
Technical article
Fire and dust explosion risk
SAFETY AND EXPLOSION RISK
The five factors of the pentagon and how to control them in the plant
The fine dust generated by blasting, machining, grinding, grain handling or woodworking can, under certain conditions, burn or even explode. Far from being a risk exclusive to very specific plants, it is present across much of everyday industrial activity. Accidents usually originate in operating and preventive-maintenance oversights, and a “routine” incident can carry high economic consequences and put operators at risk. This article explains when there is a fire or explosion risk, how its severity is measured and what measures prevent it, whatever the process generating the dust.
How a dust explosion occurs
For a dust explosion to occur, five conditions must be met simultaneously. This is what the “explosion pentagon” represents: removing just one of its elements is enough to prevent the explosion (though not necessarily the fire).
• Combustible dust, in particles fine enough to propagate the flame.
• Dispersion: the dust must be suspended in air forming a cloud.
• Concentration within the material's explosive range.
• An ignition source with enough energy (spark, flame, hot surface, static discharge).
• Confinement in a closed enclosure (equipment, ducts, building) and the presence of oxygen.
The difference from a fire is speed: in a dust cloud, combustion spreads from one particle to the next at high velocity, generating a pressure wave.
Fine particles: why size matters
Not all dust is equally dangerous. The risk rises sharply with the finest fractions.
• Particles larger than 500 µm generally present a low combustion risk.
• Processes usually produce a mix of coarse and fine material (below 420 µm): the fines ignite easily and, in doing so, also ignite the coarser particles.
• Changes in the process —speed, alloy, lubricant or abrasive— can generate finer particles and raise the risk, which makes it necessary to reassess explosivity.
• The accumulation of fine dust can cause secondary explosions: a first deflagration lifts the dust deposited in the area and, when it ignites, produces subsequent explosions that are usually more destructive than the initial one.
Kst index: how severe an explosion would be
The Kst index quantifies the potential violence of a dust explosion in an enclosed space. It is expressed in bar·m/s and represents the maximum rate of pressure rise during a deflagration: the higher the Kst, the faster the pressure rises and the greater the potential structural damage.
It is determined by a standardised test (ASTM E1226) in a 20-litre sphere, measuring the maximum pressure and the maximum rate of pressure rise, as Kst = (dP/dt)max · V^(1/3).
It is key to understand what it measures: the Kst indicates the severity of the explosion, not whether the dust can ignite.
| Classification | Kst range (bar·m/s) | Risk level |
|---|---|---|
| ST 0 | 0 | Non-explosive |
| ST 1 | 1–200 | Low explosivity |
| ST 2 | 201–300 | Medium explosivity |
| ST 3 | > 300 | High explosivity |
Explosivity of the most common industrial dusts
The following table compares the behavior of the most frequent dusts and abrasives in industry. It allows anticipating the risk level according to the material processed.
| Origin | Material / Abrasive | Kst (bar·m/s) | Class | Notes |
|---|---|---|---|---|
| Metálico | Aluminium | 400–600 | ST 3 | Highly explosive; critical risk as fine dust |
| Metallic | Iron and carbon steel | 80–200 | ST 1 | Can act as an oxidiser with Al (thermite risk) |
| Metallic | Stainless steel (fine dust) | 1–50 | ST 1 | Combustible as fine suspension; safe against thermite |
| Glass | Glass bead | 0 | ST 0 | Inert; respiratory risk if fractured |
| Metallic mineral | Copper slag | 0 | ST 0 | Generally inert; check for metallic traces |
| Mineral | Aluminium oxide (Al₂O₃) | 0 | ST 0 | Inert to explosion; main risk is inhalation |
| Mineral | Garnet | 0 | ST 0 | Inert; safe alternative to silica sand |
| Mineral | Silica sand | 0 | ST 0 | Non-explosive, but high silicosis risk |
| Organic | Flour, sugar, grain, wood | 60–300 | ST 1–ST 2 | Explosive as fine suspension (food industry) |
Note: reference values; they depend on the composition, particle size and moisture of each dust. For any installation, testing real samples per ASTM E1226 is recommended. Even everyday dusts —flour, sugar, wood— can be explosive in suspension.
Ignition sources and how to reduce them
Controlling ignition sources is one of the two variables that can be worked on daily (the other is dust concentration). They are grouped by origin.
| Origin | Source | How to reduce it |
|---|---|---|
| Electrical | Static charge | Use antistatic filter cartridges and ensure system earthing |
| Electrical | Electric shock / arc | Earth all equipment: collector, ducts, drums and metal structures |
| Thermal | Hot surfaces, welding, grinding, cigarettes | Ban hot work near the equipment without a permit (safe-work procedure); first remove all dust |
| Chemical | Decomposition, polymerisation, self-heating | Control dust storage, avoid prolonged accumulation and verify material compatibility |
| Mechanical | Friction, impact or fracture of hard materials | Do not strike the hopper or collector interior with metal tools; use anti-spark tools |
Prevention and safe dust capture
Prevention rests on reducing the available dust and eliminating ignition sources.
• Minimize the generation and dispersion of combustible dust and prevent its accumulation on floors, ducts, hoppers and structures (focus on secondary explosions).
• Keep extraction systems operational: they capture the potentially explosive fine particles at the source.
• Ensure grounding of equipment, collectors and drums to dissipate static.
• Clean without raising dust clouds: by vacuum or direct collection, never with compressed air; use natural-fiber brushes and anti-spark tools.
• Discharge the dust into grounded metal containers and empty them daily.
• Apply lockout/tagout (LOTO) before opening or servicing the equipment, and manage a hot-work permit before welding or cutting.
The choice between a dry and a wet collector depends on the dust's degree of explosivity, the location and the costs; combustible metal dusts usually steer the decision toward the wet scrubber. With combustible organic dusts —grain, flour, wood— capture is handled dry, but the collector must be protected with deflagration venting and explosion isolation.
Technical conclusion
The risk depends on the dust, not on the process
The risk level is defined by the material, not the machine. In blasting with coarse mineral or metal abrasives the explosion risk is low; by contrast, fine metal dusts, organic dusts —grain, flour, wood, food— and some plastics call for specific measures. In addition, the fine dust generated by wear, removed paint or contaminants can change the explosive behavior of any process, and material changes or the addition of lubricants can alter the effective Kst of the accumulated dust.
That is why it is advisable to prevent the accumulation of fine dust, keep the extraction always operational and test real samples whenever there are doubts about the dust composition.
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