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Determine set pressure for tank (api 650, api 2000)

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Platonicus

Petroleum
Oct 7, 2021
8
Hello!

Are there recommendations or formulas in API or other standards for determining the setting pressure of an emergency valve, safety valve, or breathing valve?

How to determine the installation pressure, knowing the operating and design pressure of the tank?
 
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Set pressure on tank safety overpressure / underpressure valves is typically at 80% of design pressure. So this enables an overpressure of 20% to get to relieving pressure. Relieving pressure in API650 tanks is not permitted to exceed design pressure i.e. accumulation permitted is zero.
 
What's "instalation pressure"?

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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.
 
See section 4.6 of API 2000 on pressure / vacuum settings for relief devices. The setting suggested of 80% of design pressure may need to be even lower in some types of relief devices in order to achieve full lift - see annex C.
 
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