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Development of a Low Cost 3-10kW Tubular SOFC Power
SystemNorman Bessette
Acumentrics CorporationMay 20, 2009
This presentation contains no proprietary, confidential, or otherwise restricted information
FC_28_Bessette
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Acumentrics Confidential
Acumentrics Corporation• ~ 80 Employees• Manufacturing since 1994•Based in Westwood, Mass.•~40,000 sq. ft facility• Critical disciplines in-house
Electrical EngineeringMechanical EngineeringChemical EngineeringThermal ModelingCeramics ProcessingManufacturingSales & MarketingAutomationFinance
Strategic Partners
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Industrial-UPS®Commercial
Rugged-UPS®Military
Acumentrics Battery based UPS
Uninterruptible Power Supplies for Harsh
Environments
Features:• Sealed electronics• Able to withstand vibration• Unity power factor input• Wide input 80VAC - 265VAC• Isolated 120 / 240VAC output• Hot swap battery case• Parallelable to 20 kWatts
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Overview
TimelineProject Start: 4/1/2008Project End: 9/30/2011Percent Complete: 25%
BarriersCell Power DensityStack Power DensityCell Cost ReductionSystem Cost ReductionSystem EfficiencyLifetime
BudgetProject Funding (BP1)
DOE Share=$6,041,012Contractor=$2,013,671
Funding Received$2,949,425
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Objectives
Improve Cell Power & StabilityCost Reduce Cell Manufacturing Increase Stack & System EfficiencyPrototype test meeting system efficiency and stability goalsIntegrate to a mCHP Platform
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ApproachPerfect the individual System pieces followed by optimizing their integration:Cell Technology: Improve power & stability of the cell building blockCell Manufacturing: Improve processing yield & productivity while decreasing material consumptionStack Technology: Refine stack assembly and improve integrity while cost reducing component costsSystem Performance: Develop simplified controls and BOP to allow for a reliable, highly efficient unit.
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Acumentrics Progress
0
20
40
60
80
100
120
140
0 50 100 150 200 250 300Cell Current, A
Cel
l Pow
er, W
Electrolyte Supported Cells- Through December 2001
0.7cm Anode Supported Tubes - January 2002-December 2003
Progress of Single Cell Power at Acumentrics
1.5cm (33 cm length) Anode Supported Tubes- 75%FU December 2003-June 2005
1.5cm anode supported tube with LaCrO3 IC- July 2005-November 2005
1.5cm (42cm length) LaCrO3 IC Anode Supported Tubes-December 2005
Two 2.2cm OD Anode Supported Tubes-January 2007
2.2 cm OD (88 cm total length)September 2007 >120W
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Power Density Improvements
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Degradation Progress
0%
1%
10%
100%
1000%
10000%
Jan-01
May-02
Oct-03
Feb-05
Jul-06
Nov-07
Date
Deg
rada
tion
Rat
e, %
100
0hr-1
1.5cm OD testing
Electrolyte-supported (EL) cells;Average over one year
7mm OD cell program
1.5cm chromite testing
75% Fuel Utilization
Re-braze experiment
SECA Generator Shows Negligble Degradation
Latest Testing
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Electrical Testing- Thermal cycles
Loaded Cell performance graphs show a loss rate of about 1%/100TC
~4000hr run time/1500hrs at power
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Single Cell Thermal Cycling•Average of 5 cells•Shows loaded performance after each thermal cycle•Degradation from >10%/100T/C to less than 1%/100T/C
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Stack Size ReductionNumber of tubes
for 1.25 kW reduced from 126 to 72 to 45
Weight reduced75% from 92 to23lbs
Volume reduced 82% from 1.55 to 0.28 cu. ft.
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Tube Fabrication Improvements
Thinner tube substrate wall possible – 45% reductionIntegral closed end – eliminates one braze jointSignificant through process yield improvement – 55% to 80%, due to firing orientationSimplified process - replaces mixing, extrusion, drying and one cutting operationThroughput up to 32 tubes per hour, immediately ready for firing
Q4 - 2008 Q1 - 2009
Isostatic pressing implementation:
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In-house Isopressed Tubes
Cells made from in-house isopressed tubes performing wellPeak power per cell approximately 57 watts on cell test
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Tube Wall Thickness ReductionFabricated and tested 35% and 45% reductions in wall thickness
Achieved Equivalent Performance of that with standard wall thickness
Standard Wall Tube Thickness 1.8mm
Reduced Wall Tube Thickness 0.9mm
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System OperationTubular Cells
Inherent strength and tolerance to rapid temperature change
High Operating Temperature (800 C)
Internal fuel reforming and cogeneration opportunity
Standard Manufacturing Process
Low capexStandard Components
Standard HVAC balance-of-plant componentsLeverage 12 years DC/AC conversion experience
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Fuel Cell Module
Cathode Air Downcomer
Offgas Injectors
Fuel Plenum
Offgas Plenum
Cathode Air Distribution Region
CatyliticOxidation Tile
Cathode Air to and from Recuperator
Anode Gas Inlet
Cathode Air Downcomer
Offgas Injectors
Fuel Plenum
Offgas Plenum
Cathode Air Distribution Region
CatyliticOxidation Tile
Cathode Air to and from Recuperator
Anode Gas Inlet
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36 Cell Stack Assembly
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Stack Stability Testing
0
0.2
0.4
0.6
0.8
1
1.2
1.4
200 205 210 215 220 225 230
Elapsed Time (hrs)
Ave
Lay
er V
olta
ge
0
5
10
15
20
25
30
Cur
rent
, Tem
pera
ture
/100
V_01 V_02 V_03 V_04 V_05 Stack AmpsAve Stack Temp/100
Schedule:•About an hour down to ~200C•Less than 30 min back to power•Run•Redo
20 thermal cycles
Purgeless cycles
Excellent recovery
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Recuperator Advancements
Generation 1 2.0ft3 143 lbs $4200 Qty 1
Generation 2 0.12ft3 17lbs $1100 Qty 1
Generation 3 0.12ft3 17lbs $550 Qty 1
Reductions:• 94% in Volume
• 88% in Weight
• 74% in Qty 1 Cost
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Improved Stack Efficiency-CPOX Results
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Improved Stack Efficiency-Steam Reformed Results
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Improved Efficiency:Cell vs Stack Comparison
Cell Test Data
Steam Reformed Stack Data
CPOX Stack Data
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mCHP vs. power plant and (condensing) boiler
Power plant heating
Primary energy 100%
Primary energy100%
Losses
Losses
72% useful energy
90% useful energy
Losses
microCHP
microCHPsimultaneous power and heat production
Common technologyseparate power and heat production
20%power
70%heat
56%heat
16%power24%
4%
10%
60%40%
= 10 – 25% lower primary energy consumption= 10 – 25% lower CO2 emissions = 10 – 25% lower energy cost
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Micro CHP
4 have been built to date
Has undergone & passed CE certification
Undergoing testing this winter in Europe
1kWel AC out, 20kWth Eff(Total)>85%,
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1kW Home CHP Appliance• 25% energy savings• Prototype delivered 2007• Demo with major European
utilities• Demonstration &
Commercialization Program with Consortium of utilities
1 Booster Boiler2 Fuel Cell Stack3 Exhaust Heat Exchanger4 Fuel desulfurizer
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ConclusionsSignificant progress in cell stabilityAdvanced Cell Manufacturing automation & material reduction while maintaining cell performance.Single cells have shown tremendous capability both in thermal cycling and in operation under gradientsSignificant progress in stack sizeGenerators and stacks have shown resiliency with purgeless thermal cyclesThe testing of a home heating appliance is currently underway
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Thanks to
Reginald Tyler of the DOE-Golden OfficeSara Dillich-DOE EEREThomas Benjamin-Argonne National LaboratoryDon Hoffman &John Heinzel - ONRMTS GroupTechnical Staff at Acumentrics