LiamBlair
Petroleum
- Dec 2, 2003
- 8
*Need Brains to Pick*
Currently i am investigating the failure of Injected moulded polypropylene used as a field joint for an offshore pipeline. The assembly process at the end of the 'stalks' of pipeline, i.e. where the 'factory' coating ends, is as follows (neglecting contaminents):
(1)Steel is heated to application temperature of fusion bonded epoxy powder(FBE is for corrosion reasons)
(2)At a particular cure time, a Copolymer adhesive is used to promote crosslinking/a good bond strength between FBE and.....
(3)Polyproylene is injected with a chemical blowing agent to form a polymer of particular density and thermal properties.
During this process, the 'factory' applied coating is fused with the 'field' applied coating by heating up the chamfered edges before the injection process takes place.
(4)After polypropylene is crsytallizing, mould is removed and water flowed across it to cool and solidify.(since time=money)
Heres the problem:
During the reeling of this pipeline, round a drum in very cold temperatures and after a particular cooldown time, the field joint produced cracking at 45 degrees to bending stress (critical path angle due to shear stresses), white stressing (overstressed plastic) and loud bangs suspected of being the FBE disbonding from the metal. I am assuming all application procedures were followed correctly and would like to know of any similar problems anyone has had relating to Polyproylene and cold temperatures effets. Does thermal shock (rate of temperature change) have a big enough influence to effectively raise the Tg of the material through the effects of strain rate polymer dependence? Manufacturers claim the film coefficient of their cooldown graphs are neglible compared to conduction through the metal pipe (obviously) and are not considered in design stage, yet surely this effects the real life actual value of the polyprop during water flowing? any advice or direction pointing would help a lot! thanking in advance.
Currently i am investigating the failure of Injected moulded polypropylene used as a field joint for an offshore pipeline. The assembly process at the end of the 'stalks' of pipeline, i.e. where the 'factory' coating ends, is as follows (neglecting contaminents):
(1)Steel is heated to application temperature of fusion bonded epoxy powder(FBE is for corrosion reasons)
(2)At a particular cure time, a Copolymer adhesive is used to promote crosslinking/a good bond strength between FBE and.....
(3)Polyproylene is injected with a chemical blowing agent to form a polymer of particular density and thermal properties.
During this process, the 'factory' applied coating is fused with the 'field' applied coating by heating up the chamfered edges before the injection process takes place.
(4)After polypropylene is crsytallizing, mould is removed and water flowed across it to cool and solidify.(since time=money)
Heres the problem:
During the reeling of this pipeline, round a drum in very cold temperatures and after a particular cooldown time, the field joint produced cracking at 45 degrees to bending stress (critical path angle due to shear stresses), white stressing (overstressed plastic) and loud bangs suspected of being the FBE disbonding from the metal. I am assuming all application procedures were followed correctly and would like to know of any similar problems anyone has had relating to Polyproylene and cold temperatures effets. Does thermal shock (rate of temperature change) have a big enough influence to effectively raise the Tg of the material through the effects of strain rate polymer dependence? Manufacturers claim the film coefficient of their cooldown graphs are neglible compared to conduction through the metal pipe (obviously) and are not considered in design stage, yet surely this effects the real life actual value of the polyprop during water flowing? any advice or direction pointing would help a lot! thanking in advance.