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NACE International, 10,000
Lakes Pipeline Corrosion
Control Seminar
BASIC CORROSION SERIES, ROOM C
TUESDAY, FEBRUARY 4, 2020
Advanced Cathodic Protection, 2:00PM – 2:50PM
Eric Langelund
Piping & Corrosion Specialties, Inc.
Main Objectives
 Understanding of the Corrosion Process and
the Units of Measure
 The natural process of Corrosion
 The four elements of the Corrosion process
 Ohms Law
 What is the Polarization Process?
 Electrical and Chemical Process
 How do we know, if we are being Cathodically
Protected?
 Measurements methodology
 Equipment Used
Definition of Corrosion
 Defined as the electrical chemical
degradation of metal as a result of a
reaction with its surrounding environment
 The tendency of the metal to return to its
natural state
The Natural Process of Corrosion
Iron Ore is electrically charged through the molding process.
Once formed into a pipeline, and placed into the ground, the pipe will
lose it’s electrical charge and try to resort back to it’s natural state.
IRON OXIDE BLAST FURNACE BESSEMER
PIPE MILL STEEL PIPE
PIPE CORRODING
IRON OXIDE
REFINING PROCESS
CORROSION PROCESS
 The Basic Four Elements to create a galvanic
corrosion cell
 Anode – on the galvanic series charts, the metal
that is the most negative charged and less noble
(The area were corrosion will occur)
 Cathode – on the galvanic series charts, the metal
that is the most positive charged and more noble
(The area that will be cathodically protected)
 Electrolyte – any substance that can conduct
electricity, the surrounding environment of the
anode and the cathode
 Metallic Connection – any metallic connection
between the anode and the cathode that exist
The Electrical Chemical Process of
Corrosion
 Conventional Current Flow
 Known as the flow of electrical current for design
and theory purpose
 Where current will flow from the “+” to “-” direction
 Electron Flow
 Contribute to ion movement
 The movement of the electrons from the “-” to the
“+” direction
 Opposite of Conventional Current Flow
The Electrical-Chemical Process of
Corrosion
 Corrosion rate can be measured by the
potential difference between the Anode and
the Cathode
 The greater of the potential difference, the
greater of the corrosion rate between the
Anode and the Cathode
 For an example,
 If the anode is measured at -1.700 V and the
cathode is measured at -.600 V
 The potential difference is equal to 1.100 V or 1100
milivolts
The Electrical-Chemical Process of
Corrosion
The Electrical-Chemical Process of
Corrosion
Cathode Anode
Positive Negative
Metallic connection
Electrolyte
Conventional
Current Flow
(positive)”+”
to
(negative)”-”
Corrosion
Golden Rule
Any time
Current
discharge
from a
metallic
surface, then
metal loss will
occur
(Corrosion)
-.600 V -1.700 V
The Electrical-Chemical Process of
Corrosion
Cathode Anode
Positive Negative
Metallic connection
Electrolyte
Electron Flow
HO-
Electron Flow
(negative)”-”
to
(positive)”+”
HO-
HO-
HO-
H+
H+
H+
H+
H2O
H2O
H2O
e-
e-
e-e-
e-
e-
e-
Fe+
Fe+
Fe+
Fe+
Fe+
-.600 V -1.700 V
H2O (water molecule)
The Electrical-Chemical Process of
Corrosion
Cathode Anode
Positive Negative
Metallic connection
Electrolyte
Electron Flow
HO-
HO-
HO-
HO-
H+
H+
H+
H+
H2O
H2O
H2O
e-
e-
e-e-
e-
e-
e-
Fe+
Fe+
Fe+
Fe+
Fe+
As the Cathode
gains the “e-”
(electrons), it
approaches to a
more negative
state
-1.000 V
-
+
The Electrical-Chemical Process of
Corrosion
Cathode Anode
Positive Negative
Metallic connection
Electrolyte
Electron Flow
HO-
HO-
HO-
HO-
H+
H+
H+
H+
H2O
H2O
H2O
e-
e-
e-e-
e-
e-
e-
Fe+
Fe+
Fe+
Fe+
Fe+
As the Anode
loses the “e-”
(electrons), it
approaches to a
more positive state
-1.200 V
-
+
The Electrical-Chemical Process of
Corrosion
Cathode Anode
Positive Negative
Metallic connection
Electrolyte
Electron Flow
HO-
HO-
HO-
HO-
H+
H+
H+
H+
H2O
H2O
H2O
e-
e-
e-e-
e-
e-
e-
Fe+
Fe+
Fe+
Fe+
Fe+
-1.200 V-1.000 V =
Polarization
Process
The Cathode
becomes more
Negative
The Anode
becomes more
positive
Polarization Process
Cathode Anode
Positive Negative
Electrolyte
Electron Flow
HO-
HO-
HO-
HO-
H+
H+
H+
H+
H2O
H2O
H2O
e-
e-
e-e-
e-
e-
e-
Fe+
Fe+
Fe+
Fe+
Fe+
-1.200 V-1.000 V =
Now, what is
the potential
difference ?
Polarization Process
 Remember –
 Corrosion rate can be measured by the potential
difference between the Anode and the Cathode
 The greater of the potential difference, the greater
of the corrosion rate between the Anode and the
Cathode
 Earlier example,
 If the anode is measured at -1.700 V and the
cathode is measured at -.600 V
 The potential difference is equal to 1.100 V or 1100
milivolts
Polarization Process
 Earlier example,
 If the anode is measured at -1.700 V and the cathode is
measured at -.600 V
 The potential difference is equal to 1.100 V or 1100 milivolts
 Now,
 The anode is measured at -1.200 V and the cathode is
measured at -1.000 V
 The potential difference is equal to .200 V or 200 milivolts
 Conclusion –
 Polarization will reduce the rate of corrosion on the anode
over time as the Cathode and the Anode approach an equal
potential, due to the loss and gain of electrons
Polarization Review - Diagram
The “True Criterion” for Cathodic
Protection
 Polarization of the Cathodes to the open
circuit potential to the anodes is the true
criterion for cathodic protection (stopping
the corrosion reaction)
How are Polarization rates affected
by Coating Characteristics
 Bare Pipe
 Will polarize and de-polarize quickly due to
larger bare metallic surface area
 Well - Coated Pipe
 Will polarize and de-polarize slowly due to a
much smaller bare metallic surface area
How are Polarization rates affected
by Coating Characteristics
Holiday
CP only protects the coating defected areas or best
known as holidays (bare area of the well coated pipeline)
Current Measurement - CP
 The following Current density is
considered
 Good soil (moist all year round) or fresh water – 1
mA sq ft
 Clay (partially moist soil) – 2 mA to 3 mA sq ft
 Sandy or Dry soils – 4 mA to 8 mA sq ft
 For an example –
Current Measurement - CP
6” coated pipeline at a 12,000’ length with .5% coating
defect.
.005 • 20,820 sq ft (total surface area) = 104.1 sq ft of bare
area A = 104.1 sq ft
i = 1 mA per sq ft
.001 • 104.1 = .104Amps or 104mA
Answer for I is 104mA If bare pipe was used then the
current requirement would be much
greater, in the range of 21 amps vs.
.1 of an amp
 In Summary,
 The bare pipe will take a large amount of CP
current to cathodically protect
 Polarization will take longer to achieved
 Therefore, the depolarization will be longer as well
 The well coated pipeline will take much less of CP
current to cathodically protect
 Polarization will be quicker to achieved
 Therefore, the depolarization will be quicker as well
Current Measurement - CP
 Remember, CP is achieved by polarizing the
Cathode to the open potential of the Anode
 On the surface of the metallic pipeline, a
galvanic corrosion cell can form with the
following criteria’s
 Anodic area (high negative potential),
 Cathodic area (Low negative potential or more
positive potential),
 Metallic connection (pipeline structure)
 Electrolyte (surrounding environment)
Polarization reduces VΔ along the
Structure
Galvanic Corrosion Cell on
Pipelines
AnodeCathode
Microscopic Corrosion Cell
on the Surface of a
Pipeline Remember the golden
rule of Corrosion – @
the point of current
discharge, metal loss
will occur (Corrosion)
 Applying CP currents to the surface
 We attempt to create the same potential
between the anode and the cathode
 If No potential difference exist, then there is
no driving force for the electrons to move, in
which will result in stopping metal discharge
(corrosion)
 Let’s look at this process closer
Polarization reduces VΔ along the
Structure
-.5 -.6 -.65 -.6 -.7 -.58
-.58 -.6 -.65 -.6 -.7 -.58
-.6 -.6 -.65 -.6 -.7 -.6
-.65 -.65 -.65 -.65 -.7 -.65
-.7 -.7 -.7 -.7 -.7 -.7
Static
Potentials
Corrosion
Mitigated
P
O
L
A
R
I
Z
A
T
I
O
N
Polarization reduces VΔ along the
Structure
Once the surface area has polarized to the same potential,
there is no “Anode” or “Cathode”, Cathodic Protection is
achieved.
1. Static Potential
2. Most positive sides
polarize first
3. Next most positive
sites polarize
4. Last most positive
site polarize
5. All sites polarized
How do we know, if we are being
Cathodically Protected?
 Structure to electrolyte potential
 Typically made at grade
 Voltmeter and reference electrode
 High input impedance voltmeter
 Compare potentials measured to
“criteria”
Pipe to Soil Potential Measurements
-.900 v
+_
Polarization Film
Reference Electrode
Voltmeters
 Analog vs. Digital
 High Input Impedance
 Field Durable
 Storage Capabilities
Voltmeter identifies More Noble
Metals
 If a voltmeter is connected such that
 the positive terminal is to the more noble
 metal and the negative terminal to the
 more active metal, the reading is
positive.
Noble Active
+ _
Voltage
measurement
is positive
.600 V
Voltmeter identifies More Noble
Metals
Pipe-to-Soil Potential Measurement
.900 v
+
_
Pipe
Electrolyte
Reference
Cell
Voltmeter Meter display is a
postive reading.
Record a negative
P/S Potential.
-.900 v
+
_
Pipe
Electrolyte
Reference
Cell
Voltmeter Meter display is a
negative reading.
Record a negative
P/S Potential.
Pipe To Soil Measurement
Be aware of the connection of the
leads to indicate a “+” or “-” reading
The Common Different Types of
Reference Electrodes
 Calomel
 Libratory use
 Silver/Silver Chloride
 Sea water use
 Zinc
 Sea water use
 Copper-Copper Sulfate
 Regular soil & neutral waters
 Most popular use in the field
Most Common for Field Use
 Copper – Copper Sulfate
 Rugged for field use
 Consistent measurements in neutral waters
and soil environments
 Contains
 Copper Rod
 Copper Crystals
 Copper solutions (antifreeze material) or distilled
water
Copper Rod
Saturated Copper
Sulfate Solution
Un-dissolved Copper
Sulfate Crystals
Porous
Plug
Visual
Window
Copper – Copper Sulfate
Reference Cell
Copper – Copper Sulfate Reference
Cell (Half Cell)
Cathode Anode
Positive Negative
Electrolyte
Copper-
Copper
Sulfate
reference
cell
Steel
Pipeline
Test station wire
The copper –
copper sulfate
reference cell
represents half of
the corrosion
cell, therefore
gets the name
“Half Cell”
Care of the CSE
 Keep the CSE clean
 Keep the cap on the tip to prevent dryness and
cracking or loss of solution
 Keep free of contamination, the tip is porous so
therefore, contaminates can pass in the CSE solution
 Perform calibration with a virgin half cell on regular
bases
 Shield clear window from sunlight, due to heat or UV
rays will cause inaccuracy in readings (normally use
black electrical tape)
 Adjust readings according to temperature
Criteria’s of CP
 .850- V CSE with current applied (IR
drop consideration)
 .850- V CSE Polarized (Instant off)
 100 mV Polarization decay
Criteria - .850– V CSE with Current
Applied
 Structure to electrolyte potential with a high
impedance volt meter and copper-copper
sulfate reference cell
 IR drop is considered by
 Placing the reference cell directly over the pipeline
as possible
 As close to the pipeline as possible
 Eliminating the resistance at the point of the
reference cell contact as much as possible
 Wetting the soil
 Removing the sod
Criteria - .850 – V CSE Polarization
 Structure to electrolyte potential with a
high impedance volt meter and copper-
copper sulfate reference cell
 Switching off the CP currents
 Measure the IR drop
 @ the point of polarization decay begins,
reading is used for criteria
Criteria - .850 – V CSE Polarization
Criteria – 100 mV Polarization
Decay
 Structure to electrolyte potential with a
high impedance volt meter and copper-
copper sulfate reference cell
 Switching off the CP currents
 Measure the IR drop (instant off)
 @ the point of polarization decay,
measure until 100 mV depolarization has
been achieved
Criteria – 100 mV Polarization
Decay
Summary
 Corrosion is the degradation of a material due
to a reaction with its’ environment
 CP is achieved when the cathodic sites are
polarized in the electronegative direction to the
potential of the most anodic sites.
 Only practical method to determine this is by
surface structure to electrolyte potentials
PIPELINE INSTALLATION
ANODE INSTALLATION
RECTIFIER
REMOTE MONITORING
DAGB
CONSUMED ANODE
CONVENTIONAL GROUNDBED
REVERSE CURRENT SWITCH
DRAINAGE SWITCH
PETROLEUM PIPE SPAN
ANODE IN HOLE
ANODES AROUND UST
WATER VALVE REPAIR
ANODE INSTALLATION
GRAPHITIZATION
PCCP
COPPER
CONTINUITY BOND
CONTINUITY BOND
CI and DI WALL
THICKNESS
REBAR COATED
DAMAGED COATING
DAMAGED COATING
POLYETHELENE
CONTINUITY BONDS
SAFETY FIRST
THANK YOU
 CATHOLIC PROTECTION
76

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Advanced Cathodic Protection - CP Series - Eric Langelund

  • 1. NACE International, 10,000 Lakes Pipeline Corrosion Control Seminar BASIC CORROSION SERIES, ROOM C TUESDAY, FEBRUARY 4, 2020 Advanced Cathodic Protection, 2:00PM – 2:50PM Eric Langelund Piping & Corrosion Specialties, Inc.
  • 2. Main Objectives  Understanding of the Corrosion Process and the Units of Measure  The natural process of Corrosion  The four elements of the Corrosion process  Ohms Law  What is the Polarization Process?  Electrical and Chemical Process  How do we know, if we are being Cathodically Protected?  Measurements methodology  Equipment Used
  • 3. Definition of Corrosion  Defined as the electrical chemical degradation of metal as a result of a reaction with its surrounding environment  The tendency of the metal to return to its natural state
  • 4. The Natural Process of Corrosion Iron Ore is electrically charged through the molding process. Once formed into a pipeline, and placed into the ground, the pipe will lose it’s electrical charge and try to resort back to it’s natural state. IRON OXIDE BLAST FURNACE BESSEMER PIPE MILL STEEL PIPE PIPE CORRODING IRON OXIDE REFINING PROCESS CORROSION PROCESS
  • 5.  The Basic Four Elements to create a galvanic corrosion cell  Anode – on the galvanic series charts, the metal that is the most negative charged and less noble (The area were corrosion will occur)  Cathode – on the galvanic series charts, the metal that is the most positive charged and more noble (The area that will be cathodically protected)  Electrolyte – any substance that can conduct electricity, the surrounding environment of the anode and the cathode  Metallic Connection – any metallic connection between the anode and the cathode that exist The Electrical Chemical Process of Corrosion
  • 6.  Conventional Current Flow  Known as the flow of electrical current for design and theory purpose  Where current will flow from the “+” to “-” direction  Electron Flow  Contribute to ion movement  The movement of the electrons from the “-” to the “+” direction  Opposite of Conventional Current Flow The Electrical-Chemical Process of Corrosion
  • 7.  Corrosion rate can be measured by the potential difference between the Anode and the Cathode  The greater of the potential difference, the greater of the corrosion rate between the Anode and the Cathode  For an example,  If the anode is measured at -1.700 V and the cathode is measured at -.600 V  The potential difference is equal to 1.100 V or 1100 milivolts The Electrical-Chemical Process of Corrosion
  • 8. The Electrical-Chemical Process of Corrosion Cathode Anode Positive Negative Metallic connection Electrolyte Conventional Current Flow (positive)”+” to (negative)”-” Corrosion Golden Rule Any time Current discharge from a metallic surface, then metal loss will occur (Corrosion) -.600 V -1.700 V
  • 9. The Electrical-Chemical Process of Corrosion Cathode Anode Positive Negative Metallic connection Electrolyte Electron Flow HO- Electron Flow (negative)”-” to (positive)”+” HO- HO- HO- H+ H+ H+ H+ H2O H2O H2O e- e- e-e- e- e- e- Fe+ Fe+ Fe+ Fe+ Fe+ -.600 V -1.700 V H2O (water molecule)
  • 10. The Electrical-Chemical Process of Corrosion Cathode Anode Positive Negative Metallic connection Electrolyte Electron Flow HO- HO- HO- HO- H+ H+ H+ H+ H2O H2O H2O e- e- e-e- e- e- e- Fe+ Fe+ Fe+ Fe+ Fe+ As the Cathode gains the “e-” (electrons), it approaches to a more negative state -1.000 V - +
  • 11. The Electrical-Chemical Process of Corrosion Cathode Anode Positive Negative Metallic connection Electrolyte Electron Flow HO- HO- HO- HO- H+ H+ H+ H+ H2O H2O H2O e- e- e-e- e- e- e- Fe+ Fe+ Fe+ Fe+ Fe+ As the Anode loses the “e-” (electrons), it approaches to a more positive state -1.200 V - +
  • 12. The Electrical-Chemical Process of Corrosion Cathode Anode Positive Negative Metallic connection Electrolyte Electron Flow HO- HO- HO- HO- H+ H+ H+ H+ H2O H2O H2O e- e- e-e- e- e- e- Fe+ Fe+ Fe+ Fe+ Fe+ -1.200 V-1.000 V = Polarization Process The Cathode becomes more Negative The Anode becomes more positive
  • 13. Polarization Process Cathode Anode Positive Negative Electrolyte Electron Flow HO- HO- HO- HO- H+ H+ H+ H+ H2O H2O H2O e- e- e-e- e- e- e- Fe+ Fe+ Fe+ Fe+ Fe+ -1.200 V-1.000 V = Now, what is the potential difference ?
  • 14. Polarization Process  Remember –  Corrosion rate can be measured by the potential difference between the Anode and the Cathode  The greater of the potential difference, the greater of the corrosion rate between the Anode and the Cathode  Earlier example,  If the anode is measured at -1.700 V and the cathode is measured at -.600 V  The potential difference is equal to 1.100 V or 1100 milivolts
  • 15. Polarization Process  Earlier example,  If the anode is measured at -1.700 V and the cathode is measured at -.600 V  The potential difference is equal to 1.100 V or 1100 milivolts  Now,  The anode is measured at -1.200 V and the cathode is measured at -1.000 V  The potential difference is equal to .200 V or 200 milivolts  Conclusion –  Polarization will reduce the rate of corrosion on the anode over time as the Cathode and the Anode approach an equal potential, due to the loss and gain of electrons
  • 17. The “True Criterion” for Cathodic Protection  Polarization of the Cathodes to the open circuit potential to the anodes is the true criterion for cathodic protection (stopping the corrosion reaction)
  • 18. How are Polarization rates affected by Coating Characteristics  Bare Pipe  Will polarize and de-polarize quickly due to larger bare metallic surface area  Well - Coated Pipe  Will polarize and de-polarize slowly due to a much smaller bare metallic surface area
  • 19. How are Polarization rates affected by Coating Characteristics Holiday CP only protects the coating defected areas or best known as holidays (bare area of the well coated pipeline)
  • 20. Current Measurement - CP  The following Current density is considered  Good soil (moist all year round) or fresh water – 1 mA sq ft  Clay (partially moist soil) – 2 mA to 3 mA sq ft  Sandy or Dry soils – 4 mA to 8 mA sq ft
  • 21.  For an example – Current Measurement - CP 6” coated pipeline at a 12,000’ length with .5% coating defect. .005 • 20,820 sq ft (total surface area) = 104.1 sq ft of bare area A = 104.1 sq ft i = 1 mA per sq ft .001 • 104.1 = .104Amps or 104mA Answer for I is 104mA If bare pipe was used then the current requirement would be much greater, in the range of 21 amps vs. .1 of an amp
  • 22.  In Summary,  The bare pipe will take a large amount of CP current to cathodically protect  Polarization will take longer to achieved  Therefore, the depolarization will be longer as well  The well coated pipeline will take much less of CP current to cathodically protect  Polarization will be quicker to achieved  Therefore, the depolarization will be quicker as well Current Measurement - CP
  • 23.  Remember, CP is achieved by polarizing the Cathode to the open potential of the Anode  On the surface of the metallic pipeline, a galvanic corrosion cell can form with the following criteria’s  Anodic area (high negative potential),  Cathodic area (Low negative potential or more positive potential),  Metallic connection (pipeline structure)  Electrolyte (surrounding environment) Polarization reduces VΔ along the Structure
  • 24. Galvanic Corrosion Cell on Pipelines AnodeCathode Microscopic Corrosion Cell on the Surface of a Pipeline Remember the golden rule of Corrosion – @ the point of current discharge, metal loss will occur (Corrosion)
  • 25.  Applying CP currents to the surface  We attempt to create the same potential between the anode and the cathode  If No potential difference exist, then there is no driving force for the electrons to move, in which will result in stopping metal discharge (corrosion)  Let’s look at this process closer Polarization reduces VΔ along the Structure
  • 26. -.5 -.6 -.65 -.6 -.7 -.58 -.58 -.6 -.65 -.6 -.7 -.58 -.6 -.6 -.65 -.6 -.7 -.6 -.65 -.65 -.65 -.65 -.7 -.65 -.7 -.7 -.7 -.7 -.7 -.7 Static Potentials Corrosion Mitigated P O L A R I Z A T I O N Polarization reduces VΔ along the Structure Once the surface area has polarized to the same potential, there is no “Anode” or “Cathode”, Cathodic Protection is achieved. 1. Static Potential 2. Most positive sides polarize first 3. Next most positive sites polarize 4. Last most positive site polarize 5. All sites polarized
  • 27. How do we know, if we are being Cathodically Protected?  Structure to electrolyte potential  Typically made at grade  Voltmeter and reference electrode  High input impedance voltmeter  Compare potentials measured to “criteria”
  • 28. Pipe to Soil Potential Measurements -.900 v +_ Polarization Film Reference Electrode
  • 29. Voltmeters  Analog vs. Digital  High Input Impedance  Field Durable  Storage Capabilities
  • 30. Voltmeter identifies More Noble Metals  If a voltmeter is connected such that  the positive terminal is to the more noble  metal and the negative terminal to the  more active metal, the reading is positive.
  • 31. Noble Active + _ Voltage measurement is positive .600 V Voltmeter identifies More Noble Metals
  • 32. Pipe-to-Soil Potential Measurement .900 v + _ Pipe Electrolyte Reference Cell Voltmeter Meter display is a postive reading. Record a negative P/S Potential. -.900 v + _ Pipe Electrolyte Reference Cell Voltmeter Meter display is a negative reading. Record a negative P/S Potential. Pipe To Soil Measurement Be aware of the connection of the leads to indicate a “+” or “-” reading
  • 33. The Common Different Types of Reference Electrodes  Calomel  Libratory use  Silver/Silver Chloride  Sea water use  Zinc  Sea water use  Copper-Copper Sulfate  Regular soil & neutral waters  Most popular use in the field
  • 34. Most Common for Field Use  Copper – Copper Sulfate  Rugged for field use  Consistent measurements in neutral waters and soil environments  Contains  Copper Rod  Copper Crystals  Copper solutions (antifreeze material) or distilled water
  • 35. Copper Rod Saturated Copper Sulfate Solution Un-dissolved Copper Sulfate Crystals Porous Plug Visual Window Copper – Copper Sulfate Reference Cell
  • 36. Copper – Copper Sulfate Reference Cell (Half Cell) Cathode Anode Positive Negative Electrolyte Copper- Copper Sulfate reference cell Steel Pipeline Test station wire The copper – copper sulfate reference cell represents half of the corrosion cell, therefore gets the name “Half Cell”
  • 37. Care of the CSE  Keep the CSE clean  Keep the cap on the tip to prevent dryness and cracking or loss of solution  Keep free of contamination, the tip is porous so therefore, contaminates can pass in the CSE solution  Perform calibration with a virgin half cell on regular bases  Shield clear window from sunlight, due to heat or UV rays will cause inaccuracy in readings (normally use black electrical tape)  Adjust readings according to temperature
  • 38. Criteria’s of CP  .850- V CSE with current applied (IR drop consideration)  .850- V CSE Polarized (Instant off)  100 mV Polarization decay
  • 39. Criteria - .850– V CSE with Current Applied  Structure to electrolyte potential with a high impedance volt meter and copper-copper sulfate reference cell  IR drop is considered by  Placing the reference cell directly over the pipeline as possible  As close to the pipeline as possible  Eliminating the resistance at the point of the reference cell contact as much as possible  Wetting the soil  Removing the sod
  • 40. Criteria - .850 – V CSE Polarization  Structure to electrolyte potential with a high impedance volt meter and copper- copper sulfate reference cell  Switching off the CP currents  Measure the IR drop  @ the point of polarization decay begins, reading is used for criteria
  • 41. Criteria - .850 – V CSE Polarization
  • 42. Criteria – 100 mV Polarization Decay  Structure to electrolyte potential with a high impedance volt meter and copper- copper sulfate reference cell  Switching off the CP currents  Measure the IR drop (instant off)  @ the point of polarization decay, measure until 100 mV depolarization has been achieved
  • 43. Criteria – 100 mV Polarization Decay
  • 44. Summary  Corrosion is the degradation of a material due to a reaction with its’ environment  CP is achieved when the cathodic sites are polarized in the electronegative direction to the potential of the most anodic sites.  Only practical method to determine this is by surface structure to electrolyte potentials
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  • 54. DAGB
  • 65. PCCP
  • 69. CI and DI WALL THICKNESS
  • 76. THANK YOU  CATHOLIC PROTECTION 76