n9ne0hse7en
Chemical
- Feb 20, 2020
- 2
Hello, I am a process engineer evaluating the venting systems on a number of tanks designed to API 650(F) in the 1990's-timeframe. I have noticed that a number of tanks have a stamped "design pressure" on the nameplate that is far lower than the MAWP pressure that would be calculated using the formulas provided in API 650 app F. Using the name plate pressure has resulted in a number of undersized vents as it appears the original emergency venting calculations were performed using the Pmax from API 650(F). I am curious if anyone knows why the tank would have such a low pressure listed as design pressure on the nameplate? Thanks in advance.