lamari
Industrial
- Jun 7, 2010
- 4
Hi,
we have experienced corrosion failures in a 6 inch SCH 80 flowline (3 mm CA) in a oil production facilities. We know that the corrosion is due to CO2 and water accumulation in the low points of the flowline. Unfortunatelly we have not received the chemicals yet to protect the flowlines and as per the flowline desing we cannot launch any pig (or intelligent pig).
The pipes are wrapped and buried (about 1.5 m) and I would like to perform a quick assesment of the integrity of that flowline. As said, since the flowline is wrapped, I cannot easly do a UT. So I'm thinking on doing a spot X-ray inspection. Now the line is full of water. What I would like to know is if the X-ray inspection procedure of a pipeline in service differs from a X-ray inspection procedure used for welding control.
I guess the exposition time and distance should not be the same for each inspection procedure, but I have no clue which could be a convenient range.
My concern is that all the UT we have done (in the above ground pipework) and the corrosion coupon inspection do not reveal such a high corrosion degree. However in two months we experienced three oil leaks at one of the lowest points of the flowline.
Thanks in advance.
we have experienced corrosion failures in a 6 inch SCH 80 flowline (3 mm CA) in a oil production facilities. We know that the corrosion is due to CO2 and water accumulation in the low points of the flowline. Unfortunatelly we have not received the chemicals yet to protect the flowlines and as per the flowline desing we cannot launch any pig (or intelligent pig).
The pipes are wrapped and buried (about 1.5 m) and I would like to perform a quick assesment of the integrity of that flowline. As said, since the flowline is wrapped, I cannot easly do a UT. So I'm thinking on doing a spot X-ray inspection. Now the line is full of water. What I would like to know is if the X-ray inspection procedure of a pipeline in service differs from a X-ray inspection procedure used for welding control.
I guess the exposition time and distance should not be the same for each inspection procedure, but I have no clue which could be a convenient range.
My concern is that all the UT we have done (in the above ground pipework) and the corrosion coupon inspection do not reveal such a high corrosion degree. However in two months we experienced three oil leaks at one of the lowest points of the flowline.
Thanks in advance.