown in the table 1:
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+
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[[File:Bielefeld-germany-model-reduction-table1.PNG|500px|center]]
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+
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<!-- [[File:Bielefeld-germany-model-inter-reaction1.PNG|900px|center]] -->
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 +
Analogous simulations have been performed for the mediator '''NMP'''. As the reaction rate ''k<sub>3</sub>'' specific for this mediator could not be obtained, the value specific for the mediator '''MB''' was applied. The diagrams presenting the results of those simulations are shown in the Figure 3 and 4 respectively.
 +
<br><br>
 +
[[File:Bielefeld-germany-model-oxid-diagramm-NMP-03.png|600px|center|thumb|'''Figure 3''': Curves for the current output, fluxes of concentration of the intermediates. Simulation performed for the start concentration of both NAD<sup>+</sup> and oxidized mediator '''NMP''' at 100 µM.]]
 +
<br><br>
 +
[[File:Bielefeld-germany-model-oxid-diagramm-NMP-04.png|600px|center|thumb|'''Figure 4''': Curves for the current output and fluxes of concentration of the intermediates. Simulation performed for the varying start concentration of the oxidized mediator '''NMP''' [M<sub>ox</sub>] .]]
 +
<br>
 +
The according .m files with MATLAB source code can be downloaded from [https://static.igem.org/mediawiki/2013/b/be/Bielefeld-germany-model-oxid-matlab-code-3.m here] and [https://static.igem.org/mediawiki/2013/9/90/Bielefeld-germany-model-oxid-matlab-code-4.m here].
 +
</p>
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==Discussion==
 +
<p align="justify">
 +
The curve for the current output simulated for the mediator '''MB''' has been presented in the Figure 1. It could be shown that the maximal output is reached rapidly after the start of the reaction system. Immediately after reaching the maximum, it decreases equally fast. At the 20 second mark it reaches a stable phase of about 20 per cent of the maximal current output.<br>
 +
The comparison of different start concentrations of the oxidized mediator can be obtained from the Figure 2. The curve form is identical for all four concentrations and the reached current values differ only slightly for the different simulations. Also the maximum output is almost identical and is reached at the same time for all four approaches.
 +
Interestingly the curves obtained from the simulation for the mediator '''NMP''' are very similar to those for the mediator '''MB'''. This points that the reaction rate ''k<sub>3</sub>''  for the oxidation of the mediator at the anode plays a predominant role in generating current.<br>
 +
Obviously it is necessary to constantly provide the system with the redox molecules in order to sustain the current at the high level.This builds a strong case for the usse of endogenous mediators that are supplied and regenerated by the bacteria themselves.
 +
Another interesting aspect emerges when comparing the modeled current output curves and those obtained with the values measured in MFC. The measurements were performed in a self-designed MFC where only M9 medium and no bacteria was present in the anode chamber.The resulting curve has been shown in the figure 5. The mediator was added to the anode chamber only once at the beginning of the measurements.
 +
<br><br>
 +
[[File:Bielefeld-germany-model-oxid-discus-01.jpg|450px|center|thumb|'''Figure 5''': .]]
 +
<br>
 +
The resulting curve form is very similar to the curves observed in the models. There are though significant differences in the dimensions of both current/voltage and time span in which the reactions take place.
 +
Those differences might result from the fact that in our model we did not take the resistance into consideration.
 +
</p>
==References==
==References==
-
 
<br><br><br><br>
<br><br><br><br>
</div>
</div>
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Latest revision as of 03:57, 29 October 2013


Modelling - Mediator Oxidation

Mediator Oxidation

In a third electrochemical reaction the reduced mediator is regenerated at the electrode.This electrochemical oxidation at the anode surface occurs as shown in equation:

Bielefeld-germany-model-oxid-reaction-1.PNG


,where Mred is the reduced mediator and
Mox the oxidized mediator.
Then the current output can be calculated based on formula according to the Faraday's law:

Bielefeld-germany-model-oxid-reaction-2.PNG



,where I is the current density [A]
[Mred] is the concentration of reduced mediator in the chamber
n is the number of electrons taking part in the electrode reaction,
F is the Faradays constant (96 500 C) and
k3 is the reaction rate of the mediator oxidation at the anode.


Simulation

The value k3 obtained as mentioned above was applied in the simulation of the current output in the final reaction of the three-reaction model. The start concentrations of the NAD+ and oxidized mediator were set as in the simulations preformed for the proceeding reactions at 100 µM. The simulation time span was set for 60 sec. The resulting plot for the mediator MB is shown in the Figure 1, below:

Figure 1: Curves for the current output, fluxes of concentration of the intermediates. Simulation performed for the start concentration of both NAD+ and oxidized mediator MB at 100 µM.



Further simulation has been performed for four different start concentrations of the oxidized mediator in order to investigate how varying start concentration influence the current output. The concentrations were set at 10 µM, 50 µM, 100 µM and 500 µM. The time span was set at 30 sec. The curves of the current outputs are presented in the Figure 2.

Figure 2: Curves for the current output and fluxes of concentration of the intermediates. Simulation performed for the varying start concentration of the oxidized mediator MB [Mox] .



The MATLAB source code for both simulations can be obtained here and here.


Analogous simulations have been performed for the mediator NMP. As the reaction rate k3 specific for this mediator could not be obtained, the value specific for the mediator MB was applied. The diagrams presenting the results of those simulations are shown in the Figure 3 and 4 respectively.

Figure 3: Curves for the current output, fluxes of concentration of the intermediates. Simulation performed for the start concentration of both NAD+ and oxidized mediator NMP at 100 µM.



Figure 4: Curves for the current output and fluxes of concentration of the intermediates. Simulation performed for the varying start concentration of the oxidized mediator NMP [Mox] .


The according .m files with MATLAB source code can be downloaded from here and here.

Discussion

The curve for the current output simulated for the mediator MB has been presented in the Figure 1. It could be shown that the maximal output is reached rapidly after the start of the reaction system. Immediately after reaching the maximum, it decreases equally fast. At the 20 second mark it reaches a stable phase of about 20 per cent of the maximal current output.
The comparison of different start concentrations of the oxidized mediator can be obtained from the Figure 2. The curve form is identical for all four concentrations and the reached current values differ only slightly for the different simulations. Also the maximum output is almost identical and is reached at the same time for all four approaches. Interestingly the curves obtained from the simulation for the mediator NMP are very similar to those for the mediator MB. This points that the reaction rate k3 for the oxidation of the mediator at the anode plays a predominant role in generating current.
Obviously it is necessary to constantly provide the system with the redox molecules in order to sustain the current at the high level.This builds a strong case for the usse of endogenous mediators that are supplied and regenerated by the bacteria themselves. Another interesting aspect emerges when comparing the modeled current output curves and those obtained with the values measured in MFC. The measurements were performed in a self-designed MFC where only M9 medium and no bacteria was present in the anode chamber.The resulting curve has been shown in the figure 5. The mediator was added to the anode chamber only once at the beginning of the measurements.

Figure 5: .


The resulting curve form is very similar to the curves observed in the models. There are though significant differences in the dimensions of both current/voltage and time span in which the reactions take place. Those differences might result from the fact that in our model we did not take the resistance into consideration.

References







Contents