PEM Fuel Cell System Manufacturing Cost ... - Austin Power Eng
Transcript of PEM Fuel Cell System Manufacturing Cost ... - Austin Power Eng
Austin Power Engineering LLC 1 Cameron St
Wellesley, MA 02482 USA
www.AUSTINPOWERENG.com
© 2015 Austin Power Engineering LLC
PEM Fuel Cell System Manufacturing Cost Analysis for Automotive Applications
Yong Yang
President
November 17, 2015
1 2015 YY
Have been working on fuel cell manufacturing cost modeling for US DOE, UK Carbon Trust, and commercial clients since 2002.
Introduction Overview
2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 2012 2013
US
DOE
TIAX
Chief Manufacturing cost model developer
Austin Power
Chief Manufacturing cost model developer
US DOE
UK Carbon Trust
Commercial Clients
Fuel Cell / Hydrogen Manufacturing Cost Modeling
2014 2015
2
Approach Manufacturing Cost Modeling Methodology
This approach has been used successfully for estimating the cost of various technologies for commercial clients and the DOE.
Technology
Assessment
Manufacturing
Cost Model
Scenario
Analyses
Verification &
Validation
• Literature research • Definition of system and component diagrams • Size components • Develop bill-of-materials (BOM)
• Define system value chain • Quote off-shelve parts and materials • Select materials • Develop processes • Assembly bottom-up cost model •Develop baseline costs
• Technology scenarios • Sensitivity analysis • Economies of Scale • Supply chain & manufacturing system optimization • Life cycle cost analysis
• Cost model internal verification reviews • Discussion with technical developers • Presentations to project and industrial partners • Audition by independent reviewers
Membrane
8.0%
Stack
Conditioning
2.7%
Seal
8.4%
Balance of Stack
2.4%
Bipolar Plate
26.1%
GDL
5.1%
Electrode
41.0%
Stack Assembly
6.3%
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Anode Ink
Anode Side
Catalyst Layer
Membrane
Processes
Cathode Side
Catalyst Layer
Cathode Ink
Hot Press
Lamination
Purchased GDL
Purchased GDL
Pt
Pt
Nafion®
Ionomer
99.9% 98.5%
99.9% 98.5%
99% 98.5%
100% 98.5%99% 98.5%
99% 98.5%
100% 100%
100% 100%
100% 100%
100% 100%
100% 100%
0
10,000
20,000
30,000
40,000
50,000
60,000
70,000
80,000
3-Year TCO 5-Year TCO 10-Year TCO 15-Year TCO
To
tal
Co
st
of
Ow
ers
hip
($
)
PEMFC Plug Hybrid Vehicle
Full Battery Electric Vehicle
3
Combining performance and cost model will easily generate cost results, even when varying the design inputs.
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Process Simulation
Energy requirements
Equipment size/ specs
Product Costs
Product cost (capital,
O&M, etc.)
Conceptual Design
System layout and
equipment requirements
Capital Cost Estimates Site Plans
Safety equipment, site
prep, land costs
High and low volume
equipment costs
Air (POX only)
Nat. Gas
Water
Fuel
Reformer PSA
H2-rich gas
H2-poor gas
Catalytic
Burner
HeatCold
Water
99.99% pure H2
Low
Pressure
Storage
Medium
Pressure
Storage
High
Pressure
Storage
Flow
cntrlr
Flow
cntrlrFlow
cntrlr
Dispenser
To Vehicle
CO2
H2O
Compressor with intercoolers
Cooling
Tower
Process cost
Material cost
Tape Cast
Anode
Powder Prep
Vacuum
Plasma
Spray
Electrolyte
Small Powder
Prep
Screen
Cathode
Small Powder
Prep
Sinter in Air
1400CSinter in Air
Forming
of
Interconnect
Shear
Interconnect
Vacuum
Plasma
Spray
Slurry
Spray
Screen
Slurry Spray
Slip Cast
Finish Edges
Note: Alternative production processes appear in gray to the
bottom of actual production processes assumed
Braze
Paint Braze
onto
Interconnect
Blanking /
Slicing
QC Leak
Check
Interconnect
Fabrication
Electrolyte CathodeAnode
Stack Assembly
Fuel Station Perimeter
Electrolyzer or SMR,
High-Pressure
Compressor
H2 High Pressure
Cascade Storage
System
Gaseous Fuel
Dispensing Islands
Underground Piping with shared conduit
Vent
Building
Covered Fueling Island
CNG High Pressure
Cascade Storage System
Fire Detector
Walls with minimum fire rating of 2 hours
Wall openings (doors & windows)
Building intake vents
Adjoining property that can be built on
Public sidewalks, parked vehicles
Streets
Railroad tracks
Other flammable gas storage
5 ft
25 ft
50 ft
10 ft
15 ft
10 ft
15 ft
10 ft
Minimum set-back distances for hydrogen and/or natural gas
storage (more stringent gas noted if relevant)
Property of:
TIAX LLC
1061 De Anza Blvd.
Cupertino, CA 95014
Task 5 CNG/Hydrogen Fueling
Site Plan - Fueling Station
Hydrogen and CNG fueling station
SIZE DWG BY DWG NO REV
A Stefan Unnasch B0228 - S0022 1
SCALE 1" = 8 ft 5 Jan 2004 SHEET 1 OF 110 ft
Security FenceNG line in
ft
ft
ft
ft
ft
ft
ft
ft
Process Cost Calcs
Material
Process
$0
$1
$2
$3
$4
$5
$6
$7
$8
$9
$10
Lapp
ing
CM
P
Wet
ther
mal
Oxida
tion
Spin
Coa
ting
Wet
Etc
hing
SiO
2
DC S
putte
ring
Ni
RF S
putte
ring
E
Spin
Coa
ting
Stepp
er
DC S
putte
ring
Ag
Stripp
ing
Spin
Coa
ting
Stepp
er
Dry
Etc
hing
SiO
2
DRIE
Si
Wet
Etc
hing
SiO
2
Dry
Etc
hing
NI
Wafe
r C
ost
($)
Approach Manufacturing Cost Modeling Methodology
0
10,000
20,000
30,000
40,000
50,000
60,000
70,000
80,000
3-Year TCO 5-Year TCO 10-Year TCO 15-Year TCO
To
tal
Co
st
of
Ow
ers
hip
($
)
PEMFC Plug Hybrid Vehicle
Full Battery Electric Vehicle
Approach Scope
4 2015 YY
Fuel Cell
System
Hydrogen
Storage
System
Hybrid
Battery
System
Inverter
Motor
Included in
the analysis
Not
included in
the analysis
Conduct a bottom-up manufacturing cost analysis of a 80kW light-duty vehicle fuel cell power system which includes a fuel cell system, a hydrogen storage tank , and a hybrid NIMH battery pack.
We published various fuel cell vehicle powertrain configurations manufacturing cost analysis in the past years.
Approach Scope
5 2015 YY
Specifications 2012 FCS 2013 FCS 2014 FCS 2015 FCS
PEM fuel cell
system •65 kWe •80 kWe •80 kWe •80 kWe
On-board hydrogen
storage
-Compressed H2 -5,000 psi -Single tank -5.6 kg usable H2
-Compressed H2 -5,000 psi -Single tank -5.6 kg usable H2
-Cryo-compressed H2 -Single tank -10 kg usable H2
-Compressed H2 -10,000 psi -Two tanks -5.6 kg usable H2
Hybrid battery pack -Li-ion battery -16 kWh
-Li-ion battery -1.2 kWh
-Li-ion battery -1.2 kWh
-NiMH battery -1.6 kWh
Comments Plug-in hybrid fuel cell vehicle
hybrid fuel cell
vehicle
hybrid fuel cell
vehicle
hybrid fuel cell
vehicle
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The 80 kWnet direct hydrogen PEM fuel cell system configuration is referenced in previous and current studies conducted by Argon National Laboratory (ANL).
PEMFC System 80 kWnet PEM Fuel Cell System Preliminary System Design
1. R. K. Ahluwalia, X. Wang, “Fuel cells systems analysis,” 2013 DOE Hydrogen and
Fuel Cells Program Review, Washington DC, May13-16, 2013.
80 kWnet Fuel Cell System Schematic1
Key Parameters Stack
• 3M NSTFC MEA
• 25 mm supported membrane
• 0.153 mg/cm2 Pt
• Power density: 834mW/cm2
• Metal bipolar plates
• Non-woven carbon fiber GDL
Air Management
• Honeywell type compressor
/expender
• Air-cooled motor / Air-foil bearing
Water Management
• Cathode planar membrane humidifier
with pre-cooler
• No anode humidifier
Thermal Management
• Micro-channel HX
Fuel Management
• Parallel ejectors
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Based on ANL’s stack performance analysis, we make the following system and material assumptions for the cost estimation.
System Assumptions 80 kWnet PEM Fuel Cell System Preliminary Design
Stack Components Unit 2012 2013 2014 2015
Production volume systems/ye
ar 500,000 500,000 500,000 500,000
Stacks’ net power kW 65 80 80 80
Stacks’ gross power kW 72 88 89.4 88
Cell power density mW/cm2 930 984 692 834
Peak stack temp. Degree C 90 87 92.3 100
Peak stack pressure Bar 2.5 2.5 2.5 2.5
Cell Voltage Volt 0.67 0.676 0.695 0.67
System Voltage (rated
power) Volt 300 300 300 300
Platinum price $/tr.oz. $1,475 $1,100 $1,100 $2,000
Pt loading mg/cm2 0.15 0.196 0.153 0.153
Membrane type Reinforced Nafion® Reinforced 3M
PFSA
Reinforced 3M
PFSA
Reinforced 3M
PFSA
Membrane thickness micro meter 20 25 25 25
GDL layer None-woven carbon
paper
None-woven carbon
paper
None-woven
carbon paper
None-woven
carbon paper
GDL thickness micro meter 185 185 185 185
MPL layer thickness micro meter 40 40 40 40
Bipolar plate type
76Fe-20Cr-4V with
nitridation surface
treatment
76Fe-20Cr-4V with
nitridation surface
treatment
SS316L with
Treadstone
Coating
SS316L with
Treadstone
Coating
Bipolar plate base
material Thickness micro meter 100 100 100 100
Seal material Viton® Viton® Viton® Viton®
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We use Pt price at $2,000/troz which is the similar to highest Pt price in the history.
System Assumptions 80 kWnet PEM Fuel Cell System Pt Price
2015 YY
2015 Study
Current Price
9
The 80 kWnet PEM fuel cell stack costs approximately $30/kW. Electrodes, bipolar plates, and seals are the top three cost drivers.
80 kWnet PEM Fuel Cell Stack Cost
($30/kWnet)
Stack
Components
2015 Stack
Cost ($/kW) Comments
Membrane $1.06 PFSA ionomer
($75/kg)
Electrode $15.37 Pt ($2,000/troz)
GDL $1.50 No-Woven carbon
paper
Bipolar Plate $7.16 Treadstone Coating
metallic plates
Seal $2.14 Viton
BOS $0.58
Manifold, end plates,
current collectors,
insulators, tie bolts,
etc.
Final Assembly $1.47 Robotic assembly
Stack
Conditioning 0.60 2 Hours
Total stack2 $29.88 1. Stack assembly cost category included MEA assembly and stack
QC; QC included visual inspection, and leak tests for fuel, air, and
coolant loops.
2. Results may not appear to calculate due to rounding of the
component cost results.
80 kWnet PEMFC System Stack Costs
2015 YY
4%
51%
5%
24%
7%
2%5% 2%
Membrane
Electrode
GDL
Bipolar Plate
Seal
BOS
Final Assembly
Stack Conditioning
10
80 kWnet PEM Fuel Cell System Cost
($4,742/system)
The 80 kWnet PEM fuel cell system costs $59/kW at the mass production volume. Stack, air management, and thermal management are the top three cost drivers.
System
Components
2015
System
Cost ($/kW)
Comments
Stack $29.9
Water
management $1.6
Cathode side
humidifier, etc.
Thermal
management $5.0
HX, coolant pump,
etc.
Air
management $10.1 CEM, etc.
Fuel
management $4.8 H2 pump, etc.
Balance of
system $3.9
Sensors, controls,
wire harness, piping,
etc.
System
assembly $3.9
Total system1, 2 $59.3
1. Assumed 15% markup to the automotive OEM for BOP components
2. Results may not appear to calculate due to rounding of the component cost
results.
80 kWnet PEMFC System System Costs
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50%
3%8%
17%
8%
7%
7%
Stack
Water management
Thermal management
Air management
Fuel management
Balance of system
System assembly
11
The 700 bar compressed hydrogen tank design is referenced in studies TIAX conducted on hydrogen storage1.
700 bar Compressed Hydrogen Storage System Schematic1, 2
Key Parameters
System Volume
• CH2 storage: 5.6kg usable H2
• System pressure: 700 bar
• # of tanks: 2
Tank
• Carbon fiber: Toray T700S
• Carbon fiber / resin ratio: 0.68 : 0.32
(weight)
• Translational strength factor: 63%
• Safety factor: 2.25
• Al liner
• Glass fiber projection layer
Compressed H2 Storage System Configurations
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Compressed
Gaseous
Hydrogen
Tank
Fill
System
Control
Module
Refueling
Interface
Hydrogen Line
to Fuel Supply Module**
Data & Comm. Line
to Fuel Cell Stack
Hydrogen Line
Data & Comm. Line
Filling
Station
Interface
Solenoid Valve
(Normally Closed)
Ball Valve
Primary
Pressure Regulator
Pressure
Relief
Device
Pre
ssu
re
Tra
nsd
ucer
Tem
pera
ture
Tra
nsd
ucer
Pressure
Relief
Valve
Check Valve
Check Valve
in Fill Port
In-Tank Regulator Compressed
Gaseous
Hydrogen
Tank
Solenoid Valve
(Normally Closed)
Ball Valve
Primary
Pressure Regulator
Pressure
Relief
Device
Pre
ssu
re
Tra
nsd
ucer
Tem
pera
ture
Tra
nsd
ucer Pressure
Relief
Valve
1. E. Carlson and Y. Yang, “Compressed hydrogen and PEM fuel
cell system,” Fuel cell tech team freedomCar, Detroit, MI,
October 20, 2004.
2. S. Lasher and Y. Yang, “Cost analysis of hydrogen storage
systems - Compressed Hydrogen On-Board Assessment –
Previous Results and Updates for FreedomCAR Tech Team”,
January , 2007
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Assumptions for the hydrogen storage tank design were based on calculations, literature reviews, and third-party discussions.
Stack Components Unit Current System Comments
Production volume systems/year 500,000 High Volume
Usable hydrogen Kg 5.6
Recoverable H2 in the tank Kg 6.0
Tank type IV With Al liner
Tank pressure PSI 10,000
# of tanks Per System 2
Safety factor 2.25
Tank length/diameter ratio 3:1
Carbon fiber type Toray T700S
Carbon fiber cost $/lbs 12
Carbon fiber vs. resin ratio 0.68:0.32 Weight
Carbon fiber translational
Strength factor 63%
Damage resistant outer layer
material S-Glass
Could be replaced
by cheaper E-glass
S-Glass cost $/lbs 7
Impact resistant end dome
material Rigid Foam
Rigid foam cost $/kg 3
Liner material Al
Compressed H2 Storage System Specification
2015 YY
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A vertically integrated manufacturing process was assumed for the tank and BOP components.
Spin
Rolling
Pressure
liner
Liner
Surface
Gel Coat
CF
Filament
Winding
Cure /
Cool
down
Ultrasonic
Inspection
Glass
Fiber
Out Layer
Winding
End
Domes
Assembly
Pressure
Test
Dimension
Weight
Inspection
Cure /
Cool
down
BOP
Assembly
Boss
Machining
Final
Inspection
Al
Stock
Al Carbon Fiber
Glass
Fiber
Rigid
Foam
BOP
Components
Gel
• In-tank primary pressure regulator
• Valves & sensors
• Filling interface
• Pressure release devices
• Piping & fitting
Major Tank Components Major BOP Components
• Aluminum End Boss
• Al liner
• Carbon fiber composite layer
• Glass fiber composite layer
• End domes (rigid foam)
Compressed H2 Storage System Manufacturing Process
2015YY
14
CH2 Storage System Cost ($3,794/system)
In the 700 bar compressed hydrogen storage system, the carbon fiber composite layers, in-tank regulators, system control valves are the top three cost drivers.
System Components
2015 CH2
Cost
($/kWh)
Liner $ 0.19
Carbon Fiber $ 12.47
Glass Fiber $ 0.85
Foam $ 0.26
Bosses $ 0.21
Regulator $ 2.68
Fill Port $ 0.54
Valves $ 1.61
Sensors $ 0.64
Pipe&Fitting $ 0.47
Assembly $ 0.24
Inspections $ 0.12
Misc $ 0.05
Total $ 20.33
Compressed H2 Storage System Cost
2015 YY
1%
62%
4%
1%1%
13%
3%
8%
3% 2%1%1%0%
Liner
Carbon Fiber
Glass Fiber
Foam
Bosses
Regulator
Fill Port
Valves
Sensors
Pipe&Fitting
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A NiMH battery pack will provide hybridization of a fuel cell vehicle which improves fuel economy as well as having the function as a startup battery. There are 34 6.5Ah-7.2V NiMH battery modules in the battery pack.
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Specifications
Battery pack voltage 245 V
Battery pack dimension 190 x 850 x 495
mm
Battery pack weight 52 kg
Battery pack energy 1.6 kWh
Number of NiMH battery modules in the
pack 34
NiMH battery module nominal voltage 7.2 V
NiMH battery module nominal capacity
6.5 Ah
NiMH battery module Output 1,350 W
Anode active material AB5
Cathode active material Ni(OH)2
http://afvsafetytraining.com/erg/Toyota-Camry-
HV-2007-11.pdf
http://www.peve.jp/en/product/np2/index.html
Battery Pack
Battery Module
PEMFC Hybrid Energy Storage Nickel Metal Hydride (NiMH) Battery Pack
16
The hybrid NiMH battery pack costs $611/kWh. Battery modules, battery management system, and sensors have higher cost contributions.
Battery System Cost ($611 /kWh)
The 1.6 kWh lithium-ion battery system cost $978 per pack at the mass production volume (500,000 packs/year).
Cost Category 2015 Pack Cost
($/kWh)
6.5 Ah modules $347
Module stack (w/o)
module $6
Battery management
system $91
Sensors, fuses, switches $70
Thermal management
system $28
Enclosure $32
Misc. $19
Assembly and Testing $17
Total ($/kWh) $611
2015 YY
PEMFC Hybrid Energy Storage Battery Pack Cost
57%
1%
15%
11%
5%
5%3% 3%
6.5 Ah modules
Module stack (w/o) module
Battery management system
Sensors, fuses, switches
Thermal management system
Enclosure
17
PEM fuel cell system, onboard hydrogen storage, and hybrid battery cost approximately $10,070 per vehicle.
• The mass production manufacturing cost of the 80 kWnet PEMFC stack is estimated to be $30/kW.
• The mass production OEM cost of the 80 kWnet PEMFC system is estimated to be $59/kW
• The 5.6 kg 2-tank compressed on-board hydrogen storage system is estimated to be $20/kWh at the mass production.
• The hybrid NiMH battery (1.6kWh) costs $978 per pack or $611/kWh.
2015 YY
Conclusion
Cost Category 2012 Pack Cost
($/pack)
2013 Pack Cost
($/pack)
2014 Pack
Cost ($/pack)
2015 Pack
Cost ($/pack)
80 kWe Fuel Cell $4,0301 $4,256 $4,713 $4,742
5.6 Kg Useable H2
Storage $3,058 $3,028 $4,5672 $3,794
Hybrid Battery Pack $4,4973 $1,034 $790 $978
Total: $11,585 $8,318 $10,070 $9,514
Comments FC-PHEV FC-HEV FC-HEV FC-HEV
1. 65kWe fuel cell system
2. 10 kg useable hydrogen.
3. 16 kWh li-ion battery pack
18
The PEM fuel cell middle size passenger vehicle purchase price is approximately $27,089 at the mass production volume.
Component Category
PEMFC
Hybrid
($/unit)
Comments
Glider Glider 7,000 Mid-size passenger vehicle
Power Chain
PEMFC 4,742 Bottom-up costing
H2 storage 3,794 Bottom-up costing
Battery system 978 Bottom-up costing
Traction motor1 1,200 Motor + controller + transmission
Power electric1 840 Battery charger, main inverter, DC/DC
converter, auxiliary inverter, etc
Power chain sub-
total 11,554
Total vehicle manufacturing cost 18,554
Markup2 46% Corporation cost & profit, dealer cost,
shipping cost, tax
Purchase price for consumer 27,089
1. The DOE advanced power electronics & electric motors (APEEM) team reported the power electronics cost
$7/kW and the motor cost $10/kW in 2012.
2. Automobile Industry Retail Price Equivalent and Indirect Cost Multipliers, EPA, 2009
2015 YY
Conclusion Vehicle Costs
19
Comparing a PEM FC vehicle with a middle size passenger electric vehicle which both have a drive range approximately 250 miles.
Conclusions Cost Comparing with Battery
2015 YY
EV Battery Pack Cost 80kWh EV Battery Pack
Cost ($)
80kW PEMFC System*
Cost ($)
$100 /kWh $8,000
$9,514
$150 /kWh $12,000
$200 /kWh $16,000
$250 /kWh $20,000
$300 /kWh $24,000
•* Includes an 80kWe PEMFC, a CH2 storage tank, and a 1.6 kWH NiMH battery
•** Assume the hydrogen to electricity efficiency is 50%
Energy (kWh) Total Energy (kWh) Cost ($/kWh)
EV battery 80kWh 80 kWh $100~300/kWh
PEMFC System* (Chemical
Energy + Electric Energy)
185 kWh (Chemical)
1.6 kWh (Electric) 186.6 kWh $51 /kWh
PEMFC System* (Converted
Chemical Energy** +
Electric Energy)
92.5 kWh (Converted
Chemical)
1.6 kWh (Electric)
94.1 kWh $101 /kWh
20
Thank You!
Contact: Yong Yang
Austin Power Engineering LLC
1 Cameron St, Wellesley, MA 02482
781-239-9988 978-263-0397
[email protected] www.austinpowereng.com
2015 YY