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Combustion Technologies
Bengt-Johan Skrifvars
Chemistry in Combustion Processes I
Åbo Akademi University, 2017
Combustion technologies
Principles
- Burning of gaseous-, liquid-, solid fuels
Practice
- Various firing techniques;
burner firing, grate firing, fluidized beds
- Furnace and flue gas
- Boiler and power plant
Combustion
Heat recovery
Flue gas
Condenser
Steam
turbine
Air Fuel
Furnace, flue gas channel
and steam cycle
G
Gas cleaningSteam
generator
Liquid fuel
Evaporation
and
gas combustion
Combustion of a liquid fuel
O2
CxHy
CO2 +H2O
Air
(Atomization)
Char forming
liquid fuel
Ash
Pyrolysis/
devolatilisation
and
gas combustion
Char
combustion
Combustion of a char forming liquid fuel
O2
O2
CxHy
CO2 +H2O
CO2
Air
Atomization
Solid fuel
Ash
Drying
Pyrolysis/
devolatilisation
and
gas combustion
Char
combustion
Combustion of a solid fuel
O2
O2
CxHy
CO2 +H2O
CO2
H2O
Air
Combustion of fuels
Gases; i) gas combustion (diffusion or pre-mixed)
Liquids; i) heating and atomization
ii) evaporation and gas combustion
(diffusion flame)
Char forming liquids;
i) heating and atomization
ii) devolatilization and gas combustion
(diffusion flame)
iii) heterogeneous char combustion
Solids; i) heating and drying
ii) devolatilization and gas combustion
(diffusion flame)
iii) heterogeneous char combustion
Different amount of time needed
to accomplish good combustion
depending on the fuel
Different types of techniques
needed for different types fuels
Combustion of fuels
Burner firing
Gas, liquid and pulverized solid fuels
High combustion temperatures (> 1000oC)
Short residence times
Burner firing of a gaseous fuel- turbulent diffusion flame
Gaseous
fuel
Combustion air
Combustion air in
swirl like motion
Detached pocket of
burning material
Burn-out pocket of
combustion products
Liquid
fuel
Pressure
atomizing
nozzle
Liquid
sheet
Filaments
Droplets
Vaporized fuel
droplets.
Behave like
a diffusion
gas flame
Burner firing of a liquid fuel
Burner firing of a solid fuel
Solid fuel
+
primary air
Secondary air
Char
combustion
Devolatilization
and
gas combustionAsh
Burner firing concepts I
Burner + furnace
Fuel +
Air
Bottom Ash
(solid fuels)
Flue Gas +
Fly Ash
Wall-fired Boxer-fired
Tangentially fired
Burner firing
Gaseous fuels
- turbulent diffusion flame
premixed flame not possible in burners
due to the back fire risk
- good mixing with air essential (turbulence)
laminar diffusion flame not possible in burners
due to too incomplete combustion (soot)
- practical applications:
burner + furnace
gas turbine
Burner firing
Liquid fuels
- atomizing (droplet formation) and
good mixing with air essential
for good combustion (high burn-out)
- fuel droplet size 10 - 100 mm
- char forming liquids
need longer residence times than
non-char forming ones
- practical applications:
burner + furnace
gas turbine (non-char forming liquids)
Burner firing
Solid fuels
- fuel milling important for good combustion
(small, even particle size distribution)
- good mixing with air essential
for good combustion (high burn-out)
- fuel particle size 0.1 - 1 mm
- longer burn-out times required than for
gas or liquid burners (affects the furnace size)
- practical applications; burner + furnace
wet bottom: ash removed as liquid slag
from the furnace bottom
dry bottom: ash removed as solid
from the flue gases
Burner firing
+ unlimited size
+ efficient combustion, high burnout
+ good load flexibility
+ user friendly fly ash (solid fuels)
- high NOx emissions if no reduction device
- SOx reduction requires separate flue gas cleaning
- high dust load in flue gas (solid fuels)
- slagging and fouling (solid fuels)
Grate firing
Solid fuels
stationary, moving grates,
spreader stokers
Fuel particle size > 1 cm
High furnace temperature (> 1000oC)
Ash removed mainly through the grate (80 %)
Grate firing
Travelling Grate
Air Air Air
Bottom ash
FuelAir
Drying
Pyrolysis and
gas combustion
Char combustion
Ash
Grate Configurations
Travelling Grate
Air Air Air
Bottom ash
AirAir
Travelling Grate Spreader StokerFuel
Fuel
Grate firing
+ suitable for small scale (simple, cheap)
+ no pretreatment of fuel
+ ash removed mainly through grate
- incomplete combustion
(CO-emissions, rest char in ash)
- slow load change rate
- some fuels unsuitable
(ash melting on the grate, fuel baking problems)
- grate construction heavy
- SOx and NOx reduction requires separate flue gas
cleaning devices
Fluidized bed combustion
Solid fuels
- bubbling fluidized bed boilers (BFB)
fluidization velocity approx. 1-3 m/s
- circulating fluidized bed boilers (CFBC)
fluidization velocity approx. 6-10 m/s
Atmospheric (AFBC) and pressurized (PFBC)
Bubbling Fluidized Bed Combustion
Air
Air
Fuel
Fuel: Fresh, Partly
Pyrolysed, Char
Bed material:
Quartz,
Limestone; fresh,
calcined, sulphated
Void Space
Ash
Flue Gas + Fly Ash
Circulating Fluidized Bed Combustion
Air
Air
Fuel
Fuel: Fresh,
Partly Pyrolysed,
Char
Limestone:Fresh, Calcined,
Sulphated
Void Space
Ash
Flue Gas + Fly AshCyclone
Fluidized bed combustion
Fuel particle size 0.1 - 10 mm
Bed material particle size 0.1 - 1 mm
Low furnace temperature (800 - 900oC)
Long residence time of fuel in the furnace
Addition of SOx sorbents to the furnace
Ash removed through bed, rest from the flue gases
Fluidized bed boilers
+ low combustion temperature
+ suitable for a variety of solid fuels
+ good combustion efficiency
+ no Thermal NOx formation
+ easy SOx reduction possibilities
- ash-bed material interactions may lead
to bed defluidisation
- residual ash may be difficult to dispose
- high efficiency reduction of all emissions (excl. CO2)
(CO, NOx, SOx, N2O) simultaneously hard to achieve
Pressurized Fluidized Bed Combustion
Pressure vessel Pressure vessel
Air
Fuel
Air
Air
Fuel
Air
BFB mode
commercially available
CFB mode
at demonstration stage
Pressurised
Combustion
Heat recovery
Flue gasCondenser
Steam
turbine
Air Fuel
Pressurised combustion
Gas cleaning
G
G
Gas turbine
Pressure
vessel
Pressurized fluidized bed combustion
Boiler inside a pressure vessel
Working pressures 10-20 bar
BFB mode commercialized, CFB mode at demo stage
+ smaller size than atmospheric versions
+ gas (expansion) turbine gives additional electricity
- new (uncertain) technology
- solids cleaning from the flue gases problematic
Combustion technologies
Definitions
• Fixed bed firing: “The bon fire”
• Grate firing: A firing system where a fuel lies on a grid when it is
burned and part of the combustion air is supplied through the
grid
• Stoker firing (Stokers): A continuously functioning grate firing
system, i.e. continuous fuel feed in and continuous ash feed out
• Burner firing (suspension firing): A firing system where the fuel
is blown as a dust or as droplets into the furnace together with
part of the combustion air and is burned in a gas suspension
(pulverized coal PC, pulverized fuel PF, gas and liquid fuels also
gas turbines)
• Fluidized bed combustion: A firing system where the fuel is fired
in a suspension of an inert solid media and combustion air.
circulating (CFBC), bubbling (BFBC), pressurized (PFBC)
Combustion
Heat recovery
Flue gas
Condenser
Steam
turbine
Air Fuel
Furnace, flue gas channel
and steam cycle
G
Gas cleaningSteam
generator
Furnace, flue gas channel, steam cycle
Definitions
• Furnace: The fireplace where the actual combustion takes place
• Burner: The device that feeds in the fuel and part of the air
• Heat exchangers: The device that transfers heat from the flue gas
to the media to be heated (here water and/or steam)
• Super heater: The heat exchangers that heat up the steam
• Boiler tubes: The heat exchangers boil that boil the water
• Economizer: The heat exchangers that heat up the feed water
• Air pre-heater (LUVO): The heat exchanger that heats up the
combustion air
• Steam drum: The device separating the steam from the water in
the conventional steam boiler
• Condenser: The device condensing the steam exiting the steam
turbine at a low as possible temperature
Meri-Pori power plant - PC fired
- Input: 1300MWth
- Output: 560MWe
- 440 kg/s, 540oC, 240 bar
- Supercritical once-through type
with reheater
- SCR, ESP, wet FGD
• Boiler: Closed pressurized vessel for production of hot water or
steam
• Steam generator: Closed pressurized vessel for production of steam
by vaporizing water with heat from a high temperature source
• Power plant: A plant that produces electricity only
• CHP plant (Combined heat and power): A plant that produces both
both heat and electricity
• Combined cycle: A power or CHP plant that consists of both a gas
turbine and a steam turbine
• Once-through type boiler: A steam cycle without a steam drum,
working at pressures near or above the critical steam pressure of 221
bars
• Supercritical steam data: A steam cycle working at pressures above
the critical steam pressure of 221 bars
Power plants
Definitions I
• Dust removal: The removing of fly ash
• ESP: Electrostatic precipitator, a device in the cold end of the flue
gas channel that removes solid particles from the flue gas by a
electrostatic (magnetic) field
• Bag filter: A device in the cold end of the flue gas channel that
removes solid particles from the flue gas by textile bags
• Ash hopper: A fly ash collector, usually at the bottom end of a flue
gas channel part where it turns. Forces the gas to turn more than
what the particles can follow.
• Cyclone: A particle/gas or liquid/gas separator where the
separation is based on gravitational and inertial forces
Power plants
Definitions II
• Primary air: That part of the combustion air that is fed into the lower
furnace close to/together with the fuel
• Secondary air: That part of the combustion air that is fed into the
furnace after the fuel feed
• Tertiary air: That part of the combustion air that is fed into the upper
part of the furnace to ensure complete combustion
• Fly ash: That part of the uncombustible rest of the fuel, the ash,
which is carried away from the furnace with the flue gases into the
flue gas channel
• Bottom ash: That part of the ash which exits the furnace from its
bottom part
• Bed: The inert solid particle bed in the furnace of fluidized bed
combustion system into which the fuel is feed and through which part
of the combustion air is fed
Power plants
Definitions III
• FGD: Flue gas desulfurization device, usually based on wet or
semi-dry absorption processes
• SCR: Selective catalytic reduction, a flue gas NOx removing
system, consisting of ammonia injection into the flue gas at some
200oC followed by a catalysator
• SNCR: Selective non-catalytic reduction, a flue gas NOx
removing system, consisting of ammonia injection into the flue
gas at some 800oC
Power plants
Definitions IV