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Circulating Fluidized Bed Boilers
Experience, Capabilities & Performance
© Metso Automation Inc. 2003 Title/AuthorDate2
Fluidized Bed Combustion (FBC) technology…achieved through efforts of government initiatives in US and Europe
Applied to small and mid-size industrial and utility plants…
• Why CFB?
- Wide range of coals & heating values
- Opportunity fuels (biomass)
- Hard-to-Burn fuels (petroleum coke, tires)
- Excellent emission performance
- Minimizes DeSOx / DeNOx systems
• CFB has reached utility scale
- Sizes over 300 MWe in operation
- 460 MWe under construction
CFB BOILER2x274 MWth, 112 kg/s, 135 bar, 538 °C
EC Chorzów Elcho Sp. zo.o., Chorzów, Poland
Control strategies perfected over 25 years of collaboration between Metso Automation and Kvaerner Power (now Metso Power)
© Metso Automation Inc. 2003 Title/AuthorDate3
Metso Automation FBC Experience – over 100 units…up to 460 MWe
050
100150200250300350400450500
1988 1993 1995 2000 2001 2002 2003 2005 2006 2007
Un
it S
ize
MW
eLagizsa
Xia Lang Tan 1 &2
Alholmens
Xin Jian Si 1 & 2Scrubgrass Yi Bin
Rauhaladati
Mt Poso
Control systems on over 300,000 MW worldwide.
© Metso Automation Inc. 2003 Title/AuthorDate5
A notable example of utility sized CFBC - Alholmens, Finland … world’s largest single bio-fired CFBC boiler
• Output: 240MWe plus + 165MW of process steam (1.5 millions #/hr)
• Fuel: bark, wood chips, recycled paper & plastic, peat, coal
• Single CFBC boiler from Metso Power
© Metso Automation Inc. 2003 Title/AuthorDate6
Alholmens Control Room
© Metso Automation Inc. 2003 Title/AuthorDate8
Another notable installation - Narva, Estonia
Balti Elektrijaam• 2 Foster Wheeler CFB Boilers• 215 MWe • 714 000/599 000 lb/h,1842/348 PSI • 995/995F• Fuel: Oil shale• District heating 160 MWth
Eesti Elektrijaam• 2 Foster Wheeler CFB Boilers• 215 MWe • 714 000/599 000 lb/h,1842/348 PSI• 995/995F• Fuel: Oil shale
© Metso Automation Inc. 2003 Title/AuthorDate9
Xiao Long Tan 2X300 MW CFB…Yunnan, PRCLargest CFB in China
• Owner: Guodian IPP
• Commercial operation: 2006
• Fuel: Lignite
• Boiler: Shanghai Boiler Works (Licensee of CE Alstom)
• Controls: Metso Automation
Yunnan Xiao Long Tan Power Plant
© Metso Automation Inc. 2003 Title/AuthorDate10
Lagizsa, Poland… world’s first supercritical CFB
• Single Foster Wheeler CFBC
• Unit size 460 MW
• Fuel: anthracite
• Pressure: 3988 PSIA
• Temperature: 1040°F
• Efficiency: 45.3%
• Startup: 2007/08
© Metso Automation Inc. 2003 Title/AuthorDate12
Circulating Fluidized Bed Boilers
Unique Issues and Challenges
© Metso Automation Inc. 2003 Title/AuthorDate14
Typical CFB plant with cyclone separator…
Convection Pass
Superheater
Economizer
Steam Drum
Secondary AirPorts
BedTemperature
CycloneSeparator
High Density
GovValves
Primary AirFan
GasRecirc
Fan
Secondary AirDamper
Secondary AirFlow
AirPreheater
Steam CoilAir Heater
FD Fan
ID Fan
Bag House
FuelFeeder
Turbine
Stack
PrimaryAir Flow
Primary SH locatedin Loop Seal
© Metso Automation Inc. 2003 Title/AuthorDate15
FBC Issues and challenges…
Disturbances are caused by…
• Low quality fuels with varying heating values
• Multiple fuel firing with varying mixture and moisture
• Load demand requirements from steam host and/or generation requires fast response and greater turndown
The consequences…
• Higher emissions
• Lower efficiency
• Imbalance between demand and supply
All lead to higher operating costs!
© Metso Automation Inc. 2003 Title/AuthorDate16
Objectives dependent upon only a few controlled variables…
NOx SO2
T
TO2 CO
T, pdT
F, P, TT
T
Objectives...• lower emissions• higher efficiency• process parameters within permitted limits• easy operation• automatic control throughout entire load rangecan be achieved...
by controlling...• fuel feed• combustion air• air distribution• limestone injection
by controlling...• fuel feed• combustion air• air distribution• limestone injection
The challenge… only a relatively few controlled variables to effect change
Circulating Fluidized Bed Boilers
Control strategies to meet objectives…
© Metso Automation Inc. 2003 Title/AuthorDate18
What control strategies are required to meet overall objectives?
1.Coordinate boiler with turbine - Match generation to demand – AGC capability to trade in energy market
- Advanced Model Predictive Control (MPC) – provides correct demand to turbine and boiler under all conditions
- Match boiler inputs with turbine energy requirement – maximize efficiency
2.Compute and control true “heat release” - Detect changes in fuel heating value – maintain constant steaming rate
- Totalize “heat release” from all sources – maintain constant overall fuel flow
- Maintain proper fuel air ratio over entire load range – maximize efficiency
3.Optimize bed/furnace temperature - Maintain temperature within operating range - lower limestone usage
- Maximize sulfur calcium association – lower SOx emissions
- Lower overall combustion temperature – lower NOx emissions
Circulating Fluidized Bed Boilers
Advanced Control Strategy 1…
Coordinated Control
© Metso Automation Inc. 2003 Title/AuthorDate21
Let us not forget the main purpose of this plant… generate electricity
• Must control generation to demand
• Must provide AGC capability
• Must operate at maximum rate of change
• Must protect the unit when equipment is not performing
at optimal conditions
© Metso Automation Inc. 2003 Title/AuthorDate22
Strategy 1 - Coordinate boiler with turbine… proven coordinated front end with Model Predictive Control.
Furnace Pressure toID Fan Control
Convection Pass
Superheater
Economizer
Steam Drum
Secondary AirPorts
BedTemperature
CycloneSeparator
High Density
O2Correction
FuelControl
EnergyDemand
GovValves
Bed TempControl
Primary AirControl
Primary AirFan
GasRecirc
Fan SecondaryAir Control
Secondary AirDamper
Secondary AirFlow
Forced DraftAir FlowControl
PressureSetpoint
AirPreheater
Steam CoilAir Heater
FD Fan
FurnacePressureControl
FurnacePressure
ID Fan
Bag House
FuelFeeder
Fuel FeedDemand
Feedforward
AirflowDemand
Pri Air /Sec AirRatio
FuelDemand
GenerationControl
Turbine
Frequency
StackMPC
MW
© Metso Automation Inc. 2003 Title/AuthorDate23
L
H
PID
PI
FIRST STAGE
PRESSURE
v
AAUnit Demand
Generation ControlInc. Dec.
ADS
A
T
FrequencyBias
PI
L
MW
Inc.Limit
Dec.Limit
RateLimit
TurbineBaseMode
Position Demandto E-H-C
BlockOverride
Main SteamPressure
PressureSet Point
Boiler DemandCoordinated Mode
T
11:47am Stop
11:07pm Start Down
9:55am Start
50 100 150 200 250 MEGAWATTS
Closed loop generation control provides a linear response…
© Metso Automation Inc. 2003 Title/AuthorDate24
Unit 1 without new system (blue)
Unit 2 with new system (Red)
Fast accurate response to AGC commands..
© Metso Automation Inc. 2003 Title/AuthorDate25
Constraint coordinator protects unit… slows rate of change in the event equipment or process is not operating at optimum
D-E-BGeneration
ControlAlgorithm
1st StagePressure
GrossGeneration
Frequency
MW Demand fromLoad Dispatch
Office
MW Demand Setby Plant Operators
Interfaceto
TurbineGovernor Valves
D-E-BUnit Demand
Algorithm
Rate LimitingHigh/ LowLimiting
ConstraintCoordinatorAlgorithm
Process Variables& Auxiliaries
Status
Overrides fromBoiler Control
Maximum ramp rate3% per minute
Constraint coordinator cutsramp rate to 1.5% per minutebecause of process orequipment limitations.
Constraint coordinatorstops ramp until conditionclears
Constraint coordinatorresumes normal ramp.
LO
AD
Time
Circulating Fluidized Bed Boilers
Advanced Control Strategy 2…
Fuel Power Compensator®
© Metso Automation Inc. 2003 Title/AuthorDate27
Strategy 2 - Advanced application to compute and control true “heat release” from all fuel sources and detect changes in heating value
Steam Flow Steam Pressure Steam Temperature Feedwater Flow Feedwater Temperature Air Flow Air temperature Flue Gas Flow Flue Gas Temperature Oxygen Level Solid Fuel Flow
Heat BalanceCalculation
OxygenConsumption
Bias for Changein EnergyContent
Fuel Power Compensator® –
Computes true “heat release” and corrects fuel and airflow demand.
© Metso Automation Inc. 2003 Title/AuthorDate29
Typical CFB with Fuel Power Compensator®…
Furnace Pressure toID Fan Control
Convection Pass
Superheater
Economizer
Steam Drum
Secondary AirPorts
BedTemperature
CycloneSeparator
High Density
O2Correction
FuelControl
EnergyDemand
GovValves
Bed TempControl
Primary AirControl
Primary AirFan
GasRecirc
FanSecondaryAir Control
Secondary AirDamper
Secondary AirFlow
Forced DraftAir FlowControl
PressureSetpoint
AirPreheater
Steam CoilAir Heater
FD Fan
FurnacePressureControl
FurnacePressure
ID Fan
Bag House
FuelFeeder
Fuel FeedDemand
FeedforwardAirflowDemand
Pri Air /Sec AirRatio
FuelDemand
GenerationControl
Turbine
Frequency
Stack
Fuel PowerCompensator
Steam Flow
Steam Temp
FW Temp
Air Temp
Flue Gas Temp
Fuel Flow
Steam Pres
FW Flow
Airflow
Flue Gas Flow
Oxygen
MPC
© Metso Automation Inc. 2003 Title/AuthorDate31
Increasing coal content in coal/bio-fuel mixture
coal
O2
steam flow
Fuel Power Compensator®...performance at Alholmens 240MW CFB plant
Circulating Fluidized Bed Boilers
Advanced Control Strategy 3…
Combustion Optimizer
© Metso Automation Inc. 2003 Title/AuthorDate33
Bed/furnace temperature and fuel/air ratio directly effect emissions, performance, operating cost… and are a function of many different variables…
SO2
HgNOX
CO2
Opacity
CO
Carbon in flyash
Slagging
Air heater fouling
• Process is difficult to model• Process defined by multiple differential equations • Process changes over time• Feedforward / feedback control cannot deal with all scenarios• Requires input based upon operating experience
CaCo3
© Metso Automation Inc. 2003 Title/AuthorDate34
© Metso Automation Inc. 2003 Title/AuthorDate35
Good bed management:
• Lower emissions
• Lower agglomeration
• Greater turndown
• Stable combustion
Poor bed management:
• Higher emissions
• Forced outages
• Less stable combustion
• Higher agglomeration due to hot spots
Bed material and temperature management:
© Metso Automation Inc. 2003 Title/AuthorDate36
An important reason to optimize bed temperature…it can cost you!
Operating outside of the optimum temperature range can cost big bucks for extra limestone!
© Metso Automation Inc. 2003 Title/AuthorDate37
NOX formation vs temperature and nitrogen content of the fuel…
© Metso Automation Inc. 2003 Title/AuthorDate38
SNCR…Selective Non-catalytic Reduction is temperature sensitive
• Ammonia (NH3) or urea (NH22CO) sprayed into the flue gas in the presence of oxygen to produce N2
• Reaction produces water and urea in addition to CO2
• If temperature is too low the ammonia does not completely react with the NO2 and causes ammonia to be released into the atmosphere …
…called “ammonia slip” Requires precise furnace temperature control!
© Metso Automation Inc. 2003 Title/AuthorDate39
The best solution is to…
• Utilize all available process data
• Make calculations that describe and predict performance
• Incorporate operator know-how, expertise and intuition
© Metso Automation Inc. 2003 Title/AuthorDate43
Tuning parameters• fuel/air• prim./sec. air• lower/upper sec. air• O2-controller setpoint• fuel distribution
Tuning parameters• fuel/air• prim./sec. air• lower/upper sec. air• O2-controller setpoint• fuel distribution
1. Calculated variables• fuel heating value• oxygen consumption• flue gas flow• emissions mg/MJ
1. Calculated variables• fuel heating value• oxygen consumption• flue gas flow• emissions mg/MJ
NOx SO2T
T O2 CO
T, pdT
F, P, T
T
T
3. Operator know-how3. Operator know-how
2. Measurements2. Measurements
(control/Compensation/
Filtering / Recipe)
Fuzzy-logic
Ad
van
ced
Co
ntro
lsFuzzy logic for Fluidized Bed BoilersPrincipal structure...
© Metso Automation Inc. 2003 Title/AuthorDate44
Bed Temperature before (upper chart) and after optimization (lower Chart)…
© Metso Automation Inc. 2003 Title/AuthorDate45
Typical CFB with Combustion Optimizer
Furnace Pressure toID Fan Control
Convection Pass
Superheater
Economizer
Steam Drum
Secondary AirPorts
BedTemperature
CycloneSeparator
High Density
O2Correction
FuelControl
EnergyDemand
GovValves
Bed TempControl
Primary AirControl
Primary AirFan
GasRecirc
Fan
SecondaryAir Control
Secondary AirDamper
Secondary AirFlow
Forced DraftAir FlowControl
PressureSetpoint
AirPreheater
Steam CoilAir Heater
FD Fan
FurnacePressureControl
FurnacePressure
ID Fan
Bag House
FuelFeeder
Fuel FeedDemand
Feedforward
AirflowDemand
Pri Air /Sec AirRatio
FuelDemand
GenerationControl
Turbine
Frequency
Stack
Fuzzy LogicController
Tbed
dTbed
Pair
Load
Pri Air Flow
Recyle GasFlow
Fuel PowerCompensator
Steam Flow
Steam Temp
FW Temp
Air Temp
Flue Gas Temp
Fuel Flow
Steam Pres
FW Flow
Airflow
Flue Gas Flow
Oxygen
MPC
© Metso Automation Inc. 2003 Title/AuthorDate46
A performance story… Alholmens availability
On-line (%) Forced Outages (hrs)
Avail (%)
2001 96.2 none 100
2002 93.0 276 96.7
2003 96.2 None 100
© Metso Automation Inc. 2003 Title/AuthorDate47
Metso’s goal... To be the outstanding supplier for environmentally driven energy solutions.
• Over 100 FBC boilers under control
• Over 400,000 MW under control
• Fast responsive generation control
• Advanced control applications for FBC boilers
• Fuel Power Compensator® computes true Heat Release
• Fuzzy logic controller for bed temperature optimization