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Producing methane from electrical current generated using renewable energy sources using methanogenic microorganisms Bruce E. Logan Penn State University Engineering Energy & Environmental Institute
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Producing methane from electrical current generated using renewable energy sources using

methanogenic microorganisms

Bruce E. Logan

Penn State University

Engineering Energy & Environmental Institute

New Water Technologies • Every revolutionary idea moves through three stages

– 1- It can’t be done

– 2- It's possible, but it's not worth doing (too $$)

– 3- I said it was a good idea all along.

• Examples in water technologies

– RO membranes for desalination

– MBRs for wastewater treatment

– Microbial electrochemical technologies? • Microbial fuel cells

• Microbial electrolysis cells for electromethanogenesis

2

New Energy Sources Available using Microbial Electrochemical Technologies (METs)

• Wastewater organic matter (WW)

– 15 GW in wastewater (Savings 3x15 + 17 = 62 GW net)

• Cellulose Biomass Energy

– 600 GW available (based on 1.34 billion tons/yr of lignocellulose)

• Salinity Gradient Energy- Natural Waters (global values)

– 980 GW (from the 1900 GW available from river/ocean water)

– 20 GW available where WW flows into the ocean

• Waste Heat Energy

– 500 GW from industrial waste heat

– 1000 GW from power production (33% efficient power plants)

(Does not include solar and geothermal energy sources)

3 Logan and Rabaey (2012) Science Logan and Elimelech (2012, Nature

Demonstration of a Microbial Fuel Cell (MFC)

MFC webcam (live video of an MFC running a fan)

www.engr.psu.edu/mfccam

4

load

Anode Cathode

Oxidation

products

(CO2)

Fuel

(wastes)

e-

Oxidant

(O2)

Reduced

oxidant

(H2O)

H+

e-

Electrical power generation in a microbial fuel

cell (MFC) using exoelectrogenic

microorganisms

Bacteria that make electrical current

5 Liu et al. (2004) Environ. Sci. Technol.

6

Getting energy from food (biomass)

C6H12O6-> 6CO2 + 24 e- NADH

Oxidation Reduction

O2 H2O

NADH

Respiration is the key for capturing energy from food… for humans and bacteria

(Electron transfer)

(e- transporter)

Electro-active Microorganisms

• Electromicrobiology – New sub-discipline of microbiology examining

exocellular electron transfer

7

8

9

10

Electro-active Microorganisms

• Exoelectrogens – Microbes able to transfer electrons to

the outside the cell

• Electrotrophs – Microbes that can accept electrons into

the cell

11

• Electrotrophs – Microbes that can accept electrons into

the cell

12

Exoelectrogens: Bacteria rapidly colonize the anode

13

Mechanisms of electron transfer in the biofilm:

Bacterium Electrode

e-

e-

e-

Nanowires produced by

bacteria !?!

Gorby & 23 co-authors (2010) PNAS

14

Electrogenic biofilm ecology Bacteria living off exoelectrogens

Direct contact

Produce nanowires

Produce mediators

Logan, Nature Rev. Microbiol. (2009)

Electro-active Microorganisms

• Exoelectrogens – Microbes able to transfer electrons to

the outside the cell

• Electrotrophs – Microbes that can accept electrons into

the cell

15

Examples of chemicals used by electrotrophs

• Dissolved oxygen

– Current generation enhanced in the absence of a platinum catalyst

• Nitrate

• Metals (Copper)

• CO2 reduction by methanogens

16

17

Electrotrophs: Biocathodes in MFCs

• Bacteria use

– Nitrate (NO3−)

10 W/m3

– Oxygen (O2) 120 W/m3 (polarization)

83 W/m3 (continuous)

Current higher compared to abiotic cathodes

Sources (Ghent University group):

NO3: Clauwert et al. (2007a), Environ. Sci. Techonol.

O2: Caluwert et. Al. (2007b), Environ. Sci. Technol. 17

Examples of chemicals used by electrotrophs

• Dissolved oxygen

– Current generation enhanced in the absence of a platinum catalyst

• Nitrate

• Metals (Copper)

• CO2 reduction by methanogens

18

19

Methanogens: Conventional model based on

interspecies hydrogen transfer

C6H12O6

+ 2 H2O

2 C2H4O2

+ 2 CO2

+ 4 H2

CH4 + 2 H2O

4 H2 + CO2

Methanogen

Fast!

Slow

Fast!

20

New model includes exoelectroactive

microorganisms: electron transfer

C6H12O6

+ 2 H2O

2 C2H4O2

+ 2 CO2

CH4

CO2

Exoelectrogen Exoelectrotroph

H+ H+

e– e–

What is the evidence for electromethanogensis?

• Nanowire connections

• Experiments:

– Mixed cultures

– Pure cultures

• New studies on methane production

21

22

Nanowires connect fermentative and methanogenic microorganisms

Figure source: Ishii et al. (2005) Appl. Environ. Microbiol.

SI- ferments propionate, releases electrons

ΔH: Methanogen accepts electrons, makes methane

First evidence of direct interspecies electron transfer (2006)

Gorby & 25 others (2006) Proc. Nat. Academy Sci. 22

Electrophic Methanogens

Potentiostat

e–

H+

CH4

CO2

Mixed culture

(Methanobacterium palustre)

0

1

2

3

4

0 20 40 60 80 100

Time (h)

Curr

ent

(mA

)

MPcontrolMixed

0

5

10

15

20

Am

ount

of

gas (

mL)

CH4-mixed H2-abiotic

0

1

2

0 20 40 60 80 100Time (h)

Am

ount of gas (

mL)

CH4-MP

H2-abiotic

A

B

0

1

2

3

4

0 20 40 60 80 100

Time (h)

Curr

ent

(mA

)

MPcontrolMixed

0

5

10

15

20

Am

ount

of

gas (

mL)

CH4-mixed H2-abiotic

0

1

2

0 20 40 60 80 100Time (h)

Am

ount of gas (

mL)

CH4-MP

H2-abiotic

A

B

0

1

2

3

4

0 20 40 60 80 100

Time (h)

Curr

ent

(mA

)

MPcontrolMixed

0

5

10

15

20

Am

ount

of

gas (

mL)

CH4-mixed H2-abiotic

0

1

2

0 20 40 60 80 100Time (h)

Am

ount of gas (

mL)

CH4-MP

H2-abiotic

A

B

Pure culture of ATCC

Methanobacterium palustre

Cheng, Call & Logan (2009) Environ. Sci. Technol. 23

Electrically conductive granules in anaerobic digesters

“The aggregates were electrically conductive, with conductivities 3-fold higher than the conductivities previously reported for dual-species aggregates of Geobacter species in which the two species appeared to exchange electrons via interspecies electron transfer.” (Morita et al. 2011; mBio)

24

Enhanced methane production in anaerobic digesters

• It is known that adding activated carbon, which is electrically conductive, to anaerobic digesters increases methane production.

• “GAC also greatly stimulated ethanol metabolism and methane production in co-cultures of G. metallireducens and Methanosarcina barkeri” (Liu et al., 2012, Energy Env. Sci.)

25

New Technologies… • The three stages of a revolutionary idea, revisited…

– 1- It can’t be done

– 2- It's possible, but it's not worth doing (too $$)

– 3- I said it was a good idea all along.

26

Lovley, 2010: “…. possibility is to use methanogenic microorganisms to reduce carbon dioxide to methane at the cathode in a process termed electromethanogenesis (Cheng et al., 2009).”…

“However, efforts to replicate production of methane with M. palustre in our laboratory have been unsuccessful (S. Hensley, unpubl. data) and, in contrast to the initial report (Cheng et al., 2009)” (i.e. it can’t be done”)

New Technologies… • The three stages of a revolutionary idea, revisited…

– 1- It can’t be done

– 2- It's possible, but it's not worth doing (too $$)

– 3- It was my idea… (Morita, Lovley… et al. 2011)

27

2011: Morita et al. This shows….“for the first time… that direct electron transfer could be an important mechanism for electron exchange in some methanogenic systems…”

28

Connections between microbes-

Specific or non-specific?

Exoelectrogen

Exoelectrotroph

Microbial Electrolysis Cell (MEC):

– Produces hydrogen or methane

– Non-spontaneous reaction (energy needed)

– Completely anaerobic (no oxygen in reactor)

GCEP PROJECT Methane production in MECs by Electrochemical Methanogenesis

29

H2 Production Using Microbial Electrolysis Cells

H2

Cathode

CO2 e-

H+

e-

Bacteria

Anode

(Membrane is optional in MEC)

No oxygen in cathode chamber

PS

O2

No oxygen in anode chamber

>0.25 V needed (vs 1.8 V for water

electrolysis)

Liu, Grot & Logan (2008) Environ. Sci. Technol.

MECs

30

CH4 from electrical current using an MEC

Cathode

e-

Anode

PEM

Add methanogens to

the cathode H+

PS

CH4 CO2

CO2

H2O

O2

31 Cheng, Xing, Call & Logan (2009) Environ. Sci. Technol.

MECs used to harvest methane from renewable forms of electricity generation

Anaerobic digesters

(methane from organic matter)

MECs Methane from renewable electricity

Electricity

Goals of GCEP Project

• Identify the methanogens that work best in MECs

• Advance cathode technology to maximize methane generation

– Test a variety of catalysts for reducing overpotential and energy input

– Test different electrode materials

– Examine separators and methods to reduce oxygen cross-over

Methanogens in various METs

• Basic types of methanogens

– Hydrogenotrophic (use H2)

– Acetoclastic (use acetate)

• Hydrogenotrophic methanogens predominate in:

– MECs for H2 production from acetate

– MFCs with electricity generation from acetate

– MEC with direct electron transfer to methanogens with minimal H2 evolution (buffer)

Reduce overpotential using non-precious metal cathode catalyts

• Goal in MEC is to reduce total applied potential:

– Total Voltage = Cathode – Anode

• Anode:

– (Biotic anode produces 0.3 V)

– Abiotic anode needs: –0.8 V to split water, releasing O2

• Cathode

– Direct electron transfer: –1 V

– H2 evolution: No catalyst, need more than – 1V

– H2 evolution: with Catalyst, need less than – 1V

Find non-precious metal catalysts that are alternatives to Pt

• Pt

– Works great for H2 evolution reaction (HER)

but it is expensive and a precious metal

• Stainless steel (SS)

– Inexpensive, but it has a high overpotential

(large energy penalty)

– Therefore, a low capital cost, but high

operating cost

• Molybdenum disulfide (MoS2)

– Proposed to be a suitable HER catalyst, but

not tested under MEC-like conditions (Reference: Hinnemann et al., J. Am. Chem. Soc., 2005,

127, 5308)

Image: NIST Standard Reference Database No. 42 by

P. R. Watson, M. A. Van Hove, and K. Hermann. 36

Direct electron transfer

0

100

200

300

400

500

600

700

-1.4-1.2-1-0.8-0.6-0.4-0.20Meth

ane pro

duction (

mm

ol d

-1m

-2)

Cathode potential (V vs Ag/AgCl)

0

5

10

15

20

25

0 0.5 1 1.5Time (days)

Ga

s p

rod

uctio

n (

mL

)

Pt-SS

Mo-SS

H2 Evolution with MoS2 (0-48 g/m2)

Region of operation

Comparison at same applied potential

Cheng, Xing, Call & Logan (2009) Environ. Sci. Technol.

Tokash & Logan (2011) Int. J. Hydrogen Energy

Kim & Logan (2011) Proc. Nat. Academy Sci.

Tests underway with cathodes

38

• This 2-Liter MFC is in on display at the London Science museum, with the help of: – KAUST, Saudi Arabia

– University of Newcastle, UK

– VITO, Belgium

• See also the MFC webcam (live video of an MFC running a fan)

– www.engr.psu.edu/mfccam

39

Scaling up MFCs

39

40

Overall goal: compact reactor design

Assume: One anode-cathode module is 1 m2 projected area (height x width) and 10 cm thick

Design: Limited by cathode area, so in this example we achieve 10 m2/m3

10 cm

Result: 10 modules = 10 m2

10 cm

10 cm

10 cm

10 cm

100 cm

40 Logan (2012) Chem. Sus. Chem.

MFC Architecture

Logan & Elimelech (2012) Nature 41

42

MECs: Bench scale, Continuous flow

2.5 L with 1 day HRT (acetate fed)

Fluid Outlet

Power Sources

Fluid Pump

Reactor

Gas Bags

Scaling up MECs

Rader & Logan (2011) Int. J. Hydrogen Energy

43

MEC components (2.5 L reactor)

Schematic

Stainless Steel Mesh Cathodes

Half Graphite Fiber Brush

Anodes

Plastic Separator

Rader & Logan (2011) Int. J. Hydrogen Energy

44

MEC Performance- 2.5 L reactor

Current monitored through each anode, resulted in consistent performance

0

10

20

30

40

50

60

70

80

90

100

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18

Pe

rce

nta

ge

of T

ota

l G

as (

%)

Time (days)

H2

CH4

CO2

H2 intially produced, but it all was converted to CH4

Rader & Logan (2011) Int. J. Hydrogen Energy 44

45 45

MEC Field test : Penn State University @ Napa Wine Company

46

MEC Reactor that has 24 modules with a total of 144 electrode pairs (1000 L)

Cusick et al. (2011) Appl. Microbiol. Biotechnol. 46

47

Individual module performance of the MEC treating Wastewater

Predicted: 380 mA/module (total of 9.2 A)

Cusick et al. (2011) Appl. Microbiol. Biotechnol. 47

0

100

200

300

400

500

1 3 5 7 9 11 13 15 17 19 21 23

Module Number

Modula

r C

urr

ent (m

A)

H2 intially produced, but it all was converted to CH4

New Frontiers in Bioelectrochemical Technologies

48

• Reverse Electrodialysis Cells (RED) meeting MFCs & MECs MRCs

• Phosphorus/struvite recovery

• Microbial desalination cells [for water desalination without electrical grid energy]

New Energy Sources Available using Microbial Electrochemical Technologies (METs)

• Cellulose Biomass Energy

– 600 GW available (based on 1.34 billion tons/yr of lignocellulose)

• Wastewater organic matter (WW)

– 17 GW in wastewaters (Savings 3x15 + 17 = 62 GW net)

• 2-5 kWh/m3 for “typical” domestic wastewater

• Salinity Gradient Energy- Natural Waters (global values)

– 980 GW (from the 1900 GW available from river/ocean water)

– 20 GW available where WW flows into the ocean

• 0.75 kWh/m3 for Typical Seawater-Freshwater

• 1 kWh/m3 using Ammonium Bicarbonate (waste heat)

• 14.1 kWh/m3 for Dead Sea-Freshwater

• Waste Heat Energy

– 500 GW from industrial waste heat

– 1000 GW from power production (33% efficient power plants)

(Does not include solar and geothermal energy sources)

49 Logan and Rabaey (2012) Science Logan and Elimelech (2012, Nature

50

Salinity Gradient Energy

+ =

270 m of Hydraulic Head

Oceanside WWTPs and

Rivers could produce

980 GW

GETTING MORE ENERGY

Electrodialysis (ED) stack

1 cell pair = Diluate cell + Concentrate cell

Anode

Concentrate

e–

2-cell pair system: 1 e – 2 cations and 2 anions

5-cell pair system: 1 e – 5 cations and 5 anions

2 cell pairs

CEM Cathode

+

AEM

Concentrate Diluate

CEM

+

AEM

Concentrate Diluate

51

Reverse electrodialysis (RED)

Each pair of seawater + river water cells ~0.1 – 0.2 V

+

River water

CEM

+

AEM

River water Seawater

+

+ +

+ +

+

+

+

+

+

– +

Salinity difference produces ion transport electrical current

Electric current

52

Batteries = motion of ions & electrons

e–

e–

e–

+ + +

1.5 V per battery

6 V (4 batteries)

54

MFC + RED = MRC (Microbial RED Cell)

Air cathodeBrush

anode5CEMs6AEMs

Diluate

CEMAEMCEM

Silicon gasket

seawater

Kim & Logan (2011) ES&T (MRCs)

New Energy Sources Available using Microbial Electrochemical Technologies (METs)

• Wastewater organic matter (WW)

– 17 GW in wastewater (Savings 3x15 + 17 = 62 GW net)

• Cellulose Biomass Energy

– 600 GW available (based on 1.34 billion tons/yr of lignocellulose)

• Salinity Gradient Energy- Natural Waters (global values)

– 980 GW (from the 1900 GW available from river/ocean water)

– 20 GW available where WW flows into the ocean

• Waste Heat Energy

– 500 GW from industrial waste heat

– 1000 GW from power production (33% efficient power plants)

(Does not include solar and geothermal energy sources)

55 Logan and Rabaey (2012) Science Logan and Elimelech (2012, Nature

NH4HCO3

NH3 CO2

High concentration

(HC) of NH4HCO3

Low concentration (LC) of NH4HCO3

56

Freshwater

NaCl

270 m

NH4HCO3

370 m

Use waste heat to create artificial “salintity gradient” energy using ammonium bicarbonate

Cusick, Kim & Logan (2011) Science

5CEMs

Exoelectrogens

6AEMs

H2 gas

Seawater

e− transfer

MREC: Microbial RED Electrolysis Cell

57 Kim & Logan (2011) Proc. Nat. Academy Sci.

58 Cusick, Kim & Logan (2011) Science

RED Stack (abiotic) with NH4HCO3 Could be used as Energy Source for CH4 Production

• Abiotic anode with water splitting

• Methanogens on cathode to use H2 gas produced CH4

59

Thanks to students and researchers in the MFC team at Penn State!

Current research sponsors KAUST (2008-2013); Air Products and Chemicals, Inc. (2006-2012); DOE- NREL (2008-2012); Chevron (2012-2013); Arpa-E (2013); DOE (2012-2015); DOD/SERDP (2012-2015); GCEP/Stanford (2012-2014)

60

Additional Information

Email: [email protected]

Logan webpage: www.engr.psu.edu/ce/enve/logan/

International MFC site: www.IS-MET.org

YouTube: YouTube/user/MFCTechnology

Twitter: MFCTechnology

MFC webcam: www.engr.psu.edu/mfccam

(live video of an MFC running a fan)


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