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02-09-2010, 01:01 AM #1
Pipe insulation breakdown large NH3 plant
Has anyone out there have information or articles on heat load imposed on refrig plant due to deteriorated lagging .
Client trying to justify replacement of lagging ( old polystyrene type ) to management .
System has -40 C & -10 C liquid overfeed system with long piperuns in ceiling & outside ( -40 outside ) .
System is installed in tropical climate which is my immiediate concern.
Thanks in advance
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02-09-2010, 11:45 AM #2
Re: Pipe insulation breakdown large NH3 plant
I can't offer any advice on calculating the heat load imposed by bad insulation but there may well be a regulatory cost associated with it.
Take a look at some OSHA citations on the matter at: http://taocompliance.com/news/?p=30
You may be able to justify it as a cost-avoidance issue.
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02-09-2010, 02:53 PM #3
Re: Pipe insulation breakdown large NH3 plant
Try this program to calculate heat gain. http://www.pipeinsulation.org/. Failed or wet polystyrene can probably be calculated as 0 insulation. The larger risk is a major leak when (not if .. when) there is a pipe failure from corrosion.
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02-09-2010, 04:01 PM #4
Re: Pipe insulation breakdown large NH3 plant
And if the insulation gets liquid water or vapor water from atmosphere it will condense and solidify expanding because of the "hydrogen bridges" and ....bumm...
To make progress is never good enough, I want to do better and better and better
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