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27
Operational
Optimization of a Municipal Waste Incinerator
F.
McKenty, L. Gravel, L. Charest
BMA – Brais Malouin &
Associates Inc, Montreal, Canada
As
part of an ongoing modernization program, Brais, Malouin and Associates
(BMA) recently undertook the simulation of a municipal waste incinerator,
with the ultimate goal of reducing pollutant emissions and improving
the overall efficiency of the process.
This incinerator in question (shown in Figure 1) is used to burn municipal waste composed of organic and inorganic matter on the primary (A) and finishing (B) grates. The incinerator has been modified over the years in order to dispose of additional waste such as dried sewage sludge, which is injected as pulverized particles (C). Over fire air is injected on the front and rear walls (D). Additionally, 8% of the hot flue gases are extracted at port (E) and used to dry the sewage sludge. The humidified flue gases are then re-injected into the incinerator (F) in order to destroy the odors resulting from the VOC’s (Volatile Organic Compounds) emanating from the drying of the sewage sludge. Current operational data showed highly fluctuating levels of carbon monoxide, which sometimes exceeded new emission standards. BMA’s goal was to find solutions to this problem.
In
order to tackle this task, a new 7-stream combustion model was developed
by BMA to take into account for multiple streams of fuels of varying
composition and humidity. Five of the streams represent different
fuel and FGR (Flu Gas Recirculation) compositions, while the two
remaining streams represent dry air and water vapor.
Four
of the five fuel streams are for waste fuels; one extra fuel stream
was included in the model to account for an auxiliary natural gas
burner, which seemed likely to be needed. The streams were modeled
by the transport of conserved scalars representing the mass fraction
of each of the fuels, dry air and water vapor. Water vapor is accounted
for separately because the concentration of water vapor varies greatly
from stream to stream.
The local mixture fraction for each of the fuels was obtained by dividing the local mass of available air and water vapor between each of the fuel streams. Each fuel was assumed to react independently.
The
reactions were modeled using a chemical equilibrium hypothesis.
Local chemical equilibrium was modeled by minimization of Gibbs
free energy. The combustion products were then recombined to yield
the local concentration of chemical species, which were passed back
to STAR-CD via the User subroutines. The burning process on the
grates (A and B) was modeled externally using a simple pyrolysis
model yielding combustion hot product streams composed of CO, CO2,
SO, SO2, H2, H2O and N2. The distribution of the waste and bypass
air on the combustion grates was modeled as air and pyrolysis product
inlets disposed in a checkerboard fashion. The dried sludge stream
(C) was modeled using Lagrangian particle tracking.
An initial
steady-state simulation was carried out using flow rates obtained
from the operational data logs. The flame contours shown in Figure
2 closely resembled those observed through the incinerator’s viewports
by BMA’s field engineers. The streamlinesshown in Figure 3 show
the flow patterns inside the incinerator. Temperature contours on
the incinerators’ centerline are shown in figure 4. Other simulations
were carried out with reduced excess air and pre-heated combustion
air in order to determine the level of reduction of CO emissions
that could be achieved. The simulations showed that these options
would reduce CO emissions. However, the comparison of predicted
emissions with the field
data
for current operational set points and reduced excess air showed
lower predicted CO emission levels than those measured
when
averaged over an entire day’s operation.
Following
the presentation of these results to the engineers and operators
responsible for the incinerator, the chief operator remarked that
the current automated control loop was based on assuring a steady
steam generation rate rather than steady state conditions for air
flow and the quantity of waste being burned. The chief operator
then proceeded to run his own tests by manually controlling the
air flow and disposition of waste on the combustion grates. The
CO emissions measured during manual control closely matched the
predicted CO emission levels to within a few ppm. Furthermore, the
fluctuation of CO emission levels was also greatly reduced.
This
study has shown that with the intimate knowledge afforded by STAR-CD
of the combustion phenomena inside these industrial units, operators
and engineers can easily devise ways of improving the process. Ongoing
studies are currently being carried out to determine if further
emission reductions can be achieved by further modification of the
operational set-points. Other physical modifications to the incinerator
are also being investigated. These include modifications to the
position and dimensions of the over fire air nozzles as well as
the pre-heating of the humidified flue gases that were used to dry
the sewage sludge prior to being reinjected into the incinerator
(F).
“STAR-CD has become an essential tool for BMA engineering. It enables us to qualify quantify ways of enhancing the environmental performance and efficiency of industrial size combustion equipment”, says Francois McKenty.
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