cacaboose
Petroleum
- Jan 23, 2015
- 3
Hi all,
Background:
Flexible piping has a number of possible failure mechanisms, one of which is caused by rapid depressurisation. i.e. polymer blistering, or in some cases, carcass collapse due to permeated gas expansion in multi-layered PVDF flexibles. API RP 17B provide general pressurisation/depressurisation limits for strength/leak testing (note: these limits are ultimately to the discretion of suppliers due to specific design and test conditions).
Question:
Is there any knowledge of using pressurisation/depressurisation limits during operations (e.g. well shutdowns)? My pipe in question is a subsea 12" unbonded oil production line with a max operating pressure of 50 barg. With an operating pressure much lower than design (210 barg), is there any chance of possible depressurisation failures or is this only seen in strength/leak testing, i.e exposing the line to 210+5% barg. Maybe there is a study that has related initial pressures and depressursiation rate to failures?
I believe there is no concern during operations as both standard and supplier do not disclose any operation rates but I would like a second opinion.
Thank you in advance.
J
Background:
Flexible piping has a number of possible failure mechanisms, one of which is caused by rapid depressurisation. i.e. polymer blistering, or in some cases, carcass collapse due to permeated gas expansion in multi-layered PVDF flexibles. API RP 17B provide general pressurisation/depressurisation limits for strength/leak testing (note: these limits are ultimately to the discretion of suppliers due to specific design and test conditions).
Question:
Is there any knowledge of using pressurisation/depressurisation limits during operations (e.g. well shutdowns)? My pipe in question is a subsea 12" unbonded oil production line with a max operating pressure of 50 barg. With an operating pressure much lower than design (210 barg), is there any chance of possible depressurisation failures or is this only seen in strength/leak testing, i.e exposing the line to 210+5% barg. Maybe there is a study that has related initial pressures and depressursiation rate to failures?
I believe there is no concern during operations as both standard and supplier do not disclose any operation rates but I would like a second opinion.
Thank you in advance.
J