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A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
Successful enrichment procedure for enhancing electron transfer in electroactive biofilms 
PIERRA Mélanie, TRABLY Eric, GODON Jean-Jacques, BERNET Nicolas. 
4th International Microbial Fuel Cell Conference 
1st - 4th September 2013 - Cairns, Queensland, Australia
.02 
Electroactive biofilm 
Rozendal et al., 2006 Int J Hydrog Energy, 31(12), pp.1632–1640. Rabaey & Verstraete, 2005. Trends Biotechnol, 23(6), pp.291–298. Liu et al., 2010. Biofuels, 1(1), pp.129–142. 
Electro-active bacteria are able to transfer electrons to an insoluble and external electron acceptor. 
MFC 
MEC 
etc… 
MXC’s 
Bioelectrochemical Systems 
(BES) 
Anode 
CxHyOz 
CO2 
e- 
e- 
H2 
CH4 
…
.03 
Food Industry 
Fish and seafood 
Slaughterhouses, salting 
Dairy industry 
Brined vegetables 
Petroleum Industry 
Raffinerie 
Chemical and pharmaceutical industry 
Saline pollutions in Industry 
Lefebvre, O. et al, Water Res. 2006. 40: p. 3671-3682; Xiao, Y. et al, Environ. Technol. 2010. 31 (8-9): p. 1025-1043 
3 
Leather Industry 
Textile Industry
.04 
Food Industry 
Fish and seafood 
Slaughterhouses, salting 
Dairy industry 
Brined vegetables 
Petroleum Industry 
Raffinerie 
Chemical and pharmaceutical industry 
Saline pollutions in Industry 
Lefebvre, O. et al, Water Res. 2006. 40: p. 3671-3682; Xiao, Y. et al, Environ. Technol. 2010. 31 (8-9): p. 1025-1043 
4 
Leather Industry 
Textile Industry 
Industries generating saline effluents: 
5% of worldwide effluents 
Lefebvre et al., 2012 Bioresource technology, 112, pp.336–40
.05 
Food Industry 
Fish and seafood 
Slaughterhouses, salting 
Dairy industry 
Brined vegetables 
Petroleum Industry 
Raffinerie 
Chemical and pharmaceutical industry 
Saline pollutions in Industry 
5 
Leather Industry 
Textile Industry 
saline conditions => good conductivity in the anodic chamber => good charge transport 
Lefebvre, O. et al, Water Res. 2006. 40: p. 3671-3682; Xiao, Y. et al, Environ. Technol. 2010. 31 (8-9): p. 1025-1043 
Lefebvre et al., 2012 Bioresource technology, 112, pp.336–40 
Rousseau et al., 2013. Electrochemistry Communications, 33, pp.1–4.
.06 
Sources of Electroactive bacteria 
Lefebvre et al, 2010. Applied microbiology and biotechnology. Chae et al., 2009. 100(14), pp.3518–3525. Harnisch et al., 2011. Energy & Environmental Science, 4(4), p.1265 Miceli et al., 2012. Environmental science & technology, 46(18), pp.10349–55. 
Various sources of electroactive bacteria 
High variability in the performances of biofilm communities [μA/m²-15 A/m²] 
•Freshwater and marine sediments 
•Salt marsh 
•Anaerobic Sludge 
•Wastewater treatment plants 
•Mangrove swamp sediments 
Mix of vinasse, compost and soil : 0,2 A/m² 
Soil : 
3,92 A/m² 
Salt marsh sediments : 
15,27 ± 1,76 A/m² 
Marine sediments : 7,19 ± 3,33 A/m² 
Need to use a reliable enrichment technique
.07 
Enrichment to enhance biofilm formation and performance 
Wang et al., 2010. Bioresource technology, 101(14), pp.5733–5735 Lovley, 2006. Nat Rev Microbiol, 4(7), pp.497–508. Nevin et al., 2008. Environ Microbiol, 10(10), pp.2505–14. Miceli et al., 2012. Environmental science & technology, 46(18), pp.10349–55. Kim et al., 1999. Microbiology and Biotechnology, 9(2), pp.127–131. 
•Most of the known electroactive bacteria are dissimilatory metal reducing bacteria (Shewanella putrefaciens, Geobacter spp, Desulfuromonas spp) 
•Most of the inoculating strategies consist in the re-use of electroactive biofilm to inoculate new electrode in a BES system 
•This study aims to develop an enrichment method to select microorganisms which can use solid iron oxides as electron acceptor to inoculate BES systems 
Anode 
CxHyOz 
CO2 
e- 
Fe(III) oxides 
CxHyOz 
CO2 
e-
.08 
Experimental Design 
Wang et al., 2010. Bioresource technology, 101(14), pp.5733–5735 Lovley & Phillips 1986. Applied and environmental 
microbiology, 51(4), pp.683–689. 
Working electrode 
Reference electrode 
Counter electrode 
U 
I 
0.2V vs SCE 
Anode (Working-electrode) : graphite 
Cathode (Counter-electrode) : platinium 
Reference electrode : Hg/Hg2Cl2/Cl- SCE 
3 electrodes system 
(Half cell MEC) 
U 
I I= f(t)
.09 
Experimental Design 
Wang et al., 2010. Bioresource technology, 101(14), pp.5733–5735 Lovley & Phillips 1986. Applied and environmental 
microbiology, 51(4), pp.683–689. 
Working electrode 
Reference electrode 
Counter electrode 
U 
I 
0.2V vs SCE 
3 electrodes system 
(Half cell MEC) 
 Inoculum : Salt marsh sediments 
 Substrate : Acetate (10 mM) 
 Initial pH : 7 
 Temperature : 37°C 
 Salinity : 35gNaCl/L 
Enrichment culture 
Electron acceptor : 
Fe(III) oxides 
U 
I I= f(t)
.010 
Materials & Methods 
푄푚푎푥 퐶 = 푖 푡 푑푡 
Anode 
CxHyOz 
CO2 
e- 
0 
1 
2 
3 
4 
5 
6 
7 
8 
9 
0 10 20 30 40 
J(A:m²) 
time (days) 
0 
500 
1 000 
1 500 
2 000 
2 500 
3 000 
3 500 
4 000 
4 500 
0 10 20 30 40 
Q(C) 
time (days) 
퐶퐸 = 
푛푒−푡푟푎푛푠푓푒푟푒푑 
푛푒−푡ℎ푒표푟푒푡푖푐푎푙 푓푟표푚 푠푢푏푠푡푟푎푡푒 
Lag Phase 
Charge transmitted : Qmax 
Coulombic efficiency :
.011 
Materials & Methods 
4x 
4x 
Sediments 
4x 
4x 
Effect of the enrichment culture stages on : 
• bioelectrochemical performance 
• electroactive biofilm community structure 
E1 
E2 
E3 
B0 
B1 
B2 
B3
.012 
Materials & Methods 
Genomic DNA, PCR-SSCP and pyrosequencing 
•SSCP = Fingerprinting technique 
• 1 species => 1 peak 
•Area under the peak => abundance of the species in the 
microbial community 
Elution time 
Species 1 
Fluorescence 
intensity 
Species 2 
CE-SSCP profile 
Microbial 
fingerprinting 
Removal of 
Biofilm 
Centrifugation of 
liquid culture 
Pyrosequencing 
0 
5 
10 
15 
20 
25 
30 
35 
40 
Bacterial communities 
Relative abundance (%) 
1 2 3 4
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.013 
1 enrichment step : Increase of the coulombic efficiency from 30,4±4% to 99±7% was shown 
Electron transfer efficiency 
Increase of Lag phase 
Efficient electroactive biofilm growth: 
From 1,6 to 4,5 A/m² obtained 
0 
5 
10 
15 
20 
25 
30 
35 
0 
1 
2 
3 
4 
5 
6 
B0 
B1 
B2 
B3 
Jmax (A/m²) 
Enrichment biofilm step 
Jmax (A/m²) 
Lag Phase (d) 
Lag Phase (days) 
0% 
20% 
40% 
60% 
80% 
100% 
120% 
140% 
B0 
B1 
B2 
B3 
Coulombic efficiency (%)
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.014 
Microbial communities: structure 
4x 
4x 
Sediments 
4x 
4x 
E1 
E2 
E3 
B0 
B1 
B2 
B3
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.015 
Microbial communities: structure 
Sediment 
s 
Similar microbial structure 
(1 or 2 most abundant 
species as electroactive 
bacteria) 
High simplification of 
microbial diversity 
SSCP patterns 
E1 
E2 
E3 
B0 
B1 
B2 
B3
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.016 
Increase of Lag Phase concurs with the emergence of Marinobacterium sp 
0 
5 
10 
15 
20 
25 
30 
35 
0 
1 
2 
3 
4 
5 
6 
B0 
B1 
B2 
B3 
Jmax (A/m²) 
Enrichment biofilm step 
Jmax (A/m²) 
Lag Phase (d) 
Lag Phase (days) 
0% 
20% 
40% 
60% 
80% 
100% 
120% 
140% 
0 
20 
40 
60 
80 
100 
B0 
B1 
B2 
B3 
Relative abundance (%) 
Coulombic efficiency (%) 
Microbial communities: structure 
Most abundant species vs electroactive performance 
Electroactive activity of biofilm is enhanced from the first enrichment culture due to the selection of Geoalkalibacter subterraneus
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.017 
Enrichments Biofilms 
Microbial communities: structure 
• Liquid enrichment cultures : Geobacteraceae 
• Biofilms : Geobacteraceae and Marinobacterium sp. 
• Liquid enrichment procedure permits the selection of efficient 
electroactive strain (of Geobacteraceae) from the first enrichment step
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.018 
PCA on Enrichment and Biofilm Microbial Community profiles 
BF3 
-0.2 
-0.1 
0.0 
0.1 
0.2 
-0.2 
-0.1 
0.0 
0.1 
Axis 1 - 37.1% 
Axis 2 - 24.0% 
BF1 
BF2 
Sediment 
Sediment BF 
E1 
E2 
E3 
Optimal performance is obtained from enrichment and biofilm converging community profiles 
Lag Phase increases from enrichment and biofilm divergent community profiles 
Principal Component Analysis 
Easier adhesion of electroactive bacteria
A L I M E N T A T I O N 
A G R I C U L T U R E 
E N V I R O N N E M E N T 
.019 
Conclusions 
•A successful enrichment strategy 
•With only 1 step required 
•Enrichment of Geoalkalibacter subterraneus 
•After 3rd enrichment step 
oDivergence of species selected 
oDecrease of electroactive performance
.020 
Acknowledgments 
Nicolas BERNET Eric TRABLY Jean Jaques GODON Anais BONNAFOUS Alessandro CARMONA Mohanakrishna GUNDA

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4ISMET, Melanie PIERRA

  • 1. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T Successful enrichment procedure for enhancing electron transfer in electroactive biofilms PIERRA Mélanie, TRABLY Eric, GODON Jean-Jacques, BERNET Nicolas. 4th International Microbial Fuel Cell Conference 1st - 4th September 2013 - Cairns, Queensland, Australia
  • 2. .02 Electroactive biofilm Rozendal et al., 2006 Int J Hydrog Energy, 31(12), pp.1632–1640. Rabaey & Verstraete, 2005. Trends Biotechnol, 23(6), pp.291–298. Liu et al., 2010. Biofuels, 1(1), pp.129–142. Electro-active bacteria are able to transfer electrons to an insoluble and external electron acceptor. MFC MEC etc… MXC’s Bioelectrochemical Systems (BES) Anode CxHyOz CO2 e- e- H2 CH4 …
  • 3. .03 Food Industry Fish and seafood Slaughterhouses, salting Dairy industry Brined vegetables Petroleum Industry Raffinerie Chemical and pharmaceutical industry Saline pollutions in Industry Lefebvre, O. et al, Water Res. 2006. 40: p. 3671-3682; Xiao, Y. et al, Environ. Technol. 2010. 31 (8-9): p. 1025-1043 3 Leather Industry Textile Industry
  • 4. .04 Food Industry Fish and seafood Slaughterhouses, salting Dairy industry Brined vegetables Petroleum Industry Raffinerie Chemical and pharmaceutical industry Saline pollutions in Industry Lefebvre, O. et al, Water Res. 2006. 40: p. 3671-3682; Xiao, Y. et al, Environ. Technol. 2010. 31 (8-9): p. 1025-1043 4 Leather Industry Textile Industry Industries generating saline effluents: 5% of worldwide effluents Lefebvre et al., 2012 Bioresource technology, 112, pp.336–40
  • 5. .05 Food Industry Fish and seafood Slaughterhouses, salting Dairy industry Brined vegetables Petroleum Industry Raffinerie Chemical and pharmaceutical industry Saline pollutions in Industry 5 Leather Industry Textile Industry saline conditions => good conductivity in the anodic chamber => good charge transport Lefebvre, O. et al, Water Res. 2006. 40: p. 3671-3682; Xiao, Y. et al, Environ. Technol. 2010. 31 (8-9): p. 1025-1043 Lefebvre et al., 2012 Bioresource technology, 112, pp.336–40 Rousseau et al., 2013. Electrochemistry Communications, 33, pp.1–4.
  • 6. .06 Sources of Electroactive bacteria Lefebvre et al, 2010. Applied microbiology and biotechnology. Chae et al., 2009. 100(14), pp.3518–3525. Harnisch et al., 2011. Energy & Environmental Science, 4(4), p.1265 Miceli et al., 2012. Environmental science & technology, 46(18), pp.10349–55. Various sources of electroactive bacteria High variability in the performances of biofilm communities [μA/m²-15 A/m²] •Freshwater and marine sediments •Salt marsh •Anaerobic Sludge •Wastewater treatment plants •Mangrove swamp sediments Mix of vinasse, compost and soil : 0,2 A/m² Soil : 3,92 A/m² Salt marsh sediments : 15,27 ± 1,76 A/m² Marine sediments : 7,19 ± 3,33 A/m² Need to use a reliable enrichment technique
  • 7. .07 Enrichment to enhance biofilm formation and performance Wang et al., 2010. Bioresource technology, 101(14), pp.5733–5735 Lovley, 2006. Nat Rev Microbiol, 4(7), pp.497–508. Nevin et al., 2008. Environ Microbiol, 10(10), pp.2505–14. Miceli et al., 2012. Environmental science & technology, 46(18), pp.10349–55. Kim et al., 1999. Microbiology and Biotechnology, 9(2), pp.127–131. •Most of the known electroactive bacteria are dissimilatory metal reducing bacteria (Shewanella putrefaciens, Geobacter spp, Desulfuromonas spp) •Most of the inoculating strategies consist in the re-use of electroactive biofilm to inoculate new electrode in a BES system •This study aims to develop an enrichment method to select microorganisms which can use solid iron oxides as electron acceptor to inoculate BES systems Anode CxHyOz CO2 e- Fe(III) oxides CxHyOz CO2 e-
  • 8. .08 Experimental Design Wang et al., 2010. Bioresource technology, 101(14), pp.5733–5735 Lovley & Phillips 1986. Applied and environmental microbiology, 51(4), pp.683–689. Working electrode Reference electrode Counter electrode U I 0.2V vs SCE Anode (Working-electrode) : graphite Cathode (Counter-electrode) : platinium Reference electrode : Hg/Hg2Cl2/Cl- SCE 3 electrodes system (Half cell MEC) U I I= f(t)
  • 9. .09 Experimental Design Wang et al., 2010. Bioresource technology, 101(14), pp.5733–5735 Lovley & Phillips 1986. Applied and environmental microbiology, 51(4), pp.683–689. Working electrode Reference electrode Counter electrode U I 0.2V vs SCE 3 electrodes system (Half cell MEC)  Inoculum : Salt marsh sediments  Substrate : Acetate (10 mM)  Initial pH : 7  Temperature : 37°C  Salinity : 35gNaCl/L Enrichment culture Electron acceptor : Fe(III) oxides U I I= f(t)
  • 10. .010 Materials & Methods 푄푚푎푥 퐶 = 푖 푡 푑푡 Anode CxHyOz CO2 e- 0 1 2 3 4 5 6 7 8 9 0 10 20 30 40 J(A:m²) time (days) 0 500 1 000 1 500 2 000 2 500 3 000 3 500 4 000 4 500 0 10 20 30 40 Q(C) time (days) 퐶퐸 = 푛푒−푡푟푎푛푠푓푒푟푒푑 푛푒−푡ℎ푒표푟푒푡푖푐푎푙 푓푟표푚 푠푢푏푠푡푟푎푡푒 Lag Phase Charge transmitted : Qmax Coulombic efficiency :
  • 11. .011 Materials & Methods 4x 4x Sediments 4x 4x Effect of the enrichment culture stages on : • bioelectrochemical performance • electroactive biofilm community structure E1 E2 E3 B0 B1 B2 B3
  • 12. .012 Materials & Methods Genomic DNA, PCR-SSCP and pyrosequencing •SSCP = Fingerprinting technique • 1 species => 1 peak •Area under the peak => abundance of the species in the microbial community Elution time Species 1 Fluorescence intensity Species 2 CE-SSCP profile Microbial fingerprinting Removal of Biofilm Centrifugation of liquid culture Pyrosequencing 0 5 10 15 20 25 30 35 40 Bacterial communities Relative abundance (%) 1 2 3 4
  • 13. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .013 1 enrichment step : Increase of the coulombic efficiency from 30,4±4% to 99±7% was shown Electron transfer efficiency Increase of Lag phase Efficient electroactive biofilm growth: From 1,6 to 4,5 A/m² obtained 0 5 10 15 20 25 30 35 0 1 2 3 4 5 6 B0 B1 B2 B3 Jmax (A/m²) Enrichment biofilm step Jmax (A/m²) Lag Phase (d) Lag Phase (days) 0% 20% 40% 60% 80% 100% 120% 140% B0 B1 B2 B3 Coulombic efficiency (%)
  • 14. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .014 Microbial communities: structure 4x 4x Sediments 4x 4x E1 E2 E3 B0 B1 B2 B3
  • 15. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .015 Microbial communities: structure Sediment s Similar microbial structure (1 or 2 most abundant species as electroactive bacteria) High simplification of microbial diversity SSCP patterns E1 E2 E3 B0 B1 B2 B3
  • 16. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .016 Increase of Lag Phase concurs with the emergence of Marinobacterium sp 0 5 10 15 20 25 30 35 0 1 2 3 4 5 6 B0 B1 B2 B3 Jmax (A/m²) Enrichment biofilm step Jmax (A/m²) Lag Phase (d) Lag Phase (days) 0% 20% 40% 60% 80% 100% 120% 140% 0 20 40 60 80 100 B0 B1 B2 B3 Relative abundance (%) Coulombic efficiency (%) Microbial communities: structure Most abundant species vs electroactive performance Electroactive activity of biofilm is enhanced from the first enrichment culture due to the selection of Geoalkalibacter subterraneus
  • 17. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .017 Enrichments Biofilms Microbial communities: structure • Liquid enrichment cultures : Geobacteraceae • Biofilms : Geobacteraceae and Marinobacterium sp. • Liquid enrichment procedure permits the selection of efficient electroactive strain (of Geobacteraceae) from the first enrichment step
  • 18. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .018 PCA on Enrichment and Biofilm Microbial Community profiles BF3 -0.2 -0.1 0.0 0.1 0.2 -0.2 -0.1 0.0 0.1 Axis 1 - 37.1% Axis 2 - 24.0% BF1 BF2 Sediment Sediment BF E1 E2 E3 Optimal performance is obtained from enrichment and biofilm converging community profiles Lag Phase increases from enrichment and biofilm divergent community profiles Principal Component Analysis Easier adhesion of electroactive bacteria
  • 19. A L I M E N T A T I O N A G R I C U L T U R E E N V I R O N N E M E N T .019 Conclusions •A successful enrichment strategy •With only 1 step required •Enrichment of Geoalkalibacter subterraneus •After 3rd enrichment step oDivergence of species selected oDecrease of electroactive performance
  • 20. .020 Acknowledgments Nicolas BERNET Eric TRABLY Jean Jaques GODON Anais BONNAFOUS Alessandro CARMONA Mohanakrishna GUNDA