adammilad
Mechanical
- May 27, 2010
- 14
Dear members,
I am working on a horizontal vessel currently that has an ID of 78" and a wall thickness of 0.375”. This is a Stainless Steel vessel therefore my goal is to keep costs as low as possible by limiting the shell thickness. I have designed the vessel in Compress and I have no deficiencies as it sits. My concern is that the D/t= 208. I have heard that there is an industry practice to keep vessels to D/t<100 due to shipping and possible deformation.
Do any of you feel that I would be wrong to leave my shell thickness at 0.375”? If any of you can shed some light as to where to get more information that would be great. I have checked in the Moss bock as well as the Pressure Vessel Design Handbook. I found some reference to D/L but nothing really for D/t.
I am working on a horizontal vessel currently that has an ID of 78" and a wall thickness of 0.375”. This is a Stainless Steel vessel therefore my goal is to keep costs as low as possible by limiting the shell thickness. I have designed the vessel in Compress and I have no deficiencies as it sits. My concern is that the D/t= 208. I have heard that there is an industry practice to keep vessels to D/t<100 due to shipping and possible deformation.
Do any of you feel that I would be wrong to leave my shell thickness at 0.375”? If any of you can shed some light as to where to get more information that would be great. I have checked in the Moss bock as well as the Pressure Vessel Design Handbook. I found some reference to D/L but nothing really for D/t.