water transport exploratory studies - us department of...
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Water Transport Exploratory Studies Office of Hydrogen, Fuel Cells, and Infrastructure Technologies 2007
kickoff meeting
February 13-14, 2007DOE Forrestal Building
Rod BorupMukundan Rangachary, Bryan Pivovar, Yu Seung Kim, John
Davey, David Wood, Tom Springer, Muhammad Arif , Ken Chen, Simon Cleghorn, Will Johnson, Karren More, Peter
Wilde, Tom Zawodzinski
Los Alamos National LabThis presentation does not contain any proprietary or confidential information
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Objectives• Develop understanding of water transport in PEM
Fuel Cells (non-design-specific) • Evaluate structural and surface properties of materials
affecting water transport and performance • Develop (enable) new components and operating
methods • Accurately model water transport within the fuel cell• Develop a better understanding of the effects of
freeze/thaw cycles and operation • Present and publish results
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Technical Targets/Barriers
N. Vanderborgh, 1994 “...... it’s all about water management ...”
≤1.550kPa (absolute)
Inlet water vapor partial pressure
20102004UnitsCharacteristic
Technical Targets:
Status
Membranes
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Approach• Develop understanding of water transport
– Experimental measurement and testing – Characterization – Modeling
• Evaluate structural and surface properties of materials affecting water transport and performance – Measure/model structural and surface properties of material
components – Determine how material properties of GDL, MPL, catalyst layers
& interfaces affect water transport (and performance) – Determine properties change during operation (degradation effects)
• Develop (enable) new components and operating methods – Prevent flooding (high power operation) – Prevent dehumidification (low RH operation - transportation)
• Develop a better understanding of the effects of freeze/thaw cycles and operation – Help guide mitigation strategies.
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Prior Work
• Prior relevant work includes (LANL):– Modeling of mass transport losses – Freeze/thaw – GDL characterization (durability)
• More team relevant prior work – Modeling – Electro-osmotic drag measurements
– MEA / GDL manufacturing (etc.) – Characterization – Neutron imaging
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0.5
0.6
0.7
0.8
0.9
1.0
MEA Overpotential Losses (Modeling to delineate degradation losses)
• Increase in cathode GDL mass-transport Overpotential
• Hydrophobicity loss
Constant Current Operation @ 0.90 A/cm2
η
η
η
Vi
( )
⇒T⇒ / 15
⇒⇒ /( /cm2
Catalyst-Layer Mass-Transport Improvement from More
Hydrated Electrode Ionomer
Time, tx,GDL
Time, tx,elec
Time, ORR
Time, R-free
Solid Symbols = 0 hr Beginning of LifeGray Symbols = 536 hr Durability Testing
White Symbols = 1014 hr Durability Testing
cell = 80°C Gas Pressure = 15
psig (A/C) RH = 75% / 75% (A/C) Flow Rates = 1.2 2.0
A/C) × 1.5 A equiv.
0.45
• Decrease in cathode electrode mass transport overpotential
• Decrease in HFR
0.40
0.35
0.30
• Increase in ORR overpotential
• S.A. decrease η (V
)
0.25
0.20
0.15
0.10
0.05
0.00
-0.05 0.00 0.25 0.50 0.75 1.00 1.25 1.50
Current Density (A/cm2)
V i R
-free
(V)
Changes in mass-transport (Æ water management)
0.4
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GDL Fiber Chemistry and Contact Angle96
78
80
82
84
86
88
90
92
94
Unaged N2, 60°C,
)
f
77
81
85
89
93
97
(θ °)
Hy
Unaged Unaged N2, 80°C, Air, 60°C, Air, 80°C,
Con
tact
Ang
le (d
eg Hydrophobic
Hydrophilic
Increasing Aggressiveness oAging Environment
Con
tact
Ang
le (d
eg)
5 wt% PTFE 20 wt% PTFE
Plain TGP-H Fiber = 80.3
Increasing Graphitization Temperature
drophobic Hydrophilic
SGL GDL 24 Spectracorp 2050-C Toray TGP-H TGP-H 120 TGP-H 090 TGP-H 090 460 hr; 460 hr; 680 hr; 680 hr; GDL Graphite Fiber Type (Plain) #1 (17.2 #2 (17.0 TGP-H 060 TGP-H 090 TGP-H 060 TGP-H 090
wt% FEP) wt% FEP) (17.2 wt% (16.7 wt% (16.9 wt% (17.0 wt% FEP) FEP) FEP) FEP)
• Fiber graphitization can increase single-fiber contact angle ~ 10°
• Both graphitization T and PTFE loading can change the liquid-water wetting regime of the GDL substrate.
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Before/After SEM Comparison of PTFE Microstructure of GDL
Fresh After Testing
• Loss of definition delineating the individual PTFE particles – (typically shaped like and ellipsoid and 200-500 nm diameter).
• Features could be associated with changes in liquid water transport characteristics or carbon fiber surface changes.
• Features are also affected by sintering time and temperature.SIGRACET GDL 24BC
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Freeze/Thaw cycling
GDL: carbon paper (SGL), Active area: 5 cm2
Confocal laser imaging Dr. Mike Hickner Sandia National Lab
• No systematic degradation observed up to 45cycles • Mechanical Failure @ 45 cycles • Fiber breakage at land/channel edge is a potential failure mechanism
• More tests required to investigate failure mechanisms
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Water Transport Exploratory Studies Project initiated in FY2007 for 4 years
Segmented cell studies/
transient operation
Water balance thawing
Conductivity of
down to -40 oC
water content steady-state and transient conditions
2007 2008 2009 2010
Quasi-3D model for simulating electrode layers
in situ water/ice imaging neutron
Start GDL surface properties
aging effects
100 freeze/thaw
crystallinity
MEA properties < 0 oC / effect of freeze/thaw cyclingshutdown
cycles on ionomer Component water removal during
Qtr. 4 based on Reasonable 1D Prediction)
Qtr. 6
Qtr. 10
Qtr. 10
Go/No-Go
o
oC) will be explored in further studies.
Demonstrate 1-D model validity in case studies. (Go/No Go Decision to Proceed to 3D
Demonstrate start up fuel cells from -20 C. Only materials and conditions that meet this decision criterion (start up from –20
z-direction imaging capability by neutrons. If not capable of performing tomography at this point, we will conclude the neutron imaging work.
Electro-osmotic drag coefficient measurements. Activity gradient cells vs. electrophoretic NMR measurements.
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Organizations / Partners
• Los Alamos National Lab – (Lead: experimental measurements, modeling)
• Sandia National Laboratory (modeling) • Case Western Reserve University
(characterization, modeling) • W. L. Gore and Associates, Inc. (MEAs) • SGL Carbon Group (GDLs, MPLs) • Oak Ridge National Lab (characterization)• National Institute of Standards and Technology
(neutron imaging)
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Budget
DOE Cost Share Recipient Cost TOTAL Share
$6,550,000 $290,811 $6,840,811
96% 4% 100%
FY07 LANL $1000k
Industrial Partners (Gore/SGL/CWRU) $300k Other National Labs (SNL/ORNL) (?) $350k FY07 Total 1650
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Input / Needs• Automotive OEM (FC Tech Team) definition of
inlet RH as a function of power/time during operating drive cycles
Wat
ts
Volts
20 min
AM
PS
W
atts
Volts
W
atts
Am
ps
6 min
VO
LTS