I have question related with API 650 Tank Design.
As we already understood that API 650 limits design pressure until 2.5 psi or around 70 in H2O
My question :
1. Why breather valve set point usually around 4-6 inH2O ? What is the specific reason behind it?
2. I do understand that breather valve is used to accomodate air in or air out due to loading/unloading and thermal reason, but what is exactly the guidelines to determine the breather valve set point?
3. Let say I've been asked about the operating pressure of the tank, is it wise to say that the operating pressure equal to breather valve set point?
4. If we'd like to design new tank, let say crude oil storage for instance, how do we determine the operating pressure? in my mind we need to calculate it based on vapor pressure at operating temperature. What is your opinion?
thanks...
