I've come across various examples of calculating the steam loss, with the most common being: Steam Loss (lb/hr) = 24.24 * Orifice Diameter^2 * PSIA

However, I recently saw a P&ID which showed the flow control valve in the condensate line, but with the flow element still in the steam line. I suppose this has the advantage of making the valve small

How do I make a closed cell foam (rigid) to use as a float to operate a level control valve (diesel fuel) ?

There's a problem is this, the compressor in the link comes with a manual drain tap / plug (underneath) which must be opened every 24hrs to drain condensate from the tank.

I am pondering the consequence of oversizing a steam trap. I can understand why an undersized steam trap would be problematic, i.e. backing condensate into your steam header. But what would an oversiz