CATHODIC PROTECTION SYSTEM DESIGN



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CATHODIC PROTECTION SYSTEM DESIGN Presented By DENIS L ROSSI P.E. CORROSION ENGINEER New England C P Inc.

Corrosion Fundamentals

What is corrosion? It is defined as the degradation or deterioration of a material, usually a metal, due to a reaction with its environment. What does that mean???

Corrosion is a natural process. Metals don t like being metals, they prefer remaining as ores. In the process of converting ores into metals, energy is added in the form of heat, this places the metal into a high-energy state. It is this energy that is given off from the metal, as the metal is returning to an ore, lower-energy state, is what we call corrosion.

Steel - Rust to Rust Mine Steel Mill Bridge Rust Iron Ore Refining Pipe Underground Pipeline Iron Oxide

Components of a corrosion cell Anode Metal loss or corrosion occurs at the anode Cathode Little or no corrosion occurs at the cathode Return Circuit/Metallic Path Provides a path for electrons to flow, between the anode and cathode Electrolyte Ionized solution capable of conducting electricity

Corrosion of Metals Current Flow Cathode Current Flow Anode Electrolyte

Practical corrosion cell Anode bare steel gas service Cathode cast iron gas main Electrolyte soil that main and service are buried in Return path service tee threaded into gas main

CARBON ROD (CATHODE) +0.30mV WIRE (CONDUCTOR) ZINC CASE (ANODE) -1.10mV MOIST PASTE (ELECTROLYTE)

Steel Gas Main (Anode) Steel Distribution System No Insulators ( i = Current Flow) i i i Soil (Electrolyte) Copper Water Line- (Cathode) Steel Gas Service (Anode) Appliance- (External Connection) i i CI Water Main (Cathode)

Steel Gas Main Steel Distribution System Insulators insulator Copper Water Line insulator Steel Gas Service CI Water Main

PRACTICAL GALVANIC SERIES Material Potential* Pure Magnesium -1.75 Magnesium Alloy -1.60 Zinc -1.10 Aluminum Alloy -1.00 Cadmium -0.80 Mild Steel (New) -0.70 Mild Steel (Old) -0.50 Cast Iron -0.50 Stainless Steel -0.50 to + 0.10 Copper, Brass, Bronze -0.20 Titanium -0.20 Gold +0.20 Carbon, Graphite, Coke +0.30 * Potentials With Respect to Saturated Cu-CuSO 4 Electrode

Factors causing corrosion on a pipeline Dissimilar metals Galvanic corrosion Brass valve or copper pipe connected to carbon steel pipe Old carbon steel pipe connected to new steel pipe Dissimilar Soils Varying oxygen content Varying resistivities Mechanical Stresses Bending and Gouges Cutting of threads Stray Currents

Coupling to Dissimilar Metals Iron Pipe (Anode) - 500mV Brass Valve (Cathode) - 300mV Iron Pipe (Anode) - 500mV

Cathodic Area (protection) Corrosion Copper Anodic Area (corrosion) Steel

Basic Corrosion Cell Earth (Electrolyte) Corrosion Current Corroding Area Return Path Protected Area Anodic Area Cathodic Area

Oxygen Concentration Corrosion Cell Backfill More Oxygen - Cathodic - Protected Pipe Corrosion Currents Less Oxygen - Anodic - Corroding Undisturbed Earth

Oxygen Concentration Corrosion Cell Rock Anodic Area Cathodic Areas Pipe Corrosion Currents Anodic Area Wood Bed Block

Scarred/Damaged Surface Corrosion Threads, scratches and dents are anodic to undisturbed surfaces along the pipe.

Dissimilar Soils Corrosion Anodic Area Cathodic Area Soil (High concentration of Salts) Soil (Low concentration of Salts)

Gas Pipeline (-) Cathodic Protection Rectifier (+) Anode Groundbed Current Discharge (Corrosion) Current Discharge (Corrosion) Water Pipeline Stray Current Due to Impressed Current Cathodic Protection System

Corrosion Current vs Metal Loss Metal loss is directly proportional to corrosion current 1 amp per year = 20 pounds of steel lost Larger area of steel exposed - more current required for cathodic protection For given current - faster wall penetration at smaller exposed surface area

Stray Current

Summary Corrosion Cell *Anode *Cathode *Electrolyte *Metallic Connection

Rules & Regulations Department of Transportation Part 192 Operations And Maintenance Manual

What Has to be Cathodically Protected? All steel pipe installed after 1971 must be protected from external corrosion. Regardless of size Regardless of Length What does that mean? All new steel pipe MUST have:

Protective Coating Applied on a properly applied surface Have sufficient adhesion to the pipe Sufficient strength to resist cracking Have sufficient strength to resist damage due handling and soil stress. Compatible with cathodic protection currents Coatings must also be: Inspected for damage prior to lowering in the ditch Must be protected from damage from adverse ditch conditions. Precautions must be taken to protect coated pipe that is to be installed by boring.

Cathodic Protection Provide a level of cathodic protection for the entire length of the underground structure. Cathodic protection levels must be controlled so as not to damage coatings.

Electrical Isolation Insulating devices must be installed on the steel pipe so as to facilitate electrical isolation. Mains @ Tie-ins and crossings with other utilities Services - @ the main and the service riser Casings insulated from the carrier unless both carrier and casing are cathodically protected as a single unit.

Test Leads and Boxes Test leads must be securely attached and minimize stress concentration on the pipe. All test lead connections at the pipe must be coated. Test leads must extend out of the test box by at least 18. Test box locations and dimensions will be indicated on the design drawings. Test leads will be connected as required.

Pipe installed prior to 1971 Bare or coated steel pipe determined to be in areas of continuing corrosion must be cathodically protected. Hot Spot Protection.

Atmospheric Corrosion Pipelines that are exposed to the atmosphere must be cleaned and either coated or jacketed with a material suitable for the prevention of atmospheric corrosion. Steel service risers and meter installations must be coated to the outlet side of the meter bar.

Other Exposed Pipe Inspection Further Investigation if additional corrosion is evident. Inspect coatings for damage Inspect bare pipe for pitting and uniform wall loss. Internal Pipe inspection Inspection Data to be kept for the LIFE of the pipe.

Cathodic Protection

Connect to more negative metal Elements of a Corrosion Control System Break electrical path to what s not being protected Coating Limit Area in Contact with Electrolyte

Protection of a Pipeline with a Sacrificial Anode Pipe Coating Current through Wire Pipe Anode Current through Soil t

Magnesium Anode Sealing Compound Black Wire Cloth Sack Lead Seal Steel Core Magnesium Bar Gypsum Powder Note: Anodes should be installed 18 below and 18 to the side of the pipe. The anode should be also be soaked with water before backfilling. Do not carry by the wire.

Sacrificial Magnesium Anode

Rectifier Groundbed IJ IJ - R Rectifier + Anode Groundbed

POLE MOUNTED RECTIFIER

Typical Arrangement of Cathodic Protection For Tanks Rectifier Tank Tank Anodes

Tidal Zone Cathodic Protection Structure Section MHW MLW Steel Pile Cathodic Protection is Afforded to Steel in Tidal Zone During Periods of High Tides. Tidal Zone Galvanic or Impressed Current Anodes

Corrosion Testing

Pipe-to-Soil Potential Test Multimeter -0.85 Cu/CuSO4 Reference Cell Pipe Lead Test Box Pipe

Corrosion Monitoring Mains - Once a Year Ensure Test Box Availabilty Services Once every Ten Years Ensure Test Wires are Connected Rectifiers and Bonds 2 Months Record Keeping For the life of the pipe.

Common Corrosion Problems

Shielding of Cathodic Protection Corrosion Wood Anode Cathodic Protection Current

Shielding Of Protective Currents Current Pipe Sheeting

Coating Disbondment & CP Shielding Cathodic Protection Current Protects Exposed Area Backfill Protected Coating Pipe Wall Cathodic Protection Current Does Not Protect Area Under Disbonded Coating

Faulty Service Isolators

Mastic Application MASTIC

Proper Mastic Application Wire brush damaged areas Apply two thin coats (paint) Let dry between coats (15 min) Let dry before backfilling.

Proper Coating Repairs with Cold Applied Tape Clean pipe with wire brush. Apply primer to clean pipe. Wrap tape around pipe.

Other Test Wires not connected to anode. No dielectric union on service entrance or service regulator vent. Underground electrical contact with other metallic structure. Isolator installed incorrectly or not at all. Isolator installed and not indicated. Test boxes paved over. Telemetry not isolated.

Summary Corrosion Cell Anode Cathode Electrolyte Metallic Connection Corrosion Control System Coating - Mastic and Cold Applied Tape Isolation - Insulating Joints Cathodic Protection - Magnesium Anode