Fuel Cells for Renewable Energy and for Transportation D17-12 Dec 24...1 Fuel Cells for Renewable...
Transcript of Fuel Cells for Renewable Energy and for Transportation D17-12 Dec 24...1 Fuel Cells for Renewable...
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Fuel Cells for RenewableEnergy and for Transportation
IFCBC Meeting 24.12.2006
Prof. E. PeledSchool of Chemistry
Tel Aviv University, Israel
TAU PU for laptops
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Outline
• The problem: dependence on oil import and ecologydamages.
• The solution: renewable energy and alternative fuels(hydrogen (the Hydrogen Economy), alcohols).
a) FC systems for cars and small electric vehicles(scooters)
b) RFC and redox battery (VRB) for renewable-energystorage and load leveling.
• World activity and markets .
• Factors that inhibit PEM FC commercialization – thecost of membranes and platinum catalysts.
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The goal: reducing oil import and producing “green” energy
• Israel imports over 95% of its oil.• Most oil reserves are located in politically unstable states.• The solution: to shift power production to renewable energy and
to develop vehicles powered by renewable energy and by newfuels.
• An efficient and “green” way to convert fuels into energy is bythe use of fuel cells.
• Most leading car manufacturers are developing FC or FC-hybridcars.
• Alternative fuels being considered are hydrogen and alcohols,with most of the effort going into the development of hydrogenFCs.
• Alcohol-fed FCs have some advantages over hydrogen FCs.• Alcohols can be produced from natural gas, which has a supply
reserve of over 50 years and is produced by biologicalprocesses.
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Basic Operation of a PCM Fuel Cell
• Chemical ReactionProduces Electricity
• Fuel - H2, O2
• By-Product - H2O
• Electrons Released atAnode
• Electrons Collected atCathode
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PEM fuel cells
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PEM FC stack
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Possible System Configurations: which is the best?
Methanol
Gasoline
DirectMethanolOr EG FC
H2-FCMethanolReformer
GasolineReformer
CompressedHydrogen
Hydrogen
SolidHydride
Hydrogen
MethanolTank
GasolineTank
Methanolor EG Tank
Methanolor EG
DOEendedfunding
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World Activity, Investments andMarkets
• Over a billion dollars per year investments.
• Estimated production rate of more than a millionFC cars per year by about 2015.
• Very large national and private-sector FCprojects in most industrial countries, includingIndia and China.
• Most car manufacturers are involved; some havealready demonstrated FC EVs and FC–batteryhybrid EVs.
• Several FC-powered scooter projects.
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FCEVsRecent GM PEM FC Stack For EVs (9.2004)
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DMFC (up) and hydrogen FC (down) Scooters
2006
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The cost problem of PEM FC for EVs
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Performance IssuePerformance Issue -- Voltage Losses in StateVoltage Losses in State--ofof--thethe--Art HArt H22/air Fuel Cells/air Fuel Cells (0.4 mgPt/cm2)
0.55
0.60
0.65
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1.00
1.05
1.10
1.15
0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 i [A/cm2]
Ec
ell
[V]
Eeq=1.169 V
(act. pH2, pair)
hOR
DEohmic
hmass-tx
= iR-free and mass-tx free
= mass-tx free Ecell
= measured Ecell
=50%mass-tx free Ecell
Eloss at 1.5A/cm2:
400 mV (68%)
70 mV (12%)
120 mV (20%)
air
major losses due to poor cathode kinetics (ORR) minor losses by ohmic resistance gains through improved flowfields/diffusion media (mass-tx)
From:
o
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0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0 2.20.0
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200C, 5psi H
2 H2Air4-0103
400C, 5psi H
2 H2Air4-0203
600C, 7psi H
2, 7psi air
H2Air4-0503
800C, 30psi H
2, 30psi air
H2Air4-0803
Vo
ltag
e[V
]
Current density [A/cm2]
Po
wer
den
sit
y[W
/cm
2]
TAU NP-PCM-Based H2/Air Fuel Cell Performanceno air humidification, 2 mg Pt/cm2 on each electrode, 2M triflic acid, PVDF
based NP-PCM (EV goal: 0.9W/cm2 at 0.65V and 0.1 mgPt/cm2).
o
o
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Recent progress in MEA development for EVs
• Improved performance and lower Ptloading (currently about 0.4 mgPt/cm2).
• Improved membrane durability.
• Better and more stable catalysts for ORR(Nina).
• Better corrosion-resistant carbon supportfor the Pt nanoparticles.
• More stop-and-start (load-change) cyclesand better cold-start.
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Interface, vol 14, #3,
Mathias et. al (2005).
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Why use Pt-alloys? Lower area loss
Interface,vol 14, #3,Mathias et.al (2005).
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Development goals for EV FCs
• Low-cost and low-RH (25-50%) high-temperaturemembrane (above 120oC) in order to reduce Ptloading and to reduce the size and power loss of thecooling system (twenty research groups in the USA).
• Target cost for catalysts: less than $10/kW• (or 0.2 gPt/cm2 (total) at $35/g Pt)• More active (by factor of only 3-4) and more stable
ORR catalysts.• Better understanding of the MEA-degradation
mechanism and of the proton-conductionmechanism at low RH.
• Hydrogen cost will be at least twice that of gasoline.Thus FC efficiency must be twice that of ICE.
• ICE delivers about 1kW/l, FCs must meet this value.• The best solution for EVs is a FC-battery hybrid
system.
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Development Goals for Small FC-powered EVs(e.g. scooters)
• The preferred fuels for this application are methanolor ethylene glycol (using a direct-oxidation FC).
• TAU novel NP-PCM based DOFC demonstrated0.5W/cm2 and 0.3 W/cm2 for DMFC and DEGFCrespectively.
• Much more active fuel-oxidation catalysts and alsoORR catalysts are needed.
• Pt loading must be reduced, preferably to less than1mg/cm2 (today it is 3-8).
• The corrosion (degradation) rate of the Pt-Ru fuel-oxidation catalyst must be reduced.
• A low-cost and low-RH (25-50%) high-temperaturemembrane is needed.
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TAU 50cm2 single-cell DMFC (or H2/air).
This cell size can be used to build a 1kW 70-cell stackwhich will have a volume of about 2-4 liters (enough to
power a scooter).
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Storage of solar and wind powerand load leveling
• Hydrogen bromine RFC for remote sites
• Vanadium Redox Battery (VRB)
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• The market is huge, many billions of dollars.
• The problem:• Today, all electric power-storage systems are too
expensive for large solar and wind generators andfor load leveling.
• The major problem is the cost of the chemicals usedfor electrical-energy storage.
The solution:• The TAU hydrogen-bromine (RFC) energy-storage
system is based on low-cost materials. Thus, whenfully developed, it will be an enable technology forlarge solar- and wind-energy storage systems andfor load leveling.
Commercialization of large solar andwind electric-power storage systems
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VRB system scheme
PEM
V 2+ / V3+V 4+ / V 5+
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VRB-ESS
Stacks
10 KWh ESS
2 MWh ESS
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HBr – Br2 aqueoussolution tank Hydrogen tank
Electrolyzer2HBr H2 +Br2
Fuel cellH2 +Br2 2HBr
LiquidPump
Compressor
Power outPower in –solar, wind
Schematic diagram for solar / wind energy storagesystem using regenerative H2 – Br2 fuel cell
H2
H2
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0.0 0.4 0.8 1.2 1.6 2.0 2.4 2.80.0
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250C
300C
500C
800C
Vo
ltag
e[V
]
Current density [A/cm2]
Po
wer
den
sit
y[W
/cm
2]
TAU NP-PCM based H2/Br2 FC - Effect of temperature onthe performance .
Ambient H2 pressure, no H2 humidification, stoich H2 = 2; 0.6M Br2, 1M HBr; 100µPVDF based NP-PCM. Anode: 1 mgPt/cm2 , cathode: 1.5 mgPt/cm2
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Scaling Up Production of NP-PCM- Continuous Coater (15m2/h)
33cm wide 2G NP33cm wide 2G NP--PCMPCM
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Comparison of Hydrogen-Bromine RFC with VRB
• VRB Power Systems produces and sells a vanadium-redox-battery (VRB) system for electrical-energy storage.These systems cost between $350-$600 per kWh, withsizes ranging from a few hundred kWhs to MWh-sizesystems
• They have just sold $6M systems to Ireland for wind-energy storage.
• The cost of bromine is much lower than that of vanadiumoxides - $3-6 per kWh compared to over $40/kWh* (upto $120/kWh) in the case of VRB.
• Conclusion: The TAU hydrogen bromine RFCsystem, based on a low cost NP-PCM, will be anenable technology (when fully developed) for solar,wind energy storage and load leveling.
* 5kg(V2O5)/kWh at $8/kg(V2O5); 3.3kg(Br2)/kWh at $0.9/kg (Br2) or 100% excess as bromide
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Summary
• In order to meet the FC cost targets for EVs we needORR catalysts that are four times more active andstable and/or high-temperature membranes.
• Methanol and ethylene glycol are promising fuels atleast for small EVs. They have some advantages overhydrogen; however better fuel oxidation and ORRcatalysts are required.
• TAU demonstrated the world most powerful directmethanol and ethylene glycol fuel cells.
• Israel and Western countries need alternative energysources.
• Broad use of solar and wind electric generators (as wellas load leveling) need large and low-cost storagesystems.
• The low-cost TAU NP-PCM-based high power hydrogen-bromine RFC appears to be an enable technology forthese applications.