engr2GW
Petroleum
- Nov 7, 2010
- 307
Hello,
Many times when you try to size a valve using sizing tools by the manufacturers, e.g. Kimsize for Kimray, Norrisize for Norriseal, Fishre etc. you will see red flag of critical flow. I have heard that sometimes it might say critical flow, but not bad to use with the dP. Is there a rule of thumb as to when to worry about that?
the cases I'm sizing for are
1. 350 to 30 psig for 500bbl/day oil and then 30psig to 4psig for the same oil rate. This is a two inch valve with trim size from 0.75 to 0.25 inches depending on component materiall, and snap acting
I have an options of
350 to 50 psig and then 50 psig to 4psig before storage tanks.
I ran all this scenario and found critical flow, is it critical in actual operation, or is there a rule of thumb, any experience/ideas/advice??
The trim in sight now is Carbide:
thanks for your help
As much as possible, do it right the first time...
Many times when you try to size a valve using sizing tools by the manufacturers, e.g. Kimsize for Kimray, Norrisize for Norriseal, Fishre etc. you will see red flag of critical flow. I have heard that sometimes it might say critical flow, but not bad to use with the dP. Is there a rule of thumb as to when to worry about that?
the cases I'm sizing for are
1. 350 to 30 psig for 500bbl/day oil and then 30psig to 4psig for the same oil rate. This is a two inch valve with trim size from 0.75 to 0.25 inches depending on component materiall, and snap acting
I have an options of
350 to 50 psig and then 50 psig to 4psig before storage tanks.
I ran all this scenario and found critical flow, is it critical in actual operation, or is there a rule of thumb, any experience/ideas/advice??
The trim in sight now is Carbide:
thanks for your help
As much as possible, do it right the first time...