Straight up to a higher elevation is problematic since propane, unlike natural gas, is heavier than air. So the results would be dependent on cross ventilation.I think answer to your question in OP is going to be dependent on whether there is any dispensing and filling operations at the tank location as well as where any pressure relief venting might be located. If dispensing/filling is at a location that is piped away from tank itself there may not be any classified location and pressure relief could possibly be piped away from the tank as well, even if just straight up to a higher elevation, that might be enough in some cases to lessen classification necessary at ground level.
Straight up to a higher elevation is problematic since propane, unlike natural gas, is heavier than air. So the results would be dependent on cross ventilation. Sent from my Pixel 4a using Tapatalk
The area classification tables in the 2001 edition are more prescriptive than those in the latest edition(s) - and fairly conservative (in my opinion). I think they should have left them as-is...(as-was)Folks, we are discussing LNG (Liquified Natural Gas). As nhee2 notes, it can act as a heavier-than-air gas until it vaporizes. (See NFPA 497, Sections 4.2.1, 4.2.4, and 4.4.5) This is why I noted in my previous post (#5) that there are other NFPA 59A spacing considerations beyond electrical area classification.
While nhee2 is also correct that 49CFR 193 uses the 2001 Edition of NFPA 59A, FedOSHA can, and often does, use any Edition it deems relevant to the installation under the "General Duty" clause if it identifies a problem as a "recognized hazard".