oxyfuel pulverized coal steam gtdl tgenerator … 1/alstom_oxpp_iea... · 30 mwth pilot steam...
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Oxyfuel Pulverized Coal Steam G t D l tGenerator Development
30 MWth Pilot Steam Generator Commissioning and TestingCommissioning and Testing
F. Kluger, P. Mönckert, B. Krohmer, G.-N. StamatelopoulosAlstom
J. Jacoby, U. BurchhardtVattenfall
1st IEA GHG International Oxyfuel Combustion Conference1st IEA GHG International Oxyfuel Combustion Conferencest G G te at o a O y ue Co bust o Co e e ceCottbus, Germany
8 - 11 September 2009
st G G te at o a O y ue Co bust o Co e e ceCottbus, Germany
8 - 11 September 2009
Agenda
Alstom’s Oxy PC Development Roadmap
Oxyfuel Pilot Steam Generator – Realisation & DescriptionOxyfuel Pilot Steam Generator – Realisation & Description
Oxyfuel Pilot Steam Generator – Results from OperationOxyfuel Pilot Steam Generator – Results from Operation
SummarySummary
Next StepsNext Steps
Roadmap Oxy PC DevelopmentStatus and Next Steps
Pilot Plants Demonstration Full-ScaleLab ScaleSource: VattenfallSource: Vattenfall
2008 2014-15 < 2020
30 MWth Oxy PC Lignite & Bit. Coal
200 – 300 MWelOxy PC Lignite
Up to 500 kWth Oxy PC Lignite & Bit Coal Testing
2004
gSchwarze Pumpe, Germany (Vattenfall, Alstom)
Oxy PC Lignite (e.g. Vattenfall Jänschwalde, Feasibility Study Performed with
400 – 1,100 MWelOxy PC Lignite
Lignite & Bit Coal Testing
Uni Stuttgart, Uni Cottbus, Uni Hamburg-Harburg, Uni Dresden
30 MW Oxy Gas Alstom Contribution)
ENCAP (EC Co-funded Project),ADECOS I & II (GER Co-funded Project), OxyBurner (EC Co-funded Project),
30 MWth Oxy Gas Natural Gas & Oil Lacq, France (TOTAL, Alstom) 200 – 300 MWel
Oxy PC Bit. Coal600 – 1,100 MWelOxy PC Bit. Coal(EC Co funded Project),
OxyCorr (EC Co-funded Project), etc.
15 MWth Oxy PC Bitum. Coal & Lignite Windsor, CT, USA (DoE, Alstom)
y
Agenda
Alstom’s Oxy PC Development Roadmap Alstom’s Oxy PC Development Roadmap
Oxyfuel Pilot Steam Generator – Realisation & Description
Oxyfuel Pilot Steam Generator – Results from OperationOxyfuel Pilot Steam Generator – Results from Operation
SummarySummary
Next StepsNext Steps
30 MWth Oxyfuel Pilot Plant - Realisation
As planned... Milestones
ct
ssio
n
Pre
ssur
e
Firs
t n oa
l Fire
xy-F
iring
onne
CO
2ed
Con
trac
Awar
dP
erm
is
Hyd
ro P
Test
PAC
Lift
of F
Col
umn
Firs
t Co
Firs
t Ox
Firs
t To
Cap
ture
6 7 7 8 8 886As realizedMain Data
11/’0
6
07/’0
7
11/’0
7
07/’0
8
08/’0
8
12/’0
8
09/’0
8
04/’0
6Thermal Capacity: 30 MWthSteam Production: 40 t/hSteam Pressure: 25 barSteam Temp : 330 °CSteam Temp.: 330 CFuel: Lignite / Bit. CoalFuel demand (Lig.): 5.2 t/hO2 demand: 10 t/h
Source: Vattenfall
2CO2 (liquid): 9 t/hCO2 capture rate: >90 %Start operation: 2008
30 MWth Oxyfuel Pilot Plant - Realisation
30 MWth Oxyfuel Pilot Plant – Process Scheme & Alstom Scope
Primary Flue Gas Recycle
Coal Dust
Burner
y y
Steam
GasSteam-
HEXSeal Gas <1,2 bar
Seal Gas 6 bar
Dry sorbent
Furnace
Steam-HEX Air
Ammonia
Filter FGC CO2-ProcessFGD
2nd Path
De-NOx ID Fan 1 ID Fan 2S d Fl
Steam-
3rd Path
Air
Nitrogen
Secondary Flue Gas Recycle
Ash
HEX
AirASUSteam-HEX
Air
Oxygen
30 MWth Oxy-Combustion Pilot Plant –Key Information
• Single burner & indirect firing system testing
Key information generated for the next Oxy-combustion development steps:
• Combustion fundamentals (emissions, burnout, fouling & slagging, excess oxygen, flue gas recycle ratio etc.)• Heat transfer (radiation, convection)• Material selection (corrosion issues)
• Operational data for validation of oxyfuel CFD models
• Dynamic behaviour of entire oxy-combustion l t (St t / h t d it h i tplant (Start-up / shut down, switch air to oxy
and vice versa)
• Interaction of ASU, Boiler, AQCS and GPUFlue-gas flow Intakeair damper Flue-gas recycledamperFlue-gas flow Intakeair damper Flue-gas recycledamper
• Control loops for oxy-combustion process and plant
• Integration Options
Flue gas flow
Oxidant flow
Air flow Recycled flue-gas flow
Intakeair damper Flue gas recycle damperFlue gas flow
Oxidant flow
Air flow Recycled flue-gas flow
Intakeair damper Flue gas recycle damper
• Component Optimisation
• Achievable CO2 capture rate and quality07:50 08:00 08:10 08:20 08:30 08:40 08:50 09:00 09:10 09:20
O2 from ASU
07:50 08:00 08:10 08:20 08:30 08:40 08:50 09:00 09:10 09:20
O2 from ASU
30 MWth Oxyfuel Pilot Plant - Boiler
BurnerIgnitionB
DeNOx-OptionBoiler Design DeNOx (optional)
ECO 5
HEX Gas Catalyst 1
Burner
SH 1ECO 4
y
Catalyst 2
SH 2 ECO 3
ECO 2B t
Catalyst 3
ECO 1
ESPHydratedLime
BurnoutOxydant
30 MWth Oxyfuel Pilot Plant – Burner / Firing System Operating Modes
OxPP : 1 x 30 MW30 MWthth
Dried lignite / Transport air
Core air core : Air
Seco
ndar
y air surround1 : Air
surround2 : Air
surround3 : Air
Air operation
core : Oxygen+RFG* core : RFG*
surround1 : Oxygen+RFG*
surround2 : Oxygen+RFG*
surround3 : Oxygen+RFG*
surround1 : RFG*
surround2 : RFG*
surround3 : Oxygen
Oxyfuel operation(premixed oxygen)
*RFG = Recirculated Flue Gas
Oxyfuel operation(direct oxygen injection)
*RFG = Recirculated Flue Gas
30 MWth Oxyfuel Pilot Plant – Oxy-Firing Operation Modes
Burner
Burner
Burner
Combustion chamber
2. Pass
Combustion chamber
2. Pass
Combustion chamber
2. Pass
(DeNOx)
3. Pass
(DeNOx)
3. Pass
(DeNOx)
3. Pass
Oxygen
Recycle
Oxygen
Recycle
Oxygen
Recycle
– Oxyfuel –Pre-mixed Mode
– Oxyfuel –Expert Mode A
– Oxyfuel –Expert Mode B
Agenda
Alstom’s Oxy PC Development Roadmap Alstom’s Oxy PC Development Roadmap
Oxyfuel Pilot Steam Generator – Realisation & DescriptionOxyfuel Pilot Steam Generator – Realisation & Description
Oxyfuel Pilot Steam Generator – Results from Operation
SummarySummary
Next StepsNext Steps
Results from OperationSwitch From Air-Firing to Oxy-Firing
Mass flows (Air, Oxidant, Flue gas)
Flue-gas flow Intakeair damper Flue-gas recycle damperFlue-gas flow Intakeair damper Flue-gas recycle damper
~ 20 – 30 min
Oxidant flowOxidant flow
Air flow Recycled flue-gas flowAir flow Recycled flue-gas flow
O2 from ASUO2 from ASU
07:50 08:00 08:10 08:20 08:30 08:40 08:50 09:00 09:10 09:2007:50 08:00 08:10 08:20 08:30 08:40 08:50 09:00 09:10 09:20Time
Results from OperationSwitch From Air-Firing to Oxy-Firing
~ 45 – 60 minFlue Gas Species
CO2 >85 vol.-% (dry) after ESP
Thermal performance
~ 20 – 30 min
SO2
H2O ca. 28 vol.-% after ESP
O2NO
xCO
07:50 08:00 08:10 08:20 08:30 08:40 08:50 09:00 09:10 09:20Time
Results from Operation - Burner / Firing System (Air-Firing)
• Burner operates in a stable and reliable way
• Limits for emissions kept easily for airLimits for emissions kept easily for air mode of operation
• Primary measures for NOx reduction appliedapplied
• Typical emission values are:Dust << 20 mg/Nm³ (dry)CO < 100 mg/m³ (dry)
Air-FiringCO < 100 mg/m (dry)NOx < 300 mg/m³(dry)SO2 < 1,000 mg/m³(dry)O2 < 4 vol.-% (wet)2 ( )
• Good burnout with low unburnt carbon in fly ash and slag
• Hydrated lime injection for SO2 controlHydrated lime injection for SO2 control causes fouling in the economizer heating surfaces
Results from Operation - Burner / Firing System (Oxy-Firing – Pre-mixed Mode)
• Burner operates in pre-mixed mode in a stable and reliable way with an oxygen concentration in the oxydant of 28 Vol.-%.y
• Limits for emissions kept easily for oxyfuel mode of operation
• Primary measures for NO reductionPrimary measures for NOx reduction applicable but not required
• Typical emission values are:Dust << 20 mg/Nm³ (dry)Dust << 20 mg/Nm (dry)CO < 300 mg/m³ (dry)NOx < 700 mg/m³(dry)O2 < 4.5 vol.-% (wet)
Oxy-Firing (pre-mixed mode)
2 ( )• Good burnout with low unburnt carbon in
fly ash and slag• In oxyfuel mode operation longer responseIn oxyfuel mode operation longer response
time due to the flue gas recirculation
Results from OperationCO-Concentration
Comparison of different operation modess
Expert Mode A
mis
sion
s
Pre-mixed Mode
Expert Mode B
CO
Em
O2 Concentration in Flue Gas
Results from OperationNOx-Concentration
Comparison of different operation modess Expert Mode
mis
sion
s Expert Mode A
NO
x Em Pre-mixed
Mode
Expert Mode B
O2 Concentration in Flue Gas
30 MWth Oxyfuel Pilot Plant – Status of Operation as End of August 2009
35
30nt (v
ol.-%
)
30
n in
Oxi
dan
Oxyfuel - Pre-mixed Mode -
25
ncen
trat
ion
Oxyfuel - Expert Mode -
20
O2 C
on
Air20
2 3 4 5 6 7O2 Concentration in Flue Gas (vol.-%)
30 MWth Oxyfuel Pilot Plant – Status of Operation as End of August 2009
Total Operation 3,100 h
Air Operation 1,500 h
Oxyfuel Operation 1,600 h
• Burner Pre-mixed Mode 1,000 h
• Burner Expert Mode 600 h
Agenda
Alstom’s Oxy PC Development Roadmap Alstom’s Oxy PC Development Roadmap
Oxyfuel Pilot Steam Generator – Realisation & DescriptionOxyfuel Pilot Steam Generator – Realisation & Description
Oxyfuel Pilot Steam Generator – Results from OperationOxyfuel Pilot Steam Generator – Results from Operation
Summary of Oxy-Steam Generator Pilot Experience to Date
Next StepsNext Steps
Summary of Oxy-Steam Generator Pilot Experience to Date
Design approach for thermal design and firing system design confirmed in practical operation
M d it h f i d t d d i k i Mode switch from air mode to oxy mode and vice versa works easier than originally anticipated
All contractually fixed parameters are met for air and oxy combustiony p y
CO2 concentrations in the flue gas downstream of the boiler >85 Vol-% dry
Oxy-Firing “Expert Mode” results in lower flue gas oxygen concentration compared to the “Pre-Mixed Mode”, O2 values below 3 Vol.-% can be achieved
Burner and firing system has demonstrated its high flexibility with good performance
Test program under execution Data for CFD model development and Test program under execution. Data for CFD model development and validation, dynamic behaviour, heat transfer etc. already generated. Extensive material testing under execution.
Agenda
Alstom’s Oxy PC Development Roadmap Alstom’s Oxy PC Development Roadmap
Oxyfuel Pilot Steam Generator – Realisation & DescriptionOxyfuel Pilot Steam Generator – Realisation & Description
Oxyfuel Pilot Steam Generator – Results from OperationOxyfuel Pilot Steam Generator – Results from Operation
SummarySummary
Next Steps
Next Steps – Testing of Alternative Alstom Burner Design
OxPP : 1 x 30 MW30 MWthth
Dried lignite / Transport air
Core airDesign A Design B
Seco
ndar
y air
Main features
• Each burner compartment can be individually enriched with oxygen up to
Main features
• Each burner compartment can be individually enriched with oxygen up toindividually enriched with oxygen up to
39 Vol.-%
• One swirl device
individually enriched with oxygen up to 39 Vol.-%
• Two swirl devices
• Ring of lances for 100% oxygen injection
• Separate ignition burner for start-up
• Annular clearance for 100% oxygen injection
• Integrated gas lance for start-up
Next Steps – Testing of Alternative Alstom Burner Design
• Testing of firing system and burner Air Mode
Oxy Mode- Pre-mixed Mode- Expert Mode A- Expert Mode B
• Measurements Gaseous Emissions Gaseous Emissions,
Ashes, Deposits
Corrosion
Heat Transfers Detailed in-flame measurements for
CFD modeling g
Thank You For Your Attention !
www.alstom.com
30 MWth Oxyfuel Pilot Plant - Realisation
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