VTechie79
Mechanical
- Aug 9, 2011
- 8
I have been asked to turn almost 50 year old API 620 storage tanks in to ASME pressure vessels. I say this jokingly, but it is the essence of what I have been tasked with. That being said, I am not sure how I would go about calculating an external/vacuum pressures above the 1 oz/in^s limit given in the API 620. I have attempted using ASME Sect VII, div 1 rules as well as API 650 guidelines. I even tried 620 rules using a negative pressure just to see how the results would compare. All ended up with different results, none of which I am confident are correct.
I am looking for some advice from an experienced tank designed as to what is the best method to use for external/vacuum pressure calculations above 1 oz/in^2 for a 620 tank short of using finite element analysis. Most of the tanks I am dealing with are carbon steel, API 620 style, cone bottom tanks. I say "620 style" because there is no record of what code the tanks were originally built to if any at all.
I am looking for some advice from an experienced tank designed as to what is the best method to use for external/vacuum pressure calculations above 1 oz/in^2 for a 620 tank short of using finite element analysis. Most of the tanks I am dealing with are carbon steel, API 620 style, cone bottom tanks. I say "620 style" because there is no record of what code the tanks were originally built to if any at all.