Jonesey1
Petroleum
- Oct 24, 2011
- 1
We have a approx. 65M diameter atmospheric storage built after API 650 (design pressure max. 0.5BarG) , which has a LP steam coil mounted in the botttom to provide heat to the crude oil when the ambient temperatures falls under approx. 10DegC. The LP steam has a design pressure of 5Barg and an operating pressure of 2.5BarG. According to Pressure Equipment Directive 97/23/EC article 1 point 2.1.2 heat exchangers consisting of pipes for the purpose of cooling or heating air shall be considered as piping. As we are not heating air, does that mean that our coil shall be considered as a pressure vessel ? Guideline 2/4 offers a little more help, but is not conclusive. I do not think that it was meant that the Pressure Equipment directive should be applied to API storage tanks, but there are people in our organisation that think it does. Any help would be appreciated.