marcleblanc12
Mechanical
- May 7, 2014
- 29
I'm designing a tank with the following parameters:
D = 17.2 m
H = 18 m
Hliquid = 17.38 m
SG = 1.48
CA = 2mm
According to API 650 Clause 5.5.3, an elastic analysis must be made to calculate the required thickness of the annular ring. I'm using Kroon's Method to calculate the thickness, and I'm a bit unsure of a couple of things.
1 - Does the calculated thickness used in this method include or exclude corrosion allowance?
2 - What is the minimum width (or internal projection) of the annular ring when performing such an analysis?
If I use L = 493 mm for my annular plate width and Tb = 17.05 mm for my annular plate thickness, then everything works out perfectly as per my attached spreadsheet.
θs = -θc
θb = 0
σ < 75000 psi
This would mean that my annular plate would be a 3/4" plate (17.05 + 2mm CA) at 19-1/2" wide. This works out great since the bottom shell course of my tank is also 3/4" Plate.
HOWEVER, according to API 650, the internal projection of the annular ring needs to be 0.035D as per Clause 5.11.2.3 and E.6.2.1.1.3. This means that L' = 602 mm and L = 672 mm.
If I use 672 mm for my plate width, and 17.05 mm for my plate thickness then:
σ < 75000 psi
θb = 0
*BUT:
θs ≠ -θc (in fact they are both the same sign) As a matter of fact once L>576mm then θs > 0 meaning regardless of what thickness you use you can't make θs = -θc and if you do push it to the limit using L = 576 mm then Tb = 103 mm, which is extremely ridiculous.
Does anyone know what governs when using Kroon's Method? Do I need to use the width as per API 650 and not worry about θs ≠ -θc? Or do I need to make sure that θs = -θc and use a more narrow annular ring?
Thanks,
Marc
D = 17.2 m
H = 18 m
Hliquid = 17.38 m
SG = 1.48
CA = 2mm
According to API 650 Clause 5.5.3, an elastic analysis must be made to calculate the required thickness of the annular ring. I'm using Kroon's Method to calculate the thickness, and I'm a bit unsure of a couple of things.
1 - Does the calculated thickness used in this method include or exclude corrosion allowance?
2 - What is the minimum width (or internal projection) of the annular ring when performing such an analysis?
If I use L = 493 mm for my annular plate width and Tb = 17.05 mm for my annular plate thickness, then everything works out perfectly as per my attached spreadsheet.
θs = -θc
θb = 0
σ < 75000 psi
This would mean that my annular plate would be a 3/4" plate (17.05 + 2mm CA) at 19-1/2" wide. This works out great since the bottom shell course of my tank is also 3/4" Plate.
HOWEVER, according to API 650, the internal projection of the annular ring needs to be 0.035D as per Clause 5.11.2.3 and E.6.2.1.1.3. This means that L' = 602 mm and L = 672 mm.
If I use 672 mm for my plate width, and 17.05 mm for my plate thickness then:
σ < 75000 psi
θb = 0
*BUT:
θs ≠ -θc (in fact they are both the same sign) As a matter of fact once L>576mm then θs > 0 meaning regardless of what thickness you use you can't make θs = -θc and if you do push it to the limit using L = 576 mm then Tb = 103 mm, which is extremely ridiculous.
Does anyone know what governs when using Kroon's Method? Do I need to use the width as per API 650 and not worry about θs ≠ -θc? Or do I need to make sure that θs = -θc and use a more narrow annular ring?
Thanks,
Marc