Aberdeen Branch
On Tuesday 22nd August 2023 the Aberdeen Branch held its annual fund-raising Corrosion awareness Day (CAD) and welcomed eight corrosion industry speakers along with multiple equipment demonstrations from Rysco, who were ICorr’s host for this one special event. CAD is designed to assist the development of those unfamiliar with Corrosion & it’s prevention and provides and understanding of the corrosion processes and causes which are specific to a range of common industries.
Delegates learnt the basics of the role of the corrosion engineer; including materials selections, corrosion mitigations; failure investigation; testing and design issues.
Delegates – Group Photo
The Welcome was provided by the Aberdeen Branch Chair, Siji Anjorin supported by Dean Smith, Bridge of Don Operations Manager for Rysco U.K for the Safety Moment.
Rysco are headquartered in Calgary and are a global provider of Corrosion Management Solutions. They are both an ICorr Gold Sustaining Member and Aberdeen Local Branch Sponsor.
Compiled: Nigel Owen and Stephen Tate
Dean Smith, Operations Manager for Rysco U.K
A comprehensive series of Talks and Demonstrations followed the Introductions, designed to cover all they key Corrosion Topics.
1. Principles and Costs of Corrosion
Steve Paterson, Ph.D, C.Eng, Arbeadie Consultants provided the opening presentation running through the fundamentals of corrosion and electrochemistry with emphasis on what drives corrosion and the corrosion process of metals. He then outlined the different types of corrosion and common corrosion mechanisms and how these related to the Oil & Gas industry. Internal Corrosion mechanisms discussed were: Acid gas corrosion (CO2/H2S) consisting: CO2 (sweet) corrosion, Preferential weld corrosion, H2S (sour corrosion, Mixed sweet & sour corrosion), Sulphide stress cracking (SSC), Hydrogen induced corrosion (HIC), Hydrogen embrittlement, Chloride pitting/crevice corrosion, Oxygen corrosion, Microbial induced corrosion (MIC) and Sand erosion.
Several methods of corrosion control and management were outlined including:
• Materials selection: The most effective solution that can remove the corrosion threat completely (e.g. CRA/Non-metallic material).
• Water removal by dehydration.
• Chemical treatments (e.g. corrosion inhibitor, biocide or oxygen scavenger) a common mitigation method for internal protection of carbon steels.
• Use of Coatings and linings.
• Anodic/Cathodic protection used to limit and control Corrosion in both internal and external situations.
• Control of process parameters/environment, e.g. by limiting temperature and chloride content can reduce the risk of SCC.
Steve then highlighted the costs and significance of corrosion and demonstrated how implementing corrosion prevention best practices could result in savings of between 15% and 35% with the NACE 2016 study quoting savings of 3.4% of global GDP (Gross Domestic Product), giving immense motivation for corrosion engineers to contribute in achieving such savings and associated improvements in integrity of infrastructure and protection of the environment
2. Materials Selection
Rob Howard, PhD, of Lloyd’s Register discussed materials selection critical to the Oil & Gas processing industry making reference to a process diagram from well to final product, he looked at the common types of corrosion witnessed in the process equipment: A selection of materials for corrosion resistance was reviewed showing how we can move from Martensitic and Austenitic Stainless steels up to Duplex and onto Ni and Titanium alloys to get sufficient resilience, albeit with some heavy cost implications.
Rob Howard graduated with a in Materials Engineering from the University of Cape Town in 1995. and worked as a post-doctoral researcher at the Corrosion and Protection Centre, University of Manchester. He joined Lloyd’s Register in 1998 and at present he is the team leader for the Offshore Materials team in LR, whose main function is to provide technical support to surveyors and clients and to review design specifications for oil and gas and offshore wind projects.
He explained how the choice of equipment materials is influenced by parameters such as corrosivity, flowrates and chloride and hydrogen sulphide levels. However, equally important are the heat treatment condition and mechanical properties required, the corrosion resistance and issues such as weldability and ongoing costs for inspection maintenance and repair of materials selected. Rob referenced a number of international sources which are particularly useful for materials selection and stressed the need to examine Manufacturer capability and quality control of the product:
• Norsok M-001 (edition 5, Sept 2014)
• ISO 21457
• ISO 15156 (NACE MR-0175)
3. Oilfield Microbiology Analysis and Data Trending
Carol Devine, PhD, BSc (Hons) of NICMB has over twenty-five years’ experience in oilfield microbiology. She has a particular interest in microbiologically influenced corrosion (MIC), sulphate-reducing bacteria (SRB), seawater injection systems and molecular microbial ecology in general. NCIMB preserve, store and supply a collection of cultures to industry and universities with the largest collection of industrial, marine and food bacteria in the UK and have approx. 10,000 strains; 300 genera; 2000 species – and still growing.
Oilfield equipment is commonly damaged by the presence and activity of micro-organisms in systems for Production, Seawater Cooling, Water Injection, Cooling/Heating and in handling of Produced Water, Firewater, reinjection (PWRI), Diesel Storage & Ballast Water. The Organisms are either Planktonic from bulk water phases or Sessile biofilms on surfaces.
Carol explained the role of the oilfield microbiologist in generating useful and appropriate data in order to:
• Predict which particular systems, vessels, pipelines, locations are under threat from microbiologically influenced corrosion (MIC)
• Prioritise areas for treatment according to budget and time available
• Apply and monitor appropriate strategies to mitigate against the effects of MIC or biofouling
Techniques for analysis where explained: Triplicate MPN’s, qPCR and Metagenomic Analysis (NGS) to assess the threat of MIC and to quantify, identify and assess the activity which needs to be monitored on a continuous basis to see trends from production changes and implement actions to control and prevent system infestation which affects flow and efficiency in the process.
4. Corrosion Mitigation by Cathodic Protection
Dr. Nigel Owen, B.Sc., D.I.C, Ph.D., MIMMM, MICorr, Aberdeen Foundries has worked in the Aluminium Industry for over 35 years on alloy development and manufacturing processes, spending his later years at Aberdeen Foundries as Sales, Technical and Plant Manager, manufacturing Sacrificial Anodes He now oversees manufacturing, testing and design of all subsea and marine sacrificial anode systems.
Nigel explained how the Galvanic table shows naturally what materials are suitable as bases for sacrificial anodes. Aluminium, Zinc and Magnesium being the primary common bases for development of the alloys. With a sufficiently electronegative potential the base material can be alloyed with other elements to make it more electronegative and efficient as an anode. Aluminium has a high current output per Kg consumed and therefore has become the material of choice for anodes, particularly on large structures.
His presentation covered:
• Alloys for Sacrificial Anodes
• Design of a CP system to protect a structure
• Applications of Anodes
• The selection of the CP system:
• The pro’s and con’s of Sacrificial and Impressed systems and their applications.
The process of designing of a sacrificial anode system was explained from assessment of (cathode) material areas and the effect of coating to the calculation of anode mass and current output for a structure in an immersed environment.
Comparison was made between Sacrificial and impressed current systems in terms of their benefits or advantages in given current demand situations and maintenance requirements. Performance being determined by the conductivity (salinity) and the temperature (water depth/ geographic region) of deployment.
5. Corrosion Mitigation by Coatings
Colin Thomson HND, FM Lead at Bilfinger Salamis, has over 20years experience working in oil and gas fabric maintenance after serving in the Merchant Navy. He has supported various clients FM requirements including, BP, and Conoco Phillips, ExxonMobil and Petrofac. He skilfully explained how Fabric Maintenance prevents corrosion, degradation and wear which could otherwise lead to safety and or operational issues. Coatings acts as a barrier to the environment therefore all locations where coatings are damaged must be maintained to prevent metal loss. Colin also brought everyone up to date with modern FM strategies and also instantaneous barrier methods such as anti-corrosion tapes (ACTs) and Corrosion Inhibiting Waxes.
Various key properties of coatings were highlighted including:
• Anti-Fouling
• Environmental Protection
• Fire Protection
• Process Flow aids.
• Safety
• Thermal protection / insulation
The complete range of surface preparation techniques were evaluated along with all factors affecting coating ‘Life Expectancy’ for example:
• Anchor Pattern (too rough or too smooth)
• Chemical Salts
• Condensation
• Existing Coatings
• Fabrication Defects (weld spatter, sharp edges)
• Mill Scale
• Oil, grease and soil
• Surface Corrosion
6. Corrosion and Chemicals Management
Jennifer Watson HNC, Senior Account Manager/Production Chemist at Champion X is currently based within the BP office supporting Glen Lyon FPSO and has over 20 years experience in Oil & Gas operations offshore and onshore. She enthusiastically described all the key chemical mitigations deployed within the energy sector including:
• Biocides for preventing MIC
• Corrosion inhibitors for internal corrosion
• Drag reduction
• Oxygen and H2S scavengers pH stabilization
Jen also discussed all commonly used monitoring processes and analysis methods for rates, chemical residuals and other dosing checks. Most importantly she emphasised the need for having appropriate Chemical & Corrosion Control Matrices (CCCM) in place. These are the basis for understanding individual threats and how they should be mitigated by applied chemical application or other barriers.
A magnificent Lunch followed with an opportunity for all to network.
One of many Networking Opportunities.
7. Integrity Management and Risk Based Inspection.
Simon Hurst, BSc, MSc has been with CAN since 2008 and is currently the Engineering Director where he is responsible for the ENGTEQ business stream and is the nominated Technical Manager under their UKAS Accreditation for Integrity Management and Pressure Systems Inspection. He commenced his talk by defining Integrity Management – BS ISO 55000:2014 states that it enables an organization to achieve its objectives through the effective and efficient management of its assets. The application of an asset management system provides assurance that those objectives can be achieved consistently and sustainably over time.
Simon went on to define some of the key components of Asset Integrity Management including the following:
• Ageing and Life Extension
• Anomaly Management
• Corrosion Control Matrices
• Failure Investigations
• Integrity Operating Windows
• Risk Based Assessments leading to Risk Based Inspection
He then defined with good detail the nature of risk and the various different methodologies for Risk Based Assessment. In relation to CRA’s Simon usefully highlighted that:
• Although the use of corrosion resistant alloys generally leads to an increase in the time between inspections, the subsequent inspection of those CRAs is normally significantly more problematic than say on Carbon Steel.
• The use of CRAs (v CS) doesn’t normally lead to a significant increase in the periodicity for the first in-service inspection as this is more about identifying fabrication type defects than in-service damage.
In closing he reminded Delegates that it is best practice to create a “Written Scheme of Examination” (WSE) that details the applicable degradation mechanisms, and the precise location and inspection technique that will be used in order to try and either find the mechanism or confirm its absence.
8. Corrosion and Erosion Monitoring
Dean Smith is an experienced Operations Manager in the Corrosion Monitoring industry, having started his career as a Retrievals Technician in 2007 and worked his way up to field services management and eventually operations management. He emphasised that erosion and corrosion pose significant challenges to oil and gas production, impacting safety, efficiency, and profitability and effective monitoring techniques, combined with ongoing innovation and investment, are essential to mitigate these challenges and ensure the sustainability of the industry.
Prior to the practical demonstrations, Dean gave a run-through of the key services of Rysco UK which cover the following:
Design & Supply of Internal Corrosion Monitoring Systems including: High & Low Pressure Access Systems:
• Custom Equipment Design & Manufacturing
• Electronic Monitoring, e.g., Electrical Resistance Instruments
• Injection & Sampling Systems
• Mechanical Monitoring, e.g., Corrosion Coupons
Field Services including: High and Low Pressure Monitoring Device Retrieval.
• Hot Tapping
• Monitoring Data Analysis and Reporting
• Monitoring System Audits
• Sampling and Lab Analysis
Online Reporting including: Custom Reporting Dashboards via Business intelligence Software and Interactive Mapping
Sponsor’s Process Equipment Demonstrations
Three separate demonstrations followed for which the 52 strong gathering was split into 3 rotating groups.
Richard Rae of Rysco U.K explains Integrated Corrosion Data Management
Retrieval Tool Demonstration
Corrosion Coupon Review
A Corrosion Quiz covering multiple aspects of the Speaker Presentations followed by a vote of thanks from the President and CPD awards closed this very successful event attended by over 50 delegates.
Delegates enjoying the Corrosion Quiz
ICorr Aberdeen welcomes suggestions for further Industrial visits.
Abstracts of potential papers for the Aberdeen Technical Programme are always welcome, and anyone wishing to join committee should correspond with the 2023/2024 Technical Programme Co-ordinator: Adesiji Anjorin anjorin@gmail.com
Further Information about the Aberdeen Branch, and past presentations, may be found on their website page: Aberdeen Branch – Institute of Corrosion (icorr.org), and to join the Aberdeen Branch mailing list, please contact: icorrabz@gmail.com
Aberdeen Branch
ICorr join forces with IMechE for a special Pre-Christmas Celebration.
On 20th December 2023, the Aberdeen ICorr Branch were guests of IMechE for a Joint Event at the Sandman Hotel in Aberdeen. This end of year Celebration that was very well attended with around 60 guests and was chaired by Steve Cromar CEng, FIMechE, IMechE Aberdeen Chair. The evening commenced with a welcome Hot Buffet Dinner, which was an excellent choice for a cold Winter night.
Tom Baxter a Chemical Engineering Consultant and founding member of the Hydrogen Science Coalition spoke on ‘Future Energies and Greenhouse Gas Reduction’.
Tom Baxter BSc (Hons), FIChemE
Tom graduated from Strathclyde University in 1975 with a B.Sc. in Chemical Engineering (first class honours) and is a Fellow of the IChemE. He started his career with ICI Petrochemicals, moved to fine chemicals with the Swiss company Ciba-Geigy before taking a position as a Process Engineer in 1980 with BNOC (British National Oil Corporation). Through privatisation and acquisitions BNOC became Britoil, then BP. Here he worked as an Operations Engineer, Development Engineer and Research Manager. In 1991 he left BP subsequently held positions with Altra Consultants as Technical Manager, as Technical Director with Genesis in 1998 and became the Aberdeen Business Unit Director in 2005. From 2010 together with became a Senior Fellow in the Chemical Engineering Department at Aberdeen University, which he helped establish and since 2003 he has been a visiting Professor of Chemical Engineering at Strathclyde University.
This coming decade is extremely important for achieving reductions and Individual impacts are great. During his most interesting talk key themes discussed were ways to use less energy and an eye-opening debate on the misconceptions about renewable alternatives, (in terms of actual energy efficiency breakdown from production through to final distribution) which was considered in great detail. Overall electrification came out as a very safe and efficient energy source.
Industrial Hydrogen Use
Hydrogen (H2) does have some favourable characteristics – particularly buoyancy and no carbon monoxide but has low caloric value. Generally, Hydrogen compares unfavourably overall with Methane properties and has limited applications presently. For example, it requires three times the amount of compression power to move it along pipelines and much talked of blending Hydrogen was not seen as a good idea although a 20% blend has much promoted of late by others presenting to the Institute.
H2 is considered applicable for Transport (although passenger car-dominated) and for some specialised industries e.g. steel making. There have been recent question marks over some H2 driven projects. Pau (in France) cancelled its H2 buses and the Redcar hydrogen project was recently cancelled.
Full electric vehicles are seen as most energy efficient, for trains only low train passenger routes in the UK (8ookms out of 15000 kms) but there are lots of Hydrogen miscellaneous uses, but batteries are the key to the future progression of renewables. Presently the accurate Hydrogen retail cost is not clearly defined.
Tom Baxter (seated) Chemical Engineering Consultant and Hydrogen Expert presented.
Tom also spoke of https://www.h100fife.co.uk/ a parliamentary party group with interests including Cadent / Shell / others – Projected costs to 2050 however are not considered reliable.
Domestic Hydrogen Use
Vested interests e.g. Catapult and EUA have recently promoted Hydrogen for heating. Tom reviewed the outcomes of hy4heat – Hy4Heat Its mission was to establish if it was technically possible, safe and convenient to replace natural gas (methane) with hydrogen in residential and commercial buildings.
Through a QRA study, they found that Hydrogen was inherently less safe than Methane QRA with three times as many potential events. Hydrogen usage requires more safety features and is 40% less energy efficient overall. Electric energy provides greater wattage.
Summary
Generally, with renewables, more government support is needed, so as to give more headroom / opportunity to recover capital cost over a longer period.
Tom Baxter was extremely knowledgeable and provided a most interesting talk.
Refer www.h2sciencecoalition.com
Hydrogen Science Coalition | Bringing an evidence based viewpoint into the political discussion on hydrogen (h2sciencecoalition.com)
Members of the Aberdeen ICorr Committee, with new member Stephanie Okoye 2nd from Left, with guest Shukun Liu (Oceaneering) far right.
Q&A
A lively Q&A followed:
- Will Hydrogen deliver in the short term? – No. Tom was of the view that the UK government was without a proper energy strategy and unfortunately its politicians are mostly not Stem educated (only about 10%) and therefore don’t ask right questions when dealing with potential energy providers.
- How do we manage the Stakeholders for H2 development? – Tom felt that key policy must come from Government but they must understand all the issues.
- How can we educate local communities properly about energy and renewables? – Tom proposed that Engineering Institutions like IMechE and ICorr are best placed to provide reliable information to the public.
Future Meetings
The Aberdeen Branch of ICorr hopes to continue its relationship with IMechE during the next Technical Session 2024-2025
IMechE Aberdeen meet on the third Wednesday of each month and may be contacted at:
Contact the Aberdeen Area – Institution of Mechanical Engineers (imeche.org)
ICorr Aberdeen meet on the last Tuesday of each month and may be contacted at:
icorrabz@googlegroups.com
Aberdeen Branch, Institute News
On Tuesday 30th May 2023 the branch welcomed David Wickham and Chris Fyfe of AkzoNobel, who gave a talk on Maintenance and Repair Solutions for Damaged or Aged PFP. This was a hybrid Joint ICorr/AMPP event with over 40 Attendees.
The branch was very pleased to be able to return to the Palm Court Hotel on this occasion, a place with which it has so long been associated.
David Wickham is a practising fire and explosion engineer with 24 years’ experience in the field of passive fire protection. He is a Chartek fire engineer / technical manager, Fire Protection, holds a Master’s degree in Fire and Explosion Engineering from the University of Leeds, UK (2002), and is also an ICorr PFP Epoxy Coating Inspector Level 3. David is currently the Fire Protection Technical Manager at International Paint (part of AkzoNobel) a member of the Institution of Fire Engineers (MIFireE), and also a visiting lecturer on the MSc course, presenting on ‘Aspects of Fire Protection in building design’. He is responsible for providing technical support for upstream and downstream oil and gas projects, fire protection in the Built Environment and ‘special projects’ and has particular expertise in the area of ‘fire testing and evaluation of test data’ to support accreditation and certification of products to global fire test standards. Along with fire protection in Maintenance and Repair (M&R), he is currently a project leader looking at solutions for fire protection for battery electrical energy storage systems (BEESS).
Chris Fyfe is a PFP Senior field auditor and coach. As a Chartered Scientist, Senior Corrosion Technologist, and Fellow of the Institute of Corrosion, Chris also holds an AMPP Senior Level 3 coating qualification. He has extensive knowledge of both new build and maintenance projects ranging over 35 years with several operators and has been employed as a surface protection specialist and fabric maintenance coordinator, understanding first-hand the many challenges for maintenance and repair.
Maintenance and Repair Solutions for Damaged or Aged Passive Fire Protection (PFP)
Many facilities have reached, or are reaching, the end of their original design life. However, in many cases, these facilities are required to continue operation beyond this time. This poses many operational health and safety issues, among them the efficacy of in-situ passive fire protection (PFP) that may have been applied when the facility was first commissioned. In many cases, this PFP will have deteriorated to a point where it may not provide the required protection in the event of a fire. Where this damage may be extensive, this can create difficult economic (M&R) decisions to overcome. M&R resources are not limitless, and where repair priorities have been identified, selecting the most efficient repair solution becomes important. The two most important requirements are demonstrable fire resistance performance and application costs (both materials and installation). In many cases, the latter may far outweigh
the former. Costs of installation may have a significant bearing in active process areas subject to limits on operational activities (such as surface preparation).
On older upstream and downstream facilities, in-situ PFP may comprise structural steel encased in dense concrete, Light-Weight Cementous (LWC) or other systems. Where these types of PFP are cracked or damaged, they may expose the substrate, leading to accelerated corrosion, operational integrity concerns, and dropped object hazards, in addition to concerns about continued PFP functionality. The true extent of all underlying corrosion may not be immediately apparent, and removal or replacement is normally the best course of action.
As a company, AkzoNobel recognises how M & R activities surrounding PFP performance are integral to maintaining plant operational safety by allocating limited M and R budgets more effectively. – this includes identifying and prioritising the damage of most concern (fire integrity assessment – what damage level will not meet the site fire scenario) and providing repair materials that: have proven fire resistance performance, and offer ease of installation.
The company has identified various schemes for items that need PFP repair:
• Scheme 1 – PFP adequate for the fire case – repair solution to arrest rate of corrosion.
• Scheme 2a) – Risk of dropped object hazard – repair required to remove the hazard and ensure repair is PFP functional.
• Scheme 2b) – loss of PFP functionality and corrosion concern – tested repair solution that reinstates the PFP and stops advancement of corrosion.
• Scheme 3 – ‘special case’– repair acceptable based on other criteria or requiring specific fire testing.
Examples were given of the putty and mortar products used in the repairs onto primed or prepared surfaces and their characteristics:
• MP: A single component mouldable putty compound.
• SFR: Single component structural grade mesh-free repair mortar.
• No tools required – MP can be applied direct from the pail by hand.
• SFR only mixing with water required – and can be applied direct by hand.
• Both the above products are completely non-hazardous and repairs can be completed without any hot work permits.
For Missing and Cracked PFP – Concrete / LWC:
• SFR product can be used; this product has been both jet and pool fire tested for over 180 minutes.
• MP is an alternative and this is jet and pool fire tested to 120 minutes. The products can fill cracks up to 50 mm wide and voids up to 900 cm2 and are Lloyds / UL verified.
For the repair, the edges of the concrete to which it will bond need to be checked for contaminants, and wire brushing should be used to clean the surfaces. Any exposed steel needs to be cleaned and an approved surface tolerant primer, such as 670HS, applied. Where the base material is concrete, the cementitious edges should be wetted to improve adhesion, and PVA glue should be used as an additive agent to help bond. The Interkote material needs to be brought flush with the concrete for this repair, no wire netting is required.
On Tuesday 28th March 2023, the branch meeting welcomed Dr Kevin McDonald – Sonomatic, with a talk entitled ‘Effective pipework analysis and inspection planning using Digital Twins’.
Kevin is a principal integrity engineer within Sonomatic’s integrity team in Aberdeen. He is a mathematician with a PhD in computing science. He has extensive experience in data analytics and inspection planning for pipework, pressure vessels and pipelines, co-authoring the recommended practice for Non-Intrusive Inspection (NII) as applied to pressure vessels. As well as integrity consulting, he is involved in the technical capability development for Sonomatic’s integrity team with a focus on statistical approaches. Recently, he has been involved in developing a statistics-based method of inspection planning and evaluation applied to subsea pipelines for a major operator.
Effective pipework analysis and inspection planning using digital twins
The integrity of pipework is essential for the safe and reliable operation of process plants. Inspections are traditionally performed at large numbers of individual test points, with results recorded in an inspection database. In general, this data is subject to relatively simple analysis, with the results used in integrity management decisions. However, this traditional approach can be heavily influenced by poor processes, outliers, or errors for example: incorrect entry of results, not recording higher thickness readings than those obtained previously, and inconsistencies in inspection location, are some examples of how error can be introduced into this process. This could lead to poor integrity decisions and misinterpretation of wall thickness trends. Analysis of pipework data, which is in general restricted to the difference between two thickness readings relative to the dates the readings were taken, can then be driven by measurement error.
Kevin proposed a novel alternative is to consider historic datasets as a whole and look at long-term statistical behaviour to consider how corrosion could be affecting pipework. This approach looks at whole datasets to determine behaviour before considering any sub-groupings of data points that are showing similar behaviour. The Sonomatic developed SPiDARS software accommodates many data formats. Boxplots can be used to display the whole of an inspection history in one view. In this example a normalised view allows all schedules of pipe to be compared. Boxplots can also be used to provide a quick overview of long-term trends (up or down) and can show stability over several years or highlight changes graphically that cannot be seen from data alone, due to spreads and errors affecting judgement.
The illustrated example shows a downward long-term trend indicative of increased corrosion activity. It provides context and a jump in the final result, indicating replacement of the pipe. Data can also be grouped for pipes by diameter which can show that larger pipes seem to have more corrosion issues than smaller ones, or by pipe configuration feature type such as bends, caps, reducers, or straight sections to search for trends.
Corrosion rates determined from Non Destructive Testing ( NDT) generally trend toward wall loss percentile values as the principal criteria. Looking at group trends mitigates measurement error and gives more accurate short and long-term corrosion rate estimates. Any point showing a concerning trend can be extrapolated to predict when an alarm limit may be reached. Corrosion rate data can be plotted in different ways to try and identify issues such as localised and unusual corrosion rates. Lots of data on wall thickness measurement may just behave in a linear sense such as presented here for selected years and locations – nothing unusual is shown and general corrosion is happening at expected rates.
Sonomatic have developed 3 different inspection planning methodologies. The Type 2 methodology was further discussed with steps detailed below:
• Define corrosion state (is it what we expect to find)
• Define a corrosion coverage from previous results
• Define extent of corroded material
• Define thresholds of concern (based on historic results)
• Consider points flagged as over/under inspected
• Consider expected corrosion mechanisms that have a bearing on applied technique
• Define detection threshold
• Define probability of detection (POD)
This approach is underpinned by simple and effective access to the data, which is linked to a 3D mini digital twin.
The mini-Twin also hosts a variety of data, as well as individual test points, corrosion maps, and can house inspection histories, photographs, and further data analysis of corrosion rates, fitness for service etc. 3D is used to present data in efficient ways to quickly provide an overview of the health of the pipework circuit, for example inspection frequency, inspection count, corrosion rates, all of which is valuable information for engineers and asset stakeholders.
For identified ‘Dropped Object’ hazards: the item can be encased using GRP wrap + Chartek 7E paste filler at 2mm or an encasement system pipe shell or epoxy box is used with product Chartek/Benarx, for which there are simple procedures (see image below).
Systems were also discussed for upgrading 3 sided beams using either Chartek 2218 at a 6mm thickness level to primed steel areas and overlapping the cementitious edges either side, or alternatively MP can be used and applied to steel surface prepared to SP11 finish. This material can be rolled out at a 30 mm layer thickness that adheres to the prepared steel. This solution is good for support beams for walkway grating supports.
Studies were also presented on fire testing of the repaired products to given standards.
Fire Testing of Repaired Products
The fire performance of both Interkote MP and SFR has shown excellent fire performance (in some cases better) than the in-situ LWC or concrete. IK MP was verified in EPFP testing (TN to update). Technical note F_021 may be deployed to select the best repair solution to meet fire protection requirements.
AkzoNobel’s PFP repair solutions extend the available range of Chartek solutions for maintaining damaged or failing PFP. The focus is on simple repairs to damaged LWC and concrete PFP (EPFP to be added for IK MP) for application simplicity and cost-effectiveness. The intention is to give customers confidence that repair solutions will provide the required fire resistance and repair integrity. All the repair solutions are backed up by third party approvals.
The branch held its AGM on June 27, 2023, and unanimously elected Adesiji Anjorin MSc, BEng, CEng, MICorr, MNSE, COREN of ENGTEQ as its next Branch Chair and Mei Ling Cheah AMPP Certified Corrosion Specialist, BEng MSc PhD CEng CSci FIMMM FICorr, of IMRANND as
its new Vice Chair.
The branch was sorry to see the departure of its 3 times Chair, Dr Muhammad Ejaz, PhD, CEng, FICorr, FIMMM, AMPP Corrosion Specialist, after 13 years of service, and a presentation will be made to him at a later date, once he has settled into his new home in Abu Dhabi.
On the same day, the branch also held an online event entitled – Direct Assessment for Unpiggable Pipelines, which covered both Internal and External Corrosion threats, and was led by Dirk L.Van Oostendorp.
Dirk is Director of Engineering and Technical Services for Corrpro, based in Houston, TX and Van Oostendorp has more than 40 years of global experience in all aspects of pipeline and structural integrity, encompassing cathodic protection, corrosion control, material selection, protective coatings, inspection technologies, and risk assessment. More recent experience includes integrity monitoring, failure analysis, and pipeline integrity issues. He holds undergraduate and graduate degrees in chemical technology and physical chemistry. He is a Fellow of the Royal Society of Chemistry, a Fellow of the Institute of Corrosion, and a NACE Corrosion Specialist. He was a member of the original INGAA-Battelle team that developed what has now become the Direct Assessment Methodology (DAM).
This presentation discussed the four essential steps of the Direct Assessment methodology, highlighted success factors, shared results from actual projects, and assessed the various challenges that can be encountered during implementation.
The majority of North American natural gas transmission pipelines were not constructed to permit inspection using intelligent tools (ultrasonic, magnetic flux leakage). This was due to the lack of launching and receiving facilities, but also throughput requirements, varying (telescopic) diameters, short radius or wrinkle bends, reduced port valves, or branch connections. In order to adequately ensure the structural integrity of these pipelines, some alternative forms of condition determination and evaluation was required. The Interstate Gas Association of America, together with the
Gas Technology Institute, assembled an expert team to address this
issue. The result was the development of an alternate inspection methodology, coined Direct Assessment, which made use of a combination of proven techniques.
Based on Federal laws signed in 2001, pipeline operators in the USA were required to develop a proactive Pipeline Integrity Management Plan (IMP) intended to manage risk and protect the public in areas near operational pipelines. Inline inspection (ILI) was the preferred methodology to inspect pipelines, and hydrostatic testing was the alternative.
AMPP, as the industry representative, was called upon to develop standard procedures to govern the correct implementation of Direct Assessment and provide guidance for practitioners. Early in the development process, it was noted that the methodology needed to be segmented, in order to address differing integrity threats, and External Corrosion Direct Assessment (ECDA), Internal Corrosion Direct Assessment (ICDA), and Stress–Corrosion Cracking Direct Assessment (SCCDA) resulted. NACE initially published RP0502 for ECDA in 2002, and other standard practices for the other methodologies followed. As living documents, these standard practises are subjected to peer review every 4–6 years.
Dirk very clearly explained the details of the processes now being followed and how supplementary investigations may come into play as the assessment proceeds.
Both the AGM and the June presentation were fully recorded and are available at: https://youtu.be/B9_4DHySnmg and at ICorr Aberdeen – YouTube
Abstracts of potential papers for the Aberdeen Technical Programme are always welcome, and anyone wishing to present should correspond with the 2023/2024 Technical Programme Co-ordinator: Adesiji Anjorin anjorin@gmail.com
Further Information about the Aberdeen Branch, and past presentations, may be found on their website page: Aberdeen Branch – Institute of Corrosion (icorr.org) and to join the Aberdeen Branch mailing list, please contact: icorrabz@gmail.com
The Branch has the following upcoming conference event for which attendance is strictly limited to 50 persons: This Event will include a number of Practical Demonstrations.
On 22nd August, the branch will hold its Corrosion Awareness Day at Rysco, Bridge of Don, Aberdeen, from 9-5pm
Attendees (and their respective companies) will gain an understanding of the fundamentals of corrosion science and engineering; which can give insights into technical corrosion / materials challenges, improve their understanding of corrosion processes, raise their awareness of corrosion management, and provide confidence to attendees when discussing corrosion-related issues and concerns; and sales people will gain insights into the corrosion problems and needs of their customers by enabling relevant technical conversations with clients regarding corrosion issues.
Registration for this Event closes on 15th August 2023.
Please see the ICorr Events Calendar for all the latest information.
TABLE:
ITEM F EXISTING PFP / SUBSTRATE DEFECT / ANOMALY TYPE
Concrete Or Cementiltious PFP / Carbon SteelDropped Object Hazard
Repair System Installation Photos/Drawings Limitations / Notes
Chartek 7E
& GRP Overwrap a) Damaged/loose concrete/cementitious should be left in place.
b) Cut the GRP material so that there is a minimum 50 mm overlap around the perimeter of the section being wrapped.
c) The GRP should be pulled tight around the damaged PFP and then left to cure. Cure time is dependent on good light levels which should be between 1-2 hours. Any top protective layer should be removed to leave a matt surface finish.
d) Once the GRP is fully , apply Chartek 7E at minimum 2 mm directly to the matt surface of the GRP. No primer required. Refer to the GRP manufacturers manual for application instructions.
Benarx Boxes & Pipe Shells a) Damaged/loose concrete/cementitious should be left in place.
b) The Benarx box/pipe shell can be fitted around the loose PFP and held in place using integral toggle & latch fasteners or stainless steel bands. Installation of Benarx solutions will require accurate measurements to ensure
correct fit.
CAPTIONS:
David Wickham and Chris Fyfe of AkzoNobel.
PFP Interkote Repair Solutions – Site in Belgium.
Failed LWC on vessel skirt.
Cut out defective LWC Simplehand application of KSFR.
Interkote SFR finished repair.
Interkote SFR@50/28mm Concrete/LWC repair –jet fire testbox.
InterkoteSFR –post jet firetest.
IMAGE Left to Right – Aberdeen Committee Members at June AGM – Mei Ling Cheah – New Branch Vice Chair, Yunnan Gao – ICorr Vice President, Nigel Owen – External Secretary, Lian Ling Beh – Internal Secretary, Leela Ramachandran – University Liaison & CPD Officer, Adesiji Anjorin – New Branch Chair and Stephen Tate – ICorr President.
Dirk L. Van Oostendorp, Director of Engineering and Technical Services for Corrpro.