Pilot production of pressure vessels at A2 licensing level
Thread Content
Request parameters or drawings for pressure vessel prototype products at A2 licensing level (TSG07-2019)
Class 3 containers with a diameter of 2000 or less are sufficient
Not less than φ800×2000, and should be equipped with a manhole or flange connections of 400mm or more. . . . . Table C-6 of TSG07 specifies this, and I would like to ask whether it has been implemented in practice: handshake
Do it; otherwise how can you obtain evidence? The boiler inspection agency and the review team still need to take a look
I was just asking if the experts have any well-prepared design documents that we could refer to: lol
You can build your own high-pressure gas tank by setting a higher design pressure
This post was last edited by A13562570752 on 2021-5-20 08:48. Find a medium for liquefied gas; as long as the PV value reaches 50, that’s fine. For example, in the case of a liquid ammonia storage tank with a diameter of around 1800 and a length of 8000, a volume of slightly over 20 cubic meters is sufficient. Reputable design institutes have ready-made ones specifically for prototype development and certification.