2013
DOI: 10.1016/j.egypro.2013.06.083
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Corrosion Investigations In 2-ethanolamine Based Post- Combustion CO2 Capture Pilot Plants

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Cited by 7 publications
(4 citation statements)
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“…Corrosion in 30 wt% MEA-based pilot plants, namely Dong Energy's Ebsjerg and TNO's Maasvlakte have recently been evaluated using weight loss technique with corrosion coupons-plant inspection and on-line monitoring using electrochemical probes. Based on this test campaign (De Vroey et al, 2013), 6 corrosion coupons placed in different locations throughout the Ebsjerg plant and one electrochemical probe installed at the stripper liquid outlet of the Maasvlakte have produced consistent corrosion rate measurements that can be correlated well between the 2 plants. Based on the results, the corrosion rates on stainless and carbon steel measured from both plants would not be expected to affect the plants' structural integrity.…”
Section: Corrosionmentioning
confidence: 99%
“…Corrosion in 30 wt% MEA-based pilot plants, namely Dong Energy's Ebsjerg and TNO's Maasvlakte have recently been evaluated using weight loss technique with corrosion coupons-plant inspection and on-line monitoring using electrochemical probes. Based on this test campaign (De Vroey et al, 2013), 6 corrosion coupons placed in different locations throughout the Ebsjerg plant and one electrochemical probe installed at the stripper liquid outlet of the Maasvlakte have produced consistent corrosion rate measurements that can be correlated well between the 2 plants. Based on the results, the corrosion rates on stainless and carbon steel measured from both plants would not be expected to affect the plants' structural integrity.…”
Section: Corrosionmentioning
confidence: 99%
“…According to De Vroey et al (2013), additional investigation on corrosion using coupons, on-line monitoring using electrochemical probe, and pilot plant inspection were also performed with MEA solvent separately in both the Dong Energy's pilot plant at Esbjerg (Denmark), and TNO's Maasvlakte pilot plant (The Netherlands). De Vroey et al (2013) reported that the weight loss measurement of coupons (placed in strategic locations throughout the process) correlated well with on-line measurement using the electrochemical techniques. Corrosion resistance in most zones in the pilot plants using carbon and stainless steels in the tests was generally good.…”
Section: Corrosionmentioning
confidence: 97%
“…Many of the degradation products of amines are known to be corrosive. ,, Several corrosion studies have been performed at laboratory and pilot plant scale with different solvents and materials. The laboratory scale studies used electrochemical measurements at different temperatures, CO 2 loadings, oxygen content, gas phase impurities such as SO 2 and NO 2 . Corrosion has been evaluated at several pilot plants using MEA and other solvents. , The process equipment that are typically vulnerable to corrosion include columns (absorber and stripper), amine heat exchanger, regenerator, and reclaimer. Typically, coupons are installed at different locations in the pilot plant and their weight loss is translated into corrosion rate as per standard norms, such as ISO 8407 and ASTM G1-03.…”
Section: Introductionmentioning
confidence: 99%