For my education can someone clarify whether it is acceptable to use a 200 bar manifold or valve on HP steel tanks? As I do the math, 200 bar x 14.7 psi = 2940 psi. Therefore this sounds like it is going to be exceeded by the 3500psi fill on HP steel tanks. While I imagine that the manifold/valve is tough enough to handle the extra pressure, what about the burst disk? Is the burst disk on a 200 bar manifold/valve set to burst at a pressure lower than 3500 psi?
Not sure to what extent this is covered in the library docs on the DRE website...
But you really need to differentiate nomenclature.... and yes - to anyone nitpicking - I'm generalizing....
HP typically refers to older high pressure steel tanks rated to 3500psi. These tanks will have a 300 bar din valve outfitted and have a 7/8ths neck threads.
LP typically refers to low pressure steel tanks, rated to 2400/2640psi w/ the 10% overfill. These tanks will have the 200 or 232 convertable valve, and have a 3/4ths neck.
Along came PST (and followed by worthington, faber, etc....) and they decided to introduce tanks rated to 3442, or 232bar, which was seen as the limit of the yoke type reg attachment. This allowed them to market a single tank/valve combination to both the DIN and YOKE (w/ doughnut\adapter) crowds with the more common 3/4ths neck......
Ok - got all that....? Now we move onto burst discs....
You should get burst discs appropriate for the pressures your tanks will be seeing. I've seen some unscrupulous shops swap out discs if they saw you had the 'wrong'/higher pressure than rated, if you went in for a fill.
In some parts of the country, it is not uncommon to have people solely use 5500psi rated discs in all of their steel tanks irregardless of the actual tank pressure rating.
-Tim