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01034 CORROSION UNDER WET GAS CONDITIONS

Picture for 01034 CORROSION UNDER WET GAS CONDITIONS
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Product Number: 51300-01034-SG
ISBN: 01034 2001 CP
Author: Y.H. Sun, T. Hong, W.P. Jepson
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CO2 wet gas corrosion rates at the top and bottom of a high pressure 10-cm diameter system have been measured under different pressures up to 1.82MPa at a temperature of 40°C. The flow patterns at test conditions are determined at gas velocities up to 1 lm/s and liquid velocities up to 0.2m/s. The liquid was de-ionized water and carbon dioxide was used as the gas phase. The flow patterns at test conditions are annular flow or near the stratified-annular flow transition zone. The corrosion rate becomes stable after 3 hours. It was found that the corrosion rate increases with the increase in gas velocity, liquid velocity, and CO2 partial pressure.
CO2 wet gas corrosion rates at the top and bottom of a high pressure 10-cm diameter system have been measured under different pressures up to 1.82MPa at a temperature of 40°C. The flow patterns at test conditions are determined at gas velocities up to 1 lm/s and liquid velocities up to 0.2m/s. The liquid was de-ionized water and carbon dioxide was used as the gas phase. The flow patterns at test conditions are annular flow or near the stratified-annular flow transition zone. The corrosion rate becomes stable after 3 hours. It was found that the corrosion rate increases with the increase in gas velocity, liquid velocity, and CO2 partial pressure.
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99045 CORROSION MANAGEMENT OF WET GAS PIPELINES

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51318-11630-Internal Corrosion Direct Assessment of a Wet Gas Pipeline

Product Number: 51318-11630-SG
Author: Xihua S. He / Debashis Basu / and Osvaldo Pensado / Jianyun Mei / Bibo Zhang / Hongbo Wu / Yongzhao Fan / Deqiang Cai / Yang Li
Publication Date: 2018
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This work applied the Wet Gas-Internal Corrosion Direct Assessment (WG-ICDA) standard to assess the severity of internal corrosion of 2 segments along a pipeline used to transport wet gas from a gas mine.
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