How to optimize my dust collection system?

Are you planning to modernize, extend or create an industrial dust collection system? Before you start, it is important to ask yourself all the questions you need to know in order to obtain the desired results.

Before adding up the necessary flow rates for each of your machines, it is important to define the operating times, the hours of use and the flexibility of the machines. The simultaneous use of each production line is an essential value for the design of the dust collection network.

Also, the products treated in dust collection require specific designs: granulometry, density, etc. When dedusting carpentry, flour mills or chemical production sites with the possibility of gas, the choice of material is essential.

The fine particles are collected in the filter box, which itself is discharged either into a skip, a big bag, a drum or a bucket. For fly ash installations, Palamatic offers specific FlowMatic® 02 Ashflow bulk bag stations to maintain the optimal containment level. When discharging into a skip, bottom screws are necessary to distribute the product in the recovery skip.  As dust collection fines have several destinations (recycling, incineration, reintroduction), it is important to define your needs.

The product being collected and transferred has a direct impact on the filtration technology.  The air velocities at the collection point, the air velocities in the dust collection ducts, as well as the rising air velocities in the dust collection box must be calculated according to the granulometry and density of the products being vacuumed. 

The concentration of the fines to be vacuumed must be carefully considered as well as the temperature and humidity. 

If the speed is too low, this will lead to poor collection, a large deposit in the pipes and a non-optimal use of the filters. On the other hand, too high air velocities lead to loss of product at the collection point, a risk of wear and tear on the pipes and control valves due to abrasion and clogging of the filters in the upper part. The reference velocities at the collection point are between 2 and 3 ft/s and 82 ft/s in the pipes.

The explosive nature of your powders is a major point in the definition of the material to be installed. The KST, the EMI, the Pmax of your products must be known for the calculation of the explosion vents and the mechanical resistances of the dust collector box. (Cf HAZLOC at Palamatic).

The filters installed in the dust collector box can be either cartridges or pockets. The choice between cartridges and pockets depends on the products you are treating and the space available. Pleated cartridges are compact but more complex to unclog. Pockets are simple to declogging by counter-current but take up more space. In the same way, the filtration qualities vary according to the granulometria treated.
 

Your dust collection system must be designed to avoid any product deposits in the piping system and minimize pressure drops as much as possible. Network pressure drops lead to the installation of fans with high suction power (depression) which are energy consuming. The more your network is optimized, the more your energy consumption is preserved.

In order to have a so-called "balanced" network, it is important to provide damper valves to adjust the suction flows at the various collection points and also to close these suction points when the machine is not working. These suction cuts must not lead to "overpowering" of the suction at the other operating points. This overpowered suction would result in loss of product or even a process malfunction. These flow control valves are essential for the correct operation of the line and their automation is often necessary to avoid any manual adjustment due to excessive handling by the line operators.

The choice of materials used must be studied according to your product and your hygienic requirements. Stainless steel piping can be considered in food processing and/or humid environments. Galvanized or painted versions can also be used outdoors thanks to C4 type paints.

The quantity of air to be treated depends on machine requirements and the type of collection points.

An extractor hood, a bag dump station, a conditioner or a silo must appear in your need for utility. For example, a flow rate of 88 CFM may be necessary for a big bag conditioner and 470 to 706 CFM for a manual sack tip tray. When you wish to dust a trap door or any type of opening, it is important to calculate the section inft² and to make a balance.

A fine calculation must be made in order not to underestimate the flow rate which would lead to an unconvincing result. Or, conversely, too high a flow rate would lead to a loss of product but also a large volume of air regenerated, which could quickly become expensive when your building air is treated, conditioned or even dried out!

To summarize the above principles, size your flow rates according to the surface area of the openings to be dusted.

• Surface area to be dusted in ft² x 2 and 3 ft/s
• Air velocity in the pipes 82 ft/s
• Control valve (damper) on each of the inlets
• Required fan depression = pressure drop due to the mains (according to the chart) + pressure drop generated by the filters in operation.
• Necessary filtering surface according to the selected technology (cartridge / pocket) with a respective ratio of 50 and 125 according to the total suction flow.

Pneumatic counter-current cleaning is currently the most effective way of using mechanical vibration solutions. Cleaning pressures are generally around 6 bars. Cleaning ramps are installed in the clean filter housing to come intermittently to clean the filters by "brutal" air injection. The sequence, the cleaning interval, is controlled by a sequencer or by a pressure sensor called Delta P. The Delta P pressure sensor detects the level of clogging of the filters by taking the differential pressure between the clean and the dirty housing. When the threshold is reached, a cleaning sequence is sent.

In case of toxic dust, a second filtration stage must be considered with absolute filtration. In addition to absolute filtration, a so-called tribo probe can be installed to detect particles in the clean air exhaust and thus stop the installation for repair.

For HAZLOC installations, an explosion vent, a flashback arrestor or quick-closing valves as well as the channeling of the fan outlets must be installed. A point of caution is to be noted for the positioning of the vents and the installation of relief ducts which may be useful in some cases.

When setting up a centralized network, it is often interesting to consider setting up a "broom" suction network. Specific outlets with manual and flexible valves should be provided at the beginning of the design. Pneumatic booster valves may be necessary if your hoses are particularly long.

When installing your dust collection network, it is important to adjust all the flow rates at the various collection points using a flow meter. The adjustment must be carried out by a specialist and all dampers must be locked in position.

For the regular maintenance of your network, the filtering quality of your cartridges must be checked periodically to ensure good performance and also to make sure that no cartridge is pierced. The delta P sensors are precious organs to define the state of your cartridges. Similarly, the vent sensors inform you in case of an explosion in your casings. Any vent rupture is reported to your PLC for shutdown and complete control of the installation.

When air is reintroduced into your building, the controls must be programmed on a periodic and mandatory basis.

Contact our experts in industrial processes dealing with powders to define your dust removal network as well as possible.