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A
Dry Scrubber System is comprised of three (3) primary
components:
- A Gas
Cooling System
- A Reagent
Injection System
- A Fabric
Filter (Baghouse) System
In addition,
there are several subsystems that all must be properly
integrated to provide a working system.
Click each
feature's title to see the system schematic.
Inlet
Breeching:
The
hot gas (usually 1800° F+) is ducted to the gas cooler
in refractory lined breeching. Support and thermal
expansion are the major design challenges. Often an
emergency dump stack is included.
Gas
Cooling:
The flue gas
must be cooled to enhance the removal of acid gases
and toxics, and to be compatible with the materials
of construction. Control of condensation and corrosion
is critical.
| TYPE |
ADVANTAGES |
DISADVANTAGES |
| Boiler |
- Heat
recovery
- Reliable
- No
water carry-over risk
- Minimizes
gas volume
|
- High
cost
- Not
justified if there is no use for the steam
- May
promote formation of dioxins
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| Evaporative
Cooler |
- Fast
cooling inhibits toxic formation
- Reasonable
cost
- No
water disposal required
|
- Risk
of water carry-over
- Possible
steam plume
- Adds
gas volume (water)
- Consumes
water
|
| Dilution
Air |
- Low
capital cost
- Small
space required
- Simple
|
- Adds
considerable gas volume
- Major
energy increase
- Dilution
causes large correction factors
- Difficult
draft control
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| Heat
Exchanger |
- Reduces
gas volume
- Easy
draft control
- Small
space required
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- Typically
used as a secondary cooling device
- Corrosion
and plugging potential
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Reagent
Injection System:
The
reagent system is comprised of Material
Selection,
Reagent
Storage,
Injection
Method,
and in the case of dry injection, Reagent
Feed.
Each of these issues has design alternatives that
need to be considered on a case specific basis.
Material
Selection:
Although there are other alternatives available, most
often the decision is between lime based reagents
(usually hydrated lime) and sodium based reagents
(sodium bicarbonate and naturally occurring sodium
carbonate/sodium bicarbonate minerals).
| REAGENT |
ADVANTAGES |
DISADVANTAGES |
| Lime
Based materials |
- Low
cost
- Readily
available
- Easy
disposal
- Low
molecular weight
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- Corrosive
and irritating to handle
- Higher
stoichiometric ratio required
- Requires
lower operating temperature
- Produces
deliquescent ash
- Poor
SO2 removal
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| Sodium
Based |
- High
efficiency
- Easy
to handle
- Lower
stoichiometric ratio required
- Effective
at higher temperatures
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- High
cost
- Limited
sources
- High
molecular weight
- Produces
leachable ash
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Reagent
Storage:
The
reagent storage method is almost always determined
by the usage rate. For the smallest systems day bins
are used with reagents that are packaged in 50 lb.
bags, and generally delivered by pallet loads. Intermediate
systems use a bulk bag system with typically 1 ton
bags, and an integral crane system for bag handling.
In larger systems, bulk storage silos are used. These
can accept full truck or even rail car deliveries.
Injection
Method:
The acid gas scrubbing reagent is either mixed into
a slurry which is atomized into fine droplets and
sprayed into a spray dryer (semi-dry scrubbing); or
the reagent is injected as a dry, fine powder into
the cooled gas (dry scrubbing). A specially designed
venturi provides thorough mixing of the reagent and
acid contaminated gas stream.
| METHOD |
ADVANTAGES |
DISADVANTAGES |
| Spray
Dryer |
- High
efficiency
- Reduces
reagent usage
- More
effective on SO2
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- High
cost
- Requires
higher maintenance
- Space
requirements
- Potential
for water carry-over
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| Dry
Injection |
- Simple
- Low
cost
- Small
space requirement
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- Lower
efficiency
- Higher
reagent usage
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Reagent
Feed:
In
the case of dry reagent injection, the material can
be conveyed either by gravity or pneumatic conveying
for injection. In come cases, mechanical conveying
can be used, but then the actual injection is still
basically by gravity.
Activated
Carbon System:
A dry activated carbon powder can be injected to adsorb
dioxins, furans, Mercury, and other toxins. This injection
takes place after the gas cooling and may be done
in a blend with a reagent for acid gas scrubbing.
The carbon can be stored and fed in the same manner
as the reagent.
Baghouse
and Reaction Vessel:
The reacted
acid gases and adsorbed toxins are removed in the
baghouse. In addition to the reaction that has taken
place in the gas stream prior to the baghouse, the
unreacted reagent becomes a part of the filter cake
in the baghouse where it provides a considerable amount
of additional gas scrubbing. Contact between the flue
gas and reagent is particularly intimate because of
the dense cake and very slow gas movement. Unlike
most competitive baghouses, the BET unit is designed
specifically to be a part of an acid gas reaction
program. There are unique features in the inlet design,
bag spacing, and cleaning mechanism that optimizes
the reaction process. See also Baghouse
System Detail for more design details and component
description.
ID
Fan and Draft Control:
An ID fan system provides fast response to a control
signal to maintain the draft at the source, regardless
of fluctuations in the process. The draft can be controlled
either by using a variable speed drive or a modulating
damper valve with an automatic operator.
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