The tank is equipped with a nitrogen breathing line.
Operation pressure - 1-2 kPa g.
Design pressure - 15 kPa g.
Additional explanations:
1. A safety valve is provided to protect against vacuum.
2. A spring-type safety valve (PSV) is also provided to protect against nitrogen breakthrough through the control valve.
3. To protect against overpressure in case of fire, an emergency valve is provided.
This design, as well as the selection of parameters, is not very familiar to me, because... We usually accept tanks not according to the API, but according to another national standard, in which everything is clearly regulated.
For example, the national standard states:
The setting values of excess pressure pu and vacuum pvu of valves must not exceed the standard values of internal pressure p and vacuum pv in the following ratios:
- for breathing valves: 0.9 p ≤ p u ≤ 1.0 p;
- for safety valves: 1.1 p < p u ≤ 1.2 p;
The standard values of excess pressure and vacuum established by the design assignment are, as a rule, p=2.0 kPa, 0.25 kPa.
The setting value of the emergency valve response pressure pa must be within the range 1.2p ≤ pa < 1.5p.
In this regard, I would like to understand whether there are similar recommendations in the API.
