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Picture for Corrosion Damage of Injection String From the Deep Geothermal Well IDDP-2 in Reykjanes Iceland
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Corrosion Damage of Injection String From the Deep Geothermal Well IDDP-2 in Reykjanes Iceland

Product Number: 51319-13247-SG
Author: Sigrun Karlsdottir
Publication Date: 2019
$20.00

The drilling of the second deep geothermal well drilled in the Iceland Deep Drilling Project (IDDP) at Reykjanes geothermal field was successfully completed in beginning of the year 2017. The previously drilled RN 15 production well 2500 m deep at the Reykjanes high temperature geothermal field was used as the base for the IDDP-2 well. The final depth of the IDDP-2 well reached 4650 m depth with a bottom hole temperature measured to be 427°C and a pressure around 340 bar. This made the bottom of the IDDP-2 well reach fluid at supercritical conditions and become the deepest geothermal well in Iceland. The well was then injected with coldwater for stimulation. During the injection the pumping was interrupted and the water in the well was able to heat up. When the injection string (pipe) was retrieved from the well extensive corrosion damages were apparent on the lowest part of the injection string. Cracks were also observed on a 500-meter interval of the injection string pipe starting from the bottom part. The injection string was visually inspected on-site and selected parts were chosen for further failure analysis. Specimens from the pipe and pipe connections were examined using an optical microscope scanning electron microscope (SEM) equipped with energy-dispersive X-ray spectroscopy (EDS) and X-ray diffraction (XRD) technique. This was done to investigate and discuss the most probably cause of the corrosion damages. Additionally the hardness of specimens of the pipe were measured and compared to the NACE MR 0175/ISO 15156 standard. This paper covers the procedure and results of the failure analysis of the injection string from IDDP-2 well.

Picture for Corrosion Data Management Using 3D Visualisation and a Digital Twin
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Corrosion Data Management Using 3D Visualisation and a Digital Twin

Product Number: 51320-14535-SG
Author: Robert Adey, Cristina Peratta, John Baynham
Publication Date: 2020
$20.00

There is a gap between the Integrity management systems used by companies to manage their assets and the needs of the CP engineer. Integrity management systems do not fully meet the needs of the engineer responsible for corrosion as they do not provide access and visualizations of all the data the engineer needs to make fast and informed decisions. There is also often no easy way to see the trends in the data, or easily access the relevant video and photographic data also recorded during the survey.

Data from surveys is normally contained in reports and EXCEL spreadsheets often with different measurement locations and inconsistent naming of the locations between reports. In this paper a system is introduced which enables engineers to manage and visualise in 3D CP survey data and provide access to all the relevant information through a 3D visual interface to any member of the teams. The software gives the engineer the ability to visualize in 3D the historical and predicted CP protection on the structure and the status of the anodes in the CP system. It also provides information on long term trends in the survey data.

By integrating the corrosion data with a simulation model a “digital twin” of the structure can be created to make predictions of the present and future protection of all parts of the structure. For example the engineer can easily use the software to systematically monitor the differences between the model predictions and survey data to identify anomalies and give early identification of problems which will require action.

The paper will describe the system developed and present applications of both the 3D corrosion data visualisation and the simulation based digital twin

Picture for Corrosion Failure Analysis And Corrosion Prevention Practice Of Water Injection Pipeline In Middle East Carbonate Oilfield
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Corrosion Failure Analysis And Corrosion Prevention Practice Of Water Injection Pipeline In Middle East Carbonate Oilfield

Product Number: 51321-16672-SG
Author: Zhengrong Ye; Xiang Zhou; Weidong Jiang; Zhichao Qiu; Xiaodong Cui; Guohao Chen; Huachang Chi; Weixiao Li; Zhiwen Yang; Maomao Wang
Publication Date: 2021
$20.00
Picture for Corrosion Failure Analysis of Corrugated UNS N10276 and Stainless Steel Flex Hoses
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Corrosion Failure Analysis of Corrugated UNS N10276 and Stainless Steel Flex Hoses

Product Number: 51321-16649-SG
Author: Surech Divi; Sri Krishna Chimbli
Publication Date: 2021
$20.00
Picture for Corrosion Fatigue and Chloride-Induced Stress Corrosion Cracking in Sulfur Recovery Units
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Corrosion Fatigue and Chloride-Induced Stress Corrosion Cracking in Sulfur Recovery Units

Product Number: 51324-20691-SG
Author: Saud I Al Otaibi; Mohamud Farah
Publication Date: 2024
$40.00
Sulfur Recovery units (SRUs) are widely used in the oil and gas industry to recover sulfur from refined products and acid gas waste from the natural gas process. This involves routing acid gas rich in hydrogen sulfide through a reaction furnace to produce molten sulfur in a thermal Claus reaction. Central to the operation of the SRUs is the Sulfur storage pit, which is an underground high depth structure used to temporarily store sulfur product before shipment. Sulfur pits contain a range of critical equipment and piping, such as sulfur product pumps and steam coils.The pumps are crucial for shipping the sulfur product, while the steam coils are used for maintaining the molten sulfur temperature between 270-280 °F to prevent solidification and higher sulfur viscosity. Consequently, any impact to the integrity of this equipment impacts the unit’s operational efficiency or worse, leads to total unit shutdown. This equipment is susceptible to a range of damage mechanisms resulting from both operational conditions, such as sulfuric acid corrosion and environmental cracking, resulting from steam leakage and ground water seepage respectively. This paper investigates sulfuric acid corrosion and corrosion fatigue — in sulfur pumps — resulting from the synergistic effects of both dynamic loading and chloride-induced pitting corrosion. The steam coils in the pit were also found to suffer from both sulfuric acid corrosion and chloride stress corrosion cracking. These damage mechanisms were determined following extensive metallurgical analysis of samples recovered from the pit. Furthemore, laboratory compositional analysis from various samples collected from the pumps and the pits showed significant quantity of sodium chloride, resulting from ground water ingress alongside corrosion, and cementitious products, such as iron sulfide, quartz – SiO2 and iron sulfate. These findings, alongside sample results of the post-inspection findings for the sulfur recovery unit pit and equipment, will be highlighted and discussed. Effective mitigations, including the use of permanent dewatering, will also be discussed.
Picture for Corrosion Fatigue Performance of Materials in Delayed Cokers and Coker Blowdown Piping System
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Corrosion Fatigue Performance of Materials in Delayed Cokers and Coker Blowdown Piping System

Product Number: 51324-20618-SG
Author: Haixia Guo; Millar Iverson; Simon Yuen; Sudeep Bohra; Liu Cao
Publication Date: 2024
$40.00