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U. S. Department of Energy’s Solid State Energy Conversion Alliance (SECA) Program – 2010 Progress and Plans December 3, 2010 Dr. Shailesh D. Vora Technology Manager, Fuel Cells National Energy Technology Laboratory United States Department of Energy

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U. S. Department of Energy’s Solid State Energy Conversion Alliance (SECA) Program – 2010 Progress and PlansDecember 3, 2010

Dr. Shailesh D. VoraTechnology Manager, Fuel Cells National Energy Technology LaboratoryUnited States Department of Energy

2

Fuel Cells

Types of Fuel Cells Fuel cells are electrochemical devices that convert the chemical energy of the fuel directly into electricity and heat (by bypassing thermal and mechanical conversion processes), and do so more efficiently than conventional combustion-based technologies.

Fuel cells can be thought of as batteries that, when provided with fuel and air, will not run down.

Characterized by the electrolyte Proton Exchange Membrane (PEM) Phosphoric Acid (PAFC) Molten Carbonate (MCFC) Solid Oxide (SOFC)

All are modular and serve as building blocks for a variety of power needs

Stationary (5 to hundreds of kW) Transportation (25 to 150 kW) Portable power (1 - 50 kW) Micro (watts)

3

Solid Oxide Fuel Cell – Operating Principle

4

Solid Oxide Fuel Cell Power System

Fuel Processor− Removes sulfur− Converts hydrocarbons

into hydrogen and carbon monoxide

Fuel Cell Power Section− Individual cells combined

into stacks− Can be matched to the

specific application − Generates dc power

Power Conditioner− Converts dc to ac

Heat Export System− Recovers usable waste heat

5

Fuel Cell Markets – Range of Applications

Portable

Combat1 kW

Laptop50 W

Mobile2 W

Methanol

ShipsSubmarine

Mobile

Car< 100 kW

Large Veh.> 100 kW

Natural GasHydrogen

Daimler

DG Power Plants> 100 kW

StationaryDG PowerResidential< 10 kW

CoalNatural Gas

Central PowerPlants> 100 MW

Natural GasHydrogen

Hydrogen

Natural/Digester/Landfill/Bio Gases

6

SOFC as green power generator

SOFC

AirCleanexhaust

High efficiencyElectricity

Heat(CHP applications, resulting in >80% cycle efficiency)

Fuel

Biofuels(renewable)

H2(storage)

Natural Gas

Logistical Fuel(storage; e.g. diesel, jet propulsion fuel)

Syngas(clean coal)

7

Fuel cells offer great value proposition ...

Green technology– Low emissions– CO2 capture potential– Renewable fuel

High quality heat & power (not all FC) High efficiency Low O&M cost, minimal moving parts No water consumption (except startup) (not all FC) Quiet Recyclable at the end of useful life Siting flexibility Large subsidy and government funding available Enhances energy independence and security

... but achieving cost targets and reliability are hurdles to commercialization

Trends / Drivers / Benefits

8

SECA Mission

• Enable the generation of efficient, cost-effectiveelectricity from domestic coal with near-zero atmosphericemissions of CO2 and air pollutants (99% CO2 capture)and minimal use of water in central power generationapplications.• Provide the technology base to permit grid-independentdistributed generation applications.

60% Efficiency

(Coal HHV)

Environmental:<0.5ppm NOx,low H2O use

Low Cost, similar footprint

to IGCC

Fuel-Flexible: Syngas, NG, H2, Diesel,

etc.

≥ 99% CO2Capture

Modular Technology

9

Research Topics

Core Technology

Program

Technology Transfer

Industry Teams

Needs

Program Management

Project Management

Industry Input

SECA Program Structure

10

Intellectual PropertyCornerstone of the Alliance

Exceptional Circumstance to Bayh-Dole Act

Industry Teams Develop Proprietary Technologies

VersaPowerSystems

SECA Core Technology R&D

Non-Exclusive Licenses

- Promotes collaboration- Limits research redundancy- Technology solution not “locked up”

11

Fossil Energy Fuel Cell Program SECA Budget – History

0

10

20

30

40

50

60

70

2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010 2011

Request Appropriation

$M

12

Fossil Energy Fuel Cell Program SECA Budget – FY10

$50MM

$34,900,000

$15,100,000

SECA Core Technology R&D(National Laboratories, Universities,

Small Businesses)

SECA Industry Teams(Cost Reduction and Coal-Based Systems)

13

Industry Teams & Major Subcontractors

VersaPowerSystems

00076A 10-22-08 WAS

Calgary

15

Solid State Energy Conversion Alliance

Industry Teams Systems Analysis

FCE & VPSUTC & DelphiRolls-Royce

Cathodes

Anodes & Coal Contaminants

Interconnects & Contact Materials

Seals

InnovativeConcepts

Fuel Processing

Power Electronics

Modeling & Simulation

Balance of Plant

ANLBUCMUGE Georgia TechLBNLMITMontana StatePNNLStanfordUNLV

Allegheny LudlumAuburn Faraday Technology PNNLNETL

Army CERDECLBNLNETLPNNLTDA ResearchWVU

AlfredCincinnatiMo-SciMSRIONRLPNNL

CellTech PowerGeneral ElectricNexTech

Eltron R&DNETLPrecision Combustion

NIST

NETLORNLPNNLUC Irvine

AcumentricsR&D Dynamics

Core Technology Program

Federal Government Management

J. Thijssen, LLCD. KeairnsOSAP-System AnalysisOSAP-Cost Analysis

Stack Materials & Stack Testing

ANLNASANAVSEAORNLPNNL

16

DOE’s Office of Fossil EnergyAdvanced (Coal) Power Systems Goals

• 2010: – 45-47% Efficiency (HHV)– 99% SO2 removal– NOx< 0.01 lb/MM Btu– 90% Hg removal

• 2015:– 90% CO2 capture– <10% increase in COE with

carbon sequestration– Multi-product capability (e.g, power + H2)– 60% efficiency (measured without carbon capture)

17

SOFC Anode

SOFC Cathode

air

Atmospheric SOFCOxy-Comb

HeatRecovery

oxygen

CO2

Condenser

CO2 Compressor& dryer

stackgas

Water Recycle

SECA Coal-Based Systems Atmospheric IGFC near-zero water requirement

(99% carbon capture, 54% efficiency)

blower

• Atmospheric SOFC with catalytic gasification 25 % Methane

• Separate Fuel and Air Streams: Oxy Combustion

• Cycle Efficiency (HHV); 99% Capture

~51% with CO2 Compression

~54% w/out CO2 Compression

air

ASU

GasCleaning(Dry or WGCU)

air

N2

coal

oxy-comb O2

Catalytic Gasification

CH4

O2

CO, H2, CH4

expander

18

ASU

GasCleaning(Dry or WGCU)

air

N2

coal

SOFC Anode

SOFC Cathode

air

Pressurized SOFCOxy-Comb

HeatRecovery

oxygen

CO2

Condenser

CO2 Compressor& dryer

oxy-comb O2

stackgas

expander

expanderCatalytic

GasificationCH4

Water Recycle

SECA Coal-Based Systems Pressurized IGFC near-zero water requirement

(99% carbon capture, 61% efficiency)

compressor

• Pressurized SOFC with catalytic gasification 25% Methane

• Separate Fuel and Air Streams: Oxy Combustion

• No steam cycle – minimal external water requirement

• Cycle Efficiency (HHV); 99% Capture

~57% with CO2 Compression

~61% w/out CO2 Compression

expander

O2

CO, H2, CH4

19

Impact of Efficiency on COEAdvanced Power Systems

With CO2 Capture, Compression and Storage

PC Baseline

IGCC Baseline

IGFCAtm

IGFC Pressure

EfficiencyHHV (%)

28.4 32.6 51.1 57.0

Capital Cost$/kW

3,570 3,330 2,150 2,100

Water Withdrawalgpm/MWnet

10.7 18.3 2.5 1.8

LevelizedCost-of-Electricity

¢/kW-hr15.0 15.1 10.8 10.3

Sources: Cost and Performance Baseline for Fossil Energy Plants, Volume 1, Revision 2 DRAFT, 2010 Anticipated ReleaseAnalysis of Integrated Gasification Fuel Cell Plant Configurations, DRAFT, 2010 Anticipated Release

20

IGFC – 53 Acres IGCC – 55 Acres

Representative Foot Print Comparison: IGFC & IGCC

• A similarly sized IGCC and IGFC will be comparable in real estate requirement.

Provided by:

21

SECA Program Milestones – 2010(OMB Performance Assessment Rating Tool)

• Stack Cost - $175/kW– 2007 Dollar Basis

• Power Block - $700/kW• Maintain Power Density with Increased Scale ~

300mW/cm2

22

Driving Down Costs For Fuels Cells(Order of Magnitude Cost Reduction)

$175/kW

Commercialize Truck APU’s Transition to Coal Applications

2000 2015 2020

450

300

150

$/kW

2000 >$1500/kW2010 ~$175/kWCost is Stack Only (ref 2007)

>$1500/kW (2000)

20122005

600

2010

• Atmospheric or Pressurized Fuel Cell• Separate Fuel to Oxy-Combustion• 25% Dry Methane/Catalytic, Methanation

or NG Pipeline

• Anode Support/Advanced Cathode, Seal & Interconnect

• Low Cost Manufacturing• Increased Power Density, Voltage &

Cell Size

•Establish Infrastructure•Manufacturing Capacity

23

Increase in Cell Size (Active Area)

• Higher active area leads to higher power per cell • Less number of cells per system• Low parts count

~ 4X increase in cell active area

24

Increase in Cell Size (Active Area)

• Higher active area leads to higher power per cell • Less number of cells per system• Low parts count

81 cm2

550 cm2

VersaPowerSystems

~ 7X increase in cell active area

25

• ~ 4 X increase in cell power density• Power density independent of cell size

Increase in Cell Power Density

0

100

200

300

400

500

600

700

800

900

2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 2012Year

Pow

er D

ensi

ty a

t 0.8

V/ce

ll (m

W/c

m2)

26

• ~ 4 X increase in cell power density• Power density independent of cell size

Increase in Cell Power Density

VersaPowerSystems

27

• Tight control over stack output since 2007 • Excellent thermal cycling capability

Cell/Stack Reliability

0.000

0.100

0.200

0.300

0.400

0.500

0.600

0.700

0.800

0.900

0 20 40 60 80 100 120

Stack

Volta

ge

Range

Average

2005 2006 2007 2008 2009

30-cell stacks – Gen. 3

Stack Thermal Cycle Progress

0

50

100

150

200

250

2004 2005 2006 2007 2008 2009

Year

Num

ber o

f The

rmal

Cyc

les

Test Stopped For Stack Analysis

New Seals Implemented

28

Cell/Stack Testing

0.000

0.200

0.400

0.600

0.800

1.000

1.200

0 1000 2000 3000 4000 5000 6000 7000 8000 9000 10000 11000

Elapsed Time, hrs

Volta

ge, V

OVERALL:30 mV over 9538 hrs3.1 mV or 0.31% / 1000 hrs

1 Cell Stack - 81 cm2 Active AreaFurnace Temperature: 750 CFuel: 55 H2:45 N2 + 3% H2O, Uf = 50%Oxidant: Air, Ua = 25%Current: 40.5 A (0.5 A/cm2)

VersaPowerSystems

29

Cell/Stack Testing

VersaPowerSystems

GT058027-0001120-Cell Stack

Cell Active Area: 550 cm2

0

0.2

0.4

0.6

0.8

1

1.2

0 250 500 750 1000 1250 1500 1750

Test Duration (hours)

Ave

rage

Cel

l Vol

tage

(V)

0

5

10

15

20

25

30

Stac

k Po

wer

(kW

)

Average Cell Voltage

Stack Power

Normal Operating Conditions (NOC)Furnace Temperature: 715 CFuel: 25.2% H2, 22.4% N2, 14.5% NG, 37.8% H2OIn-stack reforming = 70%, Uf = 68%Oxidant: Air, Ua = 15%Current: 200 A (0.364 A/cm2)

Stack conditioning

Peak power testing (24 h)

Test stand repair(full thermal cycle)

30

Solid State Energy Conversion Alliance Fuel Cells Technology Timeline

2005 2006 2007 2008 2009 2010 2011 2012 2013 2014 2015 2020

SECA R&D

SECA Cost Reduction

SECA Coal Based Systems

SECA Manufacturing

Validation test Validation test

Operate Single Module

(250 kW -1 MW) Scale

Operate Multiple Module (5 MW)

Scale with Bottoming Cycle

$700/kWRef: 2007

250 – 500 MW IGFC

Coal-Based Fuel Cell Objective

Technology Solutions and Enabling Technology

31

SECA Fuel FlexibilitySOFC Systems can produce power from many fuels

Coal Natural Gas

Gasification Anaerobic Digestion Reforming

Fuel Gas (mainly CH4, CO, H2)

Electric Power60% Electrical Efficiency

SOFC

Biomass / Waste

32

Delphi Auxiliary Power Unit Demos

Pathway to Coal Plants• Gain operational experience• Develops infrastructure for fuel cell stack

manufacture• Delphi’s diesel SECA APU demonstrated

by Peterbilt and Daimler

33

SOFCs in Unmanned Undersea Vehicles (UUVs)

• Naval Undersea Warfare Center, Division Newport, (NUWCDIVNPT) successfully tested SECA SOFCs in extreme conditions. Used SECA Stacks (2 Developers) and SECA developed High Temperature Blower.

• SOFC technology has the potential to greatly increase UUV mission time compared with current battery technology.

• Although SECA has a coal-based, central generation focus, spin-off applications are encouraged. Military applications like UUVs provide operating experience and independent validation for SECA.

• Cost and operational lifetime are not necessarily major concerns for military applications, as long as new mission capability can be delivered.

21UUV (2-5 kW) Fisher-Tropsch & Logistics Fuels SECA Stacks and Blower

34

SECA Core Technology Research Areas

Gas Seals Glass and Compressive Seals Compliant Seals Self-healing Materials High Temperature Refractive Seal

Failure Analysis Models with Electrochemistry & EMF Define Operating Window (Not possible experimentally) Structural Failure Analysis & Design Criteria (ASME)

Cathodeperformance

Understand Mechanism Ad-atom Modification of Surfaces Modification through Infiltration

Interconnect Coatings Electrode to Interconnect Interface - Contact Material

Anode /fuel processing

Establish Fuel Specification Characterize Thermodynamics/Kinetics/ Contaminants

Heat Exchangers/ High Temperature Blowers

Cost and Reliability Design Guidelines

Electronic Effect versusDefect Chemistry

35

Websites:www.netl.doe.govwww.fe.doe.govwww.grants.gov

Dr. Shailesh D. VoraTechnology Manager, Fuel CellsNational Energy Technology LaboratoryU. S. Department of Energy(Tel) 412-386-7515(Fax) [email protected]

CDs available from the website•11th Annual SECA Workshop

Proceedings•Fuel Cell Handbook (7th ed.)

For More Information on SECA…