best practice for management of pipeline integrity by pigging

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Best Practice for Management of Pipeline Integrity by Pigging 12 th February 2015 Paul Otway Senior Subsea Engineer, Jee Limited

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Page 1: Best Practice for Management of Pipeline Integrity by Pigging

Best Practice for Management of Pipeline Integrity by Pigging

12th February 2015

Paul OtwaySenior Subsea Engineer, Jee Limited

Page 2: Best Practice for Management of Pipeline Integrity by Pigging

Agenda

Pigging: What, why and when?Pipeline inspection by MFL toolsPipeline inspection by UT toolsILI tool selection

Page 3: Best Practice for Management of Pipeline Integrity by Pigging

What is ILI and why use it?

In-line inspection• Method of collecting wall thickness or metal loss data to enable

assessment of pipeline fitness for purpose

ILI can provide information on• General and local wall thickness / metal loss• Corrosion• Cracks• Laminations• Weld defects

Best practice for management of pipeline condition• Often in conjunction with operational pigging

Page 4: Best Practice for Management of Pipeline Integrity by Pigging

Operational pigging

Management of internal condition to reduce riskSphering• Liquid sweep in gas lines• Spreading inhibitors

Cleaning• Removal of debris e.g. wax

Page 5: Best Practice for Management of Pipeline Integrity by Pigging

When to do ILI?In

stal

latio

n an

d co

mm

issi

onin

g

Design operational life

Ext

ende

d op

erat

iona

l lif

e

Start-upEnd of

design life

Baseline inspection

Regular re-inspection (frequency is risk-based)

Validation for lifetime extension

Dec

omm

issi

onin

g

Re-validation

End of use

Operational pigging throughout lifecycle if required

Page 6: Best Practice for Management of Pipeline Integrity by Pigging

Pipeline piggability

Not all pipelines are suitable for piggingAvailability of suitable facilities and pig traps is criticalBore range• Single diameter preferable• Multi-diameter lines can be piggable, often need bespoke tools

Minimum bend radii• 5D preferred• 3D possible with most tools• 1.5D possible with a few tools

Pipeline features and restrictions• Back to back bends• Valves• Offtakes (tees & wyes)

Page 7: Best Practice for Management of Pipeline Integrity by Pigging

Agenda

Pigging: What, why and when?Pipeline inspection by MFL toolsPipeline inspection by UT toolsILI tool selection

Page 8: Best Practice for Management of Pipeline Integrity by Pigging

Magnetic flux leakage (MFL) tools

16” PII MFL tool

Page 9: Best Practice for Management of Pipeline Integrity by Pigging

Principle of operation

Brush

MagnetSensor

Brush

Magnet

Brush

MagnetSensor

Brush

Magnet

No defect present

Defect presentDefect

Leakage of field

N

N S

S

Section of pipe wall

Page 10: Best Practice for Management of Pipeline Integrity by Pigging

Output interpretation

Page 11: Best Practice for Management of Pipeline Integrity by Pigging

Agenda

ILI: What, why and when?Pipeline inspection by MFL toolsPipeline inspection by UT toolsILI tool selection

Page 12: Best Practice for Management of Pipeline Integrity by Pigging

Ultrasonic technology (UT) tools

12” NDT ultrasonic ILI tool

Page 13: Best Practice for Management of Pipeline Integrity by Pigging

Principle of operation

Diagram courtesy of NDT Systems & Services

Page 14: Best Practice for Management of Pipeline Integrity by Pigging

Output interpretation

Page 15: Best Practice for Management of Pipeline Integrity by Pigging

Agenda

Pigging: What, why and when?Pipeline inspection by MFL toolsPipeline inspection by UT toolsILI technology selection

Page 16: Best Practice for Management of Pipeline Integrity by Pigging

Operational constraints

What is the available drive medium?• UT – needs liquid couplant• MFL – can operate in gas or liquid

What are the process conditions during pigging and how controllable are they?• Flowrate

• UT – requires low, controlled flowrate (c. 0.5 – 1.0 m/s)• MFL – can tolerate higher flowrates and fluctuation (up to 4.0 m/s)

• Pressure• UT and MFL – most tools c. 120-150 bar, some up to 300-400 bar

• Temperature• UT and MFL – most operate up to c. 65°C

Page 17: Best Practice for Management of Pipeline Integrity by Pigging

Defect detection requirements

What is the pipeline construction?• MFL – can only magnetise carbon steel lines• UT – can measure wall loss in most materials (CS, duplex, CRA)

What are the specific degradation mechanisms and threats to the pipeline?• Global metal loss – MFL or UT generally suitable• Pitting – UT provides higher resolution data• Cracking – specific tool setup required whether UT or MFL

Page 18: Best Practice for Management of Pipeline Integrity by Pigging

Scope of inspection

What sections of the pipeline can be inspected?• Full pipeline from trap to trap

• Traditional MFL or UT tool suitable• Local riser/spools only

• Crawler tool (usually UT)• Bi-directional ILI tool (MFL or UT)

Page 19: Best Practice for Management of Pipeline Integrity by Pigging

Thank you for listening

Paul Otway

Best Practice for Management of Pipeline Integrity by Pigging