AMPP Store - Products tagged with 'carbon dioxide'

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00047 CO2-CORROSION AND WATER DISTRIBUTION TWO PHASE PIPE FLOW OF HYDROCARBON LIQUID AND WATER

Product Number: 51300-00047-SG

ISBN: 00047 2000 CP

Author: Arne Valle

Publication Date: 2003

$20.00

To analyse the influence of a non-corrosive hydrocarbon liquid phase with respect to CO2-corrosion in pipe flow and increase the understanding of use of natural inhibitors in the hydrocarbon liquid phase, an experimental study of corrosion and water distribution on the pipe wall has been carried out.

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02273 THE ROLE OF ACETATE IN CO2 CORROSION OF CARBON STEEL: HAS THE CHEMISTRY BEEN FORGOTTEN?

Product Number: 51300-02273-SG

ISBN: 02273 2002 CP

Author: Yannick Garsany, Derek Pletcher, and Bill Hedges

Publication Date: 2003

$20.00

The influence of acetate ion on the rate of corrosion of carbon steel (X65) in 3 % NaCl brine saturated with carbon dioxide has been investigated using voltammetry at a rotating disc electrode. The rate of corrosion can only be understood if it is recognised that the cathodic process in the steel corrosion is affected by acetic acid.

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05551 CO2 Corrosion Prediction Model - Basic Principles

Product Number: 51300-05551-SG

ISBN: 05551 2005 CP

Author: Stein Olsen, Statoil ASA; Anne Marie Halvorsen, Norsk Hydro ASA; Per G. Lunde, Norsk Hydro Americas;

Publication Date: 2005

$20.00

The NORSOK M-506 is an empirical model based on experiments undertaken in a single phase water flow loop. The data is from experiments with low content of iron ions in the water phase, and the model is thus regarded to give a fair representation of the maximum corrosion rate in a CO2 corrosion controlled system.

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09022 How Not to Perform a Failure Analysis

Product Number: 51300-09022-SG

ISBN: 09022 2009 CP

Author: Mark S. Schilling and Randy Nixon

Publication Date: 2009

$20.00

This paper discusses a classic example where the facts surrounding the failure of a lining system were ignored and undue reliance was placed on laboratory analysis. This “blind faith” in analytical data without a sound causal theory caused the failure analysts to disregard or overlook the obvious.

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51318-10965-Evaluation of Corrosion Inhibitor Functionality on the Mitigation of Preferential Weld Corrosion

Product Number: 51318-10965-SG

Author: R. Barson / D. D. Korwin-Kochanowski / S. Turgoose / G. Economopoulos / G. E. Dicken

Publication Date: 2018

$20.00

The work conducted produced conditions where preferential weld corrosion initiated in uninhibited conditions and was sustained throughout inhibition. Two types of weld metallurgies; one weld consumable with 1% nickel, the second matched the parent pipe.

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51318-11022-Case Study: Solving the Puzzle of 10inch Duplex Stainless Steel Flowline Weld Failure

Product Number: 51318-11022-SG

Author: Mushaid Nauman, Mohammed Rashid

Publication Date: 2018

$20.00

This paper discusses the detailed inspection, testing, metallurgical analysis and supporting factors from which the most likely cause of pitting corrosion was revealed in the DSS flowline welds.

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51318-11199-The Effect of Impurities and Pressure on Oxidation in CO2 at 700°-800°C

Product Number: 51318-11199-SG

Author: B. A. Pint / R. G. Brese / J. R. Keiser

Publication Date: 2018

$20.00

Effects of H2O and SO2 on oxidation in a CO2 environment. Experiments at 1 and 25 bar at 700° to 800°C in CO2, CO2+10%H2O and CO2+10%H2O+0.1%SO2. Alloys S30409, N07230, N07208 and superalloy N07247 exposed. Reaction products were characterized.

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51318-11232- Mechanism of CO2 Corrosion of Mild Steel: a New Narrative

Product Number: 51318-11232-SG

Author: Aria Kahyarian, Bruce Brown, and Srdjan Nesic

Publication Date: 2018

$20.00

The increased corrosion rates of mild steel in acidic solutions in the presence of CO2, previously associated with carbonic acid direct reduction, are in fact due to the increased rate of iron dissolution in the presence of CO2

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96009 FRACTURE MECHANICAL PROPERTIES OF C02 CORROSION PRODUCT SCALES AND THEIR RELATION TO LOCALIZED CORROSION

Product Number: 51300-96009-SG

ISBN: 96009 1996 CP

Author: G. Schmitt, T. Gudde and E. Strobel-Effertz

Publication Date: 1996

$20.00

Fracture mechanical properties of scales from wet corrosion were considered with respect to the initiation steps of flow induced localized corrosion (FILC) of steel under conditions of scale forming corrosion processes.

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Advancement of a Comprehensive Mechanistic CO2 Corrosion Model to Incorporate Simulated Hydrodynamics via a Turbulent Flow Model

Product Number: 51324-20657-SG

Author: Michael Jones; Gregory de Boer; Richard Woollam; Joshua Owen; Richard Barker

Publication Date: 2024

$40.00

In this work, two comprehensive mechanistic models of aqueous carbon dioxide (CO2) corrosion produced by Nordsveen et al.1 and Kahyarian et al.2 17 years apart are recreated and compared to highlight the evolution in understanding. The differences between the models include the role of carbonic acid at the surface, whether it is directly reduced or acts as a buffering agent, as well as different mechanisms for the anodic response, and varying temperature responses of multiple input variables. Through recreation and validation of these models using the same software, key comparisons are made to understand the effect of these changes on predicted corrosion rate, surface pH, and speciation through the boundary layers. These values are plotted across a range of input parameters to investigate how the change in scientific understanding influences predictive response of corrosion models.

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An Evaluation of Well Completion Materials for Impure Carbon Dioxide Supercritical Streams in Hydrocarbon Production and Geological Carbon Sequestration

Product Number: MECC23-20034-SG

Author: Manuel Marya

Publication Date: 2023

$20.00

Carbon capture and storage (CCS) represents to traditional industrial emitters a critical transitional technology to globally manage greenhouse gas emission, meet the latest carbon net-zero ambitions, and continue the commercial use of fossil fuels. In CCS, anthropogenic CO2 is captured near emission, treated, compressed, transported (usually by steel pipelines), injected underground through casings, tubings, and completion equipment, and finally permanently stored into saline formations, aquifers, depleted (abandoned) reservoirs, or un-mineable coal seams. [1] Depending upon emitters, the injected CO2 is either near or in a dense state (i.e., indistinctly including a supercritical phase and potentially liquids) having various impurities.

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Assessing Comprehensive Mechanistic CO2 Corrosion Modeling Methods and Their Impact on Predicted Corrosion Behavior

Product Number: 51324-20656-SG

Author: Michael Jones; Gregory de Boer; Richard Woollam; Joshua Owen; Richard Barker

Publication Date: 2024

$40.00

In this work, two comprehensive mechanistic models of aqueous carbon dioxide (CO2) corrosion produced by Nordsveen et al.1 and Kahyarian et al.2 17 years apart are recreated and compared to highlight the evolution in understanding. The differences between the models include the role of carbonic acid at the surface, whether it is directly reduced or acts as a buffering agent, as well as different mechanisms for the anodic response, and varying temperature responses of multiple input variables. Through recreation and validation of these models using the same software, key comparisons are made to understand the effect of these changes on predicted corrosion rate, surface pH, and speciation through the boundary layers. These values are plotted across a range of input parameters to investigate how the change in scientific understanding influences predictive response of corrosion models.

Products tagged with 'carbon dioxide'

Association for Materials Protection and Performance