To specify a block valve for a pipeline you need to specify:
- Fluid (you said air)
- Pipeline material (maybe the DIN spec is specific)
- Pipe size (you didn't say)
- Pressure (10-13 bar)
- Temperature (you didn't say)
- Volume flow rate (you didn't say)
For someone to suggest "use a butterfly valve" (or a gate valve, or a plug valve, or a globe valve, or even a ball valve) without all of this information is pretty irresponsible.
There are many situations where a butterfly valve is the best choice. I've never seen a "pipeline" that was one of those situations. Inside pipelines you accumulate compressor oil, condensed liquid, pipe scale, and corrosion products. Eventually every pipeline will accumulate this crap to the point where pressure drop becomes a problem and the operator considers pigging the line. With butterfly isolation valves located periodically through the line, you can't pig it and in a rational world the designer should be in serious trouble (in the real world he has changed jobs 4 times before his stupidity comes to light).
If the flow is really high velocity then the plate of a butterfly valve protruding into the stream will create Von Karmaan Vortex Streets that exert a very large force on the bluff body (plate) and can set up vibrations that have destroyed plates.
Please provide enough information to allow a rational discussion.
David Simpson, PE
MuleShoe Engineering
Please see FAQ731-376 for tips on how to make the best use of Eng-Tips Fora.
The harder I work, the luckier I seem