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COLVIN MANN, P.E. , NACE 3862 3
ALABAMA/MISSISSIPPI SECTION
AMERICAN WATER WORKS ASSOCIATION
M A Y , 2 0 1 6
External Corrosion Control
Iron Pipe Manufacturing
Melting Furnace (Cupola) ENERGY GAINED
Raw Materials
TransferLadle
CastingMachine
External Corrosion Control
Steel Pipe Manufacturing
Electric Arc FurnaceENERGY GAINED
Raw Materials
TransferLadle
Hot Rolling Machine
External Corrosion Control
Prestressed Concrete Cylinder Pipe
External Corrosion Control
Prestressed Concrete Cylinder PipeLined Cylinder Pipe
External Corrosion Control
Prestressed Concrete Cylinder PipeEmbedded Cylinder Pipe
External Corrosion Control
Ductile Iron Pipe
External Corrosion Control
Ductile Iron Joints
External Corrosion Control
Push-on Joint Mechanical Joint
Corrosion Mechanisms Oxygen Concentration (Iron and PCCP)
High Oxygen to Low Oxygen
Sulfate Reducing Anaerobic Bacteria (Iron and PCCP) Produces Sulfides – H SO – highly corrosive
Dissimilar Metals (Iron and PCCP) Galvanic Cell
Stray Current (Iron and PCCP)
Chlorides (PCCP)
Moisture Variations(Iron and PCCP) Fluctuating Water Table
External Corrosion Control
Corrosion Mechanisms High Sulfates (Iron and PCCP)
Sulfate Reducing Bacteria
Soil Chemistry(Iron and PCCP) Low Resistivity
Low PH
Alternating Current (Iron and PCCP) Hard To Mitigate
External Corrosion Control
Stray Current Interference
External Corrosion Control
Stray Current Interference
External Corrosion Control
External Corrosion Control
External Corrosion Control
External Corrosion Control
External Corrosion Control
Galvanic Series
Referenced to Copper-Copper Sulfate
Metal Volts
Magnesium -1.60 to -1.75
Zinc -1.10
Aluminum -1.05
Carbon Steel -0.50 to -0.80
Cast/Ductile Iron -0.50
Lead -0.50
Copper -0.20
Carbon, Graphite +0.30
Corrosion Cell Elements
All Corrosion Cells Have The Following:
ANODE
CATHODE
ELECTRONIC PATH
ELECTROLYTE
External Corrosion Control
Current
Electron
Fe++
Fe+++
e-
e-
e-
e-
e-
H+
H+
H+
H+
OH-
OH-
OH-
OH-
AnodeCathode
Electrolyte
Return current path
Galvanic Corrosion Cell
The Underground Pipe Corrosion Cell
AnodeCathode
Electrolyte
Return Current Path
Resistivity
Redox
pH
Sulfides
Moisture
Chlorides
Soil Evaluation Parameters
External Corrosion Control
10-Point Soil EvaluationResistivity - ohm-cm (based on water-saturated soil box):
< 1,500 1,500 - 1,800> 1,800 - 2,100> 2,100 - 2,500> 2,500 - 3,000> 3,000
pH:0 - 22 - 44 - 6.56.5 - 7.57.5 - 8.5> 8.5
Redox potential:> +100 mV+50 to +100 mV0 to +50 mVNegative
Sulfides:PositiveTraceNegative
Moisture:Poor drainage, continuously wetFair drainage, generally moistGood drainage, generally dry
1085210
5300*03
03.5
45
3.520
210
*3 points should be added
if low or negative redox
and sulfides are present
External Corrosion Control
ph = 3.94; resistivity = 230 ohm-cm;sulfates = 5440 ppm
External Corrosion Control
The steel, whether rebar, wire or cylinder, embedded inPortland cement concrete, forms a passive film due to the phof the cement, around 12. This film slows corrosion to a verysmall rate. The intrusion of the water soluble chloride ionfound in some ground water attacks the film and exposes thesteel to a galvanic corrosion condition. As corrosion builds, itoccupies more space than the original steel and eventuallyresults in spalling and delamination of the mortar. With thisincreased exposure, corrosion can increase to failure.
Chlorides
External Corrosion Control
Prestress
External Corrosion Control
Bar Wrap
External Corrosion Control
Polyethylene Encasement
Coatings
Sacrificial Cathodic Protection
Impressed Current Cathodic Protection
Protection
External Corrosion Control
Polyethylene Encasement
External Corrosion Control
Polyethylene Encasement
External Corrosion Control
Polyethylene Encasement
External Corrosion Control
Fusion Bonded Epoxy
External Corrosion Control
80 Mil Tape Wrap
External Corrosion Control
Cathodic Protection Principle
External Corrosion Control
Cathodic Protection Sacrificial Anode
AnodeProtectedPipe Mg
or
Zn
Maximum Driving Potential: - Mg ( -1.7 V )
Steel ( - 0.6 V )
1.1 V
External Corrosion Control
Galvanic Anode
External Corrosion Control
Magnesium Anode
External Corrosion Control
Galvanic Anodes at Every Other Joint
External Corrosion Control
Distributed Galvanic Sacrificial System
External Corrosion Control
Grouped Sacrificial Galvanic System
External Corrosion Control
Ribbon Type Galvanic Anode
External Corrosion Control
Galvanic Anode Installation
External Corrosion Control
Galvanic Anodes In Repair Conditions
External Corrosion Control
Impressed Current System Rectifier
External Corrosion Control
Impressed Current System Rectifier
External Corrosion Control
Impressed Current System Rectifier
External Corrosion Control
Impressed Current Anodes
External Corrosion Control
Impressed Current Deep Anode Installation
External Corrosion Control
Impressed Current Deep Anode Installation
External Corrosion Control
Impressed Current System
External Corrosion Control
Caution is required with CP potentials over 1100 mv withPCCP as the hydrogen production at the cathode can result inatomic hydrogen which permeates the high strength, highstress wire causing hydrogen embrittlement. The result canbe loss of ductility and tensile strength and ultimately, failure.
Impressed Current Cathodic Protection
External Corrosion Control
Stray Current DC
External Corrosion Control
Stray Current DC
External Corrosion Control
Consumed Galvanic Anode
External Corrosion Control
Consumed Galvanic Anode Origin
External Corrosion Control
Questions
Contact Information
.
Colvin Mann, P.E., NACE 38623
Neel-Schaffer, Inc.
601 948-3071