The
CETHAR CFB boiler operates on the circulating bed principle.
At high fluidizing velocities (4 to 6 m/s) part of the bed
material becomes entrained and is carried through the combustion
chamber with the flue gases. The coarser entrained particles
are separated in a water-cooled ‘hot loop’
cyclone separator and returned via a loop
seal back to the bed. Finest fly ash is carried through
the boiler convection sections and separated from the flue
gases in a dust collection system.
Fuel is fed into the fluidized bed via gravimetric or volumetric
feeders either through the front wall and / or rear wall.
Combustion takes place in the bed at about 870 - 900°C
at full load. The bed material is formed from the
fuel ash (and sand in some cases). Due to the large
heat capacity of the bed, combustion is stable and no supporting
fuels are required, provided the fuel heating value is sufficient
to raise the combustion air and the fuel itself above its
ignition temperature. The intense turbulence ensures
good mixing and combustion of the fuel. High heat
transfer is obtained through the circulating material, which
is approximately proportional to the load. That is,
the boiler has good response over a wide range of loads
with a relatively small excess air levels.
Primary air is taken from the atmosphere by centrifugal
fan. Air is being brought to the air box through an
air preheater after it gets preheated. In the air
box it is blown through the grid to fluidize the bed and
provide combustion air. Primary air fan control is
via fan IGV / Multi louver damper / VFD control / hydraulic
coupling according to the required airflow, which is measured
by the aerofoil in the discharge duct before the air heater.
There is a minimum flow of primary air required to fluidize
the bed and prevent flow of the material through the nozzles.
So at low loads the primary airflow remains constant and
does not vary with load.
Secondary air is also taken from the atmosphere by centrifugal
fan and preheated in the air heater. Secondary air
is brought in at specified levels from the grid. Secondary
air achieves the "staged" combustion and completes
the combustion of the fuel without the formation of excessive
NOx.
The secondary airflow is measured with an aerofoil in the
discharge duct before the air heater. The secondary
air fan is controlled with IGV / Multi louver damper / VFD
control / hydraulic coupling according to the pressure down
stream of the fan.
High-pressure air is used for fluidizing the circulating
bed material in the loop seal. There are two high-pressure
blowers; one is always on stand-by duty.
A tubular, multi-pass air heater system with air inside
tube design is offered at the downstream of the economizer.
The air heater preheats the combustion air that goes into
the furnace. There are separate sections for the primary
and secondary air to get heated up. The tubular system
offers an advantage of negligible air-gas leakage.
The air inside tubes design also facilitates an easy tube
cleaning system in case of burning fuels with some sticky
characteristics.
After the air heater, the finer fly ash is transported to
the dust collection system (ESP or bag filter) where the
fly ash is separated. The gas is drawn through the boiler
fly-ash separator by means of a centrifugal type induced
draft (ID) fan, after which the flue gas is discharged to
the atmosphere via the chimney (stack).
The boiler is with a balanced draft system and the ID fan
is controlled according to the pressure at the top the combustion.
Flue gas temperatures and pressure drops are measured throughout
the system mainly to indicate the operating condition of
the boiler. Similarly flue gas is analyzed for O2
to indicate the efficiency of combustion process.
- O2 is kept ~3.5 % to ensure proper combustion
and to fulfill the emission requirements
- SO2, and particulate are controlled according
to the specified requirements.
The
ID fan will be sized based on the performance fuel duty at
100% MCR load and then test block margins will be applied
to obtain a proper fan selection basis. Fan test block
duty is checked for the availability of sufficient margins
to assure the operation of the boiler when using a worst range
fuel or fuel mixture as agreed in the contract.