The Encyclopedia Of Dust Collectors
This article has been designed to educate customers by giving a brief overview of all the Dust Collection Systems available today. A detailed explanation of the benefits and drawbacks of each type of system can be found in further articles on Baghouse.com
What is a Dust Collector?
After the contaminated air is captured by a Dry Dust Collection system, either by means of a Central Collection System, or in a unit Collector. The dust filled air then needs to be treated and the contaminates removed, before the air can be recirculated back into the facility or dispersed into the atmosphere. The Dust Collector separates the particles from the airstream and sends it on to its final destination.
Why are Dust Collectors Needed?
There are many reasons why having a proper Dust Collection System installed in your facility is needed, a few important reasons are:
• To protect employees and society from exposure to pollution,
• To recover valuable products from the dust filled air
• To facilitate compliance with health and air emission standards.
Types of Dust Collectors
The five principal types of industrial dust collectors that will be discussed in this article are:
• Cyclone Collectors (Inertial separators)
• Baghouses (Fabric collectors)
• Wet scrubbers
• Electrostatic precipitators
• Unit collectors
Cyclone Collectors (Inertial Separators)
Inertial separators work by making use of one or more of the following forces centrifugal, gravitational, and inertial in order to separate dust from the airstream. Once separated, the dust is removed to a hopper by gravity for temporary storage. While this type of collect can be used in applications where particle sizes are large and only a “rough” air filtration is desired, the main usage for this type of collector is as a precleaner, to remove larger particles and debris and avoid overloading and damaging more efficient dust collectors.
The three types of Inertial Separators are:
• Settling Chambers
• Baffle Chambers
• Centrifugal Collectors
A Settling Camber is a large box installed into the ductwork. The sudden larger area for the airstream to pass through causes the air stream to slow down, which in turns causes the larger particles to settle to the bottom of the chamber. This type of collector is rarely used as the primary dust collector due to it’s large space requirements, and low efficiency. However, the fact that it can be fashioned from almost any material and its simple design, which requires little maintenance, leads it to being a wise choice as a precleaner for a more efficient Dust Collector.
A Baffle Chamber has a fixed baffle plate that causes the airflow to rapidly change its direction, first turning downward, and then making a 180 degree turn back up. In the process, the larger particles fall to the bottom of the chamber and can be collected from there. As with Settling Chambers this type of collector is best used as a precleaner for another more efficient collector further in the collection system. Also like a Settling Chamber its relatively simple design and low maintenance needs make it an excellent choice for the beginning of any large scale collection system.
Centrifugal Collectors create a vortex in the airstream within an enclosure, similar to water going down a drain. Normally this is done by having the airstream enter the collect at an angle, which causes it to spin. As the airstream is spun around the collector, the particles strike the wall and fall into the hopper below.
Within this category there are two main types of systems in use:
• Single Cyclone systems
• Multiple Cyclone systems
A Single Cyclone Collector creates a dual vortex, a main downward vortex to disperse the coarser matter, and a secondary upward vortex to remove the finer particles on the return to the outlet to the duct system.
A Multiple Cyclone Collector works in the same manner as the Single Cyclone variety albeit with several small dynamiter cyclones instead of just one. The multiple cyclones work in parallel and share the same air input and output.
Between the two, the Multiple Cyclone Collector will operate more efficiently because of being longer in length and smaller in dynamiter. The smaller dynamiter cause the centrifugal force generated to be greater, and the longer length allows for more contact with the surface of the collector by the particles thereby causing more particles to be removed from the airstream. However, a greater loss of pressure is found in Multiple Cyclone Collectors than in Single Cyclone Collectors.
Again as with the other kinds of Inertial Separators, this systems main advantage is the lack of moving parts thus requiring less maintenance and repair. While it can be designed to remove a specific size range of particles, it still remains best used as a precleaner to eliminate coarse particles and ease the load on more efficient Dust Collectors further along in the system.
Advantages & Disadvantages – Centrifugal Collectors
|Cyclones||Have no moving parts||Have low collection efficiency for respirable particulates|
|Can be used as precleaners to remove coarser particulates and reduce load on more efficient dust collectors||Suffer decreased efficiency if gas viscosity or gas density increases|
|Can be designed to remove a specific size range of particles||Are susceptible to erosion|
|Have drastically reduced efficiency due to reduction in airflow rate|
|Cannot process sticky dust|
|Multiple Cyclones||Have no moving parts||Have low collection efficiency for respirable particulates|
|Are more efficient than single-cyclone separators||Are prone to plugging due to smaller diameter tubes|
|Have low pressure drop when used as a precleaner||Improper gas distribution may result in dirty gas bypassing several tubes|
|Cannot process sticky dust|
|For a given gas volume, occupy more space than single-cyclone separators|
Common Operating Problems & Solutions – Cyclone Collectors
|Erosion||High concentrations of heavy, hard, sharp-edged particles||Install large-diameter “roughing” cyclone upstream of high-efficiency, small-diameter cyclone.|
|Line high-efficiency cyclone with refractor or erosion-resistant material.|
|Corrosion||Moisture and condensation in cyclone||Keep gas stream temperature above dewpoint.|
|Use corrosion-resistant material such as stainless steel or nickel alloy.|
|Dust Buildup||Gas stream below dewpoint||Maintain gas temperature above dewpoint.|
|Very sticky material||Install vibrator to dislodge material.|
|Leakage in ductwork of cyclone||Clean cyclone routinely.|
|Check for pluggage and leakage and unplug or seal the ductwork.|
|Close all inspection ports and openings.|
|Reduced gas velocity in cyclone||Check the direction of fan rotation; if rotation is wrong, reverse two of the tree leads on motor.|
Common Operating Problems and Solutions – Multiclones
|Erosion||High concentrations of heavy, hard, sharp-edged particles||Install cast iron tubes.|
|Install a wear shield to protect tubes|
|Overloaded tubes||Uneven gas flow and dust distribution||Install turning vanes in elbow, if elbow precedes inlet vane.|
|Loss of volume in tubes|
|Uneven pressure drop across tubes|
|Plugging in inlet vanes, clean gas outlet tubes, and discharge hopper||Low gas velocity||Install turning vanes in elbow inlet|
|Uneven flow distribution||Insulate multiclone|
|Moisture condensation||Install bin-level indicator in collection hopper.|
|Overfilling in discharge hopper||Empty hopper more frequently.|
|Reduced efficiency or dirty gas stack||Leakage in ductwork||Seal all sections of ductwork and multiclone to prevent leaks|
|Leakage in multiclone|
Startup/Shutdown Procedures – Centrifugal Collectors
|Cyclones||1. Check fan rotation.||1. Allow exhaust fan to operate for a few minutes after process shutdown until cyclone is empty.|
|2. Close inspection doors, connections, and cyclone discharge.||2. If combustion process is used, allow hot, dry air to pass through cyclone for a few minutes after process shutdown to avoid condensation.|
|3. Turn on fan.||3. Turn off exhaust fan.|
|4. Check fan motor current.||4. Clean discharge hopper.|
|5. Check pressure drop across cyclone.|
|Multiclones||1. Conduct same startup procedures as cyclones.||1. Conduct same shutdown procedures as cyclones.|
|2. At least once a month, measure airflow by conducting a pitot traverse across inlet to determine quantity and distribution of airflow.|
|3. Record pressure drop across multiclone.|
|4. If flow is significantly less than desired, block off rows of cyclone to maintain the necessary flow per cyclone.|
Preventative Maintenance Procedures – Centrifugal Collectors
|Cyclones||Daily||Record cyclone pressure drops.|
|Check stack (if cyclone is only collector).|
|Record fan motor amperage.|
|Inspect dust discharge hopper to assure dust is removed.|
|Weekly||Check fan bearings.|
|Check gaskets, valves, and other openings for leakage.|
|Monthly||Check cyclone interior for erosion, wear, corrosion, and other visible signs of deterioration.|
|Multiclones||Daily||Same as cyclones.|
|Weekly||Same as cyclones.|
|Monthly||Check multiclone interior for erosion, wear, corrosion, and improper gas and dust distribution.|
|Inspect individual cyclones and ducts for cracks caused by thermal expansion or normal wear.|
Fabric Dust Collectors
Fabric Collectors (commonly known as a Baghouse) are among the most widely used dust collection systems. They benefit from having the potential to be one of the most efficient (up to 99% of very fine particles) and cost effective dust collection systems you can choose.
The way they work
The Gas stream enters into the Baghouse via the location’s duct system. Once inside the dust filled gases come into contact with the filter bags within. As the gases pass through the filters the dust particles are trapped on the filter media. Over time a layer of cake dust is built up on the surface of the filter bags. This is the secret to this filter medium’s high efficiency potential. Once the cake dust has formed, it further impedes the passage of dust through the filters in four different ways:
• Inertial Collection: The incoming Gas stream strikes the filter media, which is located perpendicular to the Gas flow before changing direction causing the dust particles to remain on the filter.
• Interception: Particles that do not cross the fluid streamlines come in contact with fibers because of the fiber size.
• Brownian movement: By means of diffusion, there is an increased chance of contact between the filter and the dust particles due to their molecular motion.
• Electrostatic Forces: An increased attraction can occur between the dust particles and the filter media when an electrostatic charge is found on the dust particles.
Air to Cloth Ratio
An understanding of the term Air to Cloth Ratio is vital to understand the mechanics of any Baghouse system regardless of the exact type used. This ratio is defined as the amount of air or process gas entering the Baghouse divided by the sq. ft of cloth in the Baghouse. An example of an Air to Cloth Ratio is provided below courtesy of http://www.usairfiltration.com
(Bag diameter in inches x pi x bag length in inches)
Total Cloth area = 144 x total number of bags
A standard 6” bag has a 5-7/8” diameter
This bag is 12’ long
There are a total of 132 bags in the Baghouse
= (5-7/8” x 3.1416 x 144”) ÷ 144 x 132
= (5.875” x 3.1416 x 144”) ÷ 144 x 132
= (2657.79) ÷ 144 x 132
= 18.46 SF of cloth per bag x 132 bags
Total cloth area = 2,436 sq. ft.
Assume the Baghouse is handling 13,000 ACFM of air
Air to cloth ratio = ACFM ÷ total cloth area
= 13,000 ÷ 2,436
= 5.34 : 1
Different Baghouse designs
There are three main types of Baghouse systems currently in use today. The same basic mechanics are present in all of them, the main difference being how filter bags are cleaned.
• Mechanical Shaker
• Reverse Air
• Reverse Jet (Or Pulse Jet)
A Mechanical Shaker is a design where the filter bags are suspended from the top of the Baghouse by horizontal beams and fastened to a cell plate on the bottom. When the Gas stream enters at the bottom of the Baghouse it is then forced up through the inside of the tubular filter bags, thereafter passing unto the airflow outlet at the top. The cleaning of this type of Baghouse is done by a shaking of the top horizontal bar that the filter bags are attached to. This is caused by a motor driven shaft and cam system that sends waves down the surface of the filter bags causing the dust to fall off the interior of them into the hopper below. This Baghouse has a relatively low Air to Cloth Ratio requiring large amounts of space. Despite this draw back, the simple design remains a noted advantage, leading to this system being widely used in the mineral processing industry.
In a Reverse Air Baghouse, filter bags are connected to a cell plate on the bottom of the Baghouse and are suspended from an adjustable hanger frame on top. The Gas stream, as in the Mechanical Shaker design enters into the Baghouse and passes through the filter bags from the bottom leading to the dust collecting again on the interior of the filter bags, thereafter leaving through the outlet port at the top. Again the main difference in this style of Baghouse system when compared to others is the cleaning mechanism. In this system, a cleaning cycle starts with injecting clean air into the Collector in the reverse direction of the normal flow. This causes the compartment to become pressurized. The pressure causes the bags to collapse slightly releasing the cake dust to crack and fall off to be collected by the hopper below. Since it is necessary to shut down normal airflow to the Baghouse during the cleaning cycle, this type of Baghouse is normally compartmentalized so as to allow for only a partial shutdown of the system.
With a Reverse Jet or Pulse Jet Baghouse, the same basic design is found as in the other types of Baghouse design, however, with a few very important differences. In a Pulse Jet Baghouse, the baghouse filter bags are individually overlaid on a metal cage, which is then attached to a cell plate at the top of the compartment. The Gas stream enters the Baghouse at the bottom and is forced through the outside to the inside of the filter bags after which the Gas stream exits the compartment from the outlet port at the top. The main advantage of this Baghouse is that it does not require a shutdown of any kind to run a cleaning cycle. A digital sequential timer is attached to the one of the filter bags inside the Baghouse. This timer signals a solenoid valve to start the cleaning cycle when it detects a certain amount of build up on the bag. It consists of a small burst of compressed air being fired down through the filter bags. Which cause the excess cake dust to fall off into hopper at the bottom of the Baghouse where it can be collected. The cleaning cycle of the Pulse Jet collectors provides a more complete cleaning and reconditioning of the filter bags than in the Shaker, and Reverse Air designs. Also the short nature of the cleaning cycle also leads to a reduction in the recirculation and redeposit of dust. Finally, enabled by the continuous cleaning feature of the design, this kind of collection system has a higher Air to Cloth Ratio so the space requirements are much lower than in other systems.
Unlike Baghouse collectors which feature the use of woven or felt filter bags, Cartridge Collectors use perforated metal cartridges that are cylindrical shaped and open on one or both ends lined with a pleated nonwoven filtering media. Once installed, one end of the cartridge is sealed off and the open end is used for the clean exhaust. Similar to a Baghouse, the Gas stream is forced through the outside of the cartridge to the inside where it then exits back into the system. Cartridge Collectors are also compatible with Reverse or Pulse Jet cleaning. Large numbers of these Collectors can be installed and used for continuous filtration for a location’s dust collection system.
Advantages and Disadvantages – Baghouses
|Shaker Baghouses||Have high collection efficiency for respirable dust||Have low air-to-cloth ratio (1.5 to 2 ft/min)|
|Can use strong woven bags, which can withstand intensified cleaning cycle to reduce residual dust buildup||Cannot be used in high temperatures|
|Simple to operate||Require large amounts of space|
|Have low pressure drop for equivalent collection efficiencies||Need large numbers of filter bags|
|Consist of many moving parts and require frequent maintenance|
|Personnel must enter Baghouse to replace bags, creating potential for exposure to toxic dust|
|Can result in reduced cleaning efficiency if even a slight positive pressure exists inside bags|
|Reverse Air Baghouses||Have high collection efficiency for respirable dust||Have low air-to-cloth ratio (1 to 2ft/min)|
|Are preferred for high temperatures due to gentle cleaning action||Require frequent cleaning because of gentle cleaning action|
|Have low pressure drop for equivalent collection efficiencies||Have no effective way to remove residual dust buildup|
|Cleaning air must be filtered|
|Require personnel to enter baghouse to replace bags, which creates potential for toxic dust exposure|
|Pulse Jet (Reverse Jet) Baghouses||Have a high collection efficiency for respirable dust||Require use of dry compresses air|
|Can have high air-to-cloth ratio (6 to 10ft/min)||May not be used readily in high temperatures unless special fabrics are used|
|Have increased efficiency and minimal residual dust buildup due to aggressive cleaning action||Cannot be used if high moisture content or humidity levels are present in the exhaust gases|
|Can clean continuously|
|Can use strong woven bags|
|Have lower bag wear|
|Have small size and fewer bags because of high air-to-cloth ratio|
|Some designs allow bag changing without entering Baghouse|
|Have low pressure drop for equivalent collection efficiencies|
Common Operating Problems and Solutions – Baghouses*
|High Baghouse pressure drop||Baghouse undersized||consult vendor|
|Install double bags|
|Add more compartments or modules|
|Bag cleaning mechanism not properly adjusted||Increase cleaning frequency|
|Clean for longer duration|
|Clean more vigorously|
|Shaking not strong enough (S)||Increase shaker speed|
|Compartment isolation damper valves not operating properly (S, RA)||Check linkage|
|Check valve seals|
|Check air supply of pneumatic operators|
|Compressed air pressure too low (PJ)||Increase pressure|
|Decrease duration and frequency|
|Check compressed-air dryer and clean it if necessary|
|Check for obstructions in piping|
|Repressurizing pressure too low (RA)||Speed up repressurizing fan.|
|Check for leaks|
|Check damper valve seals|
|Pulsing valves failed (PJ)||Check diaphragm|
|Check pilot valves|
|Bag tension too tight (RA)||Loosen bag tension|
|Bag tension too loose (S)||Tighten bags|
|Cleaning timer failure||Check to see if timer is indexing to all contacts|
|Check output on all terminals|
|Not capable of removing dust from bags||Check for condensation on bags|
|Send dust sample and bags to manufacturer for analysis|
|Dryclean or replace bags|
|Excessive reentrainment of dust||Empty hopper continuously|
|Clean rows of bags randomly instead of sequentially (PJ)|
|Incorrect pressure-drop reading||Clean out pressure taps|
|Check hoses for leaks|
|Check for proper fluid level in manometer|
|Check diaphragm in gauge|
|Dirty Discharge at stack||Bags leaking||Replace bags|
|Isolate leaking compartment or module|
|Tie off leaking bags and replace them later|
|Bag clamps not sealing||Smooth out cloth under clamp and re-clamp|
|Check and tighten clamps|
|Failure of seals in joints at clean/dirty air connection||Caulk or weld seams|
|Insufficient filter cake||Allow more dust buildup on bags by cleaning less frequently.|
|Use precoating on bags (S, RA).|
|Bags too porous||Send bag in for permeability test and review with manufacturer|
|High compressed-air consumption (PJ)||Cleaning cycle too frequent||Reduce cleaning cycle, if possible|
|Pulse too long||Reduce pulsing duration|
|Pressure too high||Reduce supply pressure, if possible|
|Diaphragm valve failure||Check diaphragm and springs|
|Check pilot valve|
|Reduced compressed-air pressure (PJ)||Compressed-air consumption too high||See previous solutions|
|Restrictions in compressed-air piping||Check compressed-air piping|
|Compressed-air dryer plugged||Replace dessicant in the dryer|
|Bypass dryer temporarily, if possible|
|Compressed-air supply line too small||Consult design|
|Compressor worn out||Replace rings|
|Check for worn components|
|Rebuild compressor or consult manufacturer|
|Pulsing valves not working||Check pilot valves, springs, and diaphragms|
|Timer failed||Check terminal outputs|
|Moisture in Baghouse||Insufficient preheating||Run the system with hot air only before process gas flow is introduced|
|System not purged after shutdown||Keep fan running for 5 to 10 min after process is shut down|
|Wall temperature below dewpoint||Raise gas temperature|
|Lower dewpoint by keeping moisture out of system|
|Cold spots through insulation||Eliminate direct metal line through insulation|
|Water/moisture in compressed air (PJ)||Check automatic drains|
|Repressurizing air causing condensation (PJ)||Preheat repressurizing air|
|Use process gas as source of repressurizing air|
|Material bridging in hopper||Moisture in Baghouse||See previous solutions|
|Dust stored in hoppers||Remove dust continuously|
|Hopper slope insufficient||Rework or replace hoppers|
|Screw conveyor opening too small||Use a wide, flare trough|
|High rate of bag failure, bags wearing out||Baffle plate worn out||Replace baffle plate|
|Too much dust||Install primary collector|
|Cleaning cycle too frequent||Slow down cleaning|
|Inlet air not properly baffled from bags||Consult vendor|
|Shaking too violent (S)||Slow down shaking mechanism|
|Repressurizing pressure too high (RA)||Reduce pressure|
|Pulsing pressure too high (PJ)||Reduce pressure|
* S = Shaker
RA = Reverse Air
PJ = Pulse Jet
Startup/Shutdown Procedures – Baghouses
|1. For processes generating hot, moist gases, preheat Baghouse to prevent moisture condensation, even if Baghouse is insulated. (Ensure that all compartments of shaker or reverse-air Baghouses are open.)||1. Continue operation of dust-removal conveyor and cleaning of bags for 10 to 20 minutes to ensure good removal of collected dust.|
|2. Activate Baghouse fan and dust-removal conveyor.|
|3. Measure Baghouse temperature and check that it is high enough to prevent moisture condensation.|
Preventive Maintenance Procedures – Baghouses
• Check pressure drop.
• Observe stack (visually or with opacity meter).
• Walk through system, listening for proper operation.
• Check for unusual occurrences in process.
• Observe control panel indicators.
• Check compressed-air pressure.
• Assure that dust is being removed from system.
• Inspect screw-conveyor bearings for lubrication.
• Check packing glands.
• Operate damper valves.
• Check compressed-air lines, including line filters and dryers.
• Check that valves are opening and closing properly in bag-cleaning sequence.
• Spot-check bag tension.
• Verify accuracy of temperature-indicating equipment.
• Check pressure-drop-indicating equipment for plugged lines.
• Check all moving parts in shaker mechanism.
• Inspect fans for corrosion and material buildup.
• Check drive belts for wear and tension.
• Inspect and lubricate appropriate items.
• Spot check for bag leaks.
• Check hoses and clamps.
• Check accuracy of indicating equipment.
• Inspect housing for corrosion.
• Inspect baffle plate for wear.
• Inspect bags thoroughly.
• Check duct for dust buildup.
• Observe damper valves for proper seating.
• Check gaskets on doors.
• Inspect paint, insulation, etc.
• Check screw conveyor for wear or abrasion.
• Check fan belts.
• Check welds.
• Inspect hopper for wear
Another effective method of dust collection is the use of Wet Scrubbers (Air Washers). These systems use a scrubbing liquid (usually water) to filter out finer dust particles. After being filtered the Gas Stream is then sent through a mist eliminator (demister pads) to remove the excess moisture from the Gas stream. Afterward the Gas stream exits the collector through the outlet port and returns back into the system. Wet Scrubbers are ideal:
• For the collection of explosive material
• Where “slurry” produced could be reused (either in other parts of process or sold)
• Where chemical reactions could be generated with other collection methods
• To absorb excess air
Wet scrubbers have the advantage of low start up costs and low space requirements. They are well suited for treating high temperature and high humidity Gas streams. They also are able to process both air and “sticky” particulates. The main disadvantages are that they are costly to operate, require a precleaner for any heavy dust loads, cause water pollution that then needs to be addressed, and can erode with high air velocities.
There are a vast variety of different designs and applications of this type of filtration system but all of them have three basic operations they perform:
• Gas-humidification: The gas-humidification process conditions fine particles to increase their size so they can be collected more easily.
• Gas-liquid contact: This is the entire basis for the operation of this type of system. The method of contact between the liquid is done in four main ways:
• Inertial impaction takes place when the Gas stream is forced to flow around the droplets in its path. The stream separates and flows around the droplet. However the larger particles continue to be carried by inertial force in a straight path coming in direct contact with the liquid.
• Interception: Finer particles while not directly coming in contact with the droplets, do however brush up against the side of them causing them to be absorbed into the liquid.
• Diffusion occurs when a fine mist is created from the liquid being used. As the particles pass through the mist they make contact with the surfaces of the droplets by means of the Brownian effect, or diffusion.
• Condensation nucleation is the effect of a gas being cooled below its dew point while within a moisture rich environment, causing the vapor to condense of the surface of the particles thereby encapsulating them.
• Liquid separation: After going through the cleaning phase the remaining liquid and contaminates must be removed before the Gas stream can be sent back into the system. This is accomplished by means of a Mist Eliminator (Demister Pads). Which remove the liquid and dust mixture from the Gas stream and send it to a collector. Once in the collector, the solid waste settles to the bottom where it is removed by means of a drag chain system to be deposited in a dumpster or another collection area.
Wet Scrubbers are further categorized by pressure drop (in inches water gauge) as follows:
• Low-energy scrubbers (0.5 to 2.5)
• Low- to medium-energy scrubbers (2.5 to 6)
• Medium- to high-energy scrubbers (6 to 15)
• High-energy scrubbers (greater than 15)
The large amount of different Wet Scrubbers in use makes it impossible to comment on every single design in this article. However a brief overview of the most common types will enable you to understand the basic operational procedures present in all of them.
Low Energy Scrubbers:
• The most basic design is that of a Gravity Spray Tower Scrubber. In this system the contaminated air enters at the bottom of the cylindrically shaped scrubber and rises through a mist of water sprayed from nozzles at the top. The dirty water collects at the bottom of the tank and the clean air (mist) exits from the top of the collector. This collector has a relatively low efficiency compared to other kinds of Wet Scrubbers. However it’s main advantage is it can handle very heavy dust loads without getting backed up.
• Dynamic wet precipitators also called Wet Fan Scrubbers are a popular design used for medium energy scrubbing applications. In this system the Gas stream passes through a larger fan that is constantly kept wet with the cleaning liquid. The particles are trapped in the liquid and are then by means of centrifugal force thrown off the spinning fan blades unto the sides of the collector where they eventually settle at the bottom enabling them to be collected.
• Orifice Scrubbers work in a very similar way to inertial separators but with one important difference, Orifice Scrubbers use a water surface to capture the dust particles. When the Gas stream enters the collector it is rapidly redirected when it comes in contact with the water surface. Causing the dust particles to be removed from the Gas stream. A greater efficiency can be obtained by the addition of liquid spray nozzles to further separate the contaminates from the Gas stream. While these are an effective filtration system one should note that they tend to be ineffective against fine particles as these tend to be redirected off of the water surface by the high surface tension.
Low to Medium Energy Scrubbers:
• Wet Cyclone Scrubbers are nearly identical to their normal cyclone collector counterparts. In a Wet Cyclone Scrubber the Gas stream enters the collector and is then forced into a cyclone movement by the strategic placement of stationary scrubbing vanes. Liquid is introduced at the top of the collector allowing the dust particles to stick to the wet walls of the collector when they are thrown off by the vortex. As with dry Cyclone Collectors, this type of system has the benefit of few to no moving parts and it is efficient for particles up to 5um and above.
Medium to High Energy Scrubbers:
• Packed Bed Scrubbers consist of a bed of packing media, which is then sprayed with water. The packing media allows for a very wide distribution of the water, which in turn allows the Gas stream to have the maximum contact with the water during its passage though the collector. Air enters at the bottom of the collector where it first makes contact with the water in the recirculation tank. Then it is forced up through the various layers of the filtering media, and after being sent through a Mist Eliminator is sent back into the system via the exit port at the top.
Within the category of Packed Bed Scrubbers there are three different variations on the implementation of this filtering mechanism they are:
• Cross-flow scrubbers are designed to minimize height for low-profile applications. In this design the packed media is laid as sheets perpendicular to the Gas stream. The Gas stream enters in one side of the Scrubber and flows horizontally through it passing though the packing media and then exiting out the opposite side
• Co-current flow scrubbers
• Counter-current flow scrubbers
High energy Scrubbers:
• Venturi Scrubbers make use of the Venturi effect to accelerate the Gas stream to speeds of 12,000 to 36,000 ft/min. The Gas stream enters into the Scrubber through a Venturi shaped inlet where it is sprayed with water. The water hitting the extremely high speed air causes it to instantly atomize. The very fine water droplets attach to the dust particles and form a slurry, which then falls to the bottom of the collector. After passing through a Mist eliminator the Gas stream is sent back into the system.
Advantages and Disadvantages – Wet Scrubbers
|Have low capital costs and small space requirements||Have high operating and maintenance costs|
|Have low capital costs and small space requirements||Require corrosion-resistant materials if used with acidic gases|
|Are able to collect gases as well as particulates (especially “sticky” particulates)||Require a precleaner for heavy dust loadings|
|Have no secondary dust sources||Cause water pollution; require further water treatment|
|Are susceptible to erosion at high velocities|
|Collect wet products|
|Require freeze protection|
Common Operating Problems and Solutions – Wet Scrubbers
|Wet/dry buildup||Keep all areas dry or all areas flooded.|
|Use inclined ducts to a liquid drain vessel.|
|Ensure that scrubber is installed vertically.|
|Maintain liquid seal.|
|Dust buildup in fan||Install clean water spray at fan inlet.|
|Excessive fan vibration||Clean fan housing and blades regularly.|
|Liquid pump failure||Divert some of the recycle slurry to a thickener, settling pond, or waste disposal area and supply clean water as makeup.|
|Increase the water bleed rate.|
|Worn valves||Use wear-resistant orifice plates to reduce erosion on valve components.|
|Jammed valves||Provide continuous purge between valves and operating manifold to prevent material buildup.|
|Erosion of slurry piping||Maintain pumping velocity of 4 to 6 ft/s to minimize abrasion and prevent sedimentation and settling.|
|Plugged nozzles||Replace nozzles or rebuild heads.|
|Change source of scrubbing liquid.|
|Supply filtered scrubbing liquid.|
|Buildup on mist eliminators||For vane-type demisters, spray the center and periphery intermittently to clean components.|
|For chevron-type demisters, spray the water from above to clean the buildup.|
Startup/Shutdown Procedures – Wet Scrubbers
|1. Start fans and pumps to check their rotation.||1. Shut down fan and fan spray. Insulate scrubber from operation.|
|2. Disconnect pump suction piping and flush it with water from an external source.||2. Allow liquid system to operate as long as possible to cool and reduce liquid slurry concentrations.|
|3. Install temporary strainers in pump suction line and begin liquid recycle.||3. Shut off makeup water and allow to bleed normally.|
|4. With recycle flow on, set valves to determine operating conditions for desired flow rates. Record the valve positions as a future baseline.||4. When pump cavitation noise is heard, turn off pump and pump gland water.|
|5. Record all system pressure drops under clean conditions.||5. Open system manholes, bleeds, and other drains.|
|6. Perform all recommended lubrications.|
|7. Shut down fan, drain the system, and remove temporary strainers.|
|1. Allow vessels to fill with liquid through normal level controls. Fill large-volume basins from external sources.|
|2. Start liquid flow to all pump glands and fan sprays.|
|3. Start recycle pumps with liquid bleed closed.|
|4. Check insulation dampers and place scrubber in series with primary operation.|
|5. Start fan and fan inlet spray. Leave inlet control damper closed for 2 min to allow fan to reach speed.|
|6. Check gas saturation, liquid flows, liquid levels, fan pressure drop, duct pressure drops, and scrubber pressure drop.|
|7. Open bleed to pond, thickener, or other drain systems so slurry concentration can build slowly. Check final concentration as cross-check on bleed rate.|
Preventative Maintenance Procedures – Wet Scrubbers
• Check recycle flow.
• Check bleed flow.
• Measure temperature rise across motor.
• Check fan and pump bearings every 8 hours for oil level, oil color, oil temperature, and vibration.
• Check scrubber pressure drop.
• Check pump discharge pressure.
• Check fan inlet and outlet pressure.
• Check slurry bleed concentration.
• Check vibration of fan for buildup or bleeds.
• Record inlet and saturation temperature of gas stream.
• Use motor current readings to detect flow decreases. Use fan current to indicate gas flow.
• Check pressure drop across mesh and baffle mist eliminators. Clean by high-pressure spraying, if necessary.
• Check wet/dry line areas for material buildup. Clean, if necessary.
• Check liquid spray quantity and manifold pressure on mist eliminator automatic washdown.
• Inspect fans on dirty applications for corrosion, abrasion, and particulate buildup.
• Check bearings, drive mechanisms, temperature rise, sprocket alignment, sprocket wear, chain tension, oil level, and clarifier rakes.
• Check ductwork for leakage and excessive flexing, Line or replace as necessary.
• Clean and dry pneumatic lines associated with monitoring instrumentation.
• Verify accuracy of instruments and calibrate.
• Inspect orifice plates.
• Clean electrical equipment, including contacts, transformer insulation, and cooling fans.
• Check and repair wear zones in scrubbers, valves, piping, and ductwork.
• Lubricate damper drive mechanisms and bearings. Verify proper operation of dampers and inspect for leakage.
Electrostatic Precipitators use electrostatic forces to collect dust from the Gas stream. Several high power Direct Current Discharge Electrodes are places inside the collector. The incoming Gases pass by the first set of Discharging Electrodes (ionizing section) that give the particles a negative charge (ionization). The now ionized particles travel pass the next set of electrodes (the collection section) that carry a positive charge. The positively charged plates attract the negatively charged particles causing them to collect on the plates. Cleaning is accomplished by vibrating the electrodes either continuously, or at a timed interval, causing the captured dust to fall off into a hopper below. All of this can be done while the system is operating normally.
Electrostatic Precipitators are best used in an ambient capture type system with low particle loads. Without an automated self-cleaning feature, this type of collector can very easily reach its maximum particle retention limit, which will result in a system failure. Further, for a high dust load system a great amount of dust storage is needed. Media Filtration (Baghouse) or Pleated Filtering Media (Cartridge Collectors) provide a much great surface area for dust storage than Electrostatic Precipitator systems do. However the advantages of this system are great for their intended applications. They have the ability to be extremely efficient (in excess of 99.9% in some cases), can function within vary large temperature ranges (between 700 °F and -1300°F), and can have large flow rates with minimal pressure and temperature changes. They are also very well suited for the collection of fine dust particles as well as materials like acids and tars which other system may have difficulty with.
All electrostatic Precipitators have four main components:
• A Power supply to provide the system with electricity
• An Ionizing section to negatively charge the incoming particles
• A cleaning system designed to remove collected particles from the Electrode collection plates
• A housing to enclose the Precipitator section
Within the category of Electrostatic Precipitator Collectors, there are two main types of systems:
• High Voltage Single State Precipitators (Cottrell type)
• Low Voltage Dual State Precipitators (Penny type)
High Voltage Single State Precipitators are further divided between two main designs:
Plate Precipitators are made up of several flat parallel plate collectors that are usually between 8 and 12in apart. Placed directly in the middle of each set of directly adjacent plates are a series of high voltage (40,000-70,000 volts) DC Discharge Electrodes. As the Gas stream passes through the plates it is ionized by the Discharge Electrodes and then immediately deposited unto the collection plates. The plates are then cleaned by vibrating the plates causing the debris to fall into a hopper or collection bin below. The majority of Single State Precipitators in use today are of the plate variety.
Tubular Precipitators operate in the same manner as Plate Precipitators however in a different configuration. This design uses a tubular shaped collection device with the Discharge Electrodes placed in the middle of the tube. As the Gas stream flows through the tube it is first ionized by the Discharge Electrode in the center, and then the charged particles are attracted to the inside of the positively charged tube. The cleaning mechanism can be one nearly identical to that of Plate Precipitators or it can be used as part of a Wet Static Precipitator system, wherein the sides of the Precipitator are flushed with water thereby cleaning them.
Tubular Precipitators are widely used in the mineral processing industry. They are highly valuable for use in high temperature Gas streams (boiler exhaust gas on power plants) because of their ability to adjust to the expansion and contraction of metal parts in the system. In addition this type of collector is also able to handle vapor collection, containing adhesive, “sticky”, radioactive, and extremely toxic compounds.
Low Voltage Dual Stage Precipitators contain several grounded plates about one inch from each other with another intermediate plate that also contains a charge. This system uses a much lower voltage than the High Voltage type (a 13,000-15,000 volt DC supply with intermediate supply of 7,500 compared to 40,000 to 70,000). This type of system is widely used to collect fumes and particles generated by welding, grinding or burning operations. They are also used in hooded and ducted welding machines and welding booths.
Low Voltage Dual Stage Precipitators have the advantages of being highly efficient, the possibility of a self contained washing system, and a longer service life since cleaning is only required on a monthly basis. However because maintenance requires removing the Precipitator Frames and the manual cleaning of the cleaning assemblies which are quite delicate, this type of Precipitator requires a great amount more care and caution to be used when performing maintenance.
Advantages and Disadvantages – Electrostatic Precipitators
|Have collection efficiencies in excess of 99% for all particulates, including sub-micron-sized particles||Have high initial investment costs|
|Usually collect dust by dry methods||Do not respond well to process changes such as changes in gas temperature, gas pressure, gas flow rate, gaseous or chemical composition, dust loading, particulate size distribution, or electrical conductivity of the dust|
|Have lower pressure drop and therefore lower operating costs||Have a risk of explosion when gas stream contains combustibles|
|Can operate at high temperatures (up to 1200º F) and in colder climates||Product ozone during gas ionization|
|Can remove acids and tars (sticky dust) as well as corrosive materials||Require large space for high efficiency, and even larger space for dust with low or high resistivity characteristics|
|Allow increase in collection efficiency by increasing precipitator size||Require special precautions to protect personnel from exposure to high-voltage|
|Require little power||Require highly skilled maintenance personnel|
For certain applications, Unit Collectors are a better choice for a facilities needs than a conventional Central Collection System. These collectors control contamination at their source. They benefit from low initial cost, direct return of captured material to the main material flow, and very low space requirements. These collectors are best used when the dust source is isolated, portable or changes position often. Some examples of instances where this type of collector might be useful are dust-producing operations, such as bins and silos or remote belt-conveyor transfer points.
Depending on the particular desired application is there are a number of different designs available to choose from with a capacity of 200 to 2,000 ft3/min. The two main types are:
• Fabric Collectors
• Cyclone Collectors
Unit Fabric Collectors are very similar to their bigger relatives used in a Central Collection System. They usually employ either a Mechanical Shaker, or a Pulse Jet system for cleaning. This type is well suited for the collection of fine particles such as in the mineral processing industry.
Unit Cyclone Collectors also operate on the same principles are the kind used in Central Collection Systems. Dust is collected and deposited into a hopper, which then can be removed later for cleaning. This type of collector is best used in the collection of coarse of larger particles.
Central Collection System
Every Dust Collection System must have a Central Collection System in place in order to send the contaminated air to the filtration system. A Central Collection System consists of a series of collection inlets, and the necessary duct work to transport the dust laden Gas stream to the collector and afterward on to be either recirculated back into the facility or dispersed into the atmosphere. The pressure in this duct system is supplied by the Fan and Motor System.
Fan and Motor
Choosing the right Fan and Motor System requires a number of different factors to be taken into consideration including but not limited to:
• Volume required
• Fan static pressure
• Type of material to be handled through the fan (For example, a Radial Blade Fan should be used with fibrous material or heavy dust loads, and a nonsparking construction must be used with explosive or flammable materials.)
• Limitations in space
• Acceptable levels of noise caused by the fan
• Required operational temperature (For example, sleeve bearings are suitable to 250º F; ball bearings to 550º F.)
• Adequate size to handle pressure and volume requirements with minimum horsepower usage
• Whether any corrosive materials are going to be handled and what protective coatings may be needed
• Ability of fan to accommodate small changes in total pressure while maintaining the necessary air volume
• Need for an outlet damper to control airflow during cold starts (If necessary, the damper may be interlocked with the fan for a gradual start until steady-state conditions are reached.)
Also to be considered is what type of drive system for the fan you plan to use. A Direct Drive fan is run directly off of a drive shaft from the motor, this provides for lower space needs, but places the fan at a constant unchangeable speed. While Belt Driven fan, which uses a belt to flywheel configuration needs more space, it can allow for the fan speed to be easily changed which is vital for some applications.
There are two main types of fan designs that are used in industrial applications:
• Centrifugal fans
• Axial-flow fans
A Centrifugal Fan (also called a Squirrel-cage fan for its resemblance rodent exercise devices) is a fan build with blades (or ribs) surrounding a central hub. The air enters into the side of the fan and then turns 90° and is accelerated and thrown out of the fan by means of centrifugal force. The diverging shape of the scroll also converts a portion of the velocity pressure into static pressure. The fan is driven by means of a drive shaft that extends out from the center hub of the fan.
There are three main types of Centrifugal fan blades that can be used:
• Forward Curved Blades
• Backward Curved Blades
• Straight Radial Blades
Forward Curved Bladed Fans have blades that are curved in the direction of the rotation of the fan. These fans are highly sensitive to particulate buildup and are used for high airflow, low pressure applications.
Backward Curved Bladed Fans contain blades that are positioned away from the fans rotation direction. These fans will provide an efficient operation, and can be used in Gas streams with light to medium particle concentration. While they can be fitted with wear protection, this type of blade can still become backed up if the particle load gets to be too heavy. This fan type is most often employed in medium speed, high pressure, and medium airflow applications.
Straight Radial Bladed Fans provide the best choice for heavy particle loads. This design features a series of blades that extend straight out from the center hub. This design is used for high pressure, high speed and low volume applications.
Fan dampeners are metal plates that can be adjusted to reduce the energy usage of the fan. Placed on the Outlet port of a fan, they are used to impose a flow resistance to control the Gas stream. They also can be placed on the Inlet port, which can perform the same function, as well as redirect how the Gas stream enters into the fan.
Axial Flow Fans
Axial Flow Fans have blades that are mounted unto a center drive shaft. They induce the air to move parallel to the shaft the blades are mounted on by the screw-like action of the propellers. The air is blown across the axis of the fan hence the name Axial Flow Fans. This type of fan is commonly used in systems with low resistance levels.
The three main different designs of Axial Flow Fans are:
• Tube Axial
• Vane Axial
Propeller Fans is the most simple fan design. It is used to move large an amount of air against very low static pressure from the rest of the system. General and Dilution ventilation are two common uses for this type of axial fan.
The Tube Axial design is very similar to a normal propeller type fan, except that the propeller is enclosed in an open ended cylinder. This design is more efficient than simple propeller types and is often used in moving Gas streams filled with condensable fumes or pigments.
Vane Axial Fans are nearly identical to Tube Axial Fans. But these contain specially attached vanes that are designed to straighten the Gas stream as is passes through the fan. These can produce high static pressures relative to this type of fan. However these fans are in most applications used only for clean air.
Fan Rating Table
Once all of the preceding material has been examined, the final step in the selection of the proper fan for your system is to consult a Fan Rating Table. This is used to list all of the specifications for the various fans produced by a certain manufacturer. When reviewing a Fan Rating Table one must keep these few points in mind:
• The rating tables show all of the possible pressures and speeds that can be achieved within the limits of the fan’s normal operation range.
• A fan that operates at a single or fixed speed and has a fixed blade setting will only have one possible rating. The only way to gain multiple ratings is by varying the speed and the blade setting.
• It may be possible to obtain the same fan in different construction classes
• Increasing the exhaust volume will in turn increase the static and total pressure in the system
Once a system has been installed in the field, inevitably certain differences between design and field installation will require a field test to be done to find the exact measurements of static pressure and volume. This step is crucial in order for a proper fan system to be selected. A few brief points are good to keep in mind during the installation process that can cause your real world values to change from the original design specifications:
• Elbows and bends near the fan’s discharge will increase the systems resistance thereby lowering your fan’s performance
• Make sure to install the impeller in the proper direction desired.
• Certain types of fittings such as elbows, mitered elbows and square ducts, can cause a nonuniform airflow which in turn will again lower performance
• Build up of debris in the inlets, blades, passages as well as obstructions should be checked and remedied
• In a belt driven system one must check the motor sheave and fan sheave are properly aligned and that proper belt tension is present
An Electric Motor is what supplies the power necessary to operate the fan (Blower) in the Dust Collection System. Electric Motors are usually grouped as either Induction, or Synchronous designs. Induction designs are the only ones that are used in Dust Collection Systems today.
Induction Motors normally operate on three phase AC current. The two most common types used in Dust Collection Systems are:
• Squirrel Cage Motors are generally used where a constant speed is desired
• Slip Ring Motors by contrast are general purpose or continuous rated motors that are used in applications where there is a need for an adjustable speed in the motor.
Another important design consideration is whether the Motor is one of these two enclosure designs:
• Drip Proof and Splash Proof Motor are types of Open Enclosed Motors, which use a kind of electric motor enclosure that has vents to allow airflow but to prevent liquids and solids from entering the motor. This design is not suitable for application where particles that can damage the interior of a motor are found in the ambient atmosphere around the motor.
• Totally Enclosed Motors have an exterior fan mounted unto the backside of the motor drive end. The fan blows air over the motor enclosure to provide additional cooling for the motor. Since the actual motor is totally enclosed this design provides the best protection against dust and other contaminates that might damage the motor if allowed inside.
Both Types can also be constructed in explosion and dust ignition proof models to protect against accidental ignition of dust particles.
The following factors need to be considered when choosing which motor meets your needs:
• Horsepower and RPMs
• Power supply needs such as voltage, single or three phase AC and frequency
• The environment in which the motor will have to operate (humidity, temperature, open flames or corrosive elements
• What kind of load is going to be placed on the motor (fan and other drive mechanisms) and power company restrictions on cold starts.
• Sufficient power supply for cold starts
• Overload protection needed for the particular motor
Fan & Motor Troubleshooting Chart
|Insufficient airflow, low ft3/min||Fan|
|Forward curved impeller installed backwards||Reinstall impeller|
|Fan running backwards||Change fan rotation by reversing two of the three leads on the motor|
|Impeller not centered with inlet collar(s)||Make impeller and inlet collar(s) concentric|
|Fan speed too low||Increase fan speed by installing smaller diameter pulley|
|Elbows or other obstructions restricting airflow||Redesign ductwork|
|Install turning vanes in elbow|
|Remove obstruction in ductwork|
|No straight duct at fan inlet||Install straight length of ductwork, at least 4 to 6 duct diameters long, where possible|
|Increase fan speed to overcome this pressure loss|
|Obstruction near fan outlet||Remove obstruction or redesign ductwork near fan outlet|
|Sharp elbows near fan outlet||Install a long radius elbow, if possible|
|Install turning vanes in elbow|
|Improperly designed turning vanes||Redesign turning vanes|
|Projections, dampers, or other obstructions near fan outlet||Remove all obstructions|
|Actual system more restrictive (more resistant to flow) than expected||Decrease system’s resistance by redesigning ductwork|
|Dampers closed||Open or adjust all dampers according to the design|
|Leaks in supply ducts||Repair all leaks in supply duct|
|Too much airflow, high ft3/min||Fan|
|Backward inclined impeller installed backwards (high horsepower)||Install impeller as recommended by manufacturer|
|Fan speed too fast||Reduce fan speed|
|Install larger diameter pulley on fan|
|Oversized ductwork; less resistance||Redesign ductwork or add restrictions to increase resistance|
|Access door open||Close all access and inspection doors|
|Low static pressure, high ft3/min||Fan|
|Backward inclined impeller installed backwards (high horsepower)||Install impeller as recommended by manufacturer|
|Fan speed too high||Reduce fan speed|
|Install larger diameter pulley on fan|
|System has less resistance to flow than expected||Reduce fan speed to obtain desired flow rate|
|Gas Density lower than anticipated (due to high temperature gases or high altitudes)||Calculate gas flow rate at desired operating conditions by applying appropriate correction factors for high temperature or altitude conditions|
|Low static pressure, low ft3/min||Duct System|
|Fan inlet and/or outlet conditions not same as tested||Increase fan speed|
|Install smaller diameter pulley on fan|
|High static pressure, low ft3/min||Duct System|
|Obstructions in system||Remove obstructions|
|Duct system too restricted||Redesign ductwork|
|Install larger diameter ducts|
|Backward inclined impeller installed backwards||Install impeller as recommended by manufacturer|
|Fan speed too high||Reduce fan speed|
|Install larger diameter pulley on fan|
|Oversized ductwork||Redesign ductwork|
|Access door open||Close all access/inspection doors|
|Calculated horsepower requirements based on light gas (e.g., high temperature or high altitude) but actual gas is heavy (eg.,cold startup)||Replace motor|
|Install outlet damper, which will open gradually until fan comes to its operating speed|
|Fan not operating at efficient point of rating||Redesign system|
|Fan does not operate||Electrical|
|Blown Fuses||Replace Fuses|
|Electricity turned off||Turn on Electricity|
|Wrong voltage||Check for proper voltage on fan|
|Motor too small and overload protector has broken circuit||Change motor to a larger size|
|Broken belts||Replace belts|
|Loose pulleys||Tighten or reinstall pulleys|
|Impeller touching scroll||Reinstall impeller properly|
After the Airstream has been cleaned, the dust that has been collected must be disposed of in a proper way to ensure that recontamination is avoided. In many cases where the collected material is of value, it can be returned to the product stream and reused. However this is not practical in all applications. Minimizing secondary dust problems is also a key component in an effective dust disposal system. Operations such as loading and unloading of the collected material, or the transportation of wet slurry can present further contamination problems that need to be addressed.
All Disposal Systems have to accomplish these four objectives without further contaminating the environment, in order to be effective in their role in the Dust Collection System:
• Collected material from the hopper must be removed
• Transportation to storage
• Storage of the collected material
• Treatment necessary before final disposal
Removal Of Dust From The Hopper
The hopper must be emptied of the collected dust on a regular basis to prevent overfilling. Often this process is done while the collector is still operating. If this is the case, rotary air locks, or tipping valves need to be used in order to maintain a positive air seal and thus avoid massive pressure loss that would be detrimental to the normal operation of the system. Some materials display what is called a bridging tendency, which is a tendency to stick together and form long strands that can over time build up into bridge like formations that can impede the normal operations within a hopper. If material of this kind is present in the system, special equipment such as bin vibrators, rappers, or air jets should be used to ensure that the material that has a bridging tendency does not interfere with normal operation of the hopper.
Once the dust has been removed from the collector, it must be transported to a storage area where is can be given any final treatments needed before it is disposed of. There are four main systems that can be used to transport the collected material to holding there are:
• Screw conveyers
• Air conveyers
• Air Slides
• Pressurized piping system for wet material (Slurry)
Screw conveyers use rotating shaft to move material to the desired location. These systems are very effective methods of dust transportation. However several areas of concern in this type of system are that they tend to have a noted lack of easy access for maintenance purposes, the castings and bearings can wear out easily when used with abrasive materials with air leaks being the end result.
Air Conveyers are used mainly for dry dust applications. Making use of a high velocity low air volume principle, these collectors are a great choice because of their few moving parts and their ability to move dust both vertically and horizontally. The main concerns with this system are that the piping can over time suffer from excessive wear from abrasive compounds. They also require large initial investments of capital and have higher operating costs.
Air Slides are widely used for light dust loads with nonabrasive materials. Air fluidization of the dust is the main operating principle behind this system. This system while able to transport great amounts of material has the downside of only being able to do so in a horizontal direction. Areas of concern are the need to maintain a constant down pitch in the ductwork, and greater maintenance costs.
Pressurized piping systems are needed when transporting the slurry made from using a Wet Scrubber design. This system is used to send the slurry to a settling pond for further treatment. Great care must be taken by the operators of this system to ensure that no leakage occurs which would result in an environmental hazard caused by water pollution.
Storage tanks and Silos are the most common storage locations for dry dust compounds after their collection. These sites are then fitted to allow loading of the material into enclosed trucks or rail cars below.
When using a wet collection system often times a settling pond is needed. In a settling pond the captured particles are separated by means of the process of decantation. The slurry from the Wet Scrubbers is left to sit in a large pond or basin, allowing the captured particles to over time slowly settle to the bottom of the pond; afterwards the clean water is discharged. Again certain factors to consider in the use of a settling pond are that the water holding area can only be decanted in the warmer, dryer part of the year, and in most instances two settling ponds are needed to operate efficiently.
When deciding on a final disposal method, one must remember that great care needs to exercised in order to avoid recirculation of the dust by the wind. Sometimes in because of this concern, and for easier transportation, the captured material is processed into pellets before final disposal. Generally four different options are available for the final disposal of the collected material:
• Placement in a landfill
• Byproduct utilization
• Collected material may be suitable for backfilling land fills and quarries
Selection of a Dust Collector
The differences in design, operation, efficiency, space requirement, construction, and maintenance needs, as well as the initial start up, operating, and maintenance costs differ greatly between various products and systems. However in choosing which system will meet your needs the best, the following point should be considered:
Dust concentration and Particle size – Within any kind application the specific sizes and dust concentrations can vary enormously. Therefore, knowing the exact range of particle size and concentration levels that will be present will be vital in your choosing the proper Collection System.
Degree of collection required – How intensive of a filtration action is needed is determined by several factors. The exact dangers and hazards of the contaminates to be captured, its potential as a public health risk or nuisance, site location, the allowable emission rate by the regulatory body for the given substance, characteristics of the dust, and any recyclable value.
Characteristics of the Gas stream – Differences in Gas stream temperatures and humidity levels can great affect certain types of collectors. For example Gas temperatures above 180° F (82°C) will destroy many types of filter media (Filter Bags) used in Fabric Collectors (Baghouses). Water vapor or steam can blind certain types of Filter Media. Corrosive and other chemicals can erode certain metals and other materials used in the construction of many Collectors.
Types of Dust – Certain types of Collectors have a great deal of physical contact between the particles and the Collector itself. A number of different materials such as silica or metal ore are quite abrasive and can cause erosion through prolonged contact with the Collector. Other “sticky” compounds can attach themselves to the interior surfaces of the collector and cause blockages. The size and distinct shape of some types of dust render certain collection methods useless. When certain types of materials are fluidized into the air they become highly combustible. Under these circumstances Electrostatic Precipitators are instantly ruled out, along with most Inertial Separators.
Disposal Methods – Differences in disposal methods betweens different locations. Collectors can be arranged to unload their collected matter either in a continuous mode or at a predetermined time interval. Removal of collected matter from dry systems can also result in secondary causes of dust pollution and contamination. While using a Wet Scrubber System will eliminate this concern, proper handling of slurry created during the cleaning cycle will involve an entirely different set of problems, such as precautions against water pollution, and proper care and maintenance of the retention ponds.
About the Author
| Dominick DalSanto is an Author & Environmental Technologies Expert, specializing in Dust Collection Systems. With nearly a decade of hands-on working experience in the industry, Dominick’s knowledge of the industry goes beyond a mere classroom education. He is currently serving as Online Marketing Director & Content Manager at Baghouse.com. His articles have been published not only on Baghouse.com , but also on other industry related blogs and sites. In his spare time, Dominick writes about travel and life abroad for various travel sites and blogs.
Photos or sketches for the systems described would bemore convincig.
i want to know how to get a dust discharging capacity of esp
When it comes to all things ESP (electrostatic precipitators for our readers) we are not the best people to ask, since we are Baghouse experts. I would recommend you look around on LinkedIn for a group that focused on ESP technology, and ask there.
Thanks for visiting, and commenting on our site!
i m having a final year project bout bagfilters. plz help me if i get sketches / videos of bagfilter system especially air purging system.
i shall be very thanked
what type of the machine can use to remove the dust from the filter bags of the precipitator
Im afraid I am not sure exactly what you are describing. A precipitator does not have filter bags, it has large plates that collect dust. Can you explain a little more what exactly you are looking for?
Can a pulse jet baghouse operate under positive pressure? I have being doing research and I haven´t seen any pulse jet baghouse with the fan upstream of the dust collector. Is there a reason why?
Yes, they can operate this way. These are called positive pressure systems. They are used only in special applications.The source of the pressure changes, but the effect is the same. Air moves from the dirty side to the clean side of the baghouse and out the exhaust. The pulse jets still fire against the flow of air in the unit, but this is overcome by using compressed air, usually at 70 – 80 PSI.
A big problem is that positive pressure systems require the dust-laden air to pass through the fan. This causes wear and tear on the fan, which is a very expensive piece of equipment. One type of application where positive pressure systems might be used is paper recycling. Commonly, a special fan is used that will shred the paper scraps into smaller pieces/dust and then send it on to the dust collector.
How would you configure a desiccant dryer and tank for the air supply to a baghouse? Need to dry the air before pipe goes outside
The dryer you can get the air the better. There are many different systems available to ensure a clean, and dry air supply. We usually leave that up to each plant for finding the best methods. However, we do recommend you place a water trip and drain directly on the air header tank to enable any bit of moisture left to be drained out before being used in the baghouse.
I am a patent attorney and I am trying to analyze a US patent. The patent I am looking at uses two dust collectors. Inlet and outlet valves are placed at the inlet and outlet of each dust collector. Supposedly, to clean one of the collectors, its respective valves are “completely” closed to shut off the flow of air through the collector being cleaned. However, I suspect that the valves are not completely closed off..am I incorrect???
Sounds like you might be describing a multi compartment dust collector. In such a system, a very large baghouse is split into multiple compartments internally. Then when its time to clean one the inlet and outlet to that compartment closes and thus isolates it from the pull of the fan. When its done cleaning both inlet and outlet open back up.
If you have some drawings or a fully description I can probably help you more. What exactly is the underlaying problem you are trying to solve?
Great web site. I am a process engineer trying to cope with a sticky dust situation (both metaphorically and realistic wise). The dust I am dealing with is dry at times and moist at times, depending on the different stage of the process. The baghouse solution is my preferred solution. However, implementing the baghouse solution might yield extensive operational malfunctions. To the point, what are the possibilities for dry treatment for the so-called moist (sticky) dust, considering dry applications? My main concerns are the accumulation of wastewater using a wet process. Alternatively, high frequency clogging using the bag system.
Thank you very match for your help.
Can you tell me what the process is? I need to know why it goes from moist to dry conditions.
Granulation of GTSP and SSP (fertilizers). Some of the feed is introduced to the granulator via Front-end loader straight after a curing belt, obviously the moisture content is match higher at this stage (not a stage per say, rather a different feed). Other feed hoppers are feed with dry material for various purposes.
In general, the process outlet is dry. The specifics of the process are irrelevant, since the process does not allow for change in moisture content.
The question is simple and it regards the limitations of dry application with moist or sticky dust. Without considering the specific of the process.