Inchtain
Petroleum
- Feb 21, 2021
- 137
I am seeking your help in comparison between choosing the single bottom with geomembrane liner and CP protection; and the double steel bottom with leak detection and CP protection for the replacement of a Crude Oil Surge Tank floor replacement with reference to the International Standards.
Which are the advantages and disadvantages of each repair procedure?
Tank Data:
Construction Code API 650 Appendix F, Edition 2001
Design Pressure / Vacuum 3.45 kPag / 0.5 kPag (51 mmH2O)
Working Pressure (kPag) 0.9 ÷ 1.5
Contained Fluid / Blanketing Gas API 38 Crude Oil / Nitrogen
Max. Operating Temperature (°C) 90
Actual Working Temperature (°C) 57
Dimensions (m) Height 14.6 - Diameter 37.2
Nominal Capacity (15,900 m³ )(100.000 barrels)
Material Bottom: ASTM A 283 Gr. C
Annular & Shell: SA A 516 Gr. 70
Roof: S235 J0Roof Structure: S275 J0
Corrosion Allowance (mm) 1.6
Bottom/Annular/Roof Plates Thickness(mm)8 / 10 / 7
Shell Plates Thickness (mm)
1st course 14
2nd course 13
3rd course 11
4th course & up 10
Which are the advantages and disadvantages of each repair procedure?
Tank Data:
Construction Code API 650 Appendix F, Edition 2001
Design Pressure / Vacuum 3.45 kPag / 0.5 kPag (51 mmH2O)
Working Pressure (kPag) 0.9 ÷ 1.5
Contained Fluid / Blanketing Gas API 38 Crude Oil / Nitrogen
Max. Operating Temperature (°C) 90
Actual Working Temperature (°C) 57
Dimensions (m) Height 14.6 - Diameter 37.2
Nominal Capacity (15,900 m³ )(100.000 barrels)
Material Bottom: ASTM A 283 Gr. C
Annular & Shell: SA A 516 Gr. 70
Roof: S235 J0Roof Structure: S275 J0
Corrosion Allowance (mm) 1.6
Bottom/Annular/Roof Plates Thickness(mm)8 / 10 / 7
Shell Plates Thickness (mm)
1st course 14
2nd course 13
3rd course 11
4th course & up 10