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 
Microbial Fuel Cell Project 
Caitlyn Youngblood, Shannen Scott, Kelly Creswell
Recognition of Problem and Need 
 Globally energy use continues to increase 
 Most energy sources used today are non-renewable (coal, oil, natural gas) 
 Electricity production from non-renewable resources produces harmful by-products 
 Generation of electricity produces more pollution than any other single industry in the U.S. 
Define the problem at hand : 
Design a microbial fuel cell capable of producing recoverable electrical power 
from natural microorganisms.
Goals of the MFC Project 
Process goals: 
 To capture the electrons processed by microorganisms during cellular 
respiration 
 To create a process that would produce usable electrical power 
Structural goals: 
 Structure must be of lab scale magnitude 
 Materials must be biologically compatible with yeast, bacteria, and 
algae 
 Must be 75% recycled material by weight 
Mechanical Goals: 
 Must be capable of operating as either batch or CSTR
Constraints and Considerations 
 Constraints 
 Cost of materials can not exceed $10 excluding the price of the 
CEM 
 Must be able to fabricate ourselves using the available equipment 
in the fabrication shop 
 Other Considerations 
 Need to be able to safely construct the structure 
 Try incorporating natural materials (less man-made) 
 Be able to reuse the reactor 
 Ultimately be able to harness the energy produced to power a 
device
Scientific Journal References 
 “Novel anti-flooding 
poly(dimethylsiloxane) (PDMS) 
catalyst for microbial fuel cells” 
 Adopted Ideas: 
 Need a good source of 
oxygen for cathode (algae) 
 Batch Reactor 
 Differences: 
 Ours was a laboratory scale 
 We had a water cathode 
 “ Comparitive study of three 
types of microbial fuel cells” 
 Adopted Ideas: 
 General original design was 
a simplified version of theirs 
 Used same calculation for 
power and optimum 
resistance 
 Differences: 
 They were comparing the 
efficiency of three different 
types of MFC’s
Past Experiences and Heuristics 
 We incorporated a lot of 
knowledge from past labs we 
had done, Specifically the CSTR 
lab. 
 Process used to measure 
the volume of our anode 
chamber 
 Similar construction of the 
anode chamber 
 We had originally planned 
to have a stir bar in the 
anode chamber
Design Methodology 
Original Design 
 Original Design 
Final Design
Materials 
 Chose Plexiglas 
 Lexan was known to turn yellow over time 
 Wood would absorb water 
 Biochar as electrode – recycled component 
 Wire mesh was used to create the pouches to 
hold biochar 
 Copper Wire use to connect anode and cathode 
to the resistor 
 Foam plug and two plastic stoppers in the anode 
chamber (all new) 
 CEM and rubber used between the two chambers 
 Screws, washers and wing nuts used to hold the 
two chambers together 
 Algae in cathode 
 Mixed culture of heterotrophic bacteria in anode
Fabrication 
 A miter saw was used to cut the cylindrical acrylic 
as well as the flat square pieces. 
 A hole saw was used to create the holes in the 
rubber and flat acrylic in between the chambers. 
 Screw holes drilled with drill press 
 Acrylic was pieced together using a chemical 
welding process 
 Silicon was used to reinforce inlet, outlet, and 
wire ports
Chamber Solutions 
Anode Chamber 
 1 gram glucose 
 0.25 gram organic nitrogen 
source 
 0.02 gram K2HPO4 (P source) 
 50 mL viable heterotrophic 
bacteria culture 
 1 L tap water 
 0.1 mL 1% Resazurin solution 
Cathode Chamber 
 Algae media 
 Approximately 50 mL of algae
Calculation of Internal Resistance 
Ohm’s Law 푉 = 퐼 × 푅 
 Voltage produced at various resistances was used to calculate the current by re-arranging 
ohm’s law: 
 The current was then graphed vs. voltage to calculate the internal resistance of 
our MFC 
I = 
푉 
푅 
V = -381.13 (I) + 0.0116 
0.016 
0.014 
0.012 
0.01 
0.008 
0.006 
0.004 
0.002 
0 
Polarization Curve 
0 0.000005 0.00001 0.000015 0.00002 0.000025 
Voltage (V) [V] 
Current (I) [A] 
Internal Resistance = 381 Ω
Internal Resistance after a Week 
V = -760.1(I) + 0.0071 
0.008 
0.007 
0.006 
0.005 
0.004 
0.003 
0.002 
0.001 
0 
0.E+00 1.E-06 2.E-06 3.E-06 4.E-06 5.E-06 6.E-06 7.E-06 8.E-06 9.E-06 
Voltage (V) [V] 
Current (I) [A]
Arising Problems and Solutions 
 Microbes produced gas which 
accumulated in top of anode chamber 
 Water was pumped in to force the gas 
out (11/29/2012) 
 Unsure of the contact of the wire with 
the biochar 
 Used plastic ties to create contact and 
frayed the end of the wire 
(11/27/2012) 
 Media in anode chamber became 
contaminated with yeast 
 Drained and re-inoculated 
(11/30/2012)
Calculation of Power 
Ohm’s Law 푉 = 퐼 × 푅 
 Power is defined as 
푒푛푒푟푔푦 
푡푖푚푒 
, 
I has units of 
퐽표푢푙푒푠 
퐶표푢푙표푚푏 
V has units of 
퐶표푢푙표푚푏푠 
푆푒푐표푛푑 
 So to get power: 
푉2 
푅 
or 
푃 = 
푃 = 퐼 × 푉 
Sample Calculation: 
V = 0.014 V 
R = 381 Ω 
푃 = 
0.014 푉 
381 Ω 
= 3.67 × 10−5 W
Resulting Power Density 
8.E-07 
7.E-07 
6.E-07 
5.E-07 
4.E-07 
3.E-07 
2.E-07 
1.E-07 
0.E+00 
0 50 100 150 200 250 
Power Density (PDV) [W/L] 
Time (t) [hr]
Optical Density of Anode 
Absorbance 
Start: 
0.003 
End of Week: 
0.586
Conclusions 
 After re-inoculating our anode chamber 
and fraying the end of our cathode wire, 
our MFC finally began to show the results 
we were hoping for. 
 Though the power our MFC conducts is 
quite small, on a larger and more efficient 
scale it might produce a usable amount of 
power. 
 Even after data collection stopped, the 
MFC is continuing to produce more power.
Redesign 
 Use stir bar in the anode chamber and 
aerator in the cathode chamber for 
mixing 
 Position reactor on its side for 
convenience in pumping in material and 
ensuring water contact with membrane 
 Use crushed graphite over biochar to 
keep solution clear 
 Design some surface for the algae to 
grow on so it does not grow over the 
CEM
References 
 http://www.science.smith.edu/~jcardell/Courses/EGR325/Readings/ElecPollution_ 
EnvDef.pdf 
 BE 212 Fundamentals of BE Syllabus, Drapcho, Fall 2012 
 BE 212 Lab 1 Notes, Drapcho, Fall 2012 
 Zhang, Fang, Guang Chen, Michael A. Hickner, and Bruce E. Logan. "Novel Anti-flooding 
Poly(dimethylsiloxane) (PDMS) Catalyst Binder for Microbial Fuel Cell 
Cathodes." Journal of Power Sources (2012): n. pag. 4 July 2012. Web. 4 Dec. 2012. 
 Greenman, John, Ioannis A. Ieropoulos, John Hart, and Chris Melhuish. 
"Comparitive Study of Three Types of Microbial Fuel Cell." Enzyme and Microbial 
Technology 37.2 (2005): 238-45. 20 Apr. 2005. Web. 4 Dec. 2012. 
<http://dx.doi.org/10.1016/j.enzmictec.2005.03.006>. 
 BE 212 Lab 3 Notes, Drapcho, Fall 2012
Appendices 
Table 1. Values from testing MFC with media at beginning of week 
Resistance (R) [Ω] Current (I) [A] Voltage (V) [V] Power (P) [W] Power Density (PDV) [W/L] 
20 0.000E+00 0 0.000E+00 0.000E+00 
66 1.515E-05 0.001 1.515E-08 1.515E-11 
206 1.942E-05 0.004 7.767E-08 3.107E-10 
501 1.796E-05 0.009 1.617E-07 1.455E-09 
2461 2.844E-06 0.007 1.991E-08 1.394E-10 
5030 2.982E-06 0.015 4.473E-08 6.710E-10
Appendices 
Table 2. Values read or calculated during MFC run time
Appendices 
Table 3. Values used in calculating the polarization curve at end of week 
Resistance (R) [Ω] Voltage (V) [V] Current (I) [A] 
260 0.002 7.69231E-06 
554 0.002 3.61011E-06 
2486 0.006 2.41352E-06 
4900 0.007 1.42857E-06

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Be 212 presentation

  • 1.  Microbial Fuel Cell Project Caitlyn Youngblood, Shannen Scott, Kelly Creswell
  • 2. Recognition of Problem and Need  Globally energy use continues to increase  Most energy sources used today are non-renewable (coal, oil, natural gas)  Electricity production from non-renewable resources produces harmful by-products  Generation of electricity produces more pollution than any other single industry in the U.S. Define the problem at hand : Design a microbial fuel cell capable of producing recoverable electrical power from natural microorganisms.
  • 3. Goals of the MFC Project Process goals:  To capture the electrons processed by microorganisms during cellular respiration  To create a process that would produce usable electrical power Structural goals:  Structure must be of lab scale magnitude  Materials must be biologically compatible with yeast, bacteria, and algae  Must be 75% recycled material by weight Mechanical Goals:  Must be capable of operating as either batch or CSTR
  • 4. Constraints and Considerations  Constraints  Cost of materials can not exceed $10 excluding the price of the CEM  Must be able to fabricate ourselves using the available equipment in the fabrication shop  Other Considerations  Need to be able to safely construct the structure  Try incorporating natural materials (less man-made)  Be able to reuse the reactor  Ultimately be able to harness the energy produced to power a device
  • 5. Scientific Journal References  “Novel anti-flooding poly(dimethylsiloxane) (PDMS) catalyst for microbial fuel cells”  Adopted Ideas:  Need a good source of oxygen for cathode (algae)  Batch Reactor  Differences:  Ours was a laboratory scale  We had a water cathode  “ Comparitive study of three types of microbial fuel cells”  Adopted Ideas:  General original design was a simplified version of theirs  Used same calculation for power and optimum resistance  Differences:  They were comparing the efficiency of three different types of MFC’s
  • 6. Past Experiences and Heuristics  We incorporated a lot of knowledge from past labs we had done, Specifically the CSTR lab.  Process used to measure the volume of our anode chamber  Similar construction of the anode chamber  We had originally planned to have a stir bar in the anode chamber
  • 7. Design Methodology Original Design  Original Design Final Design
  • 8. Materials  Chose Plexiglas  Lexan was known to turn yellow over time  Wood would absorb water  Biochar as electrode – recycled component  Wire mesh was used to create the pouches to hold biochar  Copper Wire use to connect anode and cathode to the resistor  Foam plug and two plastic stoppers in the anode chamber (all new)  CEM and rubber used between the two chambers  Screws, washers and wing nuts used to hold the two chambers together  Algae in cathode  Mixed culture of heterotrophic bacteria in anode
  • 9. Fabrication  A miter saw was used to cut the cylindrical acrylic as well as the flat square pieces.  A hole saw was used to create the holes in the rubber and flat acrylic in between the chambers.  Screw holes drilled with drill press  Acrylic was pieced together using a chemical welding process  Silicon was used to reinforce inlet, outlet, and wire ports
  • 10. Chamber Solutions Anode Chamber  1 gram glucose  0.25 gram organic nitrogen source  0.02 gram K2HPO4 (P source)  50 mL viable heterotrophic bacteria culture  1 L tap water  0.1 mL 1% Resazurin solution Cathode Chamber  Algae media  Approximately 50 mL of algae
  • 11. Calculation of Internal Resistance Ohm’s Law 푉 = 퐼 × 푅  Voltage produced at various resistances was used to calculate the current by re-arranging ohm’s law:  The current was then graphed vs. voltage to calculate the internal resistance of our MFC I = 푉 푅 V = -381.13 (I) + 0.0116 0.016 0.014 0.012 0.01 0.008 0.006 0.004 0.002 0 Polarization Curve 0 0.000005 0.00001 0.000015 0.00002 0.000025 Voltage (V) [V] Current (I) [A] Internal Resistance = 381 Ω
  • 12. Internal Resistance after a Week V = -760.1(I) + 0.0071 0.008 0.007 0.006 0.005 0.004 0.003 0.002 0.001 0 0.E+00 1.E-06 2.E-06 3.E-06 4.E-06 5.E-06 6.E-06 7.E-06 8.E-06 9.E-06 Voltage (V) [V] Current (I) [A]
  • 13. Arising Problems and Solutions  Microbes produced gas which accumulated in top of anode chamber  Water was pumped in to force the gas out (11/29/2012)  Unsure of the contact of the wire with the biochar  Used plastic ties to create contact and frayed the end of the wire (11/27/2012)  Media in anode chamber became contaminated with yeast  Drained and re-inoculated (11/30/2012)
  • 14. Calculation of Power Ohm’s Law 푉 = 퐼 × 푅  Power is defined as 푒푛푒푟푔푦 푡푖푚푒 , I has units of 퐽표푢푙푒푠 퐶표푢푙표푚푏 V has units of 퐶표푢푙표푚푏푠 푆푒푐표푛푑  So to get power: 푉2 푅 or 푃 = 푃 = 퐼 × 푉 Sample Calculation: V = 0.014 V R = 381 Ω 푃 = 0.014 푉 381 Ω = 3.67 × 10−5 W
  • 15. Resulting Power Density 8.E-07 7.E-07 6.E-07 5.E-07 4.E-07 3.E-07 2.E-07 1.E-07 0.E+00 0 50 100 150 200 250 Power Density (PDV) [W/L] Time (t) [hr]
  • 16. Optical Density of Anode Absorbance Start: 0.003 End of Week: 0.586
  • 17. Conclusions  After re-inoculating our anode chamber and fraying the end of our cathode wire, our MFC finally began to show the results we were hoping for.  Though the power our MFC conducts is quite small, on a larger and more efficient scale it might produce a usable amount of power.  Even after data collection stopped, the MFC is continuing to produce more power.
  • 18. Redesign  Use stir bar in the anode chamber and aerator in the cathode chamber for mixing  Position reactor on its side for convenience in pumping in material and ensuring water contact with membrane  Use crushed graphite over biochar to keep solution clear  Design some surface for the algae to grow on so it does not grow over the CEM
  • 19. References  http://www.science.smith.edu/~jcardell/Courses/EGR325/Readings/ElecPollution_ EnvDef.pdf  BE 212 Fundamentals of BE Syllabus, Drapcho, Fall 2012  BE 212 Lab 1 Notes, Drapcho, Fall 2012  Zhang, Fang, Guang Chen, Michael A. Hickner, and Bruce E. Logan. "Novel Anti-flooding Poly(dimethylsiloxane) (PDMS) Catalyst Binder for Microbial Fuel Cell Cathodes." Journal of Power Sources (2012): n. pag. 4 July 2012. Web. 4 Dec. 2012.  Greenman, John, Ioannis A. Ieropoulos, John Hart, and Chris Melhuish. "Comparitive Study of Three Types of Microbial Fuel Cell." Enzyme and Microbial Technology 37.2 (2005): 238-45. 20 Apr. 2005. Web. 4 Dec. 2012. <http://dx.doi.org/10.1016/j.enzmictec.2005.03.006>.  BE 212 Lab 3 Notes, Drapcho, Fall 2012
  • 20. Appendices Table 1. Values from testing MFC with media at beginning of week Resistance (R) [Ω] Current (I) [A] Voltage (V) [V] Power (P) [W] Power Density (PDV) [W/L] 20 0.000E+00 0 0.000E+00 0.000E+00 66 1.515E-05 0.001 1.515E-08 1.515E-11 206 1.942E-05 0.004 7.767E-08 3.107E-10 501 1.796E-05 0.009 1.617E-07 1.455E-09 2461 2.844E-06 0.007 1.991E-08 1.394E-10 5030 2.982E-06 0.015 4.473E-08 6.710E-10
  • 21. Appendices Table 2. Values read or calculated during MFC run time
  • 22. Appendices Table 3. Values used in calculating the polarization curve at end of week Resistance (R) [Ω] Voltage (V) [V] Current (I) [A] 260 0.002 7.69231E-06 554 0.002 3.61011E-06 2486 0.006 2.41352E-06 4900 0.007 1.42857E-06

Editor's Notes

  1. Kelly Engineering design process
  2. Kelly
  3. Shannen
  4. Caitlyn I will talk about this one a lot For the first source I will say that their design was very different than ours in that it was actually in the soil and on a much larger scale and had an air cathode but from it we adopted two ideas which were to have ours work as a batch reactor and that we needed to have a really good source of oxygen in our cathode because they struggled with that. We also wanted to use a natural source of oxygen for our cathode and that is why we chose to use algae instead of a mechanical aerator The one one the right is pretty straight forward
  5. Discuss similarities and differences between our anode chamber and the picture of the CSTR from the lab Caitlyn
  6. Shannen Just talk about the changes we made from the original design to the final design
  7. Shannen Talk about materials here Be sure to mention was was used and what was new and what was natural blah blah blah
  8. Kelly
  9. Kelly Mix algae pic
  10. Caitlyn B/c V/I = R
  11. Caitlyn
  12. Shannen
  13. Kelly I was calculated from V and R. I was then multiplied by I to get power. ADD SAMPLE WITH NUMBERS
  14. Kelly Re-inoculated at 120 hrs.
  15. Caitlyn
  16. Caitlyn
  17. Shannen
  18. I think we need like an MLA format for the first reference
  19. Because we had so many data points I only showed the points after we had re-inoculated, Also, I am not sure if we are supposed to put this here or as another part of the appendices.