macmet
Materials
- Jul 18, 2005
- 863
I am trying to compare the pressure drops of two valves in one line. The line is the cold water return to a hot water boiler.
The two valves are as follows,
#1 -> 6" globe. Cv = 440.
#2 -> 8" globe. Kvs = 765.
But, I found a conversion of "K" to Cv, which converts to a Cv of ~70. So valve #2 becomes,
#2 -> 8". Cv = 70.
This shows a significantly higher pressure drop in the 6" valve (IMO). I expected a higher pressure drop, but not one of that magnitude.
So, my questions are,
Is my opinion, that this is a significantly larger pressure drop, fair or reasonable?
And, I seem to recall that Cv values are unitless, in which case, shouldn't the Kvs be unitless? The spec sheet says Kvs is measured in m3/hr.
The conversion factor I used converted "K" to Cv, not "Kv" to "Cv". Is this the same thing or do I need a completely different conversion equation?
Thanks for the help.
The two valves are as follows,
#1 -> 6" globe. Cv = 440.
#2 -> 8" globe. Kvs = 765.
But, I found a conversion of "K" to Cv, which converts to a Cv of ~70. So valve #2 becomes,
#2 -> 8". Cv = 70.
This shows a significantly higher pressure drop in the 6" valve (IMO). I expected a higher pressure drop, but not one of that magnitude.
So, my questions are,
Is my opinion, that this is a significantly larger pressure drop, fair or reasonable?
And, I seem to recall that Cv values are unitless, in which case, shouldn't the Kvs be unitless? The spec sheet says Kvs is measured in m3/hr.
The conversion factor I used converted "K" to Cv, not "Kv" to "Cv". Is this the same thing or do I need a completely different conversion equation?
Thanks for the help.