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Presentation on Heat Rate Improvement

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  • 8/9/2019 Presentation on Heat Rate Improvement

    1/22

    Research Triangle Park

    Steve Scavuzzo

    Babcock & Wilcox Co.

    Technical Consultant

  • 8/9/2019 Presentation on Heat Rate Improvement

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    • Plant Efficiency = Net Plant Heat Rate (NPHR)

    • HHV or LHV >4% Difference by definition

    • NPHR = (Fuel Input) / (KWGROSS

    – KWAUX

    ), btu/kWh

    • Generating Efficiency = (Turbine Eff.) (Boiler Eff.)

    • Combined =

    ~36-42% ~ 84-90%

    30-38%

  • 8/9/2019 Presentation on Heat Rate Improvement

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    On the Steam Side

    On the Bo i ler Side

    Efficiency is a Function of:• Gas Temp Leaving the air heater • Ambient Temp• Excess Air • Unburned Combustibles• Fuel Properties

    Cycles and the Second Law In 1823 Carnot Said: Max Efficiency = ≈ 65% for typical rankine cycles

    T0 = Heat Sink TemperatureT1 = Temperature at which heat is added

    • Increase T1

    to improve efficiency• Primary limiting factor is cost and availability of materials

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    A ir Heater Perfor m ance

    Affects every air pollution control and combustion device in the plant

    BURNERS

    COMBUSTION

    EMISSIONS

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    A ir Heater Perform ance

    Poorly maintained Air Heaters could degrade plant heat rate by 0.7 to 0.9%.

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    Penthouse Roof Seals Access and Observation doorsExpansion JointsFurnace Hopper Seal

    A ir Heater Perform anceMinimize Boiler Setting Air In-leakage

    Setting Leakage• Degrades Air Heater

    Performance3% air leakage ≈ +10F ≈ - 0.25% Eff

    • Degrades Combustion Systemperformance – Increases UBCL

    and some emissions

    • Requires operation at higher totalexcess air – Increases stacklosses and ID/FD fan powerconsumption

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    • Maintain boiler cleanlinessto minimize exit gastemperature and stacklosses

    A 30F Reduction in boilerexit gas temperature≈ 0.25% Heat Rate

    • Implement Intelligentsootblower control tooptimize absorptiondistribution and heat rate

    Air Heater Perform anceOperation and Maintenance of Boiler Cleaning Equipment

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    A ir Heater Perform anceOperation and Maintenance of Coal Pulverizers

    • Proper maintenance of pulverizer wearparts will increase fineness and decreasedrive motor power consumption.Increased fineness reduces unburned

    carbon loss (UBCL) and possiblyemissions

    • Upgrading to a dynamic classifier willimprove coal fineness and reduce UBCL

    • Upgrading to an auto-loading systemoptimizes primary air fan and pulverizermotor power consumption, and coalfineness

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    Ensu re Prop er O2 Measurement and Con trol

    • Due to O2 Stratification at normal measurement locations, multiple instrumentsshould be installed in a grid arrangement

    • Improper O2 measurement and control lead to off-design excess air, emissionsexcursions, slagging and fouling, absorption maldistribution, and other problems

    that degrade boiler and emissions performance, and heat rate

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    Turbine Steam Path Upg rades ≈ 4 % imp rovement in NPHR

    • Incorporate peak generating load increase

    • Requires boiler heating surface modifications to match the boiler to the revisedturbine conditions

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    Heat rate degrades as load is reduced

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    • Split / Sliding Pressure Operation

    • Allows the furnace to operate at fullpressure with turbine throttle valveswide open - full steam temperature

    to the 1 st stage - at all loads

    • Permits increased load change ratecapability

    • Can be retrofitted onto drum or once-through boilers

    • Extends RH steam temperature controlrange (better low load heat rate) Drum Boiler

    Once Through Boiler

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    • Variable Frequency Drives for Large Fans and Pumps

    • In a typical modern coal fired power plant, air and gas fans consume2-3% of gross generator electric output

    • VFDs allow fans to operate more efficiently over the rangeof ambient conditions and fuel variations

    • Most significant efficiency gains realized during reduced load operation

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    • Economizer resurfacing / heatingsurface addition

    • Air Heater Basket Upgrades

    Not a Viable Option for all Units

    • Lower economizer exittemperature reduces SCR controlrange

    • Air heater exit gas temperaturemay already be at the dew pointlimit

    Reduce Boiler Exit Gas Temperature

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    Condensing Heat Exchanger • Water vapor formed during the combustion process results in

    a large stack heat loss≈4% for a typical coal fired unit – about 1/3 of the total losses≈10% for a typical Nat. Gas fired unit – about 2/3 of the total losses

    • Most of the lost energy is due to latent heat of vaporization

    Opportunity• Condensing heat exchanges could be used to reclaim a large

    percentage of this lost energy

    Why it isn’t already a routine practice• Heat exchangers are large and expensive• Corrosion is a problem to address• What to do with the low grade energy

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    Combustion Efficiency• Burners• Overfire Air Systems• Pulverizer Upgrades

    OpportunitiesNew burners and OFA systems optimized with CFD• Reduce total excess air: 5% reduction ≈0.2%

    NPHR• Reduce UBCL

    • Maintain or reduce NOx and CO emissions

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    Su b c r i t ic al Su p erc r i t ic al (B o th at 1000/1000F

    2750

    2800

    2850

    2900

    2950

    S p e c i

    f i c

    C o a

    l C o n s u m p

    t i o n

    ( g / k W h )

    2.4Heatrate

    imprvm.

    Steam pressure @ Turbine Inlet (psig)Source: Siemens,KWU FTP2/Ka/Gs

    30.6.1997

    Data based on:2 x 660 MW units

    6500 hr/aLHV = 25MJ/kg

    2400 psigSubcritical

    3600 psigSupercritical

    5.5Heat

    rateimprvm.

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    16% better heat rate and lowerCO

    2emissions

    @ nominal 600 MW NETAverage heat rate 8858 Btu/kWhin 2013

    US Fleet Average 10,555Btu/kWh

    * Power Engineering July 2014

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    +11% reduction in fuel consumption and CO 2 emissions vs. 600C plant heat rate+29% reduction vs. the current fleet average heat rate and CO 2 emissions –could replace existing units with new A-USC plants and meet EPA CO 2 goalwithout carbon capture

    • Lower flue gas handling equipment size and fan power • Lower plant fuel handling• Lower fuel transportation system impact• Lower water consumption and condenser heat duty

    Lower CO 2 emitted and auxiliary power consumption for capture

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    +$15.2 million by B&W in previous 12 years for A-USC

    • Fireside Corrosion and Coatings

    • Steam Side Oxidation

    • Welding and Manufacturing Development

    • Conceptual Design Studies

    • Header Design 600C and 700+C (B&W projects)

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    • Opportunities to improve efficiency of existing fleet without significant capitalinvestment are incremental and unless the unit is ill-maintained, will not resultin large improvements to NPHR (


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