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Demonstration of a 75 W portable SOFC generator W SOFC...Block diagram Air blower Stack +-Fuel tank...

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Mesoscopic Devices Demonstration of a 75 W portable SOFC generator Jerry Martin—Mesoscopic Devices, LLC Tad Armstrong—MSRI Anil Virkar—Univ. of Utah Mesoscopic Devices
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Mesoscopic Devices

Demonstration of a 75 W portable SOFC generator

Jerry Martin—Mesoscopic Devices, LLCTad Armstrong—MSRI

Anil Virkar—Univ. of Utah

Mesoscopic Devices

Mesoscopic Devices

Mesoscopic Devices

OutlineWhy portable SOFC?System designStack requirementsPerformanceNext generation 250 W generator

Mesoscopic Devices

Why portable SOFC’s?Operation on hydrocarbon fuels

High energy density fuel>3X advantage over methanol or hydridesSafe, readily available fuels

Simple fuel reformingCPOX is small, fast, lightweight

Quieter than IC-engine generatorsLighter than batteries

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SOFC advantagesQuiet

<52 dBAUndetectable at 10 m outside

Good fuel efficiencyEstimated 3160 W-hr/kg fuel (~26%)

CompactLunchbox size, ~3 kg

High peak-to-average power ratiosVia battery hybridization.

Mesoscopic Devices

SOFC advantages (cont’d.)Common fuels

Propane, kerosene todayGasoline and diesel with development

Operation in wide range of ambient conditionsHigh specific energy compared to batteries

Up to 2000 W-hr/kgBetter than batteries for periods longer than 12 hours

Long periods between maintenance500 hours is a reasonable near-term goalUp to 2000 hours with development

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SOFC challengesSlow startup and shutdown(current generation)

~1 hour to power delivery~1 hour for safe shutdown Not suitable for frequent start-stop cycles

Limited sulfur tolerance Sulfur must be reduced to ppm levels in fuel

Some degradation with thermal cycling

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75W for 5 days

Left: BA-5590’sMiddle: MesoGen 75Right: fuel for MesoGen

Battery weight: 40 kgCost: >$4000Generator + fuel weight: 6 kg

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System configurationFuel options

PropaneDesulfurized keroseneFuel supply subsystem is only change

Optimized for multi-day missions:Direct power for communications equipmentBattery charging

12 or 24 V DC options

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Block diagram

Air blower Stack

+-

Fuel tank(liquid)

fuelpump

Insulation

recuperator

vaporizerpower

conditioning

partialoxidation

tail-gascombustor

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CPOX implicationsSimplest reformerNo water to recover or carryMillisecond contact time design leads to very small reformersFast start, fast response

Leads to dilute anode stream 25% H2, 21% CO47% N2, 6% H2O+CO2

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System integrationBOP components demonstrated to> 1000 hrs between maintenanceControl system

Steady state controlFully automated startup and shutdown

Battery hybridization provides peak power capability

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Integrated 75 W system

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System integration challengesAccurate fuel and air metering at minimum weight, size and power drawAir blower power draw, lifetimeStack performance at high fuel utilization

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Mass breakout: 75W system

Fuel 1.8-6 kg

Stack 0.7 kg

BOP 2.3 kg

3 day mission, 75W 10 day mission, 75W

Weight Distribution (Wet)

fuel71%

stack8%

BOP21%

Weight Distribution (Wet)

fuel42%

stack16%

BOP42%

Mesoscopic Devices

Stack requirementsHigh volumetric power densityHigh fuel utilizationHigh cell voltage

Must simultaneously achieve all three for lightweight, efficient system

Critical parameters:Stack power density >400 W/LStack specific power > 100 W/kgLow dP, <0.5 psi (3 kPa)

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Stack performance requirements

High performance on dilute reformate stream (~50% (H2 + CO), 50% N2)Multiple thermal cyclesLight weight (including compression hardware, headers, etc.)

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Planar stacks17 cells16 cm2 active area0.7 kg / 0.2 liters64 x 64 x 47 mm~450 W/liter at operating conditions12 V / 7.5 A / 90 W

1.8 in.

47 mm

2.5 in.

64 mm

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Stack power curve50% H2 in N260% fuel util.40% air util.

0

5

10

15

20

0

25

50

75

100

0 2 4 6 8 10

Volta

ge, V

Power, W

Current, A

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75 W system75 W net for battery charging130 x 180 x 250 mm5 x 7 x 10 inches

3.0 kg dry, 6.6 lb0.8 liters of fuel per day6 kg fuel, 13.2 lb for 10 days~2000 W-hr/kg @ 10 days

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TemperaturesStack temperature ~ 800 CCase temperature ~ 60 CExhaust gas ~ 120 C

250 W dissipation

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System load curve

0

5

10

15

20

0

10

20

30

40

50

60

70

80

0 1 2 3 4 5 6 7

volta

ge (V

) power (W

)

current (A)

propane5-17-2005

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Parasitic loads

0

5

10

15

20

0 2 4 6 8 10

para

sitic

pow

er (W

)

time (hours)

battery charger

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Effect of hybridization

0

5

10

15

0

10

20

30

40

50

60

0 1 2 3 4 5

volta

ge (V

) power (W

)

currrent (A)hy

brid

ope

ratio

n

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Heat-up data

0

100

200

300

400

500

600

700

800

0

5

10

15

20

0 0.2 0.4 0.6 0.8 1

stac

k to

p te

mpe

ratu

re (°

C)

stack voltage

time (hours)

TV

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Gross and net power

0

10

20

30

40

50

60

0 2 4 6 8 10 12 14

load

pow

er (W

)

time (hours)

acquire load curves

stack starts to carry internal loads (42 min)

stack power

load power

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Addressing challengesChanges for future systems

Tubular stacksTighter integration

Leads toShorter startup timesHigher power density

Air supply system changesLengthen maintenance interval

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Hot zone integrationTight integration in the hot zone is critical75 W system

Planar stacksVolume: 700 ml

250 W systemTubular stacksVolume : 1265 ml85% increase inhot zone volumetricpower density

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Tube test resultsSimulated CPOX60% fuel util.Ø10 mm

0

0.2

0.4

0.6

0.8

1

1.2

0

0.05

0.1

0.15

0.2

0.25

0.3

0 2 4 6 8 10 12 14

Vol

ts (V

)

Pow

er (W/cm

2)

Current (A)

Mesoscopic Devices

AcknowledgementsThis work was supported by

US Defense Advanced Research Projects Agency (contract MDA972-03-C-0060) Office of Naval Research (contract N00014-05-C-0051)


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