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If you or your company operates a baghouse part you are more than aware of the problems associated with bag replacements.

When a baghouse filter media becomes inefficient there are many cost and time expenditures involved with the process of bag replacement:
 

  • The costly purchase of new bags and cages
  • The timely and labor intensive installation of new bags and cages
  • High energy costs due to low permeability
  • Environment damage through Greenhouse Gas Effluent
  • The costly purchases of new equipment

BPS, through its innovative new product can save you money by more than doubling your bag house bags working life.

Task does not require downtime as it can be performed during operation and the labor involved is considerably less. Most importantly you or your company won't have to replace the baghouse filter media as frequently.
 

 

Baghouse Related Articles

Is Your Baghouse the Real Bottleneck?

Apr 1, 2000 12:00 PM
Andy Winston

An aggregate operation has many systems working together. When problems arise, detailed troubleshooting usually pinpoints several areas to address. So why is it that whenever there is an airflow problem, a dusting problem, or an emissions problem, the baghouse alone is blamed? Is the system's bottleneck just the baghouse part or baghouse filter bags? In most cases, the answer is no.

In most aggregate plants, the dust-collection system has five major components: collection hood(s), ductwork, dust collector (baghouse), fan, and material handling equipment. If any of these areas is poorly designed or operating inefficiently, the entire system will not perform properly. Instead of making major changes to one component (often the baghouse), the solution may be to make minor changes to several components.

Airflow through hoods It is easy to tell if a hood is not pulling sufficient airflow-because there is dust everywhere. But, a hood can pull too much dust-laden air (Figure 1). To design an efficient hood, capture velocity, face velocity and duct velocity must be understood.

* Capture velocity is the speed of air at any point in front of the hood that is necessary to overcome opposing air currents and to capture dust-laden air by causing it to flow into the hood.

* Face velocity is the speed of dust-laden air at the opening of the hood.

* Duct velocity is the speed of the dust-laden air once inside the ductwork. In order to move particulate to the dust collector, the duct velocity must be equal to or greater than the minimum air velocity required to move particles in the air stream.

The hood must generate a flow pattern and capture velocity sufficient to control dusting without collecting excessive dust. In standard material handling applications such as conveyor belt transfer, bucket elevators, air slides, vessel loading, and crushing and grinding, the goal is to de-dust the area without moving material off of the conveying equipment.

If the capture velocity is too high at the pick-up point, excessive particulate will be introduced into the ductwork and eventually to the dust collector. Inside the dust collector, the filters will collect more dust than they were designed for, leading to high dust loading. This leads to the baghouse operating at high differential pressure (DP) and requiring accelerated filter cleaning. Under these conditions, the filters wear out faster and require more cleaning energy.

One solution is to enclose the hoods as much as possible (Figure 1). Enclosing the hood keeps out air currents surrounding the hood, thus requiring less airflow to control the dust. This requires minimal costs and installation time.

Another problem is found on an airslide hood when the opening to the ductwork is too close to the airslide casing. This creates excessive duct velocity where air entersthe ductwork. This can result in a higher capture velocity.

The solution is to build an additional box on top of the casing with the same height and width of the casing. The box should have square sides and a 45degrees sloped transition into the duct. The vent point should be in the middle of the discharge points. This additional area will slow the capture velocity to capture just the dust, not the material. The ideal capture velocity for material handling applications is 200 to 550 fpm.

Once the hoods are designed and installed properly, blast gates need to be installed to achieve system balance. Due to changing airflows through the system, adjustments are needed to ensure proper capture velocity at each hood.

Dust highway The ductwork is the highway of the dust-collection system. Proper duct velocity for most rock-dust applications should be between 3,500 and 4,000 fpm. Speeds lower than 3,500 fpm could allow particulate in the airstream to fall, causing dust buildup in the duct. Speeds higher than 4,000 fpm could cause abrasion, especially in ductwork branches and elbows.

The most common design problems involve installing improperly sized ductwork. If the ductwork is too small in diameter, the result is high duct velocities. This is usually evident if the ductwork has numerous holes and weakened areas. If abrasion is present, a patch will soon be worn away and the problem will still exist.

If the ductwork is too large, the duct velocities will be too low and result in dust buildup. Dust buildup in the duct creates a maintenance problem and reduces the cross sectional area of the duct which affects overall flow and air velocities at the hood.

The most common mistake with ductwork is the addition of vent points after a system has been designed and installed (Figure 2). This is usually the hurried addition of a vent point, using whatever size duct is available and attaching it to the existing duct in the most convenient place.

Additional vent points installed without considering existing vent points will result in an imbalance of the system. Usually, this means the vent point furthest from the dust collector will not have adequate volume to de-dust its area.

Clearing the air The baghouse is where dirty air becomes clean air, where dust from the airstream is discharged into a hopper or vessel. Air velocities are a critical aspect of a properly working baghouse BPS.

The first problem area in a baghouse is inlet design. The secret to a good inlet design is to slow air speed from 3,500 to 4,000 fpm down to 2,800 fpm or slower. A good baffle system helps reduce speed. A baffle turns the air, making it go to the filters in a straight, even pattern. The baffle also knocks some of the heavier dust into the hopper before it even gets to the filters. If air speed is not reduced enough, the dust-laden air will blast into the filters, causing premature filter failure and emissions.

In most cases, it is best to slow air into the baghouse as much as possible, without causing a reduction in the duct velocity (resulting in dust buildup in the ducts) or the capture velocity (resulting in dusting at the pick-up point).

Baghouse sizing is critical to a properly operating system. The air-to-cloth (A/C) ratio is the relationship between the amount of dusty air per minute flowing through the baghouse and the total amount of filter media in the baghouse. These are general guidelines and will be different if a system has high grain loading, frequent temperature fluctuations, high moisture content or unique dust composition.

Can velocity is important for pulse-jet baghouse sizing. Can velocity is the speed of dust-laden air as it moves between the filters. Because a pulse-jet collector cleans the filters on-line (airflow is not stopped to clean the filters), a high can velocity (above 300 to 350 fpm) will not allow proper cleaning.

Each time a filter is pulsed with air, the dustcake is momentarily blown off the filter surface and falls down due to gravity. If the can velocity is too high, the dust is not allowed to fall off the filtersand into the hopper. It can also cause filter blinding as the small dust particles that are blown off during cleaning are blown back onto the filter and eventually forced into the interstices of the filter media.

High can velocity is caused when the filters are too close together or when air volume is too high within the baghouse. An effective solution is to use pleated filter elements. Pleated elements offer more media area per filter than a standard filter bag, which allows an operator to install fewer filters (spaced farther apart) or to install filters of staggered length. Either option can reduce problems resulting from can velocity.

One area often ignored on a baghouse is the cleaning system controls. In almost every application, filter cleaning based on DP is preferred over cleaning based on time intervals. This ensures that the filters are only being cleaned when necessary, thus prolonging filter life. Changing the cleaning control to be based on DP is simple and inexpensive.

BHA recommends starting to clean at 4.5 to 5 in. w.c. and stopping at 4 to 4.5 in. w.c. Cleaning only when necessary achieves more consistent DP and airflows. With high-efficiency filters such as ePTFE membrane filters or spun-bonded pleated filters, lower DP levels than this can be maintained.

The right fan The fan is the engine that supplies energy to the dust-collection system. An improperly sized fan can hinder the performance of other components (hoods, ductwork, baghouse). The fan must be sized to handle a calculated volume of air at a calculated system pressure. If the fan volume is undersized, it cannot pull the desired volume. If the fan pulls too much air, it puts unnecessary stress on the baghouse, which can lead to all types of maintenance problems.

cyclone dust collector
industrial dust collector
jet dust collector
torit dust collector
pulse jet dust collector
used dust collector
 

If the fan is not sized for the correct system pressure, it will not pull the correct volume of air. This usually occurs when existing fans are used on a new application with only the volume capacity taken into consideration.

Just speeding up a fan will not always result in more air volume. System pressure must be calculated and matched to a fan curve.

Dumping the dust At this point in the dust-collection process, the dust has been captured (hood), transported (ductwork), filtered and collected (baghouse). Now the unwanted dust must be conveyed away from the baghouse. To do this properly, screw conveyers, air slides, and air locks must be sized correctly to evacuate the hopper(s).

Once dust has been collected, it should be taken completely away from the dust-collection system. If hoppers are allowed to stay full of dust, commonly, the air stream coming into the baghouse lifts the dust and takes it back to the filters.

This creates a recirculating dust load in the baghouse which can quickly reduce the efficiency and life of the filters. Air locks at the bottom of the hopper must create a good seal. If not, dust will be reintrained into the inlet gas stream. It acts like a hood, picking up whatever dust it can.

This makes the baghouse work harder and deteriorates performance. Air locks must be installed and used as they were designed. In practical terms, do not take rotors out of rotary feeders or wire double flap valves open.

If air locks cause maintenance headaches, install ones that are sized properly. Air locks are reasonable in price and, if properly sized, can significantly reduce maintenance time.

When experiencing airflow or dusting problems, check all the components of the system first. Don't settle for a quick fix in one area. Usually, a quick fix just moves the problem to another area or puts unwanted stress on the whole system.

Understanding and using system guidelines on all components, and properly fixing the real problem areas, is the best way to create and maintain a reliable dust-collection system and to reduce maintenance costs.

 

 

Check out other articles from Baghouse Parts

 

Dust Collectors and Baghouses