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A methodology was developed to identify and choose the most cost-effective material and also appropriate remedial corrosion inhibition and protection methods by using 4 reputable corrosion prediction models in dry and wet oil & gas pipeline containing CO2 with and without H2S.
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The first case of top of line corrosion (TLC) in Tunu gas field was reported by Gunaltun et al in 19991. Inlineinspection (ILI) of two carbon steel pipelines distributing multiphase effluent, showed up to 50% metalloss at 11.00 – 01.00 o’clock at several sections. Visual examination of a cut section showed that the topof line was covered with iron carbonate layer with deep pits, and severe metal loss occurred on largesurfaces at these area.