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Rate of Electrical Current Flow Through the Corrosion Cell

Contents

Introduction

The presence of an electrolyte and a solution between two metals or electrodes is required for galvanic corrosion to occur. Some limitations of the calculation are non-customizable size and type of the electrode and resistivity of the solution. : I = \frac{E_a – E_c}{R_t}

I = \frac{E_a - E_c}{R_t}

Where:
𝐼 βˆ’ Rate of electrical current flow through the corrosion cell (amps)
𝐸𝑐 βˆ’ Potential of the cathode with respect to a reference electrode(V)
πΈπ‘Ž βˆ’ Potential of the anode with respect to the same reference electrode(V)
𝑅𝑑 βˆ’Total resistance to electrical current flow through cell(ohms)

Case Guide

Part 1: Create Case

  1. Select the Rate of Electrical Current Flow Through the Corrosion Cell application from the Pipeline Corrosion list.
  2. To create a new case, click the β€œAdd Case” button
  3. Enter Case Name, Location, Date and any necessary notes.
  4. Fill out all required parameters.
  5. Make sure the values you are inputting are in the correct units.
  6. Click the CALCULATE button to overview results.

Input Parameters

  • Potential of the Cathode with Respect to a Reference Electrode(V)
  • Potential of the Anode with Respect to the same Reference Electrode(V)
  • Total Resistance to Electrical Current Flow through the Cell(ohm).

Part 2: Outputs/Reports

  1. If you need to modify an input parameter, click the CALCULATE button after the change.
  2. To SAVE, fill out all required case details then click the SAVE button.
  3. To rename an existing file, click the SAVE As button. Provide all case info then click SAVE.
  4. To generate a REPORT, click the REPORT button.
  5. The user may export the Case/Report by clicking the Export to Excel icon.
  6. To delete a case, click the DELETE icon near the top of the widget.

Results

  • Rate of Electrical Current Flow through the Corrosion Cell(A)

References

  • ANSI B31.G Calculations
  • PRCI – A Modified Criterion for Evaluating the Remaining Strength of Corroded Pipe, Database for Corroded Pipe Tests and Continued Validation of RSTRENG
  • NACE – Electrical Resistance and Resistivity Calculations

FAQ

  • ASME B31G Original/Modified and RSTRENG?

    ASME B31.G Original and Modified (0.85) are Level 1 assessment along with most other metal loss calculations that are limited to pits and short lengths of pitting clusters. RSTRENG is a Level 2 metal loss calculation; however, it is not limited just to pits, but most lengths of pitting i.e., 2500 mm (100 inches) using interaction rules that is not uncommon on some pipelines. Check Out

  • Preventative and Corrective Measures to Control Corrosion Pitting?

    A corrosion rate needed to set the re-inspection interval, reassess the performance metrics and their current applicability, plus to ensure the assumptions made are correct.Β  At each direct examination where corrosion pitting is found, the operator should measure and record each pitting cluster. Check Out

  • Estimating Internal Corrosion Rates?

    Internal corrosion is most likely to occur where water first accumulates. Predicting these locations of water accumulation serve as a method for prioritizing local examinations. Predicting where water first accumulates requires knowledge about the multiphase flow behavior in the pipe requiring certain data.Β Check Out

  • Estimating External Corrosion Rates?

    All corrosion defects found during each direct examination should be measured, documented, and remediated as needed.Β  At each excavation, the pipeline operator should measure and record generic environmental characteristics (such as soil resistivity, hydrology, drainage etc.). Check Out

Updated on December 26, 2023
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