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Functional Safety Play Book

154 members • Free

3 contributions to Functional Safety Play Book
Mission Time
Hi all, thanks for accepting. First of all, I am new in functional safety and sorry for my bad english😊. Actually I have some doubt about one of variable in PFDavg calculation namely mission time, couple of question to all: 1. What will happen in the end of mission time?should end user decommissioned the plant?or just replace everything and the mission time will get restarted? 2. If it depend on end user, than based on what consideration usually for them to determine the correct mission time?and what is the reason behind that? 3. Since by the time PFDavg will get derated, and SIL claimed may decreased over the time, shouldn't end user decide to set the mission time before the SIL/RRF drops beyond the rating it should be? Hope you guys can share your knowledge. Thanks,
0 likes • 4d
This is a great question, and I've been also searching for the best answer for a long time. It directly addresses the practical aspects of functional safety, the one that the end user of the SIS system faces. Mission time is always a parameter that must align with the expectations of the installation owner and their safety management policy. If you ask them, you will find that similar issues occur in other areas of the facility—after all, other components like mechanical devices, pipelines, etc. also wear out and need to be replaced after some time. Let me give you an example from my country: currently, refineries are striving to extend the time between shutdowns to 4–5 years. As a result, most Proof Tests must also be carried out within such a time interval. Therefore, in the SRS we usually set the Mission Time to 16 or 20 years, which corresponds to 4 full production cycles. These are the values I use for my PFDavg calculations in most cases.
Hi All - Systems that pre date 61508
Hi all thanks for the add, this looks like a really good way to share experience in the functional safety world. Thanks for setting up Richard. I have a question for you all on the requirements when adding a new SIF to an existing SIL2 system that was designed over 40 years ago and was never designed to 61508. What things would we consider to make this possible without a full system redesign.
1 like • 4d
@Tom Atkinson From my experience such plants don't have also hazard identification like HAZOP done, or it was done very long time ago. They have a lack of up to date SIF documentation, etc. The best solution here is to prepare and conduct a functional safety audit which will show the best way and will force the company to prepare an appropriate plan of next actions like: fresh HAZOP study or update existing, SIF list update, SIL requirements determination and partially SRS preparation. Many things changed at site since this old SIS was implemented in most cases. Having this set of data is a great background to making a decision - what we will do with old system - new, modernization, partial modernization? This is path I proposed many times and it's working.
Hello
Greetings to all members of this community, both experienced and beginners. I'm glad to join it. I'll try to contribute as much as I can. I've used LinekdIn a lot over the past few years, but lately it's become quite irritating. A warning to those seeking reliable knowledge. LI is currently publishing a ton of posts about functional safety, written by people who have no clue about it. They're generated by AI and contain basic errors. That's why I'm glad to see new initiatives like this community emerging! I'm curious if you feel the same way?
1-3 of 3
Tomasz Barnert
1
2points to level up
@tomasz-barnert-4011
Head of process & functional safety department, CFSE, PhD

Active 21h ago
Joined Mar 11, 2026
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