peng80
Chemical
- Oct 9, 2010
- 6
Guys,
Hope you can help me out with a calculation.
I have a system with unstabilized crude. If there were a accidental release of hydrocarbons from this system, from a hole (for example 1 cm diameter), how can the flow through this hole be calculated?
I know how to calculate the flow if this was a gas or liquid service, using standard orifice sizing calcs. With a unstabilized crude service, I am not sure how to calculate due to flashing.
The system can be assumed at such pressure that the flow would be sonic (for example 40 barg system pressure, and release to atmospheric pressure)
Thanks!
Hope you can help me out with a calculation.
I have a system with unstabilized crude. If there were a accidental release of hydrocarbons from this system, from a hole (for example 1 cm diameter), how can the flow through this hole be calculated?
I know how to calculate the flow if this was a gas or liquid service, using standard orifice sizing calcs. With a unstabilized crude service, I am not sure how to calculate due to flashing.
The system can be assumed at such pressure that the flow would be sonic (for example 40 barg system pressure, and release to atmospheric pressure)
Thanks!