| Canadian Air Systems Co. is a engineering
| |
| | concurrently, counter=concurrently or in
|
| company for industrial dust collecting
| |
| | cross-flow and are used primarily for
|
| systems. Dust collecting equipment is
| |
| | applications involving gas, vapor and
|
| available in numerous designs utilizing a
| |
| | mist removal.
|
| number of principles and featuring wide
| |
| | - Wet Centrifugal Collectors
|
| variation in effectiveness, initial cost,
| |
| | Â Wet centrifugal dust collectros
|
| operating and maintenance expense, space,
| |
| | utilize centrifugal force to acceslerate
|
| arrangements and material of
| |
| | the dust particle and impigne it upon a
|
| construction.
| |
| | wetted collector surface. These
|
| Factors influencing dust collection
| |
| | collectors are more efficient than the
|
| equipment selection include:
| |
| | chamber type. Some are availbale with
|
| * Concentration and particle size of
| |
| | different number of impingement sections.
|
| contaminant;
| |
| | - Wet Dynamic Precipitators
|
| * Degree of collection required;
| |
| | Â This type uses water sprays within a
|
| * Characteristics of air or gas stream;
| |
| | fan housing and obtains precipitation of
|
| * Characteristics of contaminant;
| |
| | the dust particles on the wetted surface
|
| * Methods of disposal.
| |
| | of an impeller with special fan blade
|
| Depenging on above factors, the following
| |
| | shape. No internal pressure drop is
|
| Canadian Air Systems dust collector types
| |
| | involved although mechanical efficiency
|
| can be utilized:
| |
| | is somewhat lower than the mechanical
|
| ELECTROSTATIC PRECIPIRATORS
| |
| | efficiency of standard exhaust fans.
|
| Â The principle of collection relies on
| |
| | - Orifice Type Collectors
|
| the ability to impart a negative charge
| |
| | Â In this group of wet collectors
|
| to particles in the gas stream causing
| |
| | designs, the air flow through the
|
| them to move and adhere to the grounded
| |
| | collector is brought in contact with a
|
| or positively charged collector plates.
| |
| | sheet of water in a restricted passage.
|
| Most precipitators are made for
| |
| | Water flow may be induced by the velocity
|
| horizontal air flow with velocities 100
| |
| | of the air stream or maintained by pumps
|
| to 600 fpm.
| |
| | and weirs.
|
| - Fabric Collectors
| |
| | - Venturi Scrubbers
|
| Â Fabric arresters are high efficiency,
| |
| | Â This collector uses a venturi-shaped
|
| medium cost collectros. Dust collection
| |
| | construction to establish throat
|
| is obtained by building up a mat of the
| |
| | velocities considerably higher than those
|
| material on the dirty side of the media.
| |
| | experienced with the orifice type. The
|
| This mat provides the actual filtering or
| |
| | collection mechanism of the venturi is
|
| straining bed. By means of this bed a
| |
| | impaction. As with wet collectors in
|
| high degree of removal is obtained even
| |
| | general, the collection efficiency of the
|
| on submicron size particles.
| |
| | venturi increases with higher pressure
|
| - Intermittent-Duty Fabric Collectors
| |
| | drops. Different pressure drops are
|
| Â These types may use either envelope
| |
| | achieved by designing for selected gas
|
| or stocking arrangement of the fabric but
| |
| | velocities in the throat. The venturi
|
| will generally employ shaking or
| |
| | iteself is a gas conditioner causing
|
| vibrating as a means of reconditioning.
| |
| | intimate contact between particles in the
|
| Periodically Uusually at 4 to 6 hour
| |
| | gas and the multiple jet streams of
|
| intervals0 the air flow must be stopped
| |
| | scrubbing water.
|
| to effect reconditioning - thus the
| |
| | DRY COLLECTORS
|
| classification "intermittent".
| |
| | - Cyclone Dust Collectros
|
| - Multiple-Section, Continuous-Duty,
| |
| | Â Cyclone Collectors are frequently
|
| Automatic Fabric Collectors
| |
| | applied for the removal of coarse dusts
|
| Â The disadvanteges of stopping the air
| |
| | from an air stream, as a pre-cleaner to
|
| flow to permit vibration and variations
| |
| | more efficient dry or wet dust collectors
|
| in the airflow can be overcomed by using
| |
| | and / or as a separator in product
|
| of sectional arresters allowing
| |
| | conveying systems using an air stream to
|
| continuous operation of the exhaust
| |
| | transport material. Principle advantages
|
| system as automatic dampers periodically
| |
| | are low cost, low maintenance and low
|
| take one section out of service for
| |
| | pressure drop (in order 0.75" to 1.5"
|
| reconditioning the fabric while the
| |
| | WG), but this type dust collector can not
|
| remaining sections take the entire gas
| |
| | be used for collection of fine particles.
|
| volume.
| |
| | Â
|
| - Reverse-Jet Fabric Collectors
| |
| | - High Efficiency Centrifugal Collectors
|
| Â The reverse-jet type differs from the
| |
| | Â Have been developed whereby higher
|
| conventional arrsters in its use of high
| |
| | centrifugal forces are exerted on dust
|
| pressure air to clean the fabric. One
| |
| | particles in a gas stream. Improvement in
|
| type uses high pressure air (30" - 40"
| |
| | dust separation efficiency has been
|
| WG) froma travelling "blow ring" to
| |
| | obtained by 1) increasing velocities
|
| dislodge the collected cake from inside
| |
| | through a cyclone shape dust collector,
|
| the fabric tube. Another type uses high
| |
| | 2) utilizing a skimmer or other design
|
| pressure compressed air (100 PSI) to
| |
| | feature, 3) using a number of small
|
| break the dust cake from the exterior of
| |
| | diameter cyclones in parallel and 4)
|
| the fabric tube or envelope by the
| |
| | placing units in series in some unusual
|
| intermittent application of reverse-jet
| |
| | applications.
|
| compressed air.
| |
| | - Dry Type Dynamic Precipitators
|
| - Reverse-Flow Collapse, Continuous-Duty
| |
| | Â In this collector, dust is
|
| Collectors
| |
| | precipitated by centrifugal force on to
|
| Â Reverse-flow collapse cleaning is
| |
| | specially shaped blades on an exhauster
|
| generally used with glass media which is
| |
| | wheel and then conveyed through a dust
|
| fragile and requires a gentle cleaning
| |
| | circuit in the fan casing to the dust
|
| technique. Reversing the glass flow
| |
| | storage hopper.
|
| provides a gentle collapse of the fabric
| |
| | - Louver Type Dust Collectors
|
| usually in a "four point star" braking
| |
| | Â Centrifugal forces can be applied to
|
| the dust cake which falls by gravity into
| |
| | a particle by a rapid change in direction
|
| the hopper.
| |
| | of air flow by series of plates set at an
|
| WET COLLECTORS
| |
| | angle to the air stream. Coarse particles
|
| Â Wet collectors are available in many
| |
| | traverse the air stream and will project
|
| different designs. They have the ability
| |
| | back to the dirty air side by the forces
|
| to handle high temperature and
| |
| | that can be produced from such an impact.
|
| moisture-laden gases. The collection of
| |
| | - Settling Chambers
|
| dust in wetted form eliminates a
| |
| | Â Dust is ettled out in a large chamber
|
| secondary dust problem in disposal of
| |
| | when conveying velocities are reduced to
|
| collected material. Also, some dust
| |
| | the point where the particles are no
|
| represent explosion or fire hazard when
| |
| | longer conveyed. Extreme space
|
| dry and wet collectors eliminate or at
| |
| | requirements and the presence of edde
|
| least reduce the hazzard.
| |
| | currents to nullify the effective
|
| - Chamber or Spray Tower
| |
| | velocity mean that settling chamber type
|
| Â Consists of a round or rectangular
| |
| | of dust collectors can be used only for
|
| chamber into which water is introduced
| |
| | removal of extremely coarse particles.
|
| via spray nozzles. There are many
| |
| | - Potable Unit Collectors
|
| variations in design but the principal
| |
| | Â To fill the need for dust collection
|
| mechanism is impaction of dust particles
| |
| | from isolated, portable or frequently
|
| on the liquid droplets created by
| |
| | relocated dust producing operations, a
|
| nozzles. These droplets are separated
| |
| | number of unit collector designs are
|
| from the air stream by centrifugal force
| |
| | availbale having capacities in the range
|
| or impingement on water eliminators.
| |
| | of 200 to 1,000 CFM. Featuring small
|
| - Packed Towers
| |
| | space and designed to recirculate the
|
| Â Collectors in this group are
| |
| | air, collectors of this type have been
|
| essentially contact beds through which
| |
| | used extensively, especially in the metal
|
| gases and liquid pass either
| |
| | working industry.
|