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Picture for Evaluation of the Hydrogen Diffusion and Transport Kinetics in ASTM A508 Grade 4N
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Evaluation of the Hydrogen Diffusion and Transport Kinetics in ASTM A508 Grade 4N

Product Number: 51321-16404-SG
Author: Esteban Rodoni/Andreas Viereckl/Zakaria Quadir/Garry Leadbeater/Mariano Iannuzzi
Publication Date: 2021
$20.00
Picture for Evaluation Of The KIEC Of UNS N07718 With And Without Delta Phase In Simulated Seawater With Cathodic Protection Using Double Cantilever Beam Tests
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Picture for Evaluation Of The Suitability Of As Bent Super Duplex Stainless Steel UNS-S32750 Tubing For Refinery Sour Services
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Evaluation Of The Suitability Of As Bent Super Duplex Stainless Steel UNS-S32750 Tubing For Refinery Sour Services

Product Number: 51321-16850-SG
Author: Yong-Joo Kim; Karen Picker
Publication Date: 2021
$20.00
Picture for Evaluation of the Surface on CRA after the Actual Exposure in Sour Gas Well
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Evaluation of the Surface on CRA after the Actual Exposure in Sour Gas Well

Product Number: 51319-12946-SG
Author: Masayuki Sagara
Publication Date: 2019
$20.00

Corrosion resistant alloys (CRAs) have been used in exploration and production fields which contain high pressure high temperature and significant amounts of hydrogen sulfide carbon dioxide and chloride ion. As exploration for High-Pressure High-Temperature (HPHT) hydrocarbon reservoirs with corrosive environments has been increasing the industry needs corrosion resistant alloys (CRAs) for HPHT corrosive deeper well applications. It is highly profitable to apply CRA’s (corrosion resistant alloys) to sour gas environment. It can be thought that CRA shows the benefit for well development of these conditions from the point of minimization of life-cycle cost.With regard to the surface film formation mandatory elements of CRAs are chromium nickel and molybdenum because it is assumed that chromium forms oxide at the surface of the material and nickel and molybdenum assist the formation of the film in the condition. In this study the surface films on CRA of conventional UNS N08535 are analyzed. The film which is formed after the long term exposure in the actual well is compared with the one formed after the corrosion testing at laboratory.The surface film structure after the exposure in the actual well was composed of sulfides and oxides. This thin layer structure is consistent with laboratory results using small-scale specimens during a short exposure time (720 hours). These results clearly prove the effectiveness of the proposed corrosion resistant mechanism against corrosive environment and the validity of the original material selection.

Picture for Evaluation of Wall Shear Stress in Multiphase Flow and Its Effect on FeCO? Removal
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Evaluation of Wall Shear Stress in Multiphase Flow and Its Effect on FeCO? Removal

Product Number: 51315-5922-SG
ISBN: 5922 2015 CP
Author: Wei Li
Publication Date: 2015
$20.00
Picture for Evaluation Stress Corrosion Cracking And Localized Corrosion Influence Of Various Buffer Solutions For Simulated Well Condition
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Evaluation Stress Corrosion Cracking And Localized Corrosion Influence Of Various Buffer Solutions For Simulated Well Condition

Product Number: 51321-16577-SG
Author: Luciana I. L. Lima; Ilson Palmieri Baptista; Arthur Goncalves; Fabiana Magalhaes Teixeira Mendes; Javier ALejandro Carreno Velasco; Walter Souza; Cecile Millet; Marilia Lima
Publication Date: 2021
$20.00
Picture for Evolution Of Corrosion Potential Of Carbon Steel Storage Tanks Containing High-Level Nuclear Waste
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Evolution Of Corrosion Potential Of Carbon Steel Storage Tanks Containing High-Level Nuclear Waste

Product Number: 51321-16625-SG
Author: Pavan K. Shukla/ Roderick E. Fuentes/ Bruce J. Wiersma/ Crystal Girardot/ Jason Page/ Shawn Campbell
Publication Date: 2021
$20.00
Picture for Examination of Grounding Methodologies for HVAC Induction on Buried Pipelines
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Examination of Grounding Methodologies for HVAC Induction on Buried Pipelines

Product Number: 51315-5981-SG
ISBN: 5981 2015 CP
Author: David Kemp
Publication Date: 2015
$20.00
Picture for Excavation, Removal And Evaluation Of Coupons Exposed To AC Interference While Connected To An Operating Product Transmission Pipeline
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Excavation, Removal And Evaluation Of Coupons Exposed To AC Interference While Connected To An Operating Product Transmission Pipeline

Product Number: 51321-16566-SG
Author: Philip Simon, P.E / John McCaffery
Publication Date: 2021
$20.00
Picture for Expanded Service Temperature Limits of Polymer Liners in Water Injection Pipelines
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Expanded Service Temperature Limits of Polymer Liners in Water Injection Pipelines

Product Number: 51319-12796-SG
Author: Sai Prasanth Venkateswaran
Publication Date: 2019
$20.00

Polymer liners especially polyethylene liners are commonly used as internal liners in water injection service. Historical seawater/produced water applications have a typical design temperature of 60°C or less and are usually operated at 30 – 40°C. Handling of oilfield water in the operating temperature range of 60°C to 90°C becomes a challenge. Very limited such applications have been reported and details of specific operational conditions are not known to validate safe and reliable performance at high temperatures.This paper explores the current state of the art for the increased temperature limits of high density polyethylene liners and identifies the most credible failure modes to be mitigated. A testing campaign was conducted on commercial grade high density polyethylene to de-risk the application of the liners to operating temperatures up to 80°C. A series of small scale testing were performed to understand the material properties under different conditions (temperature oil saturation oil/water concentration etc.). Performance properties of typical high density polyethylene was benchmarked against a proposed raised temperature polyethylene grade. The material properties were used as an input to a finite element analysis tool to evaluate the strains experienced by the liner at different locations such as a weld bead flange connection vent location. The testing and analysis provides increased confidence to expand the operational envelope of polyethylene liners to higher temperatures in produced water service. A condition monitoring plan has been developed to record the liner condition during operation.