Dear Fellow Members,
What should be the criteria for replacing a process piping with respect to reduction in piping wall thickness?
How much remaining wall thickness can be allowed?
To be very specific,we have a process gas receiving header that services at high temperature say around 800 Deg C at inlet positions & pressure is around 3 Kg/Cm^2. The header material is A335 P 22 & nominal wall thickness is 21.44 mm.
The header receives hot ethylene gases from furnace and located at the top of Furnace. It may be appreciated that all inlet points in the header are subjected to Erosion & in 12 years of operation, we have observed 3 mm reduction in wall thickness.
Can some one may guide, as how mcuh reduction in wall thickness is allowed before replacemnt or repair of this header?
Also is there any standard formula available to calculate max allowbale reduction in wall thickness of process piping?
What should be the criteria for replacing a process piping with respect to reduction in piping wall thickness?
How much remaining wall thickness can be allowed?
To be very specific,we have a process gas receiving header that services at high temperature say around 800 Deg C at inlet positions & pressure is around 3 Kg/Cm^2. The header material is A335 P 22 & nominal wall thickness is 21.44 mm.
The header receives hot ethylene gases from furnace and located at the top of Furnace. It may be appreciated that all inlet points in the header are subjected to Erosion & in 12 years of operation, we have observed 3 mm reduction in wall thickness.
Can some one may guide, as how mcuh reduction in wall thickness is allowed before replacemnt or repair of this header?
Also is there any standard formula available to calculate max allowbale reduction in wall thickness of process piping?