Waste Incineration Principles
Although the design of an incineration facility
will vary to some extent according to the nature of the waste
material (the feedstock) being incinerated, the essential elements
are basically similar. Each of the essential elements of the plant
perform various functions in the handling and combustion of wastes,
and the removal and the treatment of by-products such as ash,
fumes, heat and noise.
The
following is based on descriptions in the Royal Commission's report
on incineration and the IPC Guidance note on Waste Incineration.
A plant consists of:
·
Facilities for handling, storing, and mixing feedstock without
creating a hazard or a nuisance. Typically, wastes will be
driven by truck into a bunker area and unloaded. The feedstock
will then be transferred from the bunker into a hopper, which
feeds the combustion chamber.
·
A furnace or combustion chamber. The furnace is designed
to allow the maximum combustion of the feedstock (primary combustion),
and also to subject the resulting gases and aerosol of fine particles
to further combustion (secondary combustion), reducing the content
of soot and other pollutants in the exhaust.
·
A heat recovery system for cooling the exhaust gases prior to
further pollutant removal. Heat recovery is achieved through
water cooling or air cooling the exhaust gases through a heat
exchanger. The recovered heat may be re-used as heat or used to
generate electrical power.
·
A gas cleaning system, typically consisting of a "scrubber"
(filters which absorb pollutants) and an electrostatic precipitator,
and/or fabric "bag filter", to remove fine particles
and some polluting gases (often termed fly ash).
·
A fan to draw exhaust gases through the system before being
discharged to the atmosphere via the stack (chimney).
·
Facilities for the solid waste and water residues are needed.
Ash and clinker from the furnace grate (bottom or grate ash) fall
into a water-filled quench tank and are removed as a sludge by
conveyor to a bunker. Liquid effluents from the exhaust gas cleaning
mechanism ("scrubber") and quench tank will have become
contaminated through contact with the exhaust gases and ash.
The
process will be designed to achieve as thorough a degree of combustion
as possible, which will be affected by the time in the furnace,
temperature achieved, oxygen availability and nature of the feedstock.
Fumes from the first (primary) combustion stage usually go through
secondary combustion stage to improve the degree of combustion.
Representative retention times are 30 minutes for solid waste
primary combustion of the fumes. The design temperature for secondary
combustion is usually between 850oC and 1200oC. Pollutants can
reform while the exhaust gases are cooling, so this stage us also
considered in the design.
It is more difficult achieve conditions which will allow complete
combustion if the feedstock is mixed ("heterogeneous")
- as is municipal waste or clinical waste. More homogenous (uniform)
feedstock (such as sewage sludge or some chemical wastes) will
allow combustion conditions to be optimized more easily.
Pollution
Control
Pollutants
will be present in the exhaust gases from the combustion chamber,
either having been present in the original feedstock (such as
metals) or having been produced during the combustion or gas-cooling
process. Ideally, all organic compounds would break down into
carbon dioxide and water if completely burned, but in practice
"products of incomplete combustion" (PICSs) such as
dioxins are formed. In addition nitrogen oxides are formed both
from nitrogen in the waste and in the air supplied to support
high temperature combustion.
Pollutants
will subsequently be incorporated into the ash produced from the
grate and exhaust-cleaning systems, and in liquid effluents used
to quench the ash. These effluents need to be treated and disposed
of to sewer.
Various
types of filter will be present, although the exact types and
the configuration can vary.
Scrubbers
remove acid gases and some metal content by passing the gases
and some of the metal content by passing the gases through chemical
regents. A Selective Non-Catalytic Reducer (SNCR) may be used
to convert nitrogen oxides into nitrogen by reacting with ammonia
or urea (and inhibits dioxin formation); Flue Gas Recirculation
(FGR) also reduces nitrogen oxide and dioxin formation. Ceramic
filters, fabric filters, electrostatic prewcipitators, and/or
wet scrubbers may be used to remove particulates (and any adsorbed
pollutants in or on the particulates). Activated carbon, an adsorbent,
may be used to filter out volatile substances such as mercury
and PICs.
An
incineration plant will not normally have all of these devices.
The most common pattern is a combination of physical sifting and
scrubbing.
Associated
Hazards at an incinerator site include the fly ash itself (which
contain high levels of toxic substances) and the storage of waste
before incineration occurs (e.g. chemical drums might leak).
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