moltenmetal
Chemical
- Jun 5, 2003
- 5,504
In case this topic interests you, here's a reference to an excellent paper on the subject. Regrettably it's in AIChE's Chemical Engineering Progress, so it's not public content- but if you use needle-type globe valves as control valves or manual flow regulation valves for liquids, you'll want a copy of this paper for sure. Most places which use a lot of these, particularly Badger Research Control Valves or Fisher Baumann 51000s or similar valves, have a drawer or box full of expensive replacement trimsets from valves which were mis-sized on the assumption that flow in the trim was turbulent, or because they used the garbage viscosity correction factors published by some vendors or relied on the vendor's sizing entirely. In our experience, even the most reputable vendors get this wrong, sometimes by a factor of ten in Cv or more.