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CATHODIC PROTECTION
MONITORING EFFECTIVENESS
By
Dr M B Mishra
Corrosion Consultant
Presented At
O.I.S.D. Workshop
Critical Safety Issues In Marketting
Operations
Striving For Improved Performance
January,16,2014
CORROSION
[ METAL DEGRADATON DUE TO REACTING WITH
ENVIRONMENT ]
RAVAGES VALUABLE ASSETS SUCH AS :
PIPELINES [UNDERGROUND / ABOVE GROUND]
TANKS
[UNDERGROUND/ABOVE GRADE/MOUNDED]
RUTOR STEEL IN CONCRETE
STRUCTURALS
OTHER ASSETS [PACE MAKER,JOINTS,DENTAL]
CORROSION
RESULTS IN RUPTURE
CAUSING
HAZARDS – FIRE,POLLUTION,FATALITY
[HUMAN,FLORA,FAUNA]
BESIDES
ECONONMIC LOSSES
DUE TO
PRODUCT LOSS,REPAIR COST,DOWN TIME &
COMPENSATION
5
PIPELINE FAILURES
• ONCE PIPELINE LEAK
COMMENCES IT
PROGRESSES IN
EXPONENTIAL RATE.
• CORROSION CAN BE
CONTROLLED
WITHIN ACCEPTABLE
LIMITS BY
APPLICATION OF
CATHODIC
PROTECTION FROM
CONSTRUCTION
STAGE.
FAILURE RATE COMPARISION
PITTING NEAR THE JOINT AREA
PIPELINE COATINGS AFTER EXCAVATION
Nace Corrosion 2004
TANK BOTTOM PLATE PITTING CORROSION
PIPE RUPTURE
SEVERE CORROSION
FAILURE FROM THE SEAM
CORROSION CONTROL
• THE EFFORT IS TO MINIMIZE CORROSION,A
NATURAL PHENOMENON,TO AN ACCEPTABLE
LIMIT SO THAT ECONOMIC VIABILITY IS
ENSURED
• THIS IS BEST ACHIEVED BY PROVIDING A
SUITABLE COATING SUPPLEMENTED BY A
COMPATIBLE CATHODIC PROTECTION SYSTEM
AS A COMPOSITE
CORROSION PROTECTION SYSTEM
CORROSION
• Corrosion Reactions :
• Fe ↔ Fe ++ + 2e- Anodic Reaction (1)
• 2e- + 2H+ ↔ 2H →H2
• Or H2O +2e- +½ O2 →2(OH-)
• Fe++ + 2OH- -------› Fe (OH)2
• Fe (OH)2 + ½ O2 +½ H2 O--------› Fe (OH)3
[Green Colour]
• 2Fe (OH)3 --------›2 Fe 2 O 3 +3 H2 O
[Rust, Brown colour]
•
16
17
DISCRETE IMPRESSED CURRENT ANODES
18
EFFECTS OF SOIL RESISTIVITY ON CURRENT
DISTRIBUTION
19
EFFECTS OF SOIL PROPERTIES ON CURRENT
DISTRIBUTION
20
CATHODIC PROTECTION
• IMPRESSED CURRENT CATHODIC
PROTECTION SYSTEM IS THE SECOND
METHOD AVAILABLE TO PROTECT THE
UNDERGROUND UTILITIES FOR LONGER
DURATIONS (UPTO 50 YEARS) AS IN THIS THE
POWER SOURCE & HENCE THE PROTECTIVE
CURRENT CAN BE CONTROLLED AS
REQUIRED TO PROVIDE ADEQUATE
PROTECTION THROUGHOUT. THIS INVOLVES
USE OF FOLLOWING ANODES;
21
22
23
REFERENCE ELECTRODES
• TO MEASURE REPRODUCIBLE [P-S-P] THE
FOLLOWING REFERENCE HALF CELLARE IN
USE
Cu-CuSO4(V) Zn(V) Ag-AgCl(V)
(-)0.75 (+)0.35 (-)0.7
(-)0.85 (+)0.25 (-)0.8
(-)1.0 (+)0.1 (-)0.95
(-)1.2 (-)0.1 (-)1.15
(-)1.5 (-)0.4 (-)1.45
(-)2.0 (-)0.9 (-)1.95
24
CRITERIA FOR CATHODIC PROTECTION
• THREE PRIMARY CRITERIA FOR CATHODIC
PROTECTION OF UNDERGROUND OR
SUBMERGED STEEL OR CAST IRON PIPE
ARE :
(-)0.85V w.r.t. Cu-CuSO4 HALF CELL
REFERENCE ELECTRODE WITH
PROTECTIVE CURRENT FOR CATHODIC
PROTECTION SYSTEM-APPLIED (ON).
(-)0.85V w.r.t. Cu-CuSO4 HALF CELL
REFERENCE ELECTRODE WITH
PROTECTIVE CURRENT FOR CATHODIC
PROTECTION SYSTEM-NOT APPLIED
(INSTANT OFF).
25
CRITERIA FOR CATHODIC PROTECTION
100mV POLARISATION VOLTAGE.
300mV SHIFT FROM NATURAL
POTENTIALS WITH PROTECTIVE
CURRENT APPLIED (ON).
26
27
POTENTIAL DISTRIBUTION ALONG THE
PIPELINE
28
PIPELINE COATING AND CATHODIC
PROTECTION SYSTEM ASSESSMENT
29
PIPELINE COATING AND CATHODIC
PROTECTION SYSTEM ASSESSMENT
30
CATHODIC PROTECTION FOR ABOVE GROUND
STORAGE TANK BOTTOMS
31
CATHODIC PROTECTION FOR ABOVE GROUND
STORAGE TANK BOTTOMS
32
33
CATHODIC PROTECTION FOR ABOVE GROUND
STORAGE TANK BOTTOMS
Nace Corrosion 2004
Installation of the Anodeflex System. It provides Cathodic Protection on every
point without causing any under or overprotection
COATING AND CATHODIC
PROTECTION SYSTEM ASSESSMENT
Nace Corrosion 2004
REF. ELECTRODE
CONCEPTUAL DESIGN OF CP FOR
BULLET TANKS
SAND MOUND
TO
TR UNIT
POLYMERIC ANODE
LPG BULLET
INLINE
SPLICE
CONNECTING
CABLES
Nace Corrosion 2004
LONG LINE POLYMERIC ANODE SYSTEM FOR
MOUNDED BULLET
Nace Corrosion 2004
CONCEPTUAL DESIGN OF CP FOR BULLET TANKS
POLYMERIC ANODE
LPG BULLET
INLINE
SPLICE
CONNECTING
CABLES
TR
UNIT
AJB
CJB
REJB
+ ve
- ve
Ref Cell
ISOLATING JOINT
POLARIZATON
CELL
EARTHING
Nace Corrosion 2004
REF. ELECTRODE
CONCEPTUAL DESIGN OF CP FOR BULLET TANKS
BULLET-2
SAND MOUND
POLYMERIC ANODE
BULLET-1
Corrosion Monitoring
• Cathodic Protection Of Assets Ensures
Prevention of Loss of Metal to Earth due to
Soil-side Corrosion
• This is a Dynamic Process & Requires Close
Monitoring of C P Parameters
• If C P System Fails or is not performing as per
Design,Corrosion Protection is In-Effective
• The Efficacy Of C P depends on continuous
Monitoring to Ensure Desired Level of
Parameters
Corrosion Monitoring
• Pipe to Soil Potential [P-S-P] is Monitored
[P-S-P] Vs CSE to be in the Range
(-)0.85 Minimum to (-) 1.5 V Maximum when Anaerobic
Bacteria are absent [No SRB]
and (-)0.95 Minimum to (-) 1.5 V Maximum when [SRB]are
present
Corrosion Monitoring
• Only High Impedance Voltmeter to be used
• Equipment of Standard make & proven
capability to be used
• Multichannel Recording capability
• The Record should be field verifiable through
computer display in field
• Recorded Data should be Downloaded
Corrosion Monitoring
• For this Reason it is vitally important
that utility Operators Maintain
accurate,Integrated Information on their
utility system from construction and
Installation through
Operataion,Inspection & Maintenance
Corrosion Monitoring
• The Key to Integrity Management
Programme is :
1. To Know where Potential
Problems Lie
2. To Understand How Severe the
Problem might be
3. How Best to Manage these
Problems
Corrosion Monitoring
• Survey Data to be Collated for Deciphering
Problem Areas & Effective Measures to
counter the problems detected
• Post Mitigative Measures installation Further
surveys to evaluate Adequacy of installed
mitigative measures
• Frequency of such surveys thereafter
periodically
Corrosion Monitoring
Conclusion
• The Safety factor question has been settled
many times by Research,
Experience and Tests.
• In service underground utilities are safe if
they are maintained properly and protected
against Corrosion,that Devours the Vitals
unchecked and undetected,and third party
damage.
Acknowledgements
Grateful Thanks To O.I.S.D.
For this Opportunity to Share My Perceptions
& Experience on Cathodic Protection
Monitoring With Such August Audience
Comprising Of
Engineering,Consultancy,Operations,
Maintenance,Inspection,Cosntruction &
Trouble Shooting Fraternity.
THANKS
•

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cathodic protection system.pdf

  • 1. CATHODIC PROTECTION MONITORING EFFECTIVENESS By Dr M B Mishra Corrosion Consultant Presented At O.I.S.D. Workshop Critical Safety Issues In Marketting Operations Striving For Improved Performance January,16,2014
  • 2. CORROSION [ METAL DEGRADATON DUE TO REACTING WITH ENVIRONMENT ] RAVAGES VALUABLE ASSETS SUCH AS : PIPELINES [UNDERGROUND / ABOVE GROUND] TANKS [UNDERGROUND/ABOVE GRADE/MOUNDED] RUTOR STEEL IN CONCRETE STRUCTURALS OTHER ASSETS [PACE MAKER,JOINTS,DENTAL]
  • 3. CORROSION RESULTS IN RUPTURE CAUSING HAZARDS – FIRE,POLLUTION,FATALITY [HUMAN,FLORA,FAUNA] BESIDES ECONONMIC LOSSES DUE TO PRODUCT LOSS,REPAIR COST,DOWN TIME & COMPENSATION
  • 4.
  • 5. 5 PIPELINE FAILURES • ONCE PIPELINE LEAK COMMENCES IT PROGRESSES IN EXPONENTIAL RATE. • CORROSION CAN BE CONTROLLED WITHIN ACCEPTABLE LIMITS BY APPLICATION OF CATHODIC PROTECTION FROM CONSTRUCTION STAGE.
  • 7. PITTING NEAR THE JOINT AREA
  • 9. Nace Corrosion 2004 TANK BOTTOM PLATE PITTING CORROSION
  • 13.
  • 14. CORROSION CONTROL • THE EFFORT IS TO MINIMIZE CORROSION,A NATURAL PHENOMENON,TO AN ACCEPTABLE LIMIT SO THAT ECONOMIC VIABILITY IS ENSURED • THIS IS BEST ACHIEVED BY PROVIDING A SUITABLE COATING SUPPLEMENTED BY A COMPATIBLE CATHODIC PROTECTION SYSTEM AS A COMPOSITE CORROSION PROTECTION SYSTEM
  • 15. CORROSION • Corrosion Reactions : • Fe ↔ Fe ++ + 2e- Anodic Reaction (1) • 2e- + 2H+ ↔ 2H →H2 • Or H2O +2e- +½ O2 →2(OH-) • Fe++ + 2OH- -------› Fe (OH)2 • Fe (OH)2 + ½ O2 +½ H2 O--------› Fe (OH)3 [Green Colour] • 2Fe (OH)3 --------›2 Fe 2 O 3 +3 H2 O [Rust, Brown colour] •
  • 16. 16
  • 18. 18 EFFECTS OF SOIL RESISTIVITY ON CURRENT DISTRIBUTION
  • 19. 19 EFFECTS OF SOIL PROPERTIES ON CURRENT DISTRIBUTION
  • 20. 20 CATHODIC PROTECTION • IMPRESSED CURRENT CATHODIC PROTECTION SYSTEM IS THE SECOND METHOD AVAILABLE TO PROTECT THE UNDERGROUND UTILITIES FOR LONGER DURATIONS (UPTO 50 YEARS) AS IN THIS THE POWER SOURCE & HENCE THE PROTECTIVE CURRENT CAN BE CONTROLLED AS REQUIRED TO PROVIDE ADEQUATE PROTECTION THROUGHOUT. THIS INVOLVES USE OF FOLLOWING ANODES;
  • 21. 21
  • 22. 22
  • 23. 23 REFERENCE ELECTRODES • TO MEASURE REPRODUCIBLE [P-S-P] THE FOLLOWING REFERENCE HALF CELLARE IN USE Cu-CuSO4(V) Zn(V) Ag-AgCl(V) (-)0.75 (+)0.35 (-)0.7 (-)0.85 (+)0.25 (-)0.8 (-)1.0 (+)0.1 (-)0.95 (-)1.2 (-)0.1 (-)1.15 (-)1.5 (-)0.4 (-)1.45 (-)2.0 (-)0.9 (-)1.95
  • 24. 24 CRITERIA FOR CATHODIC PROTECTION • THREE PRIMARY CRITERIA FOR CATHODIC PROTECTION OF UNDERGROUND OR SUBMERGED STEEL OR CAST IRON PIPE ARE : (-)0.85V w.r.t. Cu-CuSO4 HALF CELL REFERENCE ELECTRODE WITH PROTECTIVE CURRENT FOR CATHODIC PROTECTION SYSTEM-APPLIED (ON). (-)0.85V w.r.t. Cu-CuSO4 HALF CELL REFERENCE ELECTRODE WITH PROTECTIVE CURRENT FOR CATHODIC PROTECTION SYSTEM-NOT APPLIED (INSTANT OFF).
  • 25. 25 CRITERIA FOR CATHODIC PROTECTION 100mV POLARISATION VOLTAGE. 300mV SHIFT FROM NATURAL POTENTIALS WITH PROTECTIVE CURRENT APPLIED (ON).
  • 26. 26
  • 28. 28 PIPELINE COATING AND CATHODIC PROTECTION SYSTEM ASSESSMENT
  • 29. 29 PIPELINE COATING AND CATHODIC PROTECTION SYSTEM ASSESSMENT
  • 30. 30 CATHODIC PROTECTION FOR ABOVE GROUND STORAGE TANK BOTTOMS
  • 31. 31 CATHODIC PROTECTION FOR ABOVE GROUND STORAGE TANK BOTTOMS
  • 32. 32
  • 33. 33 CATHODIC PROTECTION FOR ABOVE GROUND STORAGE TANK BOTTOMS
  • 34. Nace Corrosion 2004 Installation of the Anodeflex System. It provides Cathodic Protection on every point without causing any under or overprotection COATING AND CATHODIC PROTECTION SYSTEM ASSESSMENT
  • 35. Nace Corrosion 2004 REF. ELECTRODE CONCEPTUAL DESIGN OF CP FOR BULLET TANKS SAND MOUND TO TR UNIT POLYMERIC ANODE LPG BULLET INLINE SPLICE CONNECTING CABLES
  • 36. Nace Corrosion 2004 LONG LINE POLYMERIC ANODE SYSTEM FOR MOUNDED BULLET
  • 37. Nace Corrosion 2004 CONCEPTUAL DESIGN OF CP FOR BULLET TANKS POLYMERIC ANODE LPG BULLET INLINE SPLICE CONNECTING CABLES TR UNIT AJB CJB REJB + ve - ve Ref Cell ISOLATING JOINT POLARIZATON CELL EARTHING
  • 38.
  • 39. Nace Corrosion 2004 REF. ELECTRODE CONCEPTUAL DESIGN OF CP FOR BULLET TANKS BULLET-2 SAND MOUND POLYMERIC ANODE BULLET-1
  • 40. Corrosion Monitoring • Cathodic Protection Of Assets Ensures Prevention of Loss of Metal to Earth due to Soil-side Corrosion • This is a Dynamic Process & Requires Close Monitoring of C P Parameters • If C P System Fails or is not performing as per Design,Corrosion Protection is In-Effective • The Efficacy Of C P depends on continuous Monitoring to Ensure Desired Level of Parameters
  • 41. Corrosion Monitoring • Pipe to Soil Potential [P-S-P] is Monitored [P-S-P] Vs CSE to be in the Range (-)0.85 Minimum to (-) 1.5 V Maximum when Anaerobic Bacteria are absent [No SRB] and (-)0.95 Minimum to (-) 1.5 V Maximum when [SRB]are present
  • 42. Corrosion Monitoring • Only High Impedance Voltmeter to be used • Equipment of Standard make & proven capability to be used • Multichannel Recording capability • The Record should be field verifiable through computer display in field • Recorded Data should be Downloaded
  • 43. Corrosion Monitoring • For this Reason it is vitally important that utility Operators Maintain accurate,Integrated Information on their utility system from construction and Installation through Operataion,Inspection & Maintenance
  • 44. Corrosion Monitoring • The Key to Integrity Management Programme is : 1. To Know where Potential Problems Lie 2. To Understand How Severe the Problem might be 3. How Best to Manage these Problems
  • 45. Corrosion Monitoring • Survey Data to be Collated for Deciphering Problem Areas & Effective Measures to counter the problems detected • Post Mitigative Measures installation Further surveys to evaluate Adequacy of installed mitigative measures • Frequency of such surveys thereafter periodically
  • 46. Corrosion Monitoring Conclusion • The Safety factor question has been settled many times by Research, Experience and Tests. • In service underground utilities are safe if they are maintained properly and protected against Corrosion,that Devours the Vitals unchecked and undetected,and third party damage.
  • 47. Acknowledgements Grateful Thanks To O.I.S.D. For this Opportunity to Share My Perceptions & Experience on Cathodic Protection Monitoring With Such August Audience Comprising Of Engineering,Consultancy,Operations, Maintenance,Inspection,Cosntruction & Trouble Shooting Fraternity. THANKS •