Hello Everybody,
I have a question related to Restriction orifices and choked flow. I've been searching in the forum and a lot of discussion related to this matter has been going on; however, I was not able to find an answer for my question. I would love to have your insights about it.
I have gas line discharging to LP Flare, in case that something goes wrong upstream, there will be a stream of really high pressuregoing through this line. That's the reason why a Restriction Orifice is required. The pressure upstream is expected to be around 320 bara and downstream (LP flare) around 1.5 bara.
Obviously, the device needs to be sized for choked flow conditions; after reading API 520, I concluded that the orifice needed to be sized for critical flow. Looking at the equations it can be seen that the estimation of the orifice area is only dependant on the upstream pressure (and fluid properties), temperature and required flowrate. However, what is the role of the downstream pressure?
In this thread: http://www.cheresour...iction-orifice/ this issue is discussed and, in post #2 it is mentioned:
"In the situations such as you mentioned above,chocked flow downstream of RO is a common occurance.
Size the RO for dP=9.6 bar and maximum flow of 4.4 MMSCFD."
This is exactly my concern, can the design of the RO affect the downstream pressure in choked flow conditions or are these conditions given by the downstream system (LP flare system backpressure)?. Is there any way to influence the downstream pressure with the design of the RO?.
Thanks in advance for any insight you can give me on this.
Regards,