Can anyone come up with a possible solution? I read this to mean they want 2 valves, one 2" or smaller and the other sized to meet the remaining CV. Any suggestions are appreciated.

Does anyone have any experience of this sort of application,things to look out for etc,Would a differnt trim help?,is it benificial to keep away from supersonic flow and what are the possible negative

I am looking for the equation for delta P across a control valve. I am looking for non-choked, compressible, turbulent flow with or without fittings attached. I have the equation to solve for C, but

Can some one provide the standard/Spec which specifies Fugitive Emmission Test Requirement and Test Method?

When describing allowable leakage, the standard refers to ".01% of rated valve capacity". Rated valve capacity is defined as "the quantity of test fluid that would pass through the valve at rated trav

Is there any relationship between trim no. specified in API 600 and leakage rate specified by DIN 3230-3 or any other standards in a globe or gate valve?

I am wanting to use globe valves for throttling flow in a marine cooling system application instead of an orifice.

I have been advised that the placement of the equalization tube (pipe) must be directed from the top of the valve to the high pressure side of the valve.