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ian_the_ex_medic  
#1 Posted : 20 October 2015 09:14:58(UTC)
Rank: Forum user
ian_the_ex_medic

Hi All, I'm looking for some help, or rather reassurance. Despite 20 years O&G experience I'm about to become involved in a major shut down. I have bucket loads of commissioning and pre-commissioning experience (my background is mostly O&G construction orientated) and I'm confident I've got my bases covered BUT there are always elements of self doubt that creep in, and I'm probably over thinking it but a sensible option would be to throw it out to the wider HS community. I'm looking for reading material / website suggestions on the subject. I've done some googling this morning but have not turned up anything particularly useful beyond the usual preparation and planning philosophy. I'm on top the HAZID - HAZOP processes, so I suppose really what I'm looking for is some background reading that will jog my brain if I've missed anything. Thoughts, suggestions etc all welcome. Thanks in advance Ian
imwaldra  
#2 Posted : 20 October 2015 10:17:16(UTC)
Rank: Super forum user
imwaldra

A key issue is how the process equipment will be 'hazard-freed' as it is shutdown. Obviously the Hazids/RAs will state this is done, but in my experience significant hazards (typically locked-in pressure) can remain unless the process to do this is VERY well planned and managed. Problems that I've experienced include: - Copying the same action list as for the last major shutdown some time ago, but not realising there is some subtle difference in the subsequent task lists, or a small modification, that should be taken into account and thus the valving sequence should be different this time. - Organisational pressures to begin the planned shutdown tasks that are on the critical path, resulting in shift handover miscommunications during the hazard-freeing phase. The shutting down preparation plan should include marking up P&IDs (e.g. with highlighter) to show how the hazard-freeing is progressing, and to help ensure no small sections are missed. - If pressure is accidentally 'locked-in' to a small section of equipment that isn't on the critical path, then by the time it's opened up some days later 'everyone knows' that there's no residual pressurised fluids, so the normal checks by permit issuer and receivers seem pointless and aren't carried out conscientiously. - Lots of time pressure towards the planned end date, so making up broken HP joints is done with less checking than required. Using a tag that names those who do this task for each joint helps to ensure no short cuts. - If the schedule goes awry, long working hours by lots of key people, and thus a greater likelihood of errors of both omission and commission. Senior management need to set a good example, including telling someone to take a real rest, if that's needed. Hope these experiences help, and that all goes well.
Alfasev  
#3 Posted : 20 October 2015 10:26:39(UTC)
Rank: Super forum user
Alfasev

ian_the_ex_medic  
#4 Posted : 20 October 2015 15:11:55(UTC)
Rank: Forum user
ian_the_ex_medic

Many Thanks Both - Useful Stuff Alfasev unfortunately the second of your two links is broken and only leads to a page not found error ? Thanks again though for taking the effort to reply. Cheers
Alfasev  
#5 Posted : 21 October 2015 09:04:50(UTC)
Rank: Super forum user
Alfasev

The second link is was to a presentation about SEISOKKI project, try http://webcache.googleus...en&ct=clnk&gl=uk
ian_the_ex_medic  
#6 Posted : 21 October 2015 09:11:20(UTC)
Rank: Forum user
ian_the_ex_medic

Many Thanks, that link good. Thanks again
neil88  
#7 Posted : 21 October 2015 10:31:51(UTC)
Rank: Forum user
neil88

Additionally, get the best PTW coordinator you can find during this hectic time.
andybz  
#8 Posted : 21 October 2015 12:56:43(UTC)
Rank: Super forum user
andybz

You may find HSG253 Safe Isolation of Plant and Equipment useful. Download from http://www.hse.gov.uk/pubns/priced/hsg253.pdf
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