Worldwide Pollution Control Associationwpca.info/pdf/presentations/IL2010/An Unbiased Comparison of...
Transcript of Worldwide Pollution Control Associationwpca.info/pdf/presentations/IL2010/An Unbiased Comparison of...
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Worldwide PollutionControl Association
IL Regional Technical SeminarIL Regional Technical SeminarAugust 3-4, 2010
Visit our website at www wpca infoVisit our website at www.wpca.info
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An Unbiased Comparison of FGD Technologies: Wet, Spray Dry and CDS
WPCA ConferenceAugust 2010
Brandy JohnsonManager, FGD Project Development
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AgendaAgendaIntroduction to FGD TechnologiesIntroduction to FGD Technologies
Wet FGDWet FGDWet FGD Wet FGD
Spray Dry Absorber (SDA)Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGDCirculating Fluidized Bed FGD
Compare and Contrast TechnologiesCompare and Contrast Technologies
SummarySummary
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AgendaAgendaIntroduction to FGD Technologies
Wet FGDWet FGDWet FGD Wet FGD
Spray Dry Absorber (SDA)Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGDCirculating Fluidized Bed FGD
Compare and Contrast TechnologiesCompare and Contrast Technologies
SummarySummary
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FGD QuestionsFGD QuestionsPermit
RequirementsRegulations
q
Byproduct and
Availability of Ab b t
yWaste Water Permitting
AbsorbentsTechnology Preferences
Schedule Requirements
Design Fuel and Fuel
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q Fuel and Fuel Flexibility
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Flue Gas Desulfurization and Acid Gas ControlFlue Gas Desulfurization and Acid Gas Control
Spray Dry FGD• Up to 95% SO2 removal• Lower sulfur fuels• Typically <1.5% sulfur coalSpray Dry FGD
System
• Up to 98+% SO2 removal
Typically 1.5% sulfur coal• Dry product for landfill• Uses lime
Up to 98+% SO2 removal• High sulfur fuels (>1.5%)• More fuel flexibility• Marketable byproduct• Typically uses limestone
Wet FGD
Circulating Dry Scrubber
• Up to 98+% SO2 removal• Higher sulfur fuels (>1.5%)• More fuel flexibility• Dry product for landfill• Uses lime which is hydrated on site• Uses lime which is hydrated on site
Dry Sorbent• Usually lime or sodium based• Injected before particulate control device• Used for SO SO HCI control
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Injection • Used for SO2,SO3, HCI control
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AgendaAgendaIntroduction to FGD TechnologiesIntroduction to FGD Technologies
Wet FGDWet FGD
Spray Dry Absorber (SDA)Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGDCirculating Fluidized Bed FGD
Compare and Contrast TechnologiesCompare and Contrast Technologies
SummarySummary
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Typical Wet FGD ConfigurationTypical Wet FGD Configuration
Construction Services
Fabric FilterSO2 Scrubber
Boiler
SCR
Fabric Filter
SO3 and Mercury
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Coal Pulverizers
Boiler
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Characteristics of Wet FGD SystemsCharacteristics of Wet FGD Systems• Coal sulfur levels of 0.2 to 8%• Inlet SO2 ranges from 200 - 6500 ppmv • Removal efficiencies up to 99%• 98% removal typically required today• 98% removal typically required today• Installed on ~ 60% exist US coal boilers • Mature technology• One tower per boiler or boilers,
up to 1300 MW Added benefit: ability to remove• Added benefit: ability to removeoxidized mercury
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Scrubber with One TrayScrubber with One Tray
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Advantages and Disadvantages of Wet FGDAdvantages and Disadvantages of Wet FGD
AdvantagesAdvantages DisadvantagesDisadvantagesAdvantagesAdvantages DisadvantagesDisadvantagesHigh removal efficiency with any coal
Sampling of multiple points in process required to understand chemistry
High reagent utilization Typically requires wastewater treatment
Excellent fuel flexibility Alloys or coatings required for hl id t tichloride protection
Mature product High water usageWet stack required
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AgendaAgendaIntroduction to FGD TechnologiesIntroduction to FGD Technologies
Wet FGDWet FGDWet FGD Wet FGD
Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGDCirculating Fluidized Bed FGD
Compare and Contrast TechnologiesCompare and Contrast Technologies
SummarySummary
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Typical SDA ConfigurationTypical SDA Configuration
Fabric Filter
D
Boiler
SCR DryScrubber
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Coal Pulverizers
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Flue Gas Distribution R f G DiFlue Gas Distribution Roof Gas Disperser
60 / 40 Split
Central Gas Disperser
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Process Flow Sheet and Control BasicsProcess Flow Sheet and Control BasicsSO2 EmissionSetpointAbsorber Outlet Temperature
Setpoint
SO2 MonitorTCs
SDA FF / ESP
LimeRecycle SlurrySolids SetpointDensity
MonitorRecycle
Slaker Temperature Setpoint
H2O
H2O
ySolids
Lime – pressurized loopto feed multiple SDAs
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Recycle – gravity return individually for each SDA
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Advantages and Disadvantages of SDAAdvantages and Disadvantages of SDA
AdvantagesAdvantages DisadvantagesDisadvantagesMature product Limited to lower sulfur coalsRecycle usage lowers lime consumption
Increased dry byproduct to dispose
Simple chemistry checks – solids in slurry
Byproduct disposal requires care
Carbon steel construction Fairly high quality water required for slaking
Low water usageNo wastewater treatmentNo wet stack required
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AgendaAgendaIntroduction to FGD TechnologiesIntroduction to FGD Technologies
Wet FGDWet FGDWet FGD Wet FGD
Spray Dry Absorber (SDA)Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGD
Compare and Contrast TechnologiesCompare and Contrast Technologies
SummarySummary
Proprietary and Confidential WPCA Conference 8-10 .16© 2010 Babcock & Wilcox Power Generation Group, Inc. All rights reserved.
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Typical CDS Arrangementyp gStack
CDS
Absorbent Silo
CDS
Clean Gas Duct
Fabric Filter
ProductSilo
Clean Gas DuctRaw Gas
Duct
Flue GasDampers
ID-Fan Clean GasRecirculation
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Dampers
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Typical Process OverviewSO2
TClean gasClean gas
Typical Process Overview
T
CDS
Silo
CDSFilter
ID Fan
tack
tack
WaterProductrecirculationΔp StSt
Clean gas
RR
Product discharge to silo
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VRaw gasRaw gas
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CFD Modeling of ArrangementsCFD Modeling of Arrangements
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VenturisVenturis
Top viewTop viewTop viewTop view
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Bottom viewBottom view
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Water InjectionWater InjectionLower water consumption than wet systemsN t ti f lNo saturation of clean gasHigh pressure injection (~600 psi)Low quality water can be used Water feed control independent from sorbent feed
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Advantages and Disadvantages of CDSAdvantages and Disadvantages of CDS
AdvantagesAdvantages DisadvantagesDisadvantagesAdvantagesAdvantages DisadvantagesDisadvantagesWater evaporation independent of sorbent feed rate
Higher pressure drop
C b l i i h f dCarbon steel construction High pressure feedwater pumps required
Small footprint / compact plant arrangement
Byproduct transport requires carearrangementNo wastewater Elevated baghouseNo wet stack required
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AgendaAgendaIntroduction to FGD TechnologiesIntroduction to FGD Technologies
Wet FGDWet FGDWet FGD Wet FGD
Spray Dry Absorber (SDA)Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGDCirculating Fluidized Bed FGD
Compare and Contrast Technologies
SummarySummary
Proprietary and Confidential WPCA Conference 8-10 .23© 2010 Babcock & Wilcox Power Generation Group, Inc. All rights reserved.
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Absorber ConfigurationsAbsorber Configurations
Wet SDA CDS
Wet/Dry Interface Inlet quench Absorber Absorber
Si C t i t 400Size ConstraintsLargest single tower (MW)Limitations
~1000 ~300atomizer
~400bed stability
# Absorbers / Unit
Slurry pH
Single
5 - 6
Multiple
11 - 12
Multiple
N/ASlurry pH
Chlorides High
Saturated
Low
Above
Low
Above
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Flue Gas Saturated Above Saturation
Above Saturation
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Material of ConstructionMaterial of Construction
Wet SDA CDS
Absorber Tower AlloyTileFiberglass
Carbon Steel
Carbon Steel
Fiberglass
Nozzles / Atomizers Ceramic Alloy / Ceramic
CS venturis/Ceramic venturis/ceramic water
Flues Lined Carbon CarbonFlues Lined Carbon SteelCoatings
Carbon SteelCoatings
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ReagentsReagents
Wet SDA CDS
Stoichiometry
Type Limestone (CaCO3)Lime
Lime(CaO)Fly Ash
Lime(CaO)Fly Ash
SodiumTypical Cost $5 - 25/ton $60 -
120/ton$60 –120/ton
Preparation Wet grinding
Grinding Slaking
Hydration
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By-Product StreamsBy Product Streams
Wet SDA CDSSolids
Composition CaSO4 Fly ashCaSO3C SO
Fly ashCaSO3C SOCaSO4
CaCl2CaSO4CaCl2
B fi i l U G A ABeneficial Uses GypsumWall-boardCement additive
AggregateMine reclaimCement
AggregateMine reclaimCement
additive
Landfill Dry / pond Dry Dry
Water Treatment None None
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Water Treatment None None
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EconomicsEconomics
Wet SDA CDSCapital Costs
Reagent Usage
Power Usage
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Lifecycle EconomicsLifecycle Economics
Wet SDA CDSEastern Mid-High Sulfur Fuel with high removal
i t
Typically N/A
requirements, <~400MW
Eastern Mid-High T i ll N/A
gSulfur Fuel with high removal requirements,
Typically N/A
>~400MWWestern Fuels
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AgendaAgendaIntroduction to FGD TechnologiesIntroduction to FGD Technologies
Wet FGDWet FGDWet FGD Wet FGD
Spray Dry Absorber (SDA)Spray Dry Absorber (SDA)
Circulating Fluidized Bed FGDCirculating Fluidized Bed FGD
Compare and Contrast TechnologiesCompare and Contrast Technologies
Summary
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Summary of Wet Spray Dry and CDS FGDSummary of Wet, Spray Dry and CDS FGD
Wet FGD Wet FGD Spray Dryer Spray Dryer CDS CDS
Typically, the lower lifecycle cost for larger
Typically, the lowest lifecycle costs if required
Typically, the lower lifecycle cost for smaller g
units burning high S coal and requiring high SO removal
qSO2 removal is achievable
units burning high S coal and requiring high SO removalSO2 removal SO2 removal
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Thank YouThank You.
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