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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
2/22
• 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
3/22
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
8/9/2019 Presentation on Heat Rate Improvement
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A ir Heater Perfor m ance
Affects every air pollution control and combustion device in the plant
BURNERS
COMBUSTION
EMISSIONS
8/9/2019 Presentation on Heat Rate Improvement
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A ir Heater Perform ance
Poorly maintained Air Heaters could degrade plant heat rate by 0.7 to 0.9%.
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
9/22
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
8/9/2019 Presentation on Heat Rate Improvement
10/22
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
8/9/2019 Presentation on Heat Rate Improvement
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Heat rate degrades as load is reduced
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
13/22
• 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
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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8/9/2019 Presentation on Heat Rate Improvement
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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.
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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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
8/9/2019 Presentation on Heat Rate Improvement
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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)
8/9/2019 Presentation on Heat Rate Improvement
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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 (