Pipeline Wall Electrode for Accurate Internal Corrosion Monitoring

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Solution Overview

Problem

Current methods for determining the internal corrosion rate of steel pipelines are inaccurate and require frequent electrode replacement, as they measure corrosion of separate specimens rather than the pipeline wall itself, leading to uncertainties and delays in monitoring changes in corrosive media.

Innovation Solution

A method using linear polarization resistance (LPR) and electrochemical impedance spectroscopy (EIS) with three probes installed along the pipeline, where the pipeline wall acts as a working electrode and additional probes provide a reference electrode, allowing for direct measurement of polarization resistance and corrosion rate, reducing uncertainty and electrode replacement frequency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Measurement precision

If separate specimens (coupons) are used to measure corrosion rate, then the measurement can be performed with simple equipment, but the measurement accuracy deteriorates because it does not reflect the actual pipeline wall corrosion

Engineering Contradiction:
Improvecorrosion rate measurement accuracyVSAvoidmeasurement system complexity
Core Design Contradiction:
Measurement precisionVSDevice complexity

Solution Approach 1:

The pipeline wall itself serves as the working electrode in the electrochemical measurement system, eliminating the need for separate coupon specimens. The pipeline structure performs the measurement function directly on itself, providing accurate corrosion rate data for the actual protected surface while maintaining relatively simple measurement equipment.

Inventive Principle:
Principle #25Self-service

2Reliability

If traditional LPR method with separate electrodes is used, then the setup is simple, but the reliability deteriorates due to electrode replacement requirements and uncertainty in representing actual pipeline corrosion

Engineering Contradiction:
Improvecorrosion monitoring reliabilityVSAvoidelectrode system complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The counter electrode and reference electrode are integrated into a single combined electrode assembly that can be installed once on the pipeline. This merged electrode system eliminates the need for separate electrode replacements and provides stable, reliable corrosion monitoring by maintaining consistent electrical contacts with the pipeline wall over time.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The combined counter-reference electrode is installed in advance on the pipeline during initial setup, establishing stable electrical connections before corrosion monitoring begins. This preliminary installation ensures that the electrodes remain in fixed positions and maintain reliable contact with the pipeline surface throughout the monitoring period.

Inventive Principle:
Principle #10Preliminary action

3Speed

If mass loss measurement with coupons is used, then the method is simple and direct, but the response time deteriorates as it provides delayed or no information about changes in corrosive medium

Engineering Contradiction:
Improvecorrosion rate response speedVSAvoidmeasurement system complexity
Core Design Contradiction:
SpeedVSDevice complexity

Solution Approach 1:

The mechanical mass loss measurement method is replaced with an electrochemical measurement system that uses electrical currents and potentials to determine corrosion rate. This substitution enables continuous, real-time monitoring of corrosion processes and immediate detection of changes in corrosive medium conditions, providing fast response speed while maintaining measurement accuracy.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach provides more accurate and reliable corrosion rate measurements directly on the pipeline wall, reducing errors and extending electrode lifespan, while enabling continuous monitoring in various media, including hydrogen-sulfide containing environments.

Implementation Method 1

The essence of it is that a voltage difference is created between the two electrodes placed in the corrosive medium and the current response is measured. If the voltage perturbation is small enough... the polarization resistance of the electrode, which is related to the value of the current as follows: jcorr=(2,303(ba−1−bc−1))−1RP−1

Methodology Applied
Scientific EffectLinear polarization resistance: Electrical Resistance

Implementation Method 2

For accurate application of the method, the resistance value of the solution must be known and the value of the solution resistance must be corrected (subtracted from the overall resistance figure). For this purpose, often two measurements are made, both with alternating current, one at high (about 1000 Hz) and the other at low (about 1 Hz) frequency.

Methodology Applied
Scientific EffectElectrochemical impedance spectroscopy: Electrical Impedance Tomography

Implementation Method 3

The corrosion rate of the inner surface of pipelines is typically determined by the coupon, the LPR and the ER techniques (corrosion monitoring)... the corrosion rate can be calculated from the mass loss... the corrosion rate is calculated from the changes in the resistance of the wire

Methodology Applied
Scientific EffectElectrochemical corrosion: Redox Reactions

Data Source

PatentUS12098995B2Method and measuring arrangement for determining the internal corrosion rate of steel structures
Publication Date: 2024.09.24 LUKACS ZOLTAN
  • US12098995B2 patent drawing
  • US12098995B2 patent drawing

AI summary

Methods for determining the internal corrosion rate of steel pipelines. During the methods the calibration constant is determined under laboratory conditions then by using the calibration constant field conditions are modeled under laboratory conditions and the corrosion rate is determined, then in the same manner as under laboratory conditions the corrosion rate is determined under field conditions. Further, the invention is a measuring arrangement for determining the calibration constant and the corrosion rate for the internal corrosion rate of steel pipelines (1) the arrangement is applicable to carry out the methods under laboratory and field conditions. The arrangement consists of a polarizing and measuring unit (5) having a two-channel power output (2), a potential-measuring input (3), and a ground connection (4), a control and data storage unit (6), and three probes (8) with counter-electrodes (7). At least one probe (8) is also provided with a reference electrode (9).