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Welded steel tanks for storage oil
What is the function of storage
tank ?
It is a device used to store liquids
such as oil , water and petrol
Steel storage tanks built before 1950 generally
do not conform to current industry standards for
explosion and fire venting
Several organizations have developed standards and
specifications for storage tank design. Such as

API 650

“ Welded Steel Tanks for Oil Storage”
issued by the American Petroleum Institute (API).
Annular bottom plates

It must have a radial width minimum 600 mm
between the inside of the shell and any lap welded joint in
the remainder of the bottom
and the maximum radial width of the annular plate is
calculated from formula
R = 215*tb /(H*G)º·

tb = thickness of the annular plates

in mm ,
H = maximum design liquid level in m ,
G = specific gravity of the liquid to be stored
Annular bottom plate thickness
plate thickness of first
shell course (mm)
t<= 19

<=190

stress in the first
shell course (mm)
Shell design
By :

The 1-foot method

Variable - design - point
method
Elastic analysis
Calculation of thickness by the 1-foot method

• It calculate the thicknesses required at design
•

points 0.3 m above the bottom of each shell
course .
This method shall not be used for tanks larger
than 60 m in diameter .
The required minimum thickness of shell plates
shall be greater than this value

td =(4.9*D*(H-0.3)*G)/Sd +CA
tt = (4.9*D*(H-0.3))/St

td = design shell thickness in mm ,
tt = hydrostatic test thickness in mm ,
D = nominal tank diameter in m ,
H =design liquid level in m ,
G = specific gravity of the liquid to be storage ,
CA = corrosion allowance in mm ,
Sd = allowable stress for the design condition in MPa ,
St = allowable stress for the hydrostatic test condition in MPa ,
The minimum thickness of shell plates shall be
computed from the stress on the vertical joints
using the formula

t = (4.9*D*(H-0.3)*G/(145*E)+CA

t = minimum thickness in mm,
D = nominal tank diameter in m ,
H = design liquid level in m ,
G = specific gravity of the liquid to be storage ,
CA = corrosion allowance in mm ,
E = joint efficiency which is either 0.85 or 0.70 .
corrosion allowance :
1 mm for gases
3 mm for liquids
6 mm for Sulphate

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Welded steel tanks for storage oil

  • 1. Welded steel tanks for storage oil
  • 2. What is the function of storage tank ? It is a device used to store liquids such as oil , water and petrol
  • 3. Steel storage tanks built before 1950 generally do not conform to current industry standards for explosion and fire venting Several organizations have developed standards and specifications for storage tank design. Such as API 650 “ Welded Steel Tanks for Oil Storage” issued by the American Petroleum Institute (API).
  • 4. Annular bottom plates It must have a radial width minimum 600 mm between the inside of the shell and any lap welded joint in the remainder of the bottom and the maximum radial width of the annular plate is calculated from formula R = 215*tb /(H*G)º· tb = thickness of the annular plates in mm , H = maximum design liquid level in m , G = specific gravity of the liquid to be stored
  • 5. Annular bottom plate thickness plate thickness of first shell course (mm) t<= 19 <=190 stress in the first shell course (mm)
  • 6. Shell design By : The 1-foot method Variable - design - point method Elastic analysis
  • 7. Calculation of thickness by the 1-foot method • It calculate the thicknesses required at design • points 0.3 m above the bottom of each shell course . This method shall not be used for tanks larger than 60 m in diameter .
  • 8. The required minimum thickness of shell plates shall be greater than this value td =(4.9*D*(H-0.3)*G)/Sd +CA tt = (4.9*D*(H-0.3))/St td = design shell thickness in mm , tt = hydrostatic test thickness in mm , D = nominal tank diameter in m , H =design liquid level in m , G = specific gravity of the liquid to be storage , CA = corrosion allowance in mm , Sd = allowable stress for the design condition in MPa , St = allowable stress for the hydrostatic test condition in MPa ,
  • 9. The minimum thickness of shell plates shall be computed from the stress on the vertical joints using the formula t = (4.9*D*(H-0.3)*G/(145*E)+CA t = minimum thickness in mm, D = nominal tank diameter in m , H = design liquid level in m , G = specific gravity of the liquid to be storage , CA = corrosion allowance in mm , E = joint efficiency which is either 0.85 or 0.70 .
  • 10. corrosion allowance : 1 mm for gases 3 mm for liquids 6 mm for Sulphate