Miscellaneous Organic Chemical Manufacturing
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Process Design and Operating Factors Influencing Emissions
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VOC and PM emissions from chemical manufacturing may be reduced through
the use of add-on control systems or through equipment and process
modifications.
VOC Control Systems
A
VOC control system typically consists of a capture device and a removal
device. The capture device (such as a hood or enclosure) captures
the VOC-laden air from the emission area and ducts the exhaust air
stream to removal equipment such as a recovery device or a destructive
control device. In either case, the purpose of the control system
is to remove VOCs from the exhaust air stream. The overall efficiency
of a control system is a function of the specific removal efficiency
for each device in the system.
EXAMPLE RECOVERY DEVICES: 
Condensers are one of the most frequently used
control devices in the chemical industry. They work by reducing
the temperature of the emission exhaust gas so that VOC vapors
are recovered through condensation.
Adsorption
devices that incorporate activated carbon are capable
of removing VOC vapors from exhaust emission streams to very
low levels in the final gas stream. Large scale adsorption based
recovery systems normally have two or more activated carbon adsorption
chambers. One carbon chamber is being used to remove VOCs from
emission stream while the spent carbon chamber is being regenerated.
VOCs are recovered from the system during the regeneration phase.
Steam is routed into the saturated carbon bed to cause the VOCs
to desorb from the carbon and condense at the condenser. Once
VOCs liquids have been collected then they may be recycled or
further purified prior to reuse in the manufacturing operation.
Dust
collectors are used to collect particulate matter from
the emission stream. Dust collectors are constructed in many
different designs. A bag house consists of a large rectangular
housing with many internal banks of vertically mounted filter
bags. The emission stream enters the bag house through the side
inlet, passes through the bag filter media, and exits the unit
through the discharge port at the top. Particulate matter builds
up on the filter media until it is shaken off by pulses of compressed
air from within each bag.
The
dust that falls from the bags during the pulsing process is collected
at the lower section of the bag house and finally discharged through
the solids outlet to a drum or other container. When designing
a bag house for an installation, it is important to select the
appropriate filter media and surface area for the particulate matter
to be collected. The pore size of the filter cloth will determine
the removal efficiency of the overall unit.
A floating roof on a storage tank helps to reduce
solvent emissions by eliminating theheadspace that is present in
conventional storage tanks. The conventional storage tank air that
is saturated with solvent vapors exits the vessel as the surrounding
temperature increases during the day. Outside air then reenters
the vessel during the evening hours as the surrounding temperature
decreases and the daily cycle prepares to be repeated. Additionally,
when a conventional storage tank is filled periodically, then emissions
occur by way of displacement. A floating roof moves up and down
the vessel vertical walls as the level of the storage tank changes.
Since the vessel contains no headspace, all breathing and filling
losses are avoided.
EXAMPLE DESTRUCTIVE CONTROL DEVICES:
Catalytic
Incinerators are used to eliminate VOCs from process
exhaust gases from a broad variety of process operations. Catalytic
incineration is a technology used in selective applications to
greatly reduce emissions due to VOCs, hydrocarbons, odors, and
opacity in process exhaust. The catalyst section operates at
between 315°C to 400°C to convert VOC to CO2 and H2O.
A properly designed and installed system can achieve a VOC destruction
efficiency of greater than 95%.
Thermal
Incinerators control VOC levels in a gas stream by passing
the stream through a combustion chamber where the VOCs are burned
in air at temperatures between 700°C to 1,300°C. Fuel
is burned in the unit to supply the necessary heat for decomposition
of the VOC’s. Heat exchangers may also be installed as
part of the unit to conserve energy by warming the inlet air
stream with the hot exhaust gases.
Venturi
Scrubbers are used to remove particulate material from
vent exhaust streams. These units normally incorporate a spray
nozzle section where liquid is discharged at a high velocity,
a mixing section where liquid droplets contact the incoming emission
gas stream, and a settling/separation section where scrubber
fluid is recycled to the inlet spray nozzle and the exit gas
is discharged to the atmosphere or to a secondary control device.
Enclosed
Oxidizing Flares convert VOCs into CO2 and H2O by way
of direct combustion. Normally an enclosed oxidizing flare is
used when the waste gas is rich enough in organic content to
be its own fuel source. If the process gas stream does not contain
an adequate level of combustible VOCs then additional fuel must
be supplied for effective operation. The removal efficiency for
each control device is a function of the specific design of the
unit and how well its capability matches the intended application.
PM/PM 10 Control Systems
PM/PM10
control systems for the chemical industry consist of a capture device
paired with a control device that is typically a fabric filter (bag
house). These systems are typically employed to reduce PM emissions
from charging pigments and other solids into mixing and grinding
devices. The captured dust may be recycled or sent for off-site disposal
or treatment.
Bag
Houses remove particulate material from an emission
gas stream by passing the emission stream through engineered
fabric filter tubes, envelopes, or cartridges. Particulate material
is retained on the filter media as the clean air is discharged
to the atmosphere. Vibrators or timed air blast are used for
removing and discharging the dust that has been collected in
the unit. When identifying a bag house for an application it
is important to consider the particle size in the emission stream,
the particle size control requirements, the air flow rate of
the emission stream, and the bag filter surface area requirements.
Additionally, it is important to identify the appropriate chemical
resistance requirements for the materials of construction in
the unit.
Fabric filters are least efficient with particles 0.1 to 0.3 µm
in diameter and with emission streams of high moisture content.
When operated under optimum conditions, they can generally achieve
control efficiencies of up to 99+ percent. However, typical control
efficiencies range from 95 to 99 percent.
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