MEX-3.2 dynamic explosion pressure detector

MEX-3.2 dynamic explosion pressure detector
Donat Czapski

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MEX-3.2 dynamic explosion pressure detector

The dynamic pressure sensor MEX 3.2 detects a dangerous pressure increase (incipient explosion) and sends a signal when preset critical values are exceeded to the control center of the explosion protection system. This component of the explosion suppression system is installed on apparatus, devices, tanks, ducts, and pipes. It detects incipient explosions for dust classes ST1–ST3, as well as gases and hybrid mixtures.

MEX-3.2 dynamic explosion pressure detector

Unique features:

 Dynamic detection of the rate of pressure increase, distinguishing an explosion from normal pressure changes occurring during the process. 

 Redundant pressure sensors ensure continuous monitoring of the protected device. 

 Three independent algorithms analyze pressure changes, providing excellent resistance to false alarms. 

Data from dynamic pressure increase sensor of the MEX3.2HT type

The dynamic pressure rise indicator MEX 3.2 is equipped with advanced software that allows for graphical presentation and analysis of collected data on pressure changes in the protected device over time. The built-in event history memory records pressure data before, during, and after the activation of the explosion protection system, facilitating the analysis of the causes of the incipient explosion. Importantly, the sensor has a programmable preliminary alarm that can be triggered in case of pressure problems in the process, indicating an increased risk of explosion.

Specifications:

  • The MEX series dynamic explosion pressure detector can sense an extreme pressure increase (incipient to an explosion) and output the detection trigger to an explosion suppression control unit when the dynamic explosion pressure threshold is exceeded;
  • Features two ceramic pressure sensors and (optionally) a temperature sensor;
  • Operated with an innovative assessment and qualification logic to identify the explosion pressure;
  • Can be interfaced with various control unit types via the FAB-3.2 terminal box;
  • MEX-3.2 pressure measurement range: 0 – 2 (4) bar abs., process temperature: 0°C to +160°C, ambient temperature: -20°C to +125°C;
  • FAB-3.2 terminal box: max. power input 1.5 W, -20°C to +55°C of ambient temperature;
  • Approved Ex-zones of use: Zone 22, 21, 2, and 1 outside the protected equipment; Zone  22, 21, 20, 2, 1, and 0 inside the protected equipment;
  • Protection type: II ½ D T 65oC IP 68, II 1G EEx ia IIC T1-T6;
  • ATEX-compliant design.
MEX-3.2 dynamic explosion pressure detector

3 design variants:

MEX 3.2
Dynamic pressure sensor adapted to detect pressure changes alone.
MEX 3.2. T
Dynamic pressure sensor adapted to detect changes in pressure and temperature.
MEX 3.2 HT
Dynamic pressure sensor designed for operation under challenging conditions due to the high ambient working temperature. Detects pressure changes.

Model approach to explosive safety in an industrial plant

Model approach to explosive safety in an industrial plant

Step 1
ATEX Audit

During the ATEX Audit, we will focus on deficiencies in explosive safety and indicate tasks that should be performed first to have the strongest impact on safety improvement.

Model approach to explosive safety in an industrial plant

Step 2
Protection Concept

The result of the ATEX Audit is also a preliminary concept of protecting the installation from explosion. It allows estimating the costs of protections. After testing the explosiveness parameters of the dust from the installation, we move on to the final concept and design.

Model approach to explosive safety in an industrial plant

Step 3
Design and selection of protections

After accepting the concept and testing the explosiveness parameters of the dust from the installation, we proceed to the final selection of explosion protections and create a design that takes into account all required changes in production.

Model approach to explosive safety in an industrial plant

Step 4
“Turnkey” delivery and installation

We coordinate the entire delivery and installation process of protections. We have our own service teams with experience in performing installation without the need to stop the investor’s plant operation.

Model approach to explosive safety in an industrial plant

Step 5
Execution of ERA and EPD

We conduct a post-implementation Explosion Risk Assessment (ERA) and prepare (or update) the Explosion Protection Document (EPD). We usually also conduct training for the crew in the field of explosive safety.

Secure your industrial plant

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