Pneumatic conveying ATEX safety

Good practices to ensure the safety of pneumatic transport systems against dust explosions

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Section summary
Introduction
Prevention
Explosion resistant construction
Explosion vents
Inerting

Bulk Solids Handling Safety
# Dust explosion physical properties # MIT - Minimum Ignition Temperature of dust # Dust explosion venting
# Dust explosion isolation

1. Introduction

Pneumatic conveying systems are generally safe systems compared to other ways of conveying bulk solids. It remains however a system conveying very often fine solids that can explode, it must therefore be the object of a certain number of explosion prevention measures, and in some cases of explosion mitigation.

2. Prevention

Pneumatic conveying are quite favorable to explosion prevention. It is a closed system, without moving parts in the flow of product. However, the following measures must be implemented to ensure its safety :

- The system must be well maintained to avoid any leakage of product that could create an ATEX zone outside of the conveying pipe

- The whole conveying line must be grounded, included the filter in the receiver, to avoid any electrostatics spark from an isolated conductive part

- If flexible are used, they should be designed and install in a such a way that they cannot trigger propagating brush discharges.

Pneumatic conveying is indeed creating a lot of static electricity because of the movement of the product in the pipe, it is important to consider these different potential ignition sources in the risk analsys.

4. Explosion vent for cone discharge risks

As mentionned, the movement of the product in the conveying pipe is creating static electricity charges at the surface of the equipment, but also on the product itself. After transport, if the material is not conductive enough, those charges may build up and suddenly flow from the product to the hopper wall, triggering a cone discharge spark which can be enough to ignite the cloud of product in the free space of the hopper.

It is possible to calculate the size of the hopper on which a risk will be present. If the silo has a diameter bigger than the calculated value, the risk exist.

In design phase, it is then recommended to reduce the diameter of the silo. In case the size is still close to the calculated limit diameter, then it is advised to protect the hopper or silo against explosion.

Such protection has generally the following equipment :

- Explosion vent on the receiving hopper, properly sized

- Quick acting valve on the feed pipe, if there is a risk of propagation to other equipment

- If necessary, Ventex valve on clean air pipe and airlock rotary valve flame proof at the hopper outlet.

5. Inerting

Another possibility to manage the risk of explosion is the prevent it through inerting. The oxygene level is kept below the low explosivity limit so that, in case of malfunction leading to a source of ignition, the explosion cannot happen due to a lack of oxygen, the comburant.

Such strategy requires a closed loop for the gas in the installation, in order to be able to keep the level of oxygen low while reducing the consumption of nitrogen. The system must be equipped with analysers to control the system by injecting nitrogen when necessary, or, even more importantly, shutting down the system the oxygen levels are too high. The system must also have a way to release an excess of gas if necessary through a balance line to keep the pressure in the system under control.


A pneumatic conveying system must be the object of a dust explosion risk analysis to identify the sources of ignitions and define the right prevention and mitigation measures. Conclusions of the risks analysis must be implemented by the factory.





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