TY - JOUR
T1 - Use of Carbon Steel for Construction of Post-combustion CO2 Capture Facilities
T2 - A Pilot-Scale Corrosion Study
AU - Li, Wei
AU - Landon, James
AU - Irvin, Bradley
AU - Zheng, Liangfu
AU - Ruh, Keith
AU - Kong, Liang
AU - Pelgen, Jonathan
AU - Link, David
AU - Figueroa, Jose D.
AU - Thompson, Jesse
AU - Nikolic, Heather
AU - Liu, Kunlei
N1 - Publisher Copyright:
© 2017 American Chemical Society.
PY - 2017/4/26
Y1 - 2017/4/26
N2 - Corrosion studies were carried out on metal coated and noncoated carbon steel as well as stainless steel in a pilot-scale post-combustion CO2 capture process. Aqueous 30 wt % monoethanolamine (MEA) solvent was used without any chemical additive for antioxidation to examine a worst-case scenario where corrosion is not mitigated. The corrosion rate of all carbon steels was almost zero in the absorber column and CO2 lean amine piping except for Ni-coated carbon steel (<1.8 mm/yr). Ni2Al3/Al2O3 precoated carbon steels showed initial protection but lost their integrity in the stripping column and CO2 rich amine piping, and severe corrosion was eventually observed for all carbon steels at these two locations. Stainless steel was found to be stable and corrosion resistant in all of the sampling locations throughout the experiment. This study provides an initial framework for the use of carbon steel as a potential construction material for process units with relatively mild operating conditions (temperature less than 80°C), such as the absorber and CO2 lean amine piping of a post-combustion CO2 capture process. It also warrants further investigation of using carbon steel with more effective corrosion mitigation strategies for process units where harsh environments are expected (such as temperatures greater than 100°C). (Figure Presented).
AB - Corrosion studies were carried out on metal coated and noncoated carbon steel as well as stainless steel in a pilot-scale post-combustion CO2 capture process. Aqueous 30 wt % monoethanolamine (MEA) solvent was used without any chemical additive for antioxidation to examine a worst-case scenario where corrosion is not mitigated. The corrosion rate of all carbon steels was almost zero in the absorber column and CO2 lean amine piping except for Ni-coated carbon steel (<1.8 mm/yr). Ni2Al3/Al2O3 precoated carbon steels showed initial protection but lost their integrity in the stripping column and CO2 rich amine piping, and severe corrosion was eventually observed for all carbon steels at these two locations. Stainless steel was found to be stable and corrosion resistant in all of the sampling locations throughout the experiment. This study provides an initial framework for the use of carbon steel as a potential construction material for process units with relatively mild operating conditions (temperature less than 80°C), such as the absorber and CO2 lean amine piping of a post-combustion CO2 capture process. It also warrants further investigation of using carbon steel with more effective corrosion mitigation strategies for process units where harsh environments are expected (such as temperatures greater than 100°C). (Figure Presented).
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U2 - 10.1021/acs.iecr.7b00697
DO - 10.1021/acs.iecr.7b00697
M3 - Article
AN - SCOPUS:85020449523
SN - 0888-5885
VL - 56
SP - 4792
EP - 4803
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 16
ER -