2010
DOI: 10.1016/j.corsci.2010.04.029
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Electrochemical characterization and computational fluid dynamics simulation of flow-accelerated corrosion of X65 steel in a CO2-saturated oilfield formation water

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Cited by 88 publications
(55 citation statements)
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“…The pH of simulated solution calculated through the present method of water chemistry calculation was 6.12, while the measured value in reference [7] was 6.15. The relative error was within AE 0.5 %, showing that this method of water chemistry calculation worked well.…”
Section: Electrochemical Reactions In Carbon Dioxide Corrosionmentioning
confidence: 69%
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“…The pH of simulated solution calculated through the present method of water chemistry calculation was 6.12, while the measured value in reference [7] was 6.15. The relative error was within AE 0.5 %, showing that this method of water chemistry calculation worked well.…”
Section: Electrochemical Reactions In Carbon Dioxide Corrosionmentioning
confidence: 69%
“…Fe ðsÞ ! Fe 2þ ðaqÞ þ2e À Anodic 3 Implementation and verification A 908 elbow with an inner diameter of 50 mm whose size was same with the one in reference [7] was selected as the geometric model. The fluid was the simulated solution (main species in Table 3) saturated with carbon dioxide at 25 8C (298.15 K) and 1 bar, and we define constant concentrations of the species at the entrance.…”
Section: Electrochemical Reactions In Carbon Dioxide Corrosionmentioning
confidence: 99%
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“…A maior perda de massa foi para o segundo ensaio de 24 horas, com uma perda de massa de 1,95g para a amostra lisa e 1,92g para a amostra rugosa. Um dos motivos para a perda de massa não ser tão acentuada foi o tempo que as amostras ficaram expostas ao CO2, a corrosão começa a cair a partir da 96 horas de ensaio [4]. Nas amostras rugosas temos a formação de vales ou cristas, onde os pontos de corrosão são formados com mais intensidade, mas devido ao pouco tempo de exposição das amostras a solução aquosa contendo CO2 não foi suficiente para a aderência da camada protetora.…”
Section: Perda De Massaunclassified
“…They concluded that a protective oxide film (FeCO 3 ) was formed only in the single phase at a low velocity with pH > 5. Fluid flow is generally responsible for an accelerated mass transfer process and damage of the protective oxide film on the steel surface (Zhang & Cheng, 2010a). The basic corrosion reactions are (Sastri, 1998) FAC is a major challenge facing the nuclear industry (Yuan, Pandey, & Bickel, 2008), with its operating temperature range of > 140℃: greater than for industrial and fossil plants (Dooley & Chexal, 2000).…”
mentioning
confidence: 99%