Menu
Search
Filters
Close
Menu

Celebrate World Corrosion Awareness Day with 20% off eCourses and eBooks with code WCAD2024 at checkout!

99031 SIMULATION OF CO2 / H2S CORROSION USING THERMODYNAMIC AND ELECTROCHEMICAL MODELS

Picture for 99031 SIMULATION OF CO2 / H2S CORROSION USING
Available for download
Product Number: 51300-99031-SG
ISBN: 99031 1999 CP
Author: Andrzej Anderko and Robert D. Young
$0.00
$20.00
$20.00
A comprehensive model has been developed for the computation of corrosion rates of carbon steels in the presence of carbon dioxide, hydrogen sulfide and aqueous brines. The model combines a thermodynamic model that provides realistic speciation of aqueous systems with an electrochemical model for partial cathodic and anodic processes on the metal surface. The partial processes taken into account by the model include the oxidation of iron and reduction of hydrogen ions, water, carbonic acid and hydrogen sulfide. Also, the model includes the formation of iron carbonate and iron sulfide scales and their effect on the rate of general corrosion as a function of temperature and solution chemistry. The model has been verified by comparing calculated corrosion rates with laboratory data under conditions that mayor may not be conducive to the formation of protective scales. Good agreement between the calculated and experimental corrosion rates has been obtained. The model has been incorporated into a program that makes it possible to analyze the effects of various conditions such as temperature, pressure, solution composition or flow velocity on corrosion rates. KEY WORDS: CO2 corrosion, H2S corrosion, iron carbonate, iron sulfide, electrochemical model, thermodynamics
A comprehensive model has been developed for the computation of corrosion rates of carbon steels in the presence of carbon dioxide, hydrogen sulfide and aqueous brines. The model combines a thermodynamic model that provides realistic speciation of aqueous systems with an electrochemical model for partial cathodic and anodic processes on the metal surface. The partial processes taken into account by the model include the oxidation of iron and reduction of hydrogen ions, water, carbonic acid and hydrogen sulfide. Also, the model includes the formation of iron carbonate and iron sulfide scales and their effect on the rate of general corrosion as a function of temperature and solution chemistry. The model has been verified by comparing calculated corrosion rates with laboratory data under conditions that mayor may not be conducive to the formation of protective scales. Good agreement between the calculated and experimental corrosion rates has been obtained. The model has been incorporated into a program that makes it possible to analyze the effects of various conditions such as temperature, pressure, solution composition or flow velocity on corrosion rates. KEY WORDS: CO2 corrosion, H2S corrosion, iron carbonate, iron sulfide, electrochemical model, thermodynamics
PRICE BREAKS - The more you buy, the more you save
Quantity
1+
5+
Price
$20.00
$20.00
Product tags
Also Purchased
Picture for 00102 SIMULATION OF FeCO3/FeS SCALE FORMATION
Available for download

00102 SIMULATION OF FeCO3/FeS SCALE FORMATION USING THERMODYNAMIC AND ELECTROCHEMICAL MODELS

Product Number: 51300-00102-SG
ISBN: 00102 2000 CP
Author: Andrzej Anderko
$20.00
Picture for 01086 A MODEL FOR CALCULATING RATES OF
Available for download

01086 A MODEL FOR CALCULATING RATES OF GENERAL CORROSION OF CARBON STEEL AND 13% Cr STAINLESS STEEL IN CO2/H2S ENVIRONMENTS

Product Number: 51300-01086-SG
ISBN: 01086 2001 CP
Author: Andrzej Anderko and Robert D. Young
$20.00
Picture for 05551 CO2 Corrosion Prediction Model - Basic
Available for download

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.
Categories
Industry
Recently viewed
Popular tags
View all

Association for Materials Protection and Performance

© AMPP All Rights Reserved.
Membership Terms of Content Use
Contact Customer Support