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Carolina Zampol Lazaro
Stagiaire postdoctoral – Université de Montréal
Supervisor: Prof. Dr. Patrick Hallenbeck
Senior Research Associate, National Research Council
Department of Biology, US Air Force Academy
Overview of microbial hydrogen
production
 Reduction of CO2 with Hydrogen
 Actual hydrogen production: natural gas via steam
methane reforming (> 90%)
 Barrier to overcome: sustainable hydrogen production -
electrolysis of water and biomass processing (using a
variety of technologies ranging from reforming to
fermentation).
Biological hydrogen producing microorganisms
 Great
diversity!
 Metabolic
versatility!
Source: Chandrasekhar, K., Lee, Y.-J., & Lee, D.-W. (2015). Biohydrogen Production: Strategies to Improve
Process Efficiency through Microbial Routes. International Journal of Molecular Sciences, 16(4).
Biophotolysis
Source: Scoma, A., Giannelli, L., Faraloni, C., & Torzillo, G. (2012). Outdoor H(2)
production in a 50-L tubular photobioreactor by means of a sulfur-deprived
culture of the microalga Chlamydomonas reinhardtii. J Biotechnol, 157(4), 620-
627.
Overview of the 50-L horizontal tubular photobioreactor
used for outdoor experiments with C. reinhardtii
• Abundant substrate = H2O
• Abundant energy source = sun light
• Simple products: H2 and O2
• Oxygen sensitive hydrogenase
• Low light conversion efficiencies
• Expensive hydrogen impermeable
photobioreactors required
• Separation of the H2 and O2
evolution reactions
1- Production of the biomass
(carbohydrates) - open ponds
2. Concentration of biomass –
settling pond;
3. Anaerobic dark fermentation
(4 H2 /glucose + 2 acetates);
4. Conversion of 2 acetates into
8 mol of H2 (under the light)
Indirect biophotolysis by Nonheterocystous
Cyanobacteria
Source: Hallenbeck, P. C., & Benemann, J. R. (2002). Biological
hydrogen production; fundamentals and limiting processes.
International Journal of Hydrogen Energy, 27(11-12), 1185-1193.
Indirect biophotolysis
by Heterocystous
Cyanobacteria
Source: P.C. Hallenbeck (ed.), Microbial Technologies in
Advanced Biofuels Production, DOI 10.1007/978-1-4614-1208-
3_2, © Springer Science+Business Media, LLC 2012
• Nitrogen deprivation → cell
differentiation
• Anaerobiosis permitting
nitrogenase to function
• Cells where PSII is absent no O2
• Calvin cycle enzymes are
absent
• Disaccharides imported to
Heterocyst
Diversity of phototsynthetic bacteria:
Rhodobacter and Rhodopseudomonas
H2 evolved by N2ase (N2 limitation);
Energetically demanding → photosynthesis
Organic acids, lactate, acetate, and succinate
→ wastewater
Also sugars → SINGLE STAGE
Photo-fermentation – basic information
Pros and Cons of Photo-fermentation
• Complete conversion of
organic acid wastes
• Potential waste treatment
credits – N-poor residues,
colorless
• Low light conversion efficiencies
• High energy demand by N2ase
• Expensive hydrogen impermeable
photobioreactors required
Experimental setup for hydrogen production
indoor and outdoor setups
D D Androga, E Özgür, I Eroglu, U Gündüz and M Yücel
(2012). Photofermentative Hydrogen Production in
Outdoor Conditions, Hydrogen Energy - Challenges and
Perspectives, Dragica Minic (Ed.), InTech, DOI:
10.5772/50390
Abo-Hashesh, M., Ghosh, D., Tourigny, A., Taous, A., &
Hallenbeck, P. C. (2011). Single stage photofermentative
hydrogen production from glucose: An attractive alternative to
two stage photofermentation or co-culture approaches. Int J
Hydrogen Energy, 36(21), 13889-13895.
Chen, C. Y., Lee, C. M., & Chang, J. S. (2006).
Feasibility study on bioreactor strategies for
enhanced photohydrogen production from R.
palustris WP3-5 using optical-fiber-assisted
illumination systems. Int J Hydrogen Energy,
31(15), 2345-2355.
Combined light
source-Optical fiber
Tungsten bulbs
Sun light
• Metabolic engineering
- redirect metabolic flux to
N2ase by blocking pathways
What can be done for improving the yield?
• Physiological manipulation –
remove the need for light!
Overcoming the barrier:
Physiological Method - Microaerobic Fermentation by PNSB
Abo-Hashesh, M., Hallenbeck, P.C. 2012. Microaerobic dark fermentative hydrogen production by the photosynthetic bacterium, R. capsulatus JP91.
International Journal of Low-Carbon Technologies.
Diverse carbon
sources and
concentrations
Strategy to improve the
Yield!
Overcoming the barrier:
Physiological Method - Microaerobic Fermentation by PNSB
 DOE and RSM – H2 yield optimization
 Variables: Inoculum size, Substrate
concentration, O2 concentration
 O2 fed batch strategy – introducing
O2 gradually (1.1 mol H2/mol lactate)
 Immobilized biomass strategy – ↑
cells
1.4 mol H2/mol lactate
Substrate degradation and
byproducts consumption
simultaneously;
↑ H2 yields;
↑ COD removal;
↓ lag phase;
Resiliency to environmental
fluctuation ↑ stability of H2
production;
Efforts to increase the overall process efficiency
CO-CULTURES: metabolic
complementary microorganisms
cultivated in the same bioreactor
C6H12O6 + 2H2O → 4H2 + 2CO2 + 2CH3COOH
2CH3COOH + 4H2O + “light energy” → 8H2 + 4CO2
C6H12O6 → 2H2 + 2CO2 + C3H7COOH
C3H7COOH + 6H2O + “light energy” → 10H2 + 4CO2
 Co-culture: C. butyricum + R. palustris
 Starch/glucose base medium
 DOE -variables:
 MO ratio (dark/photofermentative
bacterium); Buffer concentration;
Substrate concentration;
 Responses:
o H2 Yield, H2 Production, COD removal
Hitit, Z. Y., Lazaro, C. Z., & Hallenbeck, P. C. (2017). Hydrogen production by co-cultures of C. butyricum and R. palustris: Optimization of
yield using response surface methodology. Int J Hydrogen Energy, 42(10), 6578-6589.
6.4 mol H2/mol
glucose
53% Substrate
Convertion Efficiency
COD removal 25-58%
Efforts to increase the overall process efficiency
 Co-culture: Cellulomonas fimi + R. palustris
 DOE - variables:
 MO ratio (cellulolytic/photofermentative bacterium);
carbon and nitrogen source concentration
 Responses:
o Cellulose degradation, H2 Yield,
oH2 Production, COD removal
Hitit, Z. Y., Lazaro, C. Z., & Hallenbeck, P. C. (2017b). Single stage hydrogen production from cellulose through photo-
fermentation by a co-culture of C. fimi and R. palustris. Int J Hydrogen Energy, 42(10), 6556-6566.
Efforts to increase the overall process efficiency
Efforts to increase the overall process efficiency
 SEQUENTIAL SYSTEMS:
metabolic complementary
microorganisms growing
separately
 Possibility to use variety
of substrates,
 Possibility to set specific
environmental and
nutritional requirements
for microorganisms
Chen, C. Y., Yang, M. H., Yeh, K. L., Liu, C. H., &
Chang, J. S. (2008). Biohydrogen production using
sequential two-stage dark and photo fermentation
processes. Int J Hydrogen Energ, 33.
Dark Fermentation – another way to get hydrogen
 Anaerobic metabolism of substrates
 Two basic types of H2 fermentations:
- Driven by need to produce ATP (thru
acetate)
- Driven by need to reoxidize NADH
 Mainly Clostridium and Enterobacter
Dark Fermentation
•Low H2 yields
•Large amounts of side
products (acetate,
butyrate, lactate,
ethanol, etc)
•No direct energy input
needed
•Simple reactor technology
•Variety of waste
streams/energy crops can
be used
Strategies for improving the yields
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0145PM-Carolina Zampol Lazaro.pdf

  • 1. Carolina Zampol Lazaro Stagiaire postdoctoral – Université de Montréal Supervisor: Prof. Dr. Patrick Hallenbeck Senior Research Associate, National Research Council Department of Biology, US Air Force Academy Overview of microbial hydrogen production
  • 2.  Reduction of CO2 with Hydrogen  Actual hydrogen production: natural gas via steam methane reforming (> 90%)  Barrier to overcome: sustainable hydrogen production - electrolysis of water and biomass processing (using a variety of technologies ranging from reforming to fermentation).
  • 3. Biological hydrogen producing microorganisms  Great diversity!  Metabolic versatility! Source: Chandrasekhar, K., Lee, Y.-J., & Lee, D.-W. (2015). Biohydrogen Production: Strategies to Improve Process Efficiency through Microbial Routes. International Journal of Molecular Sciences, 16(4).
  • 4. Biophotolysis Source: Scoma, A., Giannelli, L., Faraloni, C., & Torzillo, G. (2012). Outdoor H(2) production in a 50-L tubular photobioreactor by means of a sulfur-deprived culture of the microalga Chlamydomonas reinhardtii. J Biotechnol, 157(4), 620- 627. Overview of the 50-L horizontal tubular photobioreactor used for outdoor experiments with C. reinhardtii • Abundant substrate = H2O • Abundant energy source = sun light • Simple products: H2 and O2 • Oxygen sensitive hydrogenase • Low light conversion efficiencies • Expensive hydrogen impermeable photobioreactors required
  • 5. • Separation of the H2 and O2 evolution reactions 1- Production of the biomass (carbohydrates) - open ponds 2. Concentration of biomass – settling pond; 3. Anaerobic dark fermentation (4 H2 /glucose + 2 acetates); 4. Conversion of 2 acetates into 8 mol of H2 (under the light) Indirect biophotolysis by Nonheterocystous Cyanobacteria Source: Hallenbeck, P. C., & Benemann, J. R. (2002). Biological hydrogen production; fundamentals and limiting processes. International Journal of Hydrogen Energy, 27(11-12), 1185-1193.
  • 6. Indirect biophotolysis by Heterocystous Cyanobacteria Source: P.C. Hallenbeck (ed.), Microbial Technologies in Advanced Biofuels Production, DOI 10.1007/978-1-4614-1208- 3_2, © Springer Science+Business Media, LLC 2012 • Nitrogen deprivation → cell differentiation • Anaerobiosis permitting nitrogenase to function • Cells where PSII is absent no O2 • Calvin cycle enzymes are absent • Disaccharides imported to Heterocyst
  • 7. Diversity of phototsynthetic bacteria: Rhodobacter and Rhodopseudomonas H2 evolved by N2ase (N2 limitation); Energetically demanding → photosynthesis Organic acids, lactate, acetate, and succinate → wastewater Also sugars → SINGLE STAGE Photo-fermentation – basic information
  • 8. Pros and Cons of Photo-fermentation • Complete conversion of organic acid wastes • Potential waste treatment credits – N-poor residues, colorless • Low light conversion efficiencies • High energy demand by N2ase • Expensive hydrogen impermeable photobioreactors required
  • 9. Experimental setup for hydrogen production indoor and outdoor setups D D Androga, E Özgür, I Eroglu, U Gündüz and M Yücel (2012). Photofermentative Hydrogen Production in Outdoor Conditions, Hydrogen Energy - Challenges and Perspectives, Dragica Minic (Ed.), InTech, DOI: 10.5772/50390 Abo-Hashesh, M., Ghosh, D., Tourigny, A., Taous, A., & Hallenbeck, P. C. (2011). Single stage photofermentative hydrogen production from glucose: An attractive alternative to two stage photofermentation or co-culture approaches. Int J Hydrogen Energy, 36(21), 13889-13895. Chen, C. Y., Lee, C. M., & Chang, J. S. (2006). Feasibility study on bioreactor strategies for enhanced photohydrogen production from R. palustris WP3-5 using optical-fiber-assisted illumination systems. Int J Hydrogen Energy, 31(15), 2345-2355. Combined light source-Optical fiber Tungsten bulbs Sun light
  • 10. • Metabolic engineering - redirect metabolic flux to N2ase by blocking pathways What can be done for improving the yield? • Physiological manipulation – remove the need for light!
  • 11. Overcoming the barrier: Physiological Method - Microaerobic Fermentation by PNSB Abo-Hashesh, M., Hallenbeck, P.C. 2012. Microaerobic dark fermentative hydrogen production by the photosynthetic bacterium, R. capsulatus JP91. International Journal of Low-Carbon Technologies. Diverse carbon sources and concentrations Strategy to improve the Yield!
  • 12. Overcoming the barrier: Physiological Method - Microaerobic Fermentation by PNSB  DOE and RSM – H2 yield optimization  Variables: Inoculum size, Substrate concentration, O2 concentration  O2 fed batch strategy – introducing O2 gradually (1.1 mol H2/mol lactate)  Immobilized biomass strategy – ↑ cells 1.4 mol H2/mol lactate
  • 13. Substrate degradation and byproducts consumption simultaneously; ↑ H2 yields; ↑ COD removal; ↓ lag phase; Resiliency to environmental fluctuation ↑ stability of H2 production; Efforts to increase the overall process efficiency CO-CULTURES: metabolic complementary microorganisms cultivated in the same bioreactor C6H12O6 + 2H2O → 4H2 + 2CO2 + 2CH3COOH 2CH3COOH + 4H2O + “light energy” → 8H2 + 4CO2 C6H12O6 → 2H2 + 2CO2 + C3H7COOH C3H7COOH + 6H2O + “light energy” → 10H2 + 4CO2
  • 14.  Co-culture: C. butyricum + R. palustris  Starch/glucose base medium  DOE -variables:  MO ratio (dark/photofermentative bacterium); Buffer concentration; Substrate concentration;  Responses: o H2 Yield, H2 Production, COD removal Hitit, Z. Y., Lazaro, C. Z., & Hallenbeck, P. C. (2017). Hydrogen production by co-cultures of C. butyricum and R. palustris: Optimization of yield using response surface methodology. Int J Hydrogen Energy, 42(10), 6578-6589. 6.4 mol H2/mol glucose 53% Substrate Convertion Efficiency COD removal 25-58% Efforts to increase the overall process efficiency
  • 15.  Co-culture: Cellulomonas fimi + R. palustris  DOE - variables:  MO ratio (cellulolytic/photofermentative bacterium); carbon and nitrogen source concentration  Responses: o Cellulose degradation, H2 Yield, oH2 Production, COD removal Hitit, Z. Y., Lazaro, C. Z., & Hallenbeck, P. C. (2017b). Single stage hydrogen production from cellulose through photo- fermentation by a co-culture of C. fimi and R. palustris. Int J Hydrogen Energy, 42(10), 6556-6566. Efforts to increase the overall process efficiency
  • 16. Efforts to increase the overall process efficiency  SEQUENTIAL SYSTEMS: metabolic complementary microorganisms growing separately  Possibility to use variety of substrates,  Possibility to set specific environmental and nutritional requirements for microorganisms Chen, C. Y., Yang, M. H., Yeh, K. L., Liu, C. H., & Chang, J. S. (2008). Biohydrogen production using sequential two-stage dark and photo fermentation processes. Int J Hydrogen Energ, 33.
  • 17. Dark Fermentation – another way to get hydrogen  Anaerobic metabolism of substrates  Two basic types of H2 fermentations: - Driven by need to produce ATP (thru acetate) - Driven by need to reoxidize NADH  Mainly Clostridium and Enterobacter
  • 18. Dark Fermentation •Low H2 yields •Large amounts of side products (acetate, butyrate, lactate, ethanol, etc) •No direct energy input needed •Simple reactor technology •Variety of waste streams/energy crops can be used