Kkula
Hey I have a question regarding how to arrive the SIL / PF level to use.
When i look in the Safety Evalution Tool there is a help that talks about missing arm or death.
But if there is Atex Zon 1 in a gas plant.
Exemple:
I have a on/off valve and apressure transmitter that is controlled by a PLC
First, the operator shall attach a bottle to the facility
Then the operator use a HMI to start the automatic filling.
open the valve control system
if the pressure increases, so everything is ok
if the pressure drops, it is a leak, the valve will close
What is the risk here?
Is there any need of safety I/O?
Do the pressure transmitter need to be safety?
Determining the appropriate Safety Integrity Level (SIL) or Performance Factor (PF) requires a thorough risk assessment. The Safety Evaluation Tool's guidance on "missing arm or death" is a starting point, but needs context.
Your scenario involves a gas plant with an ATEX Zone 1 classification, a filling process controlled by a PLC, an on/off valve, and a pressure transmitter. The primary risk is a gas leak due to valve failure or pressure transmitter malfunction. This could lead to a flammable atmosphere and potential ignition.
Given the ATEX Zone 1 environment, a risk assessment should likely lead to a SIL 2 or 3 requirement (or equivalent PF level). Here's a breakdown of considerations:
For detailed guidance and tools:
Disclaimer: This information is for general guidance only. A formal risk assessment performed by qualified personnel is essential to determine the appropriate SIL/PF level for your specific application.
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