Biomass application in circulating fluidized bed coal firing boiler
Speaker Larry Tsai
Personal Information Work experience
Yuen Foong Yu packing Inc. XinWu mill Manager project department Yuen Foong Yu packing Inc. XinWu mill senior staff maintain department Yuen Foong Yu packing Inc. XinWu mill chief co-gen section Yuen Foong Yu packing Inc. XinWu mill deputy chief stoke preparation
section Project experience
Project manager for Yuen Foong Yu packing Inc. Yangzhou mill co-gen power plant phase 1 and Phase 2
Project manager for Yuen Foong Yu packing Inc. Cheng Kong mill coal firing boiler
Project manager for Chung Hwa pulp Inc. Chiutong mill co-gen power plant Education
Advanced degree Yuan Ze university master major in mechanical engineer
Secondary degree Chung Yuan major in chemical engineer
Biomass co-firing system in Europe
CO-firing power plant
What is fluidized bed?
Which kind of fuel can use in CFB boiler?
Typical properties of solid fuel
CFB boiler construction (conventional type)
CFB boiler construction (compact type)
How to work in CFB boiler
CFB boiler operation condition
CFB boiler power plant
FGD
CEMS
FGD
CaCO3
sand
ESP+bag filter coal
25%NH4OH SNCR
wood chip or Wood pellet
SCR(20 m3)
SOx NOx Dust Velocity CO
Flue gas temp. distribution in CFB boiler
850
850
850
420
150
FGD
ESP + bag filter
Air pollution control device for CFB
CaCO3 CaO+CO2+1/2O2
CaO
SO2
CaO+SO2+1/2O2CaSO4 CaSO4
NOx 150ppm(6%O2)
25%NH4OH
SNCR
NH4OHNH3+H2O 4NO+4NH3+O24N2+6H2O 6NO2+8NH37N2+12H2O SLIP
NH3
SCR NH4OHNH3+H2O 4NO+4NH3+O24N2+6H2O 6NO2+8NH37N2+12H2O
NOx
70ppm(6%O2)
SO2 80ppm(6%O2)
Summary for CFB boiler
Why choose a CFB boiler for co-firing system ? Fuel flexibility and multi-fuel firing, Low SO2 emissions due to efficient sulfur capture with limestone in the
furnace, Low NOx emission due to low combustion temperature and air-staging, Low CO and CxHy emission due to turbulent conditions and good
mixing, Secondary flue gas clean-up systems typically not needed, Stable operating conditions and good turn-down ratio, Support firing is not needed except during start-up periods, Increased capacity possible within the same footprint as old boilers, No need for fuel preparation (e.g. pulverizing).
Challenges of biomass co-firing Risk for biomass storage and transfer
High moisture and low bulk density Risk for high temperature corrosion and de-fluidize
Slagging and fouling on heat exchange surface Sintering in combustion chamber Slagging and fouling cause flue gas channel become narrow and
flue gas velocity increase. It cause erosion increase. High amount of alkali and chloride oxide component in flying
ash decrease melting point of ash and cause high temperature corrosion
High density inpurity material in biomass cause de-fluidized, if it cant discharge from bottom ash system smoothly.
Sintering matter from Combustion chamber
Slagging on furnace and ECO
Slagging on superheater
Superheater corrosion
Biomass & waste handling system
Reclaimer for biomass feeding system
Screw conveyor for biomass storage
Biomass pretreatment process
Pelletize for wood chip system
Moisture less than 90%
The relation of boiler efficiency & co-firing ratio
Why co-firing can reduce CO2 emission ?
Steam temp. & corrosion relative
Cogeneration power plant process
130 tons/hr 130 bar(A) 536
220
338
426 464 540
Ash composition of different fuel
Why SO2 and Alumininsilicates can reduce corrosion?
Alumininsilicates can react with alkalis liberating HCl Al2Si2O72H2O Al2O3 2SiO2 Al2O3 2SiO2+2KCl+H2O K2O Al2O3 2SiO2+2HCl
Sulphation of alkali chloride 2KCl +SO2+1/2O2+H2O K2SO4+2HCl
Gas effect
Mechanism of high temp. corrosion
Co-firing with coal can reduce corrosion
Economics sensitivity analysis electricity production cost vs. full load operation hours
biomass firing boiler
Intrex superheater
Biomass firing boiler of grip
Step grid
Open grid
Step gird for fluidized bed boiler
BFB boiler open grid
Step gird in CFB boiler
SNCR+SCR
Flue gas + NH3 slip
Catalyst
420
25% NH4OH
850
NH4OHNH3+H2O 4NO+4NH3+O24N2+6H2O 6NO2+8NH37N2+12H2O
ESP + bag filter
Johnson Matthay Honeycomb Catalyst
SCR
CaCO3
SO2 CaO
CaSO4 CaCO3 CaO+CO2+1/2O2
CaO+SO2+1/2O2CaSO4
850
CFB boiler de-sulfur, temp. and Ca/S relation
Biomass application in circulating fluidized bed coal firing boilerPersonal Information Biomass co-firing system in EuropeCO-firing power plantWhat is fluidized bed?Which kind of fuel can use in CFB boiler?Typical properties of solid fuelCFB boiler construction (conventional type)CFB boiler construction (compact type)How to work in CFB boilerCFB boiler operation conditionCFB boiler power plantFlue gas temp. distribution in CFB boiler Air pollution control device for CFBSummary for CFB boilerChallenges of biomass co-firingSintering matter from Combustion chamberSlagging on furnace and ECOSlagging on superheater Superheater corrosionBiomass & waste handling systemReclaimer for biomass feeding system 23Screw conveyor for biomass storageBiomass pretreatment processPelletize for wood chip system The relation of boiler efficiency & co-firing ratioWhy co-firing can reduce CO2 emission ?Steam temp. & corrosion relativeCogeneration power plant process Ash composition of different fuelWhy SO2 and Alumininsilicates can reduce corrosion? Mechanism of high temp. corrosionCo-firing with coal can reduce corrosionEconomics sensitivity analysis electricity production cost vs. full load operation hours biomass firing boilerIntrex superheaterBiomass firing boiler of gripStep gird for fluidized bed boilerBFB boiler open gridStep gird in CFB boilerSNCR+SCR Johnson Matthay Honeycomb CatalystSCR CFB boiler de-sulfur, temp. and Ca/S relation
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