11-Presentation on Combustion Control by Online Coal Balancing

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    The Principles Used InNew technologies combustion control

    In Coal fired stations

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    Poor fuel/air control drives need to

    operate at non-optimal excess air levels

    Comfort

    Zone

    A/FA/F

    Limited capability to controlcoal & air flow distribution toeach burner

    Historical boiler capability

    > Coal flow bias up to +/-30%

    > Combustion air flow bias

    up to +/- 20%Large burner-to-burner fuel-air ratio imbalance of up to

    +/- 36%

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    Combustion optimization can help offset

    problems due to low-NOx modifications

    Main Fuel

    Air

    Overfire Air

    Reburn Fuel

    O2/CO

    SensorsCombustionSensors

    Fuel & AirControls

    Optimization

    Methodology

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    Baseline boiler emissions and

    temperature characteristics

    2,450

    2,500

    2,550

    2,600

    2,650

    1.6 2.0 2.4 2.8 3.2

    Oxygen, % wet

    FEGT,deg.F Right

    Avg.

    Left

    FEGT

    0.00

    0.10

    0.20

    0.30

    0.40

    1.6 2.0 2.4 2.8 3.2

    Oxygen, % wet

    NOx,lb/MMBtu

    0.0

    0.2

    0.4

    0.6

    0.8

    1.0

    1.2

    CO,lb/M

    MBtu

    NOx

    CO

    NOX & CO Emissions

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    Significant stratification in gas

    temperatures and oxygen profile

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    Combustion sensors installed in furnace

    and in backpassSensors Installed:

    > In-situ CO sensors = 15

    > Combustion sensor(LOI/FEGT) = 5

    > Burner Profiler = 25

    O2/CO Sensor Probe

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    0

    20

    40

    60

    80

    100

    120

    140

    160

    180

    200

    220

    240

    260

    Sensor results prior to boiler

    optimization CO Sensor DataCombustion Sensors

    0

    1

    2

    3

    4

    5

    6

    7

    8

    9

    RelativeLOI

    1 2 3 4 5

    Sensor

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    Sensor response to changing oxygen

    CO Sensors Econ. O2 Probes

    2.86 3.71

    1.53 2.26

    3.57 3.10

    2.17 N/A

    2.30 3.29

    1.01 2.05

    3.55 3.00

    1.85 N/A

    1.57 2.54

    0.50 1.43

    3.06 2.55

    1.77 N/A

    1.15 2.08

    0.36 1.46

    2.69 2.23

    1.48 N/A

    Test #2

    3.0% O2

    0

    40

    80

    120

    160

    200

    240

    280

    320

    360

    400

    440

    Test #6

    2.7% O2

    Test #7

    2.2% O2

    Test #7

    2.2% O2

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    Coal flow balancing and measurement

    systems

    Automated Coal Flow Dampers

    Coal Flow Sensors

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    Balancing dampers can significantly

    improve coal flow balance

    0

    5

    10

    15

    20

    25

    30

    35

    CoalFlow

    Balance,

    %

    (abs

    olute)

    A1A2A3A4

    A5B1B2B3B4B5

    C1C2C3C4C5

    D1D2D3D4D5E1

    E2E3E4E5

    Coal Pipe

    Baseline

    Manually Balanced

    Balancing limited

    by low air velocities

    Balancing limited

    by low air velocities

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    Automatic balancing system is

    successful attaining and maintaining fueldistribution

    -25%

    -20%

    -15%

    -10%-5%

    0%

    5%

    10%

    15%

    Baseline Manual

    Tune

    Auto

    Tune

    B

    urnerCoa

    lFlow

    Bias

    Burner C1 Burner C2 Burner C3 Burner C4 Burner C5

    Fuel Balancing PLC

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    Distributing burner air properly is a

    critical step in combustion optimizationOnce fuel distribution is balanced, the initial

    burner air settings can be set uniformly.The next step in optimizing combustion is to trim

    air distribution.Burner air adjustments are made to move air toair-starved regions in the furnace and to improve

    air and fuel mixing within regions.

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    Further Combustion optimization

    through O2 / CO sensorsCO Profile after coal flow balancing only

    0

    60

    120

    180

    240

    300

    360

    420

    480

    540600

    660

    720

    780

    840

    900

    9601020

    1080

    1150

    CO Sensor Levels (relative ppm)High CO

    In Corner

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    Adjust right-to-left air balance using upper rear wall

    burners

    Further Combustion optimization through

    O2 / CO sensors

    0

    60

    120

    180

    240

    300

    360

    420

    480

    540

    600

    660

    720

    780

    840

    900

    9601020

    1080

    1150

    CO Sensor Levels (relative ppm)

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    Adjust right-to-left air balance using lower rear wall

    burners

    Further Combustion optimization through

    O2 / CO sensors

    0

    60

    120

    180

    240

    300

    360

    420

    480

    540

    600

    660

    720

    780

    840

    900

    9601020

    1080

    1150

    CO Sensor Levels (relative ppm)

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    0

    60

    120

    180

    240

    300

    360

    420

    480

    540

    600

    660

    720

    780

    840

    900

    9601020

    1080

    1150

    Adjust right-to-center air balance using upper rear wall

    burners

    Further Combustion optimization through

    O2 / CO sensors

    CO Sensor Levels (relative ppm)

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    Further Combustion optimization through

    O2 / CO sensorsFinal result (next day)

    0

    60

    120

    180

    240

    300

    360

    420

    480

    540

    600

    660

    720

    780

    840

    900

    9601020

    1080

    1150

    0.000

    0.001

    0.002

    0.003

    0.004

    0.005

    -400 -200 0 200 400 600 800

    Coal Flow Bias, %

    ProbabilityDistr

    ibutionFunction

    Initial

    Final

    CO Sensor Levels (relative ppm)

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    Summary

    Sensors, fuel/air controls, and tuning methodology provideopportunity for continuous combustion optimization

    Available technologies:

    > Combustion Sensors> Automated coal flow balancing

    > Tuning and Optimization

    Combustion optimization can permit operation at reduced excess airand lead to:

    > Reduced NOx

    > Improved efficiency

    > Reduced unplanned outages and load drops

    > Recovered derate or increased output