EPA-452/F-03-025
Air Pollution Control Technology
Fact Sheet
Fabric Filter - Pulse-Jet Cleaned Type
(also referred to as Baghouses)
Control Device - Capture/Disposal
Particulate Matter (PM), including particulate matter less than or equal to 10
micrometers (jjm) in aerodynamic diameter (PM10), particulate matter less than or equal to 2.5 jjm in
aerodynamic diameter (PM2 5), and hazardous air pollutants (HAPs) that are in particulate form, such as most
metals (mercury is the notable exception, as a significant portion of emissions are in the form of elemental
vapor).
Achievable Emission Limits/Reductions:
Typical new equipment design efficiencies are between 99 and 99.9%. Older existing equipment have a range
of actual operating efficiencies of 95 to 99.9%. Several factors determine fabric filter collection efficiency.
These include gas filtration velocity, particle characteristics, fabric characteristics, and cleaning mechanism.
In general, collection efficiency increases with increasing filtration velocity and particle size.
For a given combination of filter design and dust, the effluent particle concentration from a fabric filter is nearly
constant, whereas the overall efficiency is more likely to vary with particulate loading. Forthis reason, fabric
filters can be considered to be constant outlet devices rather than constant efficiency devices. Constant
effluent concentration is achieved because at any given time, part of the fabric filter is being cleaned. As a
result of the cleaning mechanisms used in fabric filters, the collection efficiency is constantly changing. Each
cleaning cycle removes at least some of the filter cake and loosens particles which remain on the filter. When
filtration resumes, the filtering capability has been reduced because of the lost filter cake and loose particles
are pushed through the filter by the flow of gas. As particles are captured, the efficiency increases until the
next cleaning cycle. Average collection efficiencies for fabric filters are usually determined from tests that
cover a number of cleaning cycles at a constant inlet loading. (EPA, 1998a)
Applicable Source Type: Point
Typical Industrial Applications:
Fabric filters can perform very effectively in many different applications. Common applications of fabric filter
systems with pulse-jet cleaning are presented in Table 1, however, fabric filters can be used in most any
process where dust is generated and can be collected and ducted to a central location.
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Name of Technology:
Type of Technology:
Applicable Pollutants:
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Fabric Filter
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Table 1. Typical Industrial Applications of Pulse-Jet Cleaned Fabric Filters
(EPA 1997; EPA, 1998a)
Application Source Category Code
(SCC)
Utility Boilers (Coal)
1-01-002..
.003
Industrial Boilers (Coal, Wood)
1-02-001..
.003, 1-02-009
Commercial/Institutional Boilers (Coal, Wood)
1-03-001..
.003, 1-03-009
Ferrous Metals Processing:
Iron and Steel Production
3-03-008..
.009
Steel Foundries
3-04-007,-009
Mineral Products:
Cement Manufacturing
3-05-006..
.007
Coal Cleaning
3-05-010
Stone Quarrying and Processing
3-05-020
Other
3-05-003..
.999
Asphalt Manufacture
3-05-001..
.002
Grain Milling
3-02-007
Emission Stream Characteristics:
a. Air Flow: Baghouses are separated into two groups, standard and custom, which are further
separated into low, medium, and high capacity. Standard baghouses are factory-built, off the shelf
units. They may handle from less than 0.10 to more than 50 standard cubic meters per second
(sm3/sec) (("hundreds" to more than 100,000 standard cubic feet per minute (scfm)). Custom
baghouses are designed for specific applications and are built to the specifications prescribed by
the customer. These units are generally much larger than standard units, i.e., from 50 to over 500
sm3/sec (100,000 to over 1,000,000 scfm). (EPA, 1998b)
b. Temperature: Typically, gas temperatures up to about 260°C (500°F), with surges to about 290°C
(550°F) can be accommodated routinely, with the appropriate fabric material. Spray coolers or
dilution air can be used to lower the temperature of the pollutant stream. This prevents the
temperature limits of the fabric from being exceeded. Lowering the temperature, however,
increases the humidity of the pollutant stream. Therefore, the minimum temperature of the pollutant
stream must remain above the dew point of any condensable in the stream. The baghouse and
associated ductwork should be insulated and possibly heated if condensation may occur. (EPA,
1998b)
c. Pollutant Loading: Typical inlet concentrations to baghouses are 1 to 23 grams per cubic meter
(g/m3) (0.5 to 10 grains per cubic foot (gr/ft3)), but in extreme cases, inlet conditions may vary
between 0.1 to more than 230 g/m3 (0.05 to more than 100 gr/ft3). (EPA, 1998b)
d. Other Considerations: Moisture and corrosives content are the major gas stream characteristics
requiring design consideration. Standard fabric filters can be used in pressure or vacuum service,
but only within the range of about ± 640 millimeters of water column (25 inches of water column).
Well-designed and operated baghouses have been shown to be capable of reducing overall
particulate emissions to less than 0.05 g/m3 (0.010 gr/ft3), and in a number of cases, to as low as
0.002 to 0.011 g/m3 (0.001 to 0.005 gr/ft3). (AWMA, 1992)
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Emission Stream Pretreatment Requirements:
Because of the wide variety of filtertypes available to the designer, it is not usually required to pretreat a waste
stream's inlet temperature. However, in some high temperature applications, the cost of high temperature-
resistant bags must be weighed against the cost of cooling the inlet temperature with spray coolers or dilution
air (EPA, 1998b). When much of the pollutant loading consists of relatively large particles, mechanical
collectors such as cyclones may be used to reduce the load on the fabric filter, especially at high inlet
concentrations (EPA, 1998b).
Cost Information:
Cost estimates are presented below for pulse-jet cleaned fabric filters. The costs are expressed in 2002
dollars. The cost estimates assume a conventional design under typical operating conditions and do not
include auxiliary equipment such as fans and ductwork. The costs for pulse-jet cleaned systems are
generated using EPA's cost-estimating spreadsheet for fabric filters (EPA, 1998b).
Costs are primarily driven by the waste stream volumetric flow rate and pollutant loading. In general, a small
unit controlling a low pollutant loading will not be as cost effective as a large unit controlling a high pollutant
loading. The costs presented are forflow rates of 470 m3/sec (1,000,000 scfm) and 1.0 m3/sec (2,000 scfm),
respectively, and a pollutant loading of 9 g/m3 (4.0 gr/ft3).
Pollutants that require an unusually high level of control or that require the fabric filter bags or the unit itself
to be constructed of special materials, such as Gore-Tex or stainless steel, will increase the costs of the
system (EPA, 1998b). The additional costs for controlling more complex waste streams are not reflected in
the estimates given below. For these types of systems, the capital cost could increase by as much as 75%
and the operational and maintenance (O&M) cost could increase by as much as 20%.
a. Capital Cost: $13,000 to $55,000 per sm3/s ($6 to $26 per scfm)
b. O & M Cost: $11,000 to $50,000 per sm3/s ($5 to $24 per scfm), annually
c. Annualized Cost: $13,000 to $83,000 per sm3/s ($6 to $39 per scfm), annually
d. Cost Effectiveness: $46 to $293 per metric ton ($42 to $266 per short ton)
Theory of Operation:
In a fabric filter, flue gas is passed through a tightly woven or felted fabric, causing PM in the flue gas to be
collected on the fabric by sieving and other mechanisms. Fabric filters may be in the form of sheets,
cartridges, or bags, with a number of the individual fabric filter units housed together in a group. Bags are
most common type of fabric filter. The dust cake that forms on the filter from the collected PM can significantly
increase collection efficiency. Fabric filters are frequently referred to as baghouses because the fabric is
usually configured in cylindrical bags. Bags may be 6 to 9 m (20 to 30 ft) long and 12.7 to 30.5 centimeters
(cm) (5 to 12 inches) in diameter. Groups of bags are placed in isolable compartments to allow cleaning of
the bags or replacement of some of the bags without shutting down the entire fabric filter. (STAPPA/ALAPCO,
1996)
Operating conditions are important determinants of the choice of fabric. Some fabrics (e.g., polyolefins,
nylons, acrylics, polyesters) are useful only at relatively low temperatures of 95 to 150°C (200 to 300°F). For
high-temperature flue gas streams, more thermally stable fabrics such as fiberglass, Teflon®, or Nomex® must
be used (STAPPA/ALAPCO, 1996).
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Practical application of fabric filters requires the use of a large fabric area in order to avoid an unacceptable
pressure drop across the fabric. Baghouse size for a particular unit is determined by the choice of air-to-cloth
ratio, or the ratio of volumetric air flow to cloth area. The selection of air-to-cloth ratio depends on the
particulate loading and characteristics, and the cleaning method used. A high particulate loading will require
the use of a larger baghouse in order to avoid forming too heavy a dust cake, which would result in an
excessive pressure drop As an example, a baghouse for a 250 MW utility boiler may have 5,000 separate
bags with a total fabric area approaching 46,500 m2 (500,000 square feet). (ICAC, 1999)
Determinants of baghouse performance include the fabric chosen, the cleaning frequency and methods, and
the particulate characteristics. Fabrics can be chosen which will intercept a greater fraction of particulate, and
some fabrics are coated with a membrane with very fine openings for enhanced removal of submicron
particulate. Such fabrics tend to be more expensive.
Pulse-jet cleaning of fabric filters is relatively new compared to othertypes of fabric filters, since they have only
been used for the past 30 years. This cleaning mechanism has consistently grown in popularity because it
can treat high dust loadings, operate at constant pressure drop, and occupy less space than othertypes of
fabric filters. Pulse-jet cleaned fabric filters can only operate as external cake collection devices. The bags
are closed at the bottom, open at the top, and supported by internal retainers, called cages. Particulate-laden
gas flows into the bag, with diffusers often used to prevent oversized particles from damaging the bags. The
gas flows from the outside to the inside of the bags, and then out the gas exhaust. The particles are collected
on the outside of the bags and drop into a hopper below the fabric filter. (EPA, 1998a)
During pulse-jet cleaning, a short burst, 0.03 to 0.1 seconds in duration, of high pressure [415 to 830
kiloPascals (kPa) (60 to 120 pounds per square inch gage (psig))] air is injected into the bags (EPA, 1998a;
AWMA, 1992). The pulse is blown through a venturi nozzle at the top of the bags and establishes a shock
wave that continues onto the bottom of the bag. The wave flexes the fabric, pushing it away from the cage,
and then snaps it back dislodging the dust cake. The cleaning cycle is regulated by a remote timer connected
to a solenoid valve. The burst of air is controlled by the solenoid valve and is released into blow pipes that
have nozzles located above the bags. The bags are usually cleaned row by row (EPA, 1998a).
There are several unique attributes of pulse-jet cleaning. Because the cleaning pulse is very brief, the flow
of dusty gas does not have to be stopped during cleaning. The other bags continue to filter, taking on extra
duty because of he bags being cleaned. In general, there is no change in fabric filter pressure drop or
performance as a result of pulse-jet cleaning. This enables the pulse-jet fabric filters to operate on a
continuous basis with solenoid valves as the only significant moving parts. Pulse-jet cleaning is also more
intense and occurs with greater frequency than the other fabric filter cleaning methods. This intense cleaning
dislodges nearly all of the dust cake each time the bag is pulsed. As a result, pulse-jet filters do not rely on
a dust cake to provide filtration. Felted (non-woven) fabrics are used in pulse-jet fabric filters because they
do not require a dust cake to achieve high collection efficiencies. It has been found that woven fabrics used
with pulse-jet fabric filters leak a great deal of dust after they are cleaned. (EPA, 1998a)
Since bags cleaned by the pulse-jet method do not need to be isolated for cleaning, pulse-jet cleaned fabric
filters do not need extra compartments to maintain adequate filtration during cleaning. Also, because of the
intense and frequent nature of the cleaning, they can treat higher gas flow rates with higher dust loadings.
Consequently, fabric filters cleaned by the pulse-jet method can be smaller than othertypes of fabric filters
in the treatment of the same amount of gas and dust, making higher gas-to-cloth ratios achievable. (EPA,
1998a)
Advantages:
Fabric filters in general provide high collection efficiencies on both coarse and fine (submicron) particulates.
They are relatively insensitive to fluctuations in gas stream conditions. Efficiency and pressure drop are
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relatively unaffected by large changes in inlet dust loadings for continuously cleaned filters. Filter outlet air
is very clean and may be recirculated within the plant in many cases (for energy conservation). Collected
material is collected dry for subsequent processing or disposal. Corrosion and rusting of components are
usually not problems. Operation is relatively simple. Unlike electrostatic precipitators, fabric filter systems
do not require the use of high voltage, therefore, maintenance is simplified and flammable dust may be
collected with proper care. The use of selected fibrous or granular filter aids (precoating) permits the high-
efficiency collection of submicron smokes and gaseous contaminants. Filter collectors are available in a large
number of configurations, resulting in a range of dimensions and inlet and outlet flange locations to suit
installation requirements. (AWMA, 1992)
Disadvantages:
Temperatures much in excess of 290°C (550°F) require special refractory mineral or metallic fabrics, which
can be expensive. Certain dusts may require fabric treatments to reduce dust seepage, or in other cases,
assist in the removal of the collected dust. Concentrations of some dusts in the collector, approximately 50
g/m3 (22 gr/ft3), may represent a fire or explosion hazard if a spark or flame is accidentally admitted. Fabrics
can burn if readily oxidizable dust is being collected. Fabric filters have relatively high maintenance
requirements (e.g., periodic bag replacement). Fabric life may be shortened at elevated temperatures and
in the presence of acid or alkaline particulate or gas constituents. They cannot be operated in moist
environments; hygroscopic materials, condensation of moisture, or tarry adhesive components may cause
crusty caking or plugging of the fabric or require special additives. Respiratory protection for maintenance
personnel may be required when replacing fabric. Medium pressure drop is required, typically in the range
of 100 to 250 mm of water column (4 to 10 inches of water column). (AWMA, 1992)
A specific disadvantage of pulse-jet units that use very high gas velocities is that the dust from the cleaned
bags can be drawn immediately to the other bags. If this occurs, little of the dust falls into the hopper and the
dust layer on the bags becomes too thick. To prevent this, pulse-jet fabric filters can be designed with
separate compartments that can be isolated for cleaning. (EPA, 1998a)
Other Considerations:
Fabric filters are useful for collecting particles with resistivities either too low or too high for collection with
electrostatic precipitators. Fabric filters therefore may be good candidates for collecting fly ash from low-sulfur
coals or fly ash containing high unburned carbon levels, which respectively have high and low resistivities, and
thus are relatively difficult to collect with electrostatic precipitators. (STAPPA/ALAPCO, 1996)
References:
AWMA, 1992. Air & Waste Management Association, Air Pollution Engineering Manual. Van Nostrand
Reinhold, New York.
EPA, 1997. U.S. EPA, Office of Air Quality Planning and Standards, "Compilation of Air Pollutant
Emission Factors, Volume I, Fifth Edition, Research Triangle Park, NC., October.
EPA, 1998a. U.S. EPA, Office of Air Quality Planning and Standards, "Stationary Source Control
Techniques Document for Fine Particulate Matter," EPA-452/R-97-001, Research Triangle Park, NC.,
October.
EPA, 1998b. U.S. EPA, Office of Air Quality Planning and Standards, "OAQPS Control Cost Manual,"
Fifth Edition, Chapter 5, EPA 453/B-96-001, Research Triangle Park, NC. December.
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ICAC, 1999. Institute of Clean Air Companies internet web page www.icac.com, Control Technology
Information - Fabric Filters, page last updated January 11, 1999.
STAPPA/ALAPCO, 1996. State and Territorial Air Pollution Program Administrators and Association of
Local Air Pollution Control Officials, "Controlling Particulate Matter Under the Clean Air Act: A Menu of
Options," July.
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