Changes in Corrosion of X70 Steel in Water-Saturated Supercritical CO2 System Caused by Impurity

During the process of Carbon Capture and Storage, some impurity may be found in the supercritical CO2 fluid. The changes in corrosion of X70 Steel in water-saturated supercritical CO2 system caused by impurity has been studied by the simulation experiment. The average corrosion rate was got from weight loss measurement. The morphologies and compositions of corrosion products were analyzed by SEM, EDS and XRD. It was observed that the existence of separate impurity would aggravate the corrosion of X70 steel in the water-saturated supercritical CO2 system. The average corrosion rate was the highest when NO2 or SO2 was included, followed by H2S, and the average corrosion rate was the smallest when O2 was contained. Among them, X70 steel suffered local corrosion when NO2 was contained. The corrosion scale was monolayer structure of FeCO3 under the supercritical CO2-H2O system. After the addition of O2, Fe2O3 appeared in the corrosion scale, indicating that the oxygen corrosion process occurred. While with the addition of H2S, corrosion scales were double layers. FeS was mainly present in the outer layer. The corrosion process was controlled by CO2 and H2S. The corrosion products were mostly FeSO3·xH2O and a spot of FeCO3 when SO2 was contained. SO2 mainly governed the corrosion process. Besides, corrosion product was Fe2O3 without FeCO3 in the supercritical CO2-H2O-NO2 system, NO2 completely controlled the corrosion process.

[1]  Guoan Zhang,et al.  Effect of O2 and H2S impurities on the corrosion behavior of X65 steel in water-saturated supercritical CO2 system , 2016 .

[2]  Z. Wang,et al.  Effect of temperature on corrosion behaviour of X70 steel in high pressure CO2/SO2/O2/H2O environments , 2013 .

[3]  Zhe Wang,et al.  Effect of Exposure Time on the Corrosion Rates of X70 Steel in Supercritical CO2/SO2/O2/H2O Environments , 2013 .

[4]  Aki Sebastian Ruhl,et al.  Investigation of corrosive effects of sulphur dioxide, oxygen and water vapour on pipeline steels , 2013 .

[5]  Arne Dugstad,et al.  Effect of SO2 and NO2 on Corrosion and Solid Formation in Dense Phase CO2 Pipelines , 2013 .

[6]  A. Kranzmann,et al.  Investigation of Pipeline Corrosion in Pressurized CO2 Containing Impurities , 2013 .

[7]  Aki Sebastian Ruhl,et al.  Corrosion behavior of various steels in a continuous flow of carbon dioxide containing impurities , 2012 .

[8]  Weidou Ni,et al.  The upper limit of moisture content for supercritical CO2 pipeline transport , 2012 .

[9]  N. Birbilis,et al.  State of the aqueous phase in liquid and supercritical CO2 as relevant to CCS pipelines , 2012 .

[10]  Arne Dugstad,et al.  Internal Corrosion In Dense Phase CO2 Transport Pipelines - State of the Art And the Need For Further R&D , 2012 .

[11]  Chao Xu,et al.  Impact of SO2 concentration on the corrosion rate of X70 steel and iron in water-saturated supercritical CO2 mixed with SO2 , 2011 .

[12]  Luuk Buit,et al.  CO2 EuroPipe study of the occurrence of free water in dense phase CO2 transport , 2011 .

[13]  Yoon-Seok Choi,et al.  Effect of impurities on the corrosion behavior of CO2 transmission pipeline steel in supercritical CO2-water environments. , 2010, Environmental science & technology.

[14]  Yoon-Seok Choi,et al.  Effect Of Impurities On The Corrosion Behavior Of Carbon Steel In Supercritical CO2 - Water Environments , 2009 .

[15]  S. Nešić Key issues related to modelling of internal corrosion of oil and gas pipelines - A review , 2007 .

[16]  Wei Sun,et al.  Iron Carbonate Scale Growth and the Effect of Inhibition in CO2 Corrosion of Mild Steel , 2005 .

[17]  Aage Stangeland,et al.  A Mechanistic Model for Carbon Dioxide Corrosion of Mild Steel in the Presence of Protective Iron Carbonate Films—Part 2: A Numerical Experiment , 2003 .

[18]  S. Nešić,et al.  CORROSION IN MULTIPHASE FLOW CONTAINING SMALL AMOUNTS OF H2S , 2003 .

[19]  A. Dugstad Mechanism of Protective Film Formation During CO2 Corrosion of Carbon Steel , 1998 .