Fuel Cells for Renewable Energy and for Transportation D17-12 Dec 24...1 Fuel Cells for Renewable...

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1 Fuel Cells for Renewable Energy and for Transportation IFCBC Meeting 24.12.2006 Prof. E. Peled School of Chemistry Tel Aviv University, Israel TAU PU for laptops

Transcript of Fuel Cells for Renewable Energy and for Transportation D17-12 Dec 24...1 Fuel Cells for Renewable...

Page 1: Fuel Cells for Renewable Energy and for Transportation D17-12 Dec 24...1 Fuel Cells for Renewable Energy and for Transportation IFCBC Meeting 24.12.2006 Prof. E. Peled School of Chemistry

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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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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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ltag

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]

Current density [A/cm2]

Po

wer

den

sit

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/cm

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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.