GreenHawk
Chemical
- Jan 13, 2012
- 9
I have been working on a flare system to which the PSVs’ relief load due to fire scenario is exceeding the capacity of the flare system (due to an expansion in the plant). I know that using API's methodology for relief load calculation normally gives smaller relief load as compared to NFPA's methodology.
Additionally, I have also been told that if we divide the plant area into different fire zones with some restricting boundary wall around each fire zone, this can prevent flow of flammable fluids from one zone to another. By construction of this restriction boundary wall around each fire zone, we could be able to reduce the relief load to flare due to fire scenario. I had tried to look in API-521, API-537, etc. but was not able to find anything which endorses the use of this method and which gives more details on how to implement this boundary wall concept in the plant. Can anyone share their experience of implementing a similar idea in their plant? Additionally, can you also guide me if this aspect of flare load reduction has been discussed in any API or NFPA standard? Any other associated advice is also very appreciated.
Thanks.
Additionally, I have also been told that if we divide the plant area into different fire zones with some restricting boundary wall around each fire zone, this can prevent flow of flammable fluids from one zone to another. By construction of this restriction boundary wall around each fire zone, we could be able to reduce the relief load to flare due to fire scenario. I had tried to look in API-521, API-537, etc. but was not able to find anything which endorses the use of this method and which gives more details on how to implement this boundary wall concept in the plant. Can anyone share their experience of implementing a similar idea in their plant? Additionally, can you also guide me if this aspect of flare load reduction has been discussed in any API or NFPA standard? Any other associated advice is also very appreciated.
Thanks.