NIST neutron imaging facility for fuel cell imaging. David Jacobson Daniel Hussey (NIST) Muhammad...
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Transcript of NIST neutron imaging facility for fuel cell imaging. David Jacobson Daniel Hussey (NIST) Muhammad...
NIST neutron imaging facility for fuel cell imaging.
David JacobsonDaniel Hussey (NIST)
Muhammad Arif (NIST)
Jon Owejan (GM – FCA)Thomas Trabold (GM – FCA)
Daniel Baker(GM – FCA)Satish Kandlikar (RIT)
Fuel CellsNeutron Imaging
National Institute of Standards and Technology Technology AdministrationU.S. Department of Commerce
Support
• DOE – Energy Efficiency and Renewable Energy– Nancy Garland Program Coordinator
• DOC – NIST– NIST Directors office competence funding
• NIST Intramural Advanced Technology Program– Gerald Caesar
• NIST Physics Laboratory (www.physics.nist.gov)• NIST Center for Neutron Research (www.ncnr.nist.gov)
– Patrick Gallagher (director), Charlie Glinka and many others who provide tremendous technical assistance.
Variable beam diameter Variable resolution
Intense neutron beam Single or multi-stack cell
OLD NIST Neutron Imaging Facility
Beam Stop
Cable Ports
Drum shutter and collimator
6 meter flight
path
LN Cooled Bismuth Filter
2.13 mCable Ports
Steel pellet and wax filled shield walls
1. New facility 14.6 m2 (157 ft2) floor space2. Accessible 2 meters to 6 meters3. Variable L/d ratio
1. At 2 m L/d = 100 → ∞2. At 6 m L/d = 300 → ∞
4. Maximum Intensity without filters1. At 2 m = 1 x 109 n cm-2 sec-1 (L/d =100), 8 cm diameter beam size2. At 6 m = 1 x 108 n cm-2 sec-1 (L/d =300), 25 cm diameter beam size
5. Maximum Intensity with 15 cm LN cooled Bismuth Filter1. At 2 m = 2 x 108 n cm-2 sec-1 (L/d =100), 8 cm diameter beam size2. At 6 m = 2 x 107 n cm-2 sec-1 (L/d =300), 25 cm diameter beam size
6. Support for fuel cell experiments1. Hydrogen flow rates 18.8 lpm2. 50 cm2 fuel cell controller with 5 lpm flow rates.3. Nitrogen, Air, Coolant and Hydrogen Venting
7. Detection capabilities1. Real-Time Varian Paxscan, 30 fps @ 0.254 mm pitch or 7.5 fps @ 0.127 mm pitch2. Second Varian detector will upgrade to 30 fps @ 0.127 mm pitch3. 2048 x 2048 Cooled (50° C) Andor CCD based box with 30 cm maximum field of view.4. 2 more 1024 x 1024 Cooled (30° C) Apogee CCD based
8. Sample Manipulation1. Motor controlled2. 5 axis tomography capability
9. Phase imaging capable10. Open for business January-March 2006
NEW Neutron Imaging Facility (NIF)
1. New facility 14.6 m2 (157 ft2) floor space2. Accessible 2 meters to 6 meters3. Variable L/d ratio
1. At 2 m L/d = 100 → ∞2. At 6 m L/d = 300 → ∞
4. Maximum Intensity without filters1. At 2 m = 1 x 109 n cm-2 sec-1 (L/d =100), 8 cm diameter beam size2. At 6 m = 1 x 108 n cm-2 sec-1 (L/d =300), 25 cm diameter beam size
5. Maximum Intensity with 15 cm LN cooled Bismuth Filter1. At 2 m = 2 x 108 n cm-2 sec-1 (L/d =100), 8 cm diameter beam size2. At 6 m = 2 x 107 n cm-2 sec-1 (L/d =300), 25 cm diameter beam size
6. Support for fuel cell experiments1. Hydrogen flow rates 18.8 lpm2. 50 cm2 fuel cell controller with 5 lpm flow rates.3. Nitrogen, Air, Coolant and Hydrogen Venting
7. Detection capabilities1. Real-Time Varian Paxscan, 30 fps @ 0.254 mm pitch or 7.5 fps @ 0.127 mm pitch2. Second Varian detector will upgrade to 30 fps @ 0.127 mm pitch3. 2048 x 2048 Cooled (50° C) Andor CCD based box with 30 cm maximum field of view.4. 2 more 1024 x 1024 Cooled (30° C) Apogee CCD based
8. Sample Manipulation1. Motor controlled2. 5 axis tomography capability
9. Phase imaging capable10. Open for business January-March 2006
NEW Neutron Imaging Facility (NIF)
Hydrogen Safety
• Computational Fluid Dynamics modeling
– Free software
– NIST Fire Dynamics Simulator (FDS)
– http://www.fire.nist.gov/fds/
• Release point in reactor confinement building
• Extremely high buoyancy turbulently mixes hydrogen resulting in low concentrations throughout room
Diffusion coefficient at STP in air = 0.61 cm2 s-1
Diffusion velocity at STP in air 2 cm/s
Buoyant velocity at STP in air = (1.9 m/s to 9 m/s)
Explosive equivalent at 28% H2 in air 1 g H2
= 24 g TNT
Lower explosive limit by volume fraction 4%
Upper explosive limit by volume fraction 77%
Hydrogen Plume 22 lpm
Modeling Building ReleaseM
ass (kg/kg) x 10-4
Modeling the Release Point
Below 1 meter a maximum of 68 mg of hydrogen is expected to be within the range of 77% to 4% and so an unlikely detonation of such a mixture is expected to have an explosive yield similar to a few firecrackers.
Lower flammability limit
Upper flammability limit
Neutron scintillator• Converts neutrons to light 6LiF/ZnS:Cu,Al,Au
6Li + n0 4He + 3H + 4.8 MeV
• Light is emitted in the green part of the spectrum
• Neutron absorption cross section for 6Li is huge (940 barns)
CCD
Scintillator
Neutrons inGreen light out
• Neutron to light conversion efficiency is 20%
Real-Time Detector Technology
• Amorphous silicon • Radiation hard• High frame rate (30 fps)• 127 micron spatial resolution• Picture is of water with He
bubbling through it• No optics – scintillator directly
couples to the sensor to optimize light input efficiency
Neutron beam
scintillator
aSi sensor
Side view
Readout electronics
Scintillator aSi sensor
Front view
Helium through water at 30 fps
Hydrogen Fuel Cells
Water Sensitivity
=
Wet cuvet Dry cuvet water only
=-ln
• Steps machined with 50 micron.• CCD camera exposure of 1 s yields a
sensitivity of 0.005 g cm-2 s-1
• After 100 s a factor of 10 improvement gives 0.0005 g cm-2 s-1
• New amorphous silicon detector should have a least a factor of 7 improvement in temporal sensitivity
1 s exposure time
50 micron water thickness
Sensitivity required for fuel cells (assumes maximum water content)
• Flow fields 0.020 g cm-2
• Gas diffusion media 0.012 g cm-2
• Electrode 0.0005 g cm-2
• Membrane 0.0005 g cm-2
Single Cell Assembly
Flow Fields
Current Collectors
Compression Plates
Locating Pins
Gaskets - GDM - MEA
PEM Fuel Cell Operation
200 m 200 m25 m
15 m 15 m
Flow rates of reactants
• Definitions
– J : Current density Amp cm-2
– A : Active area of cell
– n : (mols electrons)/(mol reactant)
RatioStoich1
RateFlowVol.reactant
ideal
tot
p
pA
nF
J
– F : Farday constant 96484 Coulomb mol-1
ideal : ideal molar gas density (1/22400) mol cm-3
– Stoich. Ratio
Fuel Cell Performance
1.2H2 + ½ O2 H2O
Neutron sensitive screen
Point Source
Fuel cell
Orientation of Cell in all Images
Cathode
Anode
Inlet
Inlet
channel width = 1.4 mm; channel depth = 0.5 mm; land width = 1.5 mm
Orientation of Cell in all Images
Cathode
Anode
Inlet
Inlet
channel width = 1.4 mm; channel depth = 0.5 mm; land width = 1.5 mm
Amount of Water Possible
Volume of one channel = 0.176 cm3
Volume of one flow field = 0.980 cm3Volume of anode DM + cathode DM (70% porosity) + electrode (50% porosity) + membrane (20% uptake) = 1.160 cm3
Max water volume possible = 3.12 cm3
Volume of one port = 0.050 cm3
Channel Geometries
Channel Geometries explored
Triangular X-sect
Rectangular X-sect
94°
1.37 mm 1.45 mm
0.76
mm
1.37 mm 1.45 mm
0.38
mm
X-sect Area = 0.52 mm2
Triangular X-sect
Rectangular X-sect
94°
1.37 mm 1.45 mm
0.76
mm
1.37 mm 1.45 mm
0.38
mm
X-sect Area = 0.52 mm2Rectangular X-sect
94°
1.37 mm 1.45 mm
0.76
mm
1.37 mm 1.45 mm
0.38
mm
X-sect Area = 0.52 mm2
• Rectangular channels– Water flow is laminar tending to constrict and plug the channels– Water plugs form as large slugs and can be difficult to remove.
• Triangular channels– Water stays at the corner interface with the diffusion media leaving the
apex of the channel more clear.– Water tends to come out in smaller droplets instead of large slugs,
which require a high pressure differential to remove
Flow Field Properties
Rectangular X-sect
Triangular X-sect
Gold Coated w/PTFEContact Angle = 93°
Graphite Uncoated Gold Coated Gold w/PTFE
0.01170 ohm/cm2 0.00044 ohm/cm2 0.00052 ohm/cm2
Gold Uncoated Contact Angle = 50°
Contact Resistance Values
94°
1.37 mm 1.45 mm
0.7
6 m
m
1.37 mm 1.45 mm
0.3
8 m
m
Xsect Area = 0.52 mm2
Cathode Channel Cross Section Geometry and Surface Energy Study
Test Parameters• 100% Humidified• 80°C• 100kPag • Approx. 150% exit RH• 1 Hr 0.6V Start Up• Gore 25m 0.4/0.4 • Toray 060/090 Teflon
ground
Cathode Flow Field Variation
(Anode constant rect. x-sect no coating)
• 2 Channel Geometries– Rectangular– Triangular
• 2 Surface Energies– Gold– Gold coated ionic PTFE
• 4 Cathode FFs Total– Rect and Tri (gold only)– Rect and Tri (gold coated w/
ionic PTFE)
Rectangular Comparison 0.5 A/cm2
Uncoated PTFE Coated
Triangular Comparison 0.5 A/cm2
Uncoated PTFE Coated
Geometry Comparison 0.5 A/cm2
Uncoated Triangular
Uncoated Rectangular
Total Water Mass TendsWater Mass Comparison
0
0.10.2
0.3
0.40.5
0.6
0.7
0.80.9
1
0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6Current Density (A/cm2)
Wate
r M
ass (g)
Rect No PTFERect PTFETri No PTFETri PTFE
Flow Field Study Performance Data
0.35
0.45
0.55
0.65
0.75
0.85
0.95
0 0.2 0.4 0.6 0.8 1
I (A/cm2)
Vo
lta
ge
(V
)
Toray Rect No PTFE
Toray Rect PTFE
Toray Tri No PTFE
Toray Tri PTFE
Conclusions• Neutron imaging is an important and effective tool to study fuel cells in situ.
• Computational fluid dynamics can be an extremely useful tool in analyzing safety of hydrogen gas released in a reactor hall.
• Channel surface energy has a consistent effect on water slug shape and size. Higher contact angle increases average water mass retained, but distribution of smaller slugs more evenly in the channel area increases performance.
• Triangular cross-sectional geometry accumulates water in the corners adjacent to diffusion media. The center of the channel does not become obstructed by stagnant slugs.
Key Observations and Conclusions (cont’)Channel surface energy has a consistent effect on water
slug shape and size. Higher contact angle increases average water mass retained, but distribution of smaller slugs more evenly in the channel area increases performance.
• Triangular cross-sectional geometry accumulates water in the corners adjacent to diffusion media. The center of the channel does not become obstructed by stagnant slugs.