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Thermal Relief Spacing

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PMarinshaw

Mechanical
Jun 19, 2002
47
Does anyone know of an existing "rule of thumb" for spacing thermal reliefs in a pipeline (every 1000' etc.) due to solar radiation? I know there are many variables to consider such as pipe size, product contained, elevation changes, where in the world the pipeline is, P&T, etc. I'm not looking rer anything scientific.
 
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You must be able to relieve the expanded volume. Spacing is therefore a function of expanded volume, which is a function of blocked-in volume and temperature change. Normal practice as I know it is to calculate the volume that can be blocked-in, such as volume actually between adjacent block valves, calculate the expanded volume at the high temperature and the time to raise to that temperature, then size the valve for [Δ]V/[Δ]t.

Trying to size multiple relief valves in any one blocked-in segment spaced a certain distance apart has the potential to complicate the problem considerably, as it becomes a problem with possible multiple flow paths being set up within the same pipe, even if you don't consider elevation differences between relief points, or a nonuniformtemperature distribution along the pipe segment.

What would you be doing, if you knew that you could not fail?
 
What is the product in the pipeline?
 
Old thread with info

For liquid that could not vaporize given the conditions and would not flash when relieved, we considered 250 liters as the maximum blocked-in liquid volume in pipes exposed to sunlight before installing a thermal relief valve
We had a liquid expansion coefficient limit to exclude some liquids from that, but I can't find it right now.
 
That won't get you very far with a 36" pipe.

What would you be doing, if you knew that you could not fail?
 
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