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- W78553650 abstract "The principal alternative for long-distance transportation of CO 2 from source to storage site is in pipelines. To a large extent pipelines can be made in carbon steel as pure, dry CO 2 is essentially non-corrosive. More corrosion-resistant materials or corrosion inhibition must be considered when the CO 2 contains water that condenses out during transportation. This will occur where it is impossible to dry CO 2 to a dew point well below the ambient temperature. Water-saturated CO 2 is corrosive when water precipitates, but experiments exhibit that corrosion rates at high CO 2 pressures in systems containing only water or water/MEG (monoethylene glycol) mixtures are considerably lower than predicted by corrosion models. This applies particularly at low temperatures that are typical for sub-sea pipelines in northern waters. This chapter focuses on determining the corrosion rate as function of CO 2 pressure up to 80 bar. The results are compared to existing corrosion models that have been developed to cover a pressure range relevant for oil and gas transportation, that is, pressures up to 20 bar. The experiments show that the models overestimate the corrosion rate when they are used above their CO 2 partial pressure input limit. At low temperature the models predict more than 10 times the measured corrosion rate. Finally, the results indicate that the corrosion rate has a maximum as function of CO 2 pressure at 40 and 50 ℃. The maximum is at 30-50 bar depending on temperature." @default.
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- W78553650 date "2005-01-01" @default.
- W78553650 modified "2023-09-30" @default.
- W78553650 title "Materials Selection for Capture, Compression, Transport and Injection of CO2" @default.
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- W78553650 doi "https://doi.org/10.1016/b978-008044570-0/50143-4" @default.
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