kiade
Chemical
- Jan 23, 2009
- 12
Hi all,
I am using the RO (Restriction Orifice) to let-down the pressure from 900# (ANSI Class) to 300#. The steam is flowing through the pipe and sends to some consumers. I have manual valve downstream of the RO. These are my questions:
1. Do I need any PSV (Pressure Safety Valve) for protection of the downstream piping in case of closing the downstream valve inadvertently? Valve is so far from RO and installed next to the consumers. (Note: We know if steam doesn't flow through the RO, upstream and downstream pressure is going to be the same pressure and all system needs to be in 900# class which I don’t want to be).
2. If we need the PSV how can I calculate the PSV’s relief load?
Please let me know your thought. Thanks guys.
Kia
I am using the RO (Restriction Orifice) to let-down the pressure from 900# (ANSI Class) to 300#. The steam is flowing through the pipe and sends to some consumers. I have manual valve downstream of the RO. These are my questions:
1. Do I need any PSV (Pressure Safety Valve) for protection of the downstream piping in case of closing the downstream valve inadvertently? Valve is so far from RO and installed next to the consumers. (Note: We know if steam doesn't flow through the RO, upstream and downstream pressure is going to be the same pressure and all system needs to be in 900# class which I don’t want to be).
2. If we need the PSV how can I calculate the PSV’s relief load?
Please let me know your thought. Thanks guys.
Kia