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CO2 corrosion is one of the most common problems faced during oil and gas production, although steelpipes offer a long-term economical use in CO2 corrosive environments with the application of carefullyselected corrosion inhibitors. Inhibitor efficiency is affected by many variables, including temperature,pressure, flow velocity, pH, and composition of produced water. The impact of brine composition oncorrosion inhibitor performance is elucidated in this work; more specifically, the question of whetherhigh salinity or high Ca2+ concentration has a greater impact on corrosion inhibitor performance isanswered. Corrosion inhibition performance of various inhibitors, including quaternary amines and alkylpyridine quat, were evaluated with brines of varying Ca2+ concentration (0 to 20,000 mg/L) and salinity[57,000 to 250,000 total dissolve solids (TDS)]. The corrosion inhibition was studied in situ by linearpolarization resistance (LPR), using a UNS G10180(1) (carbon steel). The goal of this study is to helpimprove corrosion inhibitor design for high calcium containing brines.
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