Update on Oxy-fuel Combustion System Design for Natural Gas … · 2013. 1. 11. · 2013 Research &...
Transcript of Update on Oxy-fuel Combustion System Design for Natural Gas … · 2013. 1. 11. · 2013 Research &...
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Update on Oxy-fuel Combustion System Design for Natural Gas-fired Power Plants
Chendhil Periasamy and Rob Gagliano l DRTC l R&D-Combustion l Air Liquide
McIlvaine Company Hot Topic Hour January 10, 2013
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Air Liquide, world leader in gases for industry, health and the environment 2013 Research & Development
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Overview
■ Oxy-fuel Combustion Process with FGR
■ Current Activities at Air Liquide
■ Recent Developments
■ Burner Design
■ Combustion System Optimization
■ Challenges Ahead
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Oxy-fuel Combustion Process Overview
■ Oxy-fuel combustion process with flue gas recirculation
Key Drivers:
Clean power generation
■ Lower emissions with CO2 capture
Enhanced oil recovery
■ Steam or CO2 injection
Flue Gas Capture and TreatmentFuel CO2 capture/
sequestration
Flue Gas Recirculation
Oxygen
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Activities at Air Liquide
Level of Activities
■ Technology development
- R&D and semi-pilot scale
■ Demonstration
- Pilot and large scale
■ Collaboration with industrial and academic partners
Flue Gas Capture and TreatmentFuel CO2 capture/
sequestration
Flue Gas Recirculation
Oxygen
ASU Oxygen
Production
CryoCapTM
PSA
Gas-oxy
Burners
Air Liquide R&D Center ,
Delaware, USA
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Oxy-fuel Combustion – Key Challenges
■ Design considerations
Operational requirement
■ Oxy only or Oxy with air back up
Emission levels
■ Burner design
Flame stability
Control of heat flux distributions
Optimization of pollutant emission levels
■ Combustion system operation
Air, oxygen, or any combination
Optimization of flue gas recirculation
Integration with other components
Large-scale oxy flame, Farzan et al. (2008)
Pilot-scale oxy flames (air mode), Marcano et al. (2011)
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Experimental Test Facilities
■ Major R&D Centers for Combustion:
CRCD – France, DRTC – USA
1 MW and 6 MW test boilers
■ Burner operations up to 6 MW with
closed-loop heat extraction
■ Flue gas capture, treatment and
recirculation
■ Flexible fuel options with full oxy to any
level oxy-enrichment tests
■ Fully integrated, automated test facility
1 MW
6 MW
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Developments in Gas Oxy Burner
■ No Oxygen-FGR premixing
■ Control of FGR and oxygen
injection to burner
■ Flexible start-up in oxygen or
air mode
■ Ultra-low NOx design
■ Matched heat transfer profile
ICCD image of near-
flame zone with FGR
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Combustion System Operation
■ Start-up in oxy or air mode; Heat-up FGR lines
■ Initiate flue gas recirculation to burner and attain stable flame
■ Adjust FGR ratio by controlling:
Flame stability
O2 content in flue gas
CO level
BURNER
Fuel
Oxygen
RFG
Test ChamberFlue Gas
FGR Ratio
= X / Y
Y
X
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Influence of Flue Gas Recirculation Ratio
■ FGR impacts:
Flame stability
NO emission level
Load on related systems
■ Significant decrease noticed in NO at higher FGR
0
0.25
0.5
0.75
1
No FGR FGR = 1 FGR = 2 FGR = 3
Reference NO level = 1 unit
Influence of FGR on NO level
FGR = 2
FGR = 3
Air or Oxy mode also
influences the selection
of FGR ratio!
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Developments in Computer Modeling
■ Specific to oxy-combustion
■ Fine-tuned with experimental data
■ Our approach:
Develop and validate models at lab
scale and intermediate scale
Use the model for scale-up to pilot
scale and full scale designs
Provides confidence to our design
Simulation results of gas-oxy burners
for Lacq pilot
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Challenges Ahead
Technical
development
at lab scale
Validation at
lab scale
Large-scale / Full-scale Demonstration
Modeling and
Design
Improvements
Pilot scale testing and integration
with other systems
Market
Drive
Government
Regulations
More combustion
models specific to
oxy-combustion
w/ FGR
Design scale-up rules for
different sizes
Availability of test facilities
Characterization of in-flame
structure for better understanding
of burner design
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Thank you for your attention