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Experiences from the Lahti and RuienPlants
25th of May 2005Timo Anttikoski
Foster Wheeler Energia Oy
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
• Circulating fluidized bed (CFB) boilers- Up to 600 MWe, all solid fuels
• Bubbling fluidized bed (BFB) boilers- Up to 100 MWe, biomass, & other
high volatile fuels
• Atmospheric CFB gasifiers
• Heat recovery steam generators (HRSGs)- For gas turbines up to 250 MWe
Foster Wheeler Global Power GroupProducts
• Pulverized coal-fired (PC) boilers- Up to 1,000 MWe
• Waste heat boilers (WHBs)- For metallurgical and
waste incinerating processes
• Package boilers
• Condensers and heat exchangers
- Repairs and spare parts- Boiler modifications- Process improvements- Emergency service- Coal mills, burners- Environmental retrofits (BFB, SCR, SNCR, etc.)- OM&S agreements
• Complete boiler islands/power plants- EPC deliveries
• Service
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
EC
Ch
orz
ów
Elc
ho
The world leader in fluidized bed boiler technology
227 CFB BOILERS DELIVERED TO DATE
• 202 in operation• 25 under construction• Largest unit currently in operation: 300 MWe• Largest unit contracted: 460 MWe
Over 40 years experience in fluidized bed combustion
• First BFB boilers delivered in the 1970s, based on work started in the 1960s• World’s first CFB for power generation supplied in 1979; second-generation technology in 1992• World’s first once-through supercritical CFB project won in 2003• Benefits: simple construction, reliable, excellent efficiency and availability, multifuel capability• Meets tough emission regulations without additional flue gas cleaning systems
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Foster Wheeler Gasifier Concept
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Foster Wheeler Atmospheric CFB/BFB Gasification
• Developed in the end of 1970’s - in the beginning of 1980’s
• Driving force the dramatical increase in oil price
• First commercial applications produced gas for lime kilns (4 units)
• Foster Wheeler has supplied 7 commercial scale CFB/BFB gasifiersproducing low heat value gas for different applications
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Foster Wheeler Atmospheric Gasifier References
Hans Ahlstrom Laboratory, Finland 3 Misc. Test unit 1981
Oy W. Schauman Ab, Finland 35 Lime kiln fuel 1983
Norrsundet Bruks Ab, Sweden 25 Bark Lime kiln fuel 1984
ASSI Karlsborg, Sweden 27 Bark Lime kiln fuel 1984
Portucel, Rodao, Portugal 15 Bark Lime kiln fuel 1985
Kemira Oy, Vuorikemia, Finland 4 1986
Lahden Lämpövoima Oy, Finland 40-70 Biofuels 1997
Corenso United Ltd., Finland 40 2000Aluminious plastic waste Cyclone cleanedgas to boiler
Electrabel, Belgium 50 Biofuels 2002
Customer MW Fuel Application Year
Coal, peat
Bark, sawdust
Test unit, clean gas
Hot raw gas to boiler
Hot raw gas to boiler
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Foster Wheeler CFB Gasifier
850 °C
900 °C
BOTTOM ASH COOLING SCREW
HOT LOW CALORIFICGAS (750 - 650 °C)
UNIFLOW CYCLONE
BIOFUEL FEED
REACTOR
BOTTOM ASH
GASIFICATION AIR FAN
COOLING WATER
AIR PREHEATER
RE
TU
RN
LE
G
850 °C
900 °C
BOTTOM ASH COOLING SCREW
HOT LOW CALORIFICGAS (750 - 650 °C)
UNIFLOW CYCLONE
BIOFUEL FEED
REACTOR
BOTTOM ASH
GASIFICATION AIR FAN850 °C
900 °C
BOTTOM ASH COOLING SCREW
HOT LOW CALORIFICGAS (750 - 650 °C)
UNIFLOW CYCLONE
BIOFUEL FEED
REACTOR
BOTTOM ASH
GASIFICATION AIR FAN
COOLING WATER
AIR PREHEATER
RE
TU
RN
LE
G
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
• Concepts– Gasification à combustion of raw product gas– NEW: gasification + gas cooling and filtration à combustion of clean
product gas
• Energy production– Co-combustion of raw gas / clean gas in existing PC boiler– NEW: stand alone plant with steam turbine island
• Size of gasifier– Raw gas 20 – 150 MWfuel– Clean gas 20 – 80 MWfuel
• References– Lahti Energia 40 – 70 MW (raw gas, co-firing)– Corenso Varkaus 50 MW (raw gas, stand alone)– Electrabel Ruien, Belgia 50 MW (raw gas, co-firing)
Status of FW Fluidized Bed Gasification
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Fuel: Status:
Wood, bark, chips, saw dust Commercial
REF, plastics, (RDF) Commercial
Coal, straw, peat, RDF Demonstrated
ASR (Automotive ShredderResidue), other special wastes Under development
Fuels Used in FW CFB Gasifiers
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
ReferencesLahti & Ruien
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Power Station Kymijärvi, Lahti Finland
GASIFIER
MAIN BOILER
(OLD PC BOILER)
BIOFUEL PREPARATION PLANT
COAL BUNKERS & MILLS
COAL YARD
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Bottomash
Gasifier
Coal
540 °C/170 bar
Processing
Biomass
Fly ash
Pulverized coal flames
Gas flame
Natural Gas
50 MW
350 GWh/a -15 % fuel input
1850 GWh/a -80 %
360 MW
100 GWh/a -5 %
Power* 600 GWh/aDistrict Heat* 1000 GWh/a
Lahti Gasifier Process
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005 Lahti Gasifier
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN PROCESS
Bottomash
Gasifier
Coal
540 °C/180 bar
Processing
Biomass
Fly ash
Pulverized coal flames
Gas flame
50 MW
100.000 ton/year
500.000 ton/year
540 MW
CO2 Reduction –120.000 ton
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005Electrabel Ruien Gasifier
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Electrabel Ruien Gasifier
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Ruien Design
• Biomass gasifier producing “green electricity” in co-combustion with coal in an existing PC boiler
• Using of renewable fuels to cut CO2 emissions
• Design 50 MWth with 50 % fuel moisture (86 MWth with 20 % fuel moisture)
• Electric efficiency 34 % (Boiler 36 %, gasifier 98 %)
• Produced “green” electricity 17 MWe
• Annual production 120 GWh
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN GASIFIER REACTOR
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN CYCLONE
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN GASIFIER REACTOR
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN, AIRHEATER
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN, PRODUCT GAS BURNER
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Experiences from Lahti & Ruien
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Lahti fuels
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Lahti fuel conveyor
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Lahti Fuels
6348 49
3925
14
9
9 1515
3136
15
2329
34 31 38
5 147 11 11 11
0 %
20 %
40 %
60 %
80 %
100 %
225GWh
342GWh
295GWh
445GWh
407GWh
415GWh
1998 1999 2000 2001 2002 2003
YEAR
Rlw. Sleepers
Tires
Paper
Plastic
REF
Wood w. glue
Wood
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
LAHTI OPERATIONAL EXPERIENCES 1998-2003
• Stable operation of the Gasifier and Gas Burners
• Coal combustion in the main boiler has not been disturbed by thegasifier
• No additional fouling or corrosion in the main boiler has been noticed compared to coal combustion
• Main boiler fly ash composition and utilization has not been changed
• Main boiler availability has not been worsened by the Gasifier
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Gasifier Effects To Main Boiler Emissions
NOx Decrease 10 mg/MJ (= 5 ... 10 %)
SOx Decrease 20 - 25 mg/MJ
CO No change
HCl Increase 5 mg/MJ , base level low
Particles Decrease 15 mg/m3n
Heavy metals Slight increase, base level low
Dioxines No change
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Ruien Fuels
• Bark
• Demolition wood
• Crushed wood based boards, chip boards, etc.
• Moisture 25-30 %
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Ruien Process Performance
The gasifier in operation since May 2003
Environmental benefits– NOx & SOx reduced– CO & dust emission about the same or slightly reduced– Trace metals & dioxins no change– CO2 reduction 120.000 t/a, substituting of coal 50.000 t/a
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
RUIEN, GASIFIER CAPACITY
0
10
20
30
40
50
60
70
80
90
100
60 50 40 30 20
Moisture of the fuel %
Heats to the boiler
MW
Carbon dust
Gas sensible
Gas chemical
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Lahti & Ruien Summary
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Gasifier - PC Boiler Combustion Offers
• Lower environmental emissions– use of coal is reduced =>– lower CO2, SO2 and NOx emissions
• Better fuel flexibility• Possibility to use local fuel (biomass, REF, plastics, etc.) resources in high
efficiency steam cycle• Low investment and operation costs• Utilization of existing power plant capacity• Only small modifications to the main boiler• High plant availability: If problems in the gasification system, still possible to
get full output from the main boiler
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Future gasifier concepts
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Main boiler feed water
Main boiler furnace
Recycled fuels
CFB Gasifier
Pulsing gas
Cooling water
Flare
LP Steam
Filters
Fly ash
Bed materials
Gas cooler
Fuel feed system
Clean Gas Concept for REF/RDF
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Power Production Efficiency in Clean Gas Co-Combustion Concept
Vaasa, Vaskiluodon voima
Condensing power plant:
Waste to power 35...40 %
CHP plant:
Waste to power 30…35 %
Vantaa, Vantaan Energia
Gasifier
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Clean Gas Concept & CO-Combustion in PC BoilerOffers
• Possibility to utilize waste fuels in existing PC boilers
– To replace coal => CO2 Reduction
– To utilize high steam parametres => High electrical power production
– Utilization of the existing boiler & turbine => Significantly lower investment costs compared to stand alone waste incineration plant
– Effective emission control => Effective chlorine and heavy metal removal, effective combustion in the PC boiler furnace, no dioxineformation, utilization of the existing PC boiler flue gas treatment, coal ash and waste ash will be separated from each others
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Stand Alone Gasification Plant for RDF
RDF gasifier
Fuel gas boiler
Gas cooling and cleaning
Bag filter
Electricity, district heat
Steam turbine
RDF fuel
Flue gas
HP steam
Stack
Bottom ash
Auxiliary fuel (natural gas/oil)
Filter ash Fly ash
Additive feed
Additive feed
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
REF feeding
Gas fired boiler GasifierGas coolerGas
filtration
Turbine
Stand Alone Gasification Plant for RDF
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IEA Bioenergy ExCo 55Copenhagen 25 May 2005
Electricity Production 160 MWfuel
ηe = 36 %
40 MWe
57 MWe
53 MWe
ηe = 25 %
ηe = 33 %
Gasification
120 bar, 540 ºC
CFB combustion
65 bar, 465 ºC
Grate firing
40 bar, 400 ºC