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Corrosion And Chemical Reactions In Simulated Ship Transport CO2 Containers

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  • Corrosion And Chemical Reactions In Simulated Ship Transport CO2 Containers
Picture for Corrosion And Chemical Reactions In Simulated Ship Transport CO2 Containers
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Product Number: 51321-16669-SG
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Pitfalls And Artefacts In Corrosion Experiments With Dense Phase CO2

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Picture for Corrosion reactions in simulated CO2 ship transport conditions
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Corrosion reactions in simulated CO2 ship transport conditions

Product Number: 51320-14572-SG
Author: Morten Tjelta, Bjørn Helge Morland
Publication Date: 2020
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For certain CCS (carbon capture and storage) projects, ship transport of captured CO2 to the storage site may prove more optimal than pipeline transport. The CO2 will be transported under two-phase conditions at low temperature (-10 to -25 °C) and moderate pressure (1.7 – 2.7 MPa), which are quite different from the typical pipeline transport conditions (5 – 60 °C and 7 – 12 MPa). Corrosion under pipeline conditions has been relatively well studied, and several conditions (impurity mixtures) that results in formation of corrosive acids have been identified. In contrast, almost no research exists on corrosion under ship transport conditions when the CO2 contains impurities. The present work tested corrosion of carbon steel at -25°C in CO2 with different concentrations of H2O, H2S, O2, NO2 and SO2. The experiments demonstrated that certain combinations of impurities gave no chemical reactions and no corrosion, while other combinations resulted in formation of solids and corrosive components that attacked carbon steel. The mass loss corrosion rate was around 0.1 mm/y. 
Picture for Effects of CO2 Phase SO2 content and flow on the Corrosion of CO2 Transmission Pipeline Steel
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51312-01322-Effects of CO2 Phase SO2 content and flow on the Corrosion of CO2 Transmission Pipeline Steel

Product Number: 51312-01322-SG
ISBN: 01322 2012 CP
Author: Fernando Farelas
Publication Date: 2012
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