AMPP Store - Products tagged with 'cathodic protection'

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Experimental Study and Finite Element Modelling of the Cathodic Protection Influence on Parallel Pipelines During Maintenance Operations

Product Number: 51324-20713-SG

Author: Erwan Diler; Yves Zannier; Alexandre Billot; Flavien Vucko; Tiphaine Lutzler

Publication Date: 2024

$40.00

Dense buried pipelines network, such as in implemented in parallel, can be installed in different process and storage mills, such as geological gas and hydrocarbon storages. Their corrosion resistance is ensured by a combination of organic coating and cathodic protection (CP). For maintenance operation on a specific pipeline, the CP can be turned off for safety reasons. Thus, the operated pipeline can be affected by CP influence from other surrounding protected ones. This phenomenon is supported in the field by different pigging inspections, highlighting local corrosion induced by output stray current on coating defects. In the literature, many studies focused on CP influences by finite and/or boundary element modeling. However, usually the foreign structures considered (under influence) are limited to bare steel or fully coated pipeline. Moreover, most of these studies are not confronted with experimental works. To our knowledge, the actual influence between the different pipelines is not much documented in the literature and not quantified. In this study, an experiment consisting in 3.00 x 1.80 x 0.80 m sand tank, equipped with 4 full scale parallel pipelines, with 17 model defects were realized. The model defects reproduce uniformly degraded coating and local defects. The experimental work allows i) measuring the DC influence under different CP configurations, and ii) providing stray current data for finite element modelling (FEM). The FEM was performed in a two steps i) a CP distribution in terms of current demand and electric field on protected pipelines, and ii) application of this electric field to the foreign pipeline. The good agreement obtained allows a validation the proposed approach and globally assess the riskier scenario in terms of nature of the defect, applied CP and soil environment.

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Feasibility Assessment for Cathodic Protection of High Level Nuclear Waste Tanks

Product Number: 51324-21160-SG

Author: Kenton Lawson; Bruce Wiersma; Barbara Nicole Padgett; Sandeep Chawla; John Beavers

Publication Date: 2024

$40.00

This paper summarizes an assessment of the feasibility of implementing cathodic protection (CP) as an internal corrosion prevention strategy for nuclear waste storage tanks. The study investigates the principles of cathodic protection and its applicability to the unique environment of nuclear waste storage. By reviewing the relevant literature, this research explores the various threats and challenges associated with implementing CP in this specific context. A boundary element analysis (BEA) model of a steel tank with a simplified impressed current cathodic protection (ICCP) system was developed using polarization curves that were experimentally measured from coupons in simulated waste. This model was developed to evaluate the interaction of electrochemical potentials of the various waste layers within the tank. The modeling results indicate that the simulated ICCP system is capable of shifting the polarized potentials of the internal tank surfaces to levels required to mitigate stress corrosion cracking (SCC) and corrosion.

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FEM Simulation Analysis Of The Pipe-Casing Under Cathodic Protection

Product Number: 51322-17713-SG

Author: Andrea Brenna, Luca Paterlini, Mehdi Attarchi, Marco Ormellese

Publication Date: 2022

$20.00

A crossing between buried pipelines and transportation arteries such as railways and highways is a common reality. Nowdays it is ordinary practice, and standards are available for such pratctise¹, to protect such pipelines by encasing them in a wider pipe, named Casing. The goal is to protect the carrier pipe providing an outer shell capable of withstanding mechanical stresses and eventual corrosion, without leakage risk. In usual conditions this kind of safety measure should not be necessary, still due to the difficult maintenance and monitoring accessibility below railways and highways it becomes a dependable protection method and device.

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Field Data Collection for Cathodic Protection and Hydrogen Embrittlement of Super Duplex Stainless Steel for Deep Sea Application - Use of Low Voltage Anode

Product Number: 51324-20693-SG

Author: Nicolas Larché; Jean Vittonato; Anne-Marie Grolleau; Erwan Diler; Dominique Festy

Publication Date: 2024

$40.00

High-strength steels (HSS) might undergo hydrogen embrittlement (HE) in seawater under cathodic protection (CP) with traditional Aluminum-Indium (Al-In) or zinc (Zn) galvanic anodes. The actual failure risk will also depend on metallurgy, mechanical properties and local loads. Even though super duplex stainless steels (SDSS) generally do not require CP, they can unintentionally become polarized due to electrical continuity with protected carbon steel structures. CP current demand and hydrogen evolution depend on various factors, like dissolved oxygen, temperature, flow, microbial activity, calcareous deposits, and depth. Hence, the risk of HE varies with exposure site and must be assessed. Aluminum-gallium (Al-Ga) is a low-voltage anodic material aimed at reducing protective potential to mitigate HE in high-strength steels in seawater. However, long-term field data is limited. This study aimed to gather long-term CP data for SDSS at different depths and seawater types, and to assess HE risk using Al-Ga vs. conventional anode materials. Instrumented anchored lines, including CP sensors, stressed samples, and environmental sensors were deployed for over a year in shallow, intermediary, and deep seawaters. Results showed varying cathodic current demands, with deep seawater having the highest. Biofilm formation on SDSS caused depolarization at all sites, with differences noted between sites. Al-Ga significantly reduced hydrogen-induced cracks in SDSS.

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Forensic Evaluation of Long-Term Galvanic Cathodic Protection of Bridge Pilings in a Marine Environment

Product Number: 51320-14485-SG

Author: Douglas L. Leng, Matthew Duncan, Ivan R. Lasa

Publication Date: 2020

$20.00

Marine environments can be very aggressive and present significant challenges in maintaining key infrastructure from the effects of corrosion. In Florida, thousands of bridges are in coastal areas and are continually, or periodically exposed to saltwater conditions. A clear majority of these bridges were constructed using steel reinforced concrete and are supported by precast pilings situated in saltwater, so for this reason, cathodic protection is a necessary strategy for controlling the effects of saltwater induced corrosion.

Toward the early 1980s, the Florida Department of Transportation (FDOT) began the evaluation of different approaches to control saltwater induced corrosion. Some of these included the use of integral pile jackets, specialty materials for concrete repairs, surface applied coatings and other innovative approaches utilizing galvanic anode technology. One such system was jointly developed with industry partners and sponsored by the Federal Highway Administration (FHWA) using integral pile jackets lined with expanded zinc mesh anodes to apply cathodic protection. This innovative approach provides for the problem of concrete repair while at the same time stopping the on-going process of corrosion both combined in one application. Both laboratory and field trials validated the benefits to this approach and confirmed that the system can mitigate corrosion and extend the useful service life of pilings by more than 20 years.

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From galvanic anodes to ICCP system for offshore jackets revamping

Product Number: 51323-19177-SG

Author: Eric Agel, Mamady Obame-Diakite, Thiago Mesquita, Christian Yogoulou-Joly

Publication Date: 2023

$20.00

Sacrificial or Galvanic Anodes Cathodic Protection System is an excellent anticorrosion solution which offers to immerse structures a long-term protection. In TotalEnergies and in the Oil & Gas Industry in general, such system provides confidence, efficiency together with little maintenance over years which is a very good point for the subsea integrity of jackets (or pipelines) when knowing all other operational constraints or corrosion issues that can be met at the surface level.

Thus, from TotalEnergies experience, it has been established that as long as:1/ the CP system is correctly designed (taking into account the applied - or not - painting on the jacket) following the recognized international codes and standards (DNV RP-B-401, ISO 15589-2.

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Fusion Bonded Epoxy Coatings (FBE) and Disbondment

Product Number: 51316-7246-SG

ISBN: 7246 2016 CP

Author: Mehrooz Zamanzadeh

Publication Date: 2016

$20.00

In this paper, failure analysis methodology will be applied to the principal mechanisms by which FBE coatings fail during long term service; with specific application to case studies involving blistering. The case studies apply standard failure analysis techniques to determine the primary causes and modes of failures.

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Galvanic Corrosion Protection of Reinforced Concrete Structures

Product Number: MECC23-20192-SG

Author: Laith Haboubi; George Sergi C.Eng.; David Whitmore P.Eng

Publication Date: 2023

$20.00

Chloride induced corrosion of steel reinforcement in concrete structural elements is a major worldwide problem [1]. Chlorides can be introduced into the concrete via de-icing salts, seawater, high salinity groundwater or sabkha soils [1.2]. This leads to localised breakdown of the normally passive steel reinforcement in the form of pitting corrosion [2].

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Guidelines For The Collection Of Reliable And Practicable ECDA Indirect Inspection Data

Product Number: 51322-17978-SG

Author: Miqdaad Fatakdawala

Publication Date: 2022

$20.00

The External Corrosion Direct Assessment (ECDA) is formally listed as an acceptable integrity assessment method within Subpart O, Part 192 of the code of federal regulations regarding gas transmission pipeline integrity management2. It is a 4 step continuous improvement process to identify and address locations where external corrosion activity has occurred, is occurring or may occur1. In the pre-assessment phase, a comprehensive right-of-way inspection is performed, and pipeline operability data is collected to verify the feasibility of conducting a full ECDA for the pipeline under evaluation. In the indirect inspection phase, the status of cathodic protection and pipeline coating is tested using methods such as Close Interval Potential Surveys (CIPS) and Direct Current Voltage Gradient (DCVG) surveys.

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High-strength Nickel Low Alloy Steels for Oil and Gas Equipment: ASTM A508 Grade 4N under cathodic protection and simulated sour environments.

Product Number: 51320-14706-SG

Author: Andreas Viereckl, Esteban Rodoni, Zakaria Quadir, Garry Leadbeater and Mariano Iannuzzi, Yuta Honma

Publication Date: 2020

$20.00

Low alloy steels (LASs) combine relatively low cost with exceptional mechanical properties, making LASs commonplace in Oil and Gas equipment. However, the strength and hardness of LASs for sour environments and for applications that generate atomic hydrogen at the surface, e.g., cathodic protection, is limited to prevent different forms of hydrogen embrittlement (HE) such as hydrogen stress cracking (HSC) and sulfide stress cracking (SSC). As a result, the specified minimum yield strength (SMYS) of forged LASs for, e.g., subsea components, rarely exceeds 550 MPa (80 ksi), while the most common pipeline steels are API(1) X65 to X70, with a SMYS of 450 MPa (65 ksi) and 482 MPa (70 ksi), respectively. Moreover, ISO(2) 15156-2 restricts LASs to a maximum of 1.0 wt% Ni due to SSC concerns. The LASs that exceed the ISO 15156-2 limit have to be qualified for service, lowering their commercial appeal.

In this work, the HSC resistance of the high-nickel (3.41 wt%), quenched and tempered (Q&T), nuclear-grade ASTM(3) A508 Gr.4N LAS was investigated using slow strain rate testing (SSRT) as a function of applied cathodic potential. Results showed that the yield strength (YS) and ultimate tensile strength (UTS) were unaffected by hydrogen, even at a high negative potential of -2.0 VAg/AgCl. HE effects were observed once the material started necking, manifested by a loss in ductility with increasing applied cathodic potentials. Indeed, A508 Gr.4N was less affected by H at high cathodic potentials than a low-strength (YS = 340 MPa) ferritic-pearlitic LAS of similar nickel content. SSRT results were linked to microstructure features, which were characterized by light optical microscopy (LOM), scanning electron microscopy (SEM) coupled to electron backscatter diffraction (EBSD).

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Horizontal Directional Drilling (HDD) Method Pipe Update

Product Number: 51323-18948-SG

Author: Joe Pikas

Publication Date: 2023

$20.00

The case history will discuss HDD methodology and challenges. With all the benefits of HDD comes the disadvantages especially from pipeline maintenance, corrosion control and integrity management. HDD can impose additional strain on the pipeline during the pull through process and can increase both installation stress and operational stress. HDD installed pipeline crossings are deep and could easily become low points for liquid hold up causing flow issues.

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Horizontal Directional Drilling In External Pipeline Coating Integrity

Product Number: 51322-17785-SG

Author: Eric Pintueles

Publication Date: 2022

$20.00

The purpose of the “Bore Test” is to know the external quality of the coating after the installation of the pipe section, as picture 1. NACE standard “TM-102-2002-SG”1a defines four kinds of coating quality such as: excellent, good, fair and poor. To know the final quality of coating with this procedure. It was used two different electrical tests. DC current test using minimum voltage drop method and, the 3 pole test which is called by the same manufacture of the Multifunction Ground Resistance tester.

Products tagged with 'cathodic protection'

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