I have question regarding Blowdown analysis.
So I was doing blowdown calculation in which I'm confused about which philosophy to follow and Why?
1. Lumped Vessel Calculation
- In lumped vessel which thickness we have to specify to fire zone vessel? (Metal Mass Calculation or according to GAD)
- How to decide which pipes we have to add in lumped vessel calculation?
2. or Model all pipes individually in Blowdown Utility.
Also, I have some other questions Please answer
> for LODMAT case why we Isochorically cool down and use that stream for Blowdown (Cooling down Isochorically leads to decrease in pressure)?
> How do we define fire zone or fire circle area in specific system?