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10379 Internal Co2 Corrosion of Mild Steel Pipelines Under Inert Solid Deposits

Product Number: 51300-10379-SG
ISBN: 10379 2010 CP
Author: Jin Huang, Bruce Brown, Xiu Jiang, Brian Kinsella and Srdjan Nesic
Publication Date: 2010
$0.00
$20.00
$20.00
Under-deposit CO2 corrosion occurs when solids like sand, corrosion products, wax or a variety of other particles deposit on the bottom of pipelines, forming a bed or layer of solids. Underdeposit CO2 corrosion is different from “regular” CO2 corrosion as the aqueous solution beneath the solids is chemically and physically different from the “bulk” solution in the pipe. The presence of solids can also limit inhibitor access to the metal surface which can initiate severe localized corrosion.

Initial testing was directed towards defining and modeling the fundamental mild steel CO2 corrosion mechanisms occurring in the presence of clean inert solid deposits with different particle sizes and shapes (SiO2 powder, glass beads (GB) and sand). Experiments were conducted in a glass cell at a total pressure of 1 bar for temperatures of 25°C and 80°C. The mild steel sample was immersed in 1 wt% NaCl electrolyte for one day. Corrosion behavior was characterized by electrochemical techniques, including LPR (linear polarization resistance), EIS (electrochemical impedance spectroscopy) and potentiodynamic sweeps. Steel surface morphologies have been analyzed by using SEM (scanning electron microscope) and EDX (energy dispersive x-ray). Keywords: solids, under-deposit, CO2 corrosion, mild steel, pipelines
Under-deposit CO2 corrosion occurs when solids like sand, corrosion products, wax or a variety of other particles deposit on the bottom of pipelines, forming a bed or layer of solids. Underdeposit CO2 corrosion is different from “regular” CO2 corrosion as the aqueous solution beneath the solids is chemically and physically different from the “bulk” solution in the pipe. The presence of solids can also limit inhibitor access to the metal surface which can initiate severe localized corrosion.

Initial testing was directed towards defining and modeling the fundamental mild steel CO2 corrosion mechanisms occurring in the presence of clean inert solid deposits with different particle sizes and shapes (SiO2 powder, glass beads (GB) and sand). Experiments were conducted in a glass cell at a total pressure of 1 bar for temperatures of 25°C and 80°C. The mild steel sample was immersed in 1 wt% NaCl electrolyte for one day. Corrosion behavior was characterized by electrochemical techniques, including LPR (linear polarization resistance), EIS (electrochemical impedance spectroscopy) and potentiodynamic sweeps. Steel surface morphologies have been analyzed by using SEM (scanning electron microscope) and EDX (energy dispersive x-ray). Keywords: solids, under-deposit, CO2 corrosion, mild steel, pipelines
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