takiyasamsama
Chemical
- Feb 10, 2015
- 108
Hi,
I got a vessel, which the design pressure is even lower than atmospheric (around 0.035MPaG). The vessel design temperature on the other hand is at 300 degC and wrapped with a half-pipe jacket of 0.7 MPaG. Should I design the vessel at atmospheric pressure instead of 0.035 MPag? The reason for saying this would be that some of the manufactures, when we issue purchase order they quoted the design pressure of the vessel to be Full Water + 3 barg, sometimes Vacuum + 3 barg.
I got a vessel, which the design pressure is even lower than atmospheric (around 0.035MPaG). The vessel design temperature on the other hand is at 300 degC and wrapped with a half-pipe jacket of 0.7 MPaG. Should I design the vessel at atmospheric pressure instead of 0.035 MPag? The reason for saying this would be that some of the manufactures, when we issue purchase order they quoted the design pressure of the vessel to be Full Water + 3 barg, sometimes Vacuum + 3 barg.