We just completed the IP of an 8" x 3km gas flowline that was installed in 1987. This line has an external bullet ponit defect measuring 16mm long x 11mm wide x 5mm deep at 3 O'clock position with the bultt in place and is a schedule 100 pipe with Nominal wall thickness of 15.1mm. The final IP...
We just concluded the intelligent pigging of an 8"x3km gas flowline that was installed in 1987 but the final IP report from the contractor revealed no defect. This line is a schedule 100 pipe with Nominal wall thickness of about 15.1mm and has a bullet pierce of 16mm length x 11mm width x 5mm...
Hi cooleagues,
I had a proposal to use the alloys in our company but do not have a full grasp of their corrosion properties, chemical composition and application. I will obliged if you could educate me on the above and sent web links where I can get more idea.
Thanks
March 1971
I am incharge of asset intergrity in my place of work and is saddled with the role of determining facilities retirement. I would be obliged if some one can give me guide on the critera to used in taking decision on the above matter. The piping in question are crude oil and gas production piping...
I am presently faced with a new challenge of taking charge of the risk based inspection of the surface facilities in my company's crude oil flowstations. Please I will be obliged if someone can give me guidelines on the above subject matter or give link on where to find information on the above...
During the process of start-up of one of our flowstations,while pumping down the high liquid level from a vertical crude oil surge vessel with two pumps, the vessel suddenly imploded. All pumps were immediately stopped, facility closed in and wells secured. Pleases what colud be the...
