Fario
Mechanical
- Jun 17, 2014
- 19
Hy guys
How I can to check the stress in hydrostatic condition when the corrosion tolerance is zero?
Does is possible to define the MAWP equal to design pressure when corrosion tolerance is zero?
My problem is follows:
The MAWP must be calculated (equations) in corroded condition of vessel.
Hydrostatic test is 1,3xMAWPxLSR, then...
If we want to calculate the verification of stress on hydrostatic test condition, we will have stress 1,3 times bigger (or plus) than admisible stress, as the corrosion is zero so the thickness of MAWP is equal to thickness in hydrostatic test.
For example
LSR = 1
corr. = 0,0 mm
Pd = 10 barg
t req = 10,5 mm
t defined = 14 mm
a)MAWP calculated to 14 mm = 13 barg @ Td, then HT = 16,9 barg @ T HT
Stress on hydrostatic test condition > S adm @ T HT
b)If I take MAWP = 10 barg @ Td, then HT = 13 barg @ T HT
Stress on hydrostatic test condition < S adm @ T HT (OK !!)
Is it mandatory to calculate the MAWP using the equations described in the standard (corroded condition) or is it possible to define it as a value equal to the Pd, in this case?
How I can to check the stress in hydrostatic condition when the corrosion tolerance is zero?
Does is possible to define the MAWP equal to design pressure when corrosion tolerance is zero?
My problem is follows:
The MAWP must be calculated (equations) in corroded condition of vessel.
Hydrostatic test is 1,3xMAWPxLSR, then...
If we want to calculate the verification of stress on hydrostatic test condition, we will have stress 1,3 times bigger (or plus) than admisible stress, as the corrosion is zero so the thickness of MAWP is equal to thickness in hydrostatic test.
For example
LSR = 1
corr. = 0,0 mm
Pd = 10 barg
t req = 10,5 mm
t defined = 14 mm
a)MAWP calculated to 14 mm = 13 barg @ Td, then HT = 16,9 barg @ T HT
Stress on hydrostatic test condition > S adm @ T HT
b)If I take MAWP = 10 barg @ Td, then HT = 13 barg @ T HT
Stress on hydrostatic test condition < S adm @ T HT (OK !!)
Is it mandatory to calculate the MAWP using the equations described in the standard (corroded condition) or is it possible to define it as a value equal to the Pd, in this case?