Microbial Fuel Cell

Overview

Figure 1: Schematic illustration of the general microbial fuel cell functional principle, showing the flow of charged species during operation.

A microbial fuel cell (MFC) can be utilized for power generation through the conversion of organic and inorganic substrates using microorganisms. The fuel cell generally consists of two separate units, the anode and cathode compartment, which are separated by a proton exchange membrane (PEM). Microorganisms, acting as biocatalysts, release electrons during metabolic reactions and transfer them to the anode of the fuel cell. The protons being freed up during this process are transferred to the cathode compartment through the PEM. The electrons pass through an external load circuit to the cathode, where they reduce an electron acceptor. Thus, an electric current is generated. The most important property of such a system is the bacteria's ability to transfer electrons to the anode. There are lots of other aspects to consider though, all of which are vital for the successful operation of a fuel cell.
Most existing projects rely on using mixed cultures of different bacteria in the anode compartment. However, in most cases these systems are not very well characterized. Often it is not even known which species are part of these cultures. This makes it almost impossible to improve the system by directed genetic engineering. Applying such a black box system outside of a laboratory might also pose safety risks, since it may contain pathogenic cultures. Another disadvantage is, that some of the species might be quite sensitive to different kinds of stress, like Geobacter sulfurreducens, which is very susceptible to oxidative stress.
For these reasons, Bielefelds 2013 iGEM Team decided to develop a system which only relies on Escherichia coli for power generation. The main benefit being that these bacteria grow fast and are quite robust regarding cultivation conditions. Another advantage over a mixed culture is that the potential risks of using such a single-strain culture are much more easily assessed and can be reduced by systematic manipulation of the bacterial genome.

Theory

General design

Figure 2: Schematical illustration of a possible fuel cell design.

The basic design of a microbial fuel cell is mainly influenced by the shape of the electrode chambers. A very simple design is called the “H” shape, which usually consists of two bottles or other vessels, connected by a tube containing material suitable for proton exchange. Further investigations underlined usefulness of such systems for testing of materials or parameters, but the power gain is rather low. This is most likely the case because of the slow proton exchange through the tubes and because of a high internal resistance (Oh et al., 2004; Oh and Logan, 2006).

There are many other possible shapes, like a cylindrical reactor with a concentric inner tube that acts as the cathode to enable a continuous flow. One specific design, proposed by H. P. Bennetto (Bennetto, 1990), is often used for research purposes. The system consists of plastic elements in form of two solid plates and two frames, as shown in Figure 2. The frames are placed between the plates and form two reaction compartments, separated by a cation exchange membrane. Furthermore, every compartment is equipped with electrodes to enable a flow of electrons. To ensure the system is air-tight, rubber gaskets are fitted between the plastic parts. The endplates are held together by four threaded rods.

• Requirements:
  • formation of a closed system
  • possibility for axenic cultivation
  • possibility for anaerobic conditions
  • large internal surface

Anode

Materials have to be highly conductive, biocompatible and chemically stable under the conditions present inside the fuel cell in order to be used as an anode. Many traditional materials like copper are not suitable, because they corrode or have a toxic effect on the bacteria. Platinum works excellent, but is extremely expensive. Several carbon-based materials provide a cheap but practical alternative. Regardless of the type of material, the electrodes surface area is a very important factor for current production. Previous investigations showed that current increases with the overall internal surface in the following order: carbon felt > carbon foam > graphite (Chaudhuri and Lovley, 2003).

• Requirements:
  • high conductivity
  • good biocompatibility
  • long-term physical and chemical stability

Cathode

Because of its low overpotential in combination with carbon electrodes and the resulting working potential, which is close to its open circuit potential, potassium ferricyanide (K₃)[Fe(CN) ₆]) is the most frequently used electron acceptor in microbial fuel cells in research scenarios (Logan et al., 2006). However, one has to consider that the reoxidation by oxygen is very low and the diffusion through the PEM is not negligible, so the oxidation of this substance can affect the performance of the MFC when operated for long periods of time (Rabaey et al., 2005). Alternatively, oxygen can be used as a very effective electron acceptor in combination with an open-air electrode. For an effective oxygen reduction, however, high-cost platinum catalysts are necessary. For this reason, this option is rarely used (Sell et al., 1989).

• Requirements:
  • good reduction performance
  • good reoxidation
  • high long term stability

Compartment separation

Although almost all microbial fuel cells use proton exchange membranes as the separation element between anode and cathode compartment, it is possible to use more simple constructions like salt or agarose bridges. These basic separation systems, however, do not reach the power output of membrane based systems because of their high internal resistance. Cation exchange membranes offer defined properties and ensure a better current output because of their high selectivity for the passage of positive charged ions. However, in this context it has to be considered that the PEM could be permeable to chemicals and oxygen, which might influence the long term performance of the fuel cell (Logan et al.,2006).

• Requirements:
  • high selectivity for positive ions
  • impermeability for chemicals and oxygen

Cultivation conditions

In general, microorganisms utilize three different methods to release electrons produced during the metabolic oxidation of high-energy organic or inorganic substrates. Because the reduction of oxygen, also called aerobic respiration, is the most efficient method for many bacteria, including Escherichia coli, these metabolic pathways are preferred when oxygen is available. In a microbial fuel cell, however, an aerobic metabolism is not desirable, since the electrons are directly transferred to oxygen and thereby cannot be used to produce current. Thus, anaerobic cultivation conditions are necessary.
Without oxygen, bacteria can generate energy through different forms of fermentation and anaerobic respiration. During fermentation and anaerobic respiration, electrons are directly transferred to soluble electron acceptors. In case of Escherichia coli, mixed acid fermentation under formation of metabolic end products like lactate, acetate and ethanol has to be avoided by the choice of suitable cultivation parameters. Their formation and accumulation would effect a comparatively limited electron production and hamper bacterial survival.
Based on these considerations, anaerobic respiration is left as the only suitable option for current generation in a fuel cell, when using the electrode as the terminal electron acceptor. For this reason, construction of the fuel cell, cultivation parameters as well as genetic modifications of Escherichia coli are aimed at enabling anaerobic respiration.

Measurement system and protocol

The setup described here is intended for acquisition of comparable data regarding the power output gained with different bacteria strains while using mediators for the electron transfer.
When operating a microbial fuel cell, numerous different factors influence the power output that can be measured. Number and growth phase of the bacteria in the anode chamber are among the most important. The reaction taking place in the cathode is just as critical, since a bad setup can lead to the speed of the anode reaction significantly declining over time or not taking place at all. The properties of the proton exchange membrane and the electrodes are also quite important for the speed of the reaction.
Choosing an appropriate resistance is also vital. If the resistance is too high, reduced mediator species accumulate at the anode and the voltage measured does not provide information about how fast the bacteria are able to reduce the mediator. Other factors come into play as well: The diffusion speed of the mediator, diffusion of cations through the membrane, agitation of the solution and the buildup of a biofilm at the anode have an influence at the power output of the fuel cell. When choosing a multimeter to measure the data, the internal resistance of the device, generating a so called burden voltage has to be kept in mind.
A standard measurement set up was established to generate data with fuel cell experiments. The experiments were carried out in the third generation fuel cell if not specified otherwise. A Nafion N117 proton exchange membrane manufactured by DuPont (for further information [http://www2.dupont.com/FuelCells/en_US/assets/downloads/dfc101.pdf see here]) was used to separate the anode and the cathode chamber. The surface area is 25 cm² in each chamber. The 50 x 50 mm carbon cloth electrodes, including two circular recesses are placed in the middle of each chamber. The cross-sectional area of each electrode is approximately 24.215 cm². The exact surface area of the electrodes is unknown, since the carbon cloth is composed of extremely thin filaments and has a rough surface. However, it is assumed that the surface area is roughly the same for each electrode used, since the material is identical. The cathode chamber was filled with 29 mL of a 20 mM solution of potassium ferricyanide in M9 medium. Bacteria were grown aerobically in shaker flasks in M9 minimal medium with 10.223 g L^-1 glycerol as a carbon source. When cultivating bacteria carrying a plasmid with an inducible promoter, induction was carried out 2 hours after inoculation. The optical density of the culture was periodically measured until it reached 1. At this point, 29 mL of the medium containing the bacteria were injected into the anode chamber of the fuel cell. When using an exogenous mediator 1 mL of a 10mM mediator solution in M9 medium was injected after 15 minutes.

Figure 3: Arrangement used for MFC-characterization containing a voltmeter and an adjustable resistance parallel-connected.

A 200 Ω resistor was wired between the anode and the cathode chamber. To measure the voltage across the resistor, a UT 803 multimeter by UNI-T was used. The according electrical schematic is presented in Figure 3. To generate polarization and power curves, the resistance was changed from 10 Ω to 10 kΩ in a cascade of 6 different values, using a self-constructed resistor box, shown in Figure pink camouflage desert mole rat. The voltage measured for every resistance was registered after 10 minutes to enable the system to reach a constant value.

MFC Evolution

The Film Canister Cell

Our first model was constructed out of film canisters and was designed to gain a better understanding of the general concept of galvanic cells and microbial fuel cells. It was used with different chemicals, yeast and the E. coli KRX strain. It also allowed to gather experience with the equipment used for measurement. The anode and cathode chambers are film canisters. Both are connected by a segment of a 15 mL centrifugation tube with a total length of two centimeters. The individual parts are held together by hot-melt glue. The centrifugation tube is filled with 3 % agarose, which acts as a salt bridge to allow protons to pass from anode to cathode chamber. In both chambers, pieces of carbon tissue (see Figure 4) act as the electrode.

Figure 4: Carbon tissue material. It shows a more flexible characteristic and seems noticeably more tearproof in comparison to carbon cloth.

Figure 5: Carbon cloth material. It shows a higher conductivity, but can be easily ruptured and therefore is difficult to mount inside the fuel cell chambers.

The biggest problem of this design is the salt bridge connecting both chambers. After being submerged in liquid for a while, it tends to become loose and glide out of the centrifugation tube. Furthermore, the construction does not allow for anaerobic operating of the fuel cell.

• Dimensions per Chamber:
  • height: 50 mm
  • diameter: 32 mm
  • volume: 40.2 mL
    
    

Figure 6: The Film Canister Cell.

Figure 7: Exploded view of the Film Canister Cell.

The Film Canister Stack

Connecting single batteries in series can be used to increase the output voltage. Likewise, the film canister stack consists of five film canister cells connected with copper wires in series. Because of the higher voltage generated, it was possible to operate a single low power light-emitting diode, using a high concentrated baker's yeast suspension and the exogenous mediator methylene blue in the anode chamber.

Figure 8: The Film Canister Stack made up of five cathode and anode canisters respectively. The canisters are wired in parallel.

The Second Generation Fuel Cell

This cell was designed with anaerobic operation in mind. The plastic parts needed were ordered from the workshop of the Faculty of Biology at Bielefeld University. The overall design is inspired by the fuel cell proposed by Benetto (Bennetto, 1990). Two frames make up the anode and cathode chamber. They are enclosed by two flat plates, each containing four bores. Threaded rods are put through the bores. The construction is held together by these rods, which have tightly fastened nuts on their ends.
All plastic parts are separated by thin rubber gaskets. A Nafion N117 membrane is placed between the two frames to allow cations to travel between the chambers. The two electrodes were initially cut out of the same carbon tissue as the ones used in the film canister cells. The rims were sown together with extra durable yarn to prevent the material from frazzling. These electrodes were held in place by two plastic parts plugged in each chamber. The copper wire connecting the electrode runs through two holes on the top of each plastic frame.
Initial testing revealed that the carbon cloth electrodes did not seem to be as conductive as expected. For this reason, they were replaced with electrodes made from another kind of carbon material, which were obtained from University of Readings [http://www.ncbe.reading.ac.uk/ National Centre for Biotechnology Education ]. However, the material is not very strong and easily ruptures, especially when wet. This made it difficult to connect the copper wires and to hold the electrodes in place within the chambers. The design also lacked means to drive out the oxygen from medium with nitrogen, an important prerequisite to establish anaerobic conditions within the fuel cell.

• Dimensions per chamber:
  • height: 40 mm
  • width: 40 mm
  • depth: 14 mm
  • volume 22,4 mL
    

Figure 9: The Second Generation Fuel Cell. The model consists of four plastic parts, two of which bearing the electrodes and jamming the proton exchange membrane between them. The remaining two parts are used to tighten the construct with nuts and threaded rods.

The Third Generation Fuel Cell

The fuel cell consists of six plastic parts. The overall design is similar to 2^nd generation cell, but the frames are split up into two parts each. This allows for the carbon electrodes to be mounted between two frames, as was already the case for the membrane before. This ensures the fragile carbon cloth is fixed in the center of each chamber and can be tapped by squeezing a wire between the gaskets. Since the material is highly porous, bacteria and medium can diffuse through the electrode and travel between both halves of a single chamber.
The second important change from the previous design is the introduction of four tube connectors on each frame. This allows aeration of the anode chamber with nitrogen gas and, e.g., introducing fresh medium in the system. The copper wire connecting the electrodes is replaced with platinum, because of the rapid copper-oxidation, resulting in a decreased conductivity.

• Dimensions per chamber:
  • height: 50 mm
  • width: 50 mm
  • depth: 12 mm
  • volume: 30 mL

Figure 11: The Third Generation Fuel Cell. This advanced design allows nitrogen aeration and the easy refill of the cell through the newly introduced tube connectors. The anode and cathode compartments were furthermore split into two plastic parts each, jamming the electrodes inbetween to prevent their rupture.

The Fuel Cell Generation three ^plus

This modified model of the 3^rd generation fuel cell was designed and constructed to enable the use of an [http://www.meinsberger-elektroden.de/labor/bezug.html#se10 Ag/AgCl reference electrode]. The power output was also increased, as well as the ability to maintain it for a long time. To fit the reference electrode inside the chambers, the outer frames of both chambers are thicker, 10 mm acrylic glass plates. In addition to tube connectors of the third generation fuel cell 5 mm fittings for the [http://www.meinsberger-elektroden.de/labor/bezug.html#se10 reference electrode SE11] were added. Beside these technical changes the aeration with nitrogen was increased in comparison to previous experiments. This was to compensate the increased distance between the bacteria and the anode. Since the new chambers were thicker, mediator diffusion would otherwise have become even more of an issue.

• Dimensions per chamber:
  • height: 50 mm
  • width: 50 mm
  • depth: 18 mm
  • volume: 45 mL

The iGEM York Cell

Since the iGEM Team York_UK is also doing work related to microbial fuel cells this year, we offered to send them one of our fuel cells to conduct their experiments in. Our design did not fully meet their requirements, especially since it was too large. After consulting with two of their team members, we constructed a small fuel cell based on the 3^rd generation design and sent it to York.

Figure 13: The Fuel Cell designed for the iGEM Team York.

The Stack

In order to increase the power output of the fuel cell, a fuel cell stack was built based on the third generation design. It consists of alternating anode and cathode chambers, five of each, placed between two cover plates. Using copper wiring, the five chamber-pairs are connected in series. Physically, they are separated by 1 mm thick stainless steel tiles, which act as bipolar plates.

Figure 14: The Fuel Cell Stack.

3D printing

To make the microbial fuel cell accessible to everyone, an additional model was developed which can be produced using a 3D printer. 3D printers are becoming more and more common and if none is available, the model can be ordered online from a 3D printing shop.
For our 3D printed microbial fuel cell it was important to apply material that does not inhibit microbial growth. To make sure this is the case, E. coli KRX was cultivated in the presence of two different kinds of plastic commonly used for 3D printing. These materials were acrylonitrile butadiene styrene (ABS) and polylactic acid (PLA), which are both thermoplastics that become moldable when heated and return to solid once the temperature drops.
A proper material for gaskets is essential as well, so different kinds of polysiloxane were tested in the same way. The rubber gaskets used in second and third generation MFC designs were also probed.

• Acrylonitrile butadiene styrene
  
  

Figure: NACHTBLAUER WEIßKOPFSEEADLER Lewis structure of the three mayor compounds of acrylonitrile butadiene styrene(ABS). The material is an amorphous termoplastic and consists of polymerized styrene and acrylonitrile in the presence of polybutadiene. Typically, a long chain of polybutadiene with cross-linked shorter chains of poly(styrene-co-acrylonitrile) is formed.

• ABS as a polymer can take many forms and can be engineered to have many properties. In general, it is a strong plastic with mild flexibility (compared to PLA).

• It's strength, shapeability and higher temperature resistance make it often a preferred plastic by engineers and those with mechanical uses in mind.
  
  
• ABS can be smelted down and recycled very easily provided it is available in suitable purity. Sorting methods do exist to separate ABS from mixed wastes with high efficiency.

• Polylactic acid
  
  

Figure CAMOUFLAGE CHAMÄLEON: Lewis structure of polylactic acid.

• Created from processing any number of plant products including corn, potatoes or sugar-beets, PLA is considered a more 'environmental friendly' plastic compared to petroleum based ABS.
  
  
• When properly cooled, PLA seems to have higher maximum printing speeds, lower layer heights, and sharper printed corners.
  
  
• PLA is biodegradable, having a typical lifetime of about 6 months to 2 years until microorganisms break it down into water and carbon dioxide.

To assess the issue of possible growth retardation, we cultivated E. coli with each material and compared the measured growth curves to a control cultivation without addition of plastics.

Figure BRONZE NARWAL: Testing of ABS and PLA plastics for biocompatibility. Both plastics were added to E. coli cultivations and growth was monitored. The resulting growth curves were compared to wild type curves to determine a possible alteration in growth behaviour.

The results shown in in figure LILA PAVIAN and figure UMBRA SEEPFERDCHEN demonstrate, that both ABS and PLA are biocompatible. Also, all brands of polysiloxane except B1 and the rubber are suitable as gasket material.

Figure LILA PAVIAN: Results of E. coli KRX cultivation in the presence of different kinds of plastic.

Figure UMBRA SEEPFERDCHEN: Results of E. coli KRX cultivation in the presence of different kinds of polysiloxane and rubber.

Models

Figure 17: A print of one of the earlier models.

Figure 18: An early model that was designed but never actually printed.

3D models were programmed with the software [http://www.openscad.org/ openSCAD], exported as .stl-files and translated into G-Code using [http://slic3r.org/ Slic3r].
Initially, slicing and printing took place at the local [http://hackerspace-bielefeld.de/ hackerspace] with counseling by experienced members of the groups. The printer, a [http://printrbot.com/ Printrbot Plus v2] was made available by the hackerspace community as well. After a total of roughly 34 hours of work, a first model was successfully printed from ABS. Like the models described in the MFC-Evolution paragraph, the design was changed several times. Some of the results can be seen in Figure 17. In early August, Bielefeld Universities Faculty of Physics offered their help. They printed out all subsequent designs with their [http://www.reprappro.com/products/mono-mendel/ RepRapPro Mono-Mendel] using PLA plastic and also executed the slicing process.

Figure 19: The final model for the 3D-print printed using PLA plastic.

The final model, illustrated in Figure 19, was finished in September. It features a 4-part design like the second generation model described in the MFC-Evolution section and has tube connectors for aeration of each individual chamber. Polysiloxane is used instead of rubber gaskets, the membrane and electrodes are fixed between the four frames of the reaction chambers. The end plates are held together by M3 threaded rods with M3 nuts. The materials necessary for building this fuel cells chassis cost less than 4€ and the cell is biodegradable. The .stl-file is available for download here.

Media and carbon sources

As explained previously, E. coli has to respire under anaerobic conditions in order for the microbial fuel cell to work. This might be a problem when using media such as LB, because in the absence of oxygen the bacteria might use the available carbon source for fermentation. To prevent this the different strains, which were tested in the fuel cell were cultivated in M9 minimal medium. After consulting Dr. Falk Harnisch concerning the fermentation problem, we decided to supplement the M9 medium with different carbon sources to test how this affects bacterial growth under anaerobic conditions. The goal of this experiment was to find a carbon source which is well suited for anaerobic respiration, but cannot be used for fermentation by the bacteria.

Tests were carried out with glucose, glycerol and acetate. The amount of substrate supplemented into the medium was adjusted, so that the amount of carbon atoms was the same for each culture. The concentrations were 5.0 g/L for glucose, 5.1 g/L for glycerol and 6.8 g/L for acetate. In all cultivation experiments, two biological replica of every strain and substrate combination were prepared and each sample was diluted and measured twice. Anaerobic cultivations were conducted in 30 mL test tubes with rubber lids. Samples were taken by piercing the lid with a syringe. For aerobic cultivations shaker flasks were used. The strains tested were the KRX wild type and the KRX carrying oprF under control of the T7 promoter ([http://parts.igem.org/wiki/index.php?title=Part:BBa_K1172502 BBa_K1172502]) strain. The latter overexpresses large porin proteins when induced with rhamnose. Induction was carried out with 4,2 mL/L of a 240 g/L rhamnose solution 1 hour after inoculation. All cultures were inoculated with an optical density of 0.22. Temperature was kept at 37°C during cultivation.

Figure 20: Growth of E. coli KRX and E. coli KRX BBa_K1172503 strains on media supplemented with different carbon sources under anaerobic conditions.

Figure 20 shows that under anaerobic conditions both strains grow well on glucose but seem to be unable to use acetate or glycerol efficiently.

Figure 21: Growth of E. coli KRX and E. coli KRX BBa_K1172503 strains on media supplemented with different carbon sources under aerobic conditions after 26 hours.

To ascertain whether glucose, glycerol or acetate are suitable substrates under aerobic conditions, eight additional cultures were inoculated with both strains. For these cultures only an end-point determination was carried out. The results can be seen in Figure 21. They indicate that acetate is, as expected, not a suitable substrate. Growth is best with glucose as a substrate, but glycerol yields satisfactory results as well.
The data acquired points to glycerol being the most suitable substrate, since the bacteria seem to have difficulties using it for fermentation but show satisfactory growth under conditions allowing for aerobic respiration. To make sure glycerol can also be used for respiration with terminal electron acceptors other than oxygen, bacteria were cultivated under anaerobic conditions in M9 medium containing glycerol as a carbon source and potassium nitrate as a soluble electron acceptor.

Figure 23: Growth of E. coli KRX and E. coli KRX BBa_K1172503 strains on media supplemented with glycerol under aerobic condition. Graphs marked KNO3 were supplemented with potassium nitrate.

The results of this experiment are shown in Figure 23. Cultures which were supplemented with KNO₃ grow significantly faster than those without, indicating that potassium nitrate is indeed used as a terminal electron acceptor for anaerobic respiration.

Based on these results, M9 medium with 5.1 g of glycerol per liter is used for all future experiments with the fuel cell.

Exogenous Mediators

Redox molecules which are chemically synthesized can be added into the anode chamber of the fuel cell to act as mediators, transporting electrons from the bacteria to the fuel cells anode. Here, these chemicals are referred to as exogenous mediators.

To identify exogenous mediators which can easily be reduced by E. coli, a simple experiment was conducted. A culture of E. coli KRX was split into 1.5 mL reaction tubes. Methylene blue and neutral red were added in varying concentrations. Since all mediators tested lose their color when reduced, a change in the color of the solution indicates that the bacteria are able to reduce the respective compound. Incubation took place at 24°C for 24 hours.

Figure 24: Reaction tubes with bacteria and different concentrations of methylene blue and neutral red after 24 hours of incubation.

In Figure 24 it can be seen that the samples containing methylene blue show a reduction of color intensity after incubation. Oxygen is able to reoxidize leucomethylene blue to the molecules blue form, so a blue color near the liquids surface is to be expected. Based on these results, methylene blue was chosen as the preferred exogenous mediator for further experiments.

Figure 25: Lewis structures of the cationic form of methylene blue (right side) and the reduced form, called leucomethylene blue (left side).

When methylene blue salts are dissolved in water, they dissociate into anions and methylene blue cations (see Figure 25). The conjugated electron systems of the molecule causes methylene blue solutions to appear in a dark blue color.
The compound can be reduced, accepting an electron and a proton in the process (see Figure 25). This interrupts the conjugated electron system, which is why leucomethylene blue is colorless. The [http://employees.csbsju.edu/hjakubowski/classes/ch331/oxphos/standredpotentialtab.htm standard potential] of the methylene blue/ leucomethylene blue reaction is +0.01 V.

Results

One possibility for the analysis and characterization of microbial fuel cells are polarization and power curves. By using different microorganisms, while keeping all other conditions the same, this measurement method allows a direct comparison of the electrical power provided.
To record a polarization curve for the whole fuel cell the electrical circuit described in Figure 3 was used with a variable resistor box and a second multimeter for current measurement. The self-constructed box, shown in Figure pink-camouflage desert mole rat contains 6 different potentiometers, which are each connected with a switch for easy and fast shifting between the different resistance values. Beginning with the lowest one, a periodic increase of the resistance from 10 Ω to 10 kΩ is performed. Like presented in Figure 26, the system expectedly reacts with an increase of voltage and, after a few minutes, reaches a constant value, which is used for further investigations. When looking at the recorded voltage values in Figure 26 it is obvious, that a mediator, in this case methylene blue, in combination with the biocatalyst E. coli is essential for electron transport. In contrast to the voltage values reached with this setup even for low resistances, both E. coli KRX solution without mediator and cell free M9 medium with mediator show much lower values.

Figure 26: Microbial fuel cell results from cultivation of E. coli KRX with and without redox-mediator and a negative control without bacteria. The resistance used was periodically increased from 10 Ω to 10 kΩ.

The polarization curve presented in Figure 27 confirms this fact. Plotting the measured voltage values as a function of the according current shows the characteristic correlation between voltage and current, depending on the used resistance.

Figure 27: Polarization curve, calculated based on the measurement values presented in Figure 26.

By calculating the appropriate electrical power values and plotting them in the form of a power curve as a function of the current (Figure 28), the differences becomes even more visible. While the cultivation of E. coli and the test with only M9 Medium show no significant differences, the cultivation containing 345 µmol L^-1 methylene blue achieves a significantly higher wattage, but still does not nearly reach the level of bacteria and mediators in combination. It should also be noted that in comparison to the power-values shown in the following text, the results presented in Figure 26 to 28 are significantly lower, because of a deviant measure arrangement. During this investigation it became apparent, that the used A UT 803 multimeter, connected in series for current-measurement, had an internal resistance of about 550 Ω which was not specified in the manual. For that reason, there was a significant voltage drop over the multimeter which distorted all data collected. Based on this fact the measure arrangement was changed to the circuit presented in Figure 3 for all future experiments and the current was calculated using Ohms law.
All in all, the calculation of polarization and power curves by changing the load of the system using different resistors shows the importance of a suitable electron transfer system. A comparison of the different fuel cell generations was not possible, because the experimental setup was optimized over the course of the project.

Figure 28: Power curve, calculated based on the data presented in Figure 26.

Besides the calculation of power curves the temporal process of power output is a very important parameter evaluating the overall performance of a microbial fuel cell, too. Exemplary, Figure 29 illustrates the electrical power as a function of time for the wild type E. coli KRX and a genetically modified strain of E. coli KRX containing the BioBrick (<bbpart>BBa_K1172502</bbpart>) with the oprF gene under control of the T7 promoter.

Figure 29: Results from cultivation of Escherichia coli KRX expressing OprF (<bbpart>BBa_K1172502</bbpart>) in contrast to Escherichia coli KRX wild type in the fuel cell. M9 medium, including 10,2 g L^-1 was used with mediator methylene blue, the resistor between cells was set to 200 Ω.

The general course of the measurement data shows, that the used strains cannot produce a high power output for a long period of time. For both measurements the maximum voltage is reached after approximately 30 minutes and the voltage values decrease simultaneously after this point. The exact reason for this performance cannot be determined. Possible reasons for this might be the supply of nutriments, aeration problems or the insufficient ability of the cells to maintain their metabolism under conditions of anaerobic respiration. As a constant power output is necessary for generation of significant polarization and power curves, the temporal process of power, respectively the average power output, was used to characterize different BioBricks.
Because of the identical cultivation conditions, using two identical MFCs with equivalent cell numbers in a temperature stabilized cultivation chamber and synchronized aeration with nitrogen, the visible difference shown in Figure 29 has to be a result of the BioBrick inserted in the OprF expressing strain. The expression of the OprF protein leads to a higher power output of nearly 500 µW for a 200 Ω resistance, while the KRX strain reaches only 150 µW.

Looking at the measurement curves presented in Figure 29 a distinct fluctuation of the calculated power values becomes visible. However this fact can be explained when considering Figure 30. It shows a small field of view of the voltage values, which were recorded to calculate the power values presented in Figure 29.

Figure 30: Illustration of a small segment of the cultivation, shown in Figure 29 with interrupted axes, to underline the characteristic course of voltage course, caused by the aeration of the anode chamber.

It is apparent, that the fluctuation is nearly identical for both voltage values. A closer look at the different parameters reveals, that this is caused by the aeration of the anode chamber with nitrogen. The periodic aeration intervals correspond directly with the variation of measurements values. Because of the slight mixing through the rise of nitrogen bubbles, reduced mediator molecules are transported to the anode and the voltage increases. Therefore, the system works under diffusion-limited molecular transport conditions. An improved agitation of the cell suspension or a decrease of the distance between membrane and anode could increase the power output.
However, these results show the high accuracy of the measurement procedure and its usability to generate valid data for comparing even small differences between the performances of different strains.

Besides these scientific results, the usage of the developed microbial fuel cell for various applications is possible. Since many of these applications need higher voltages than one fuel cell can deliver, several have to be combined in a series circuit. One easy way to realize a compact multi-cell system is building a stack of several cells. The construction, described in the MFC evolution part, contains 5 membranes, 10 electrodes, 20 frames and 40 gaskets and supplies a voltage of up to 2.4 Volts. Using the OprF (<bbpart>BBa_K1172502</bbpart>) expressing strain it can be used for permanent operation of LEDs or little buzzers, or to power a small ventilator like shown in the video below.

Watch our stack of five MFCs with genetically optimized E. coli produce 2.4 V and thereby lighting several LEDs, enable sound output from a little buzzer and power a small fan.

References

• Bennetto, H. P. (1990). Electricity generation by microorganisms. [http://www.ncbe.reading.ac.uk/NCBE/MATERIALS/METABOLISM/PDF/bennetto.pdf Biotechnology Education, 1](4), 163-168.
  
  

• Chaudhuri, S. K., & LovleyF, D. R. (2003). Electricity generation by direct oxidation of glucose in mediatorless microbial fuel cells. [http://www.nature.com/nbt/journal/v21/n10/abs/nbt867.html Nature biotechnology, 21](10), 1229-1232.
  
  

• Logan, B. E., Hamelers, B., Rozendal, R., Schröder, U., Keller, J., Freguia, S., ... & Rabaey, K. (2006). Microbial fuel cells: methodology and technology. [http://pubs.acs.org/doi/abs/10.1021/es0605016 Environmental science & technology, 40](17), 5181-5192.
  
  

• Oh, S., Min, B., & Logan, B. E. (2004). Cathode performance as a factor in electricity generation in microbial fuel cells. [http://pubs.acs.org/doi/abs/10.1021/es049422p Environmental science & technology, 38](18), 4900-4904.
  
  

• Rabaey, K., Clauwaert, P., Aelterman, P., & Verstraete, W. (2005). Tubular microbial fuel cells for efficient electricity generation. [http://pubs.acs.org/doi/abs/10.1021/es050986i Environmental science & technology, 39](20), 8077-8082.
  
  

• Sell, D., Krämer, P., & Kreysa, G. (1989). Use of an oxygen gas diffusion cathode and a three-dimensional packed bed anode in a bioelectrochemical fuel cell. [http://link.springer.com/article/10.1007/BF00262465 Applied microbiology and biotechnology, 31](2), 211-213.