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  • Le, Quynh Hoa (35)
  • Bäßler, Ralph (21)
  • Bettge, Dirk (17)
  • Kratzig, Andreas (9)
  • Kranzmann, Axel (7)
  • Knauer, S (4)
  • Aristia, Gabriela (3)
  • Knauer, S. (3)
  • Yevtushenko, Oleksandra (3)
  • Beck, M. (2)
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  • Corrosion (15)
  • CCUS (14)
  • Carbon steel (9)
  • Carbon steels (9)
  • CO2 (8)
  • Impurities (6)
  • Martensitic steel (6)
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  • CCS (5)
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Organisationseinheit der BAM

  • 7 Bauwerkssicherheit (35)
  • 7.6 Korrosion und Korrosionsschutz (35)
  • 5 Werkstofftechnik (29)
  • 5.1 Materialographie, Fraktographie und Alterung technischer Werkstoffe (29)

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Corrosion on pipeline steel by acid condensation induced by impurities in CO2 streams (2017)
Le, Quynh Hoa ; Kratzig, Andreas ; Bettge, Dirk
Carbon Capture Utilization and Storage (CCUS) is a promising technology for the reduction of CO2 emissions from fossil-fuel operated power plants, steel and cement mills or refineries. Crucial points for a sustainable and future-proof CCUS procedure are reliability and cost efficiency of the pipeline transport network especially concerning corrosion risks under impurities and moisture in the CO2 stream. Recent studies have shown that even high alloyed steels might be susceptible to general and/or localized corrosion caused by condensates. It was concluded from our study on carbon steels in normal and high pressure conditions, that the combination of these gas impurities, resulted in the acidic condensate, is not only a simple sum of each corrosive effect, but highly accelerates the corrosion rate of the pipeline steel, indicating the need of dynamic tests before installing the network pipeline system.
Synergistic effects of impurities in the condensate on the corrosion of CO2 transport pipeline (2017)
Le, Quynh Hoa ; Bäßler, Ralph ; Yevtushenko, Oleksandra ; Kratzig, Andreas ; Bettge, Dirk
For the reliability of transport pipelines the corrosion resistance of the materials used needs to be determined in conditions, which are possible during the transport process. In some situations condensation of components out of the CO2 stream can occur. To study the effect of condensate on transport pipeline steel, a “worst-case scenario” gas mixture, containing 2.5 % H2O, 1.8 % O2, 1000 ppmv NO2, and 220 ppmv SO2, was proposed, fed (1.5 L/min) into a glass reactor containing coupon-shaped specimens for 120 600 h at 278 K (to simulate the underground pipeline transport), and resulted in the condensate containing 0.114 M H2SO4 and 0.0184 M HNO3 (pH 2.13). Basing on this “original” condensate, exposure tests and electrochemical characterization together with pH and conductivity in CO2 saturated condition at the same temperature were carried out. The role of each gas impurity and the combination of them, when the condensate is formed, was studied by investigating the role of individual and varying combination of acidic components in the condensate on the corrosion behaviors of the commercial pipeline-steel (L360NB). It can be concluded that although the condensation of NOx in form of HNO3 causes faster corrosion rate, it is the condensation of SOx or the combination of SOx and NOx that may cause much more severe problems in form of localized and pitting corrosions. Different to the corrosion products formed in CO2 atmosphere without impurities (mainly iron carbonate) the corrosion products resulted from these acidic condensation have no protectability, indicating the need of controlling gas quality during the transportation within the pipeline network.
Synergistic effects of impurities in the condensate on the corrosion of CO2 transport pipeline (2017)
Le, Quynh Hoa
For the reliability of transport pipelines the corrosion resistance of the materials used needs to be determined in conditions, which are possible during the transport process. In some situations condensation of components out of the CO2 stream can occur. To study the effect of condensate on transport pipeline steel, a “worst-case scenario” gas mixture, containing 2.5 % H2O, 1.8 % O2, 1000 ppmv NO2, and 220 ppmv SO2, was proposed, fed (1.5 L/min) into a glass reactor containing coupon-shaped specimens for 120 600 h at 278 K (to simulate the underground pipeline transport), and resulted in the condensate containing 0.114 M H2SO4 and 0.0184 M HNO3 (pH 2.13). Basing on this “original” condensate, exposure tests and electrochemical characterization together with pH and conductivity in CO2 saturated condition at the same temperature were carried out. The role of each gas impurity and the combination of them, when the condensate is formed, was studied by investigating the role of individual and varying combination of acidic components in the condensate on the corrosion behaviors of the commercial pipeline-steel (L360NB). The stability and protectability of the corrosion film were further studied by periodically changing the condensate during the exposure tests. It can be concluded that although the condensation of NOx in form of HNO3 causes faster corrosion rate, it is the condensation of SOx or the combination of SOx and NOx that may cause much more severe problems in form of localized and pitting corrosions. Different to the corrosion products formed in CO2 atmosphere without impurities (mainly iron carbonate) the corrosion products resulted from these acidic condensation have no protectability, indicating the need of controlling gas quality during the transportation within the pipeline network.
Korrosion von Stählen in flüssigen und überkritischen CO2–Strömen unter realitätsnahen Bedingungen (2017)
Kratzig, Andreas ; Le, Quynh Hoa
CCUS-Technologie gilt als eine vielversprechende Methode zur Abschwächung des Beitrags von fossilen Emissionen zur globalen Erwärmung. Dabei wird das in den Verbrennungsprozessen entstandene Treibhausgas aufgefangen, zu verschiedenen Lagerstätten transportiert und langzeitig gespeichert bzw. einer chemischen Nutzung zugeführt. CO2-Transport-Pipelines sind potentiell gefährdet, wenn sie korrosiven Begleitstoffen des CO2-Stroms, wie SOx, NOx bei einem hohen Wasserdampfanteil ausgesetzt sind. Screening-Tests zeigten, dass bei einer Konzentration von 1000 ppmv H2O die Reaktionen und Kondensation von SO2 und NO2 mit O2 und H2O zu Säuretropfen (pH ~ 0,5) auf der Oberfläche von Metall-Prüfkörpern und Gefäßen führen. Die Werkstoffe 1.4313 1.8977 und 1.4562 wurden in CO2-Atmosphäre mit unterschiedlichen Verhältnissen der säurebildenden Komponenten SO2, NO2, H2S mit H2O untersucht. Diese Studien zeigten grundsätzlich den Mechanismus sowie die Rolle jedes CO2-Strom-Begleitstoffes auf den Korrosionsprozess.
Interaction of oxidizing and reductive components in CO2 fluids in transport pipelines at low and high pressure and low temperature (2017)
Kratzig, Andreas ; Le, Quynh Hoa ; Bettge, Dirk ; Bäßler, Ralph ; Kranzmann, Axel
Carbon Capture Utilization and Storage (CCUS) is a promising technology for the reduction of CO2 emissions, e.g. from fossil-fuel operated power plants or cement mills. Crucial points for a sustainable and future-proof CCUS procedure are reliability and cost efficiency of the pipeline transport network. Due to the absence of certified benchmarks for upper limits, systematic experiments with impurities in the CO2 stream were carried out. For oxidation processes SO2 and NO2 acted as corrosive components, and for reductive atmosphere H2S. Carbon steel L485MB (pipeline), martensitic steel 1.4313 (compression) and austenitic steel 1.4562 (injection) were selected as specimens. Experiments were performed at 0 bar or 100 bar and within a temperature range 278 K ≤ T ≤ 313 K. High-alloyed Cr-Ni steels revealed no corrosion (1.4562, 1.4313), while for carbon steel considerable corrosion was observed. The type and intensity of corrosion was strongly coupled with the applied corrosive species and the level of humidity in the CO2 stream, leading to different compositions of acidic condensates. Applying a reducing atmosphere results in very little corrosion rates, but provokes pitting corrosion. In contrast, oxidizing or mixed settings lead to a clearly increased growth of the corrosion layer, but exhibit shallow uniform corrosion. Exceptional nitric acid results in intergranular corrosion. Investigations on the specimens were carried out by optical microscopy, XRD, SEM/EDX, and AAS/IC.
Electrochemiluminescence Based Enzymatic Urea SensorUsing Nanohybrid of Isoluminol-gold Nanoparticle-graphene Oxide Nanoribbons (2017)
Ismail, N. S. ; Le, Quynh Hoa ; Vu, T. H. ; Inoue, Yuki ; Yoshikawa, H. ; Saito, M. ; Tamiya, E.
This study evaluates on the possibility of using gold nanoparticles functionalizedwith the luminol derivative N-(aminobutyl)-N-(ethylisoluminol)(ABEI) and hybridizedwith graphene oxidenanoribbons on acarbon based screen-printedelectrode (ABEI-AuNP-GONR/SPE) as an enzymaticelectrochemiluminescence (ECL) urea sensor.The electrocatalytic activity and ECL intensity of ABEI-AuNP-GONR/SPE were found to increase proportionally with the concentrationofurea in the analyte sample,owing to the rise in pH value.These phenomena are attributed to increased formation of luminol monoanion precursors for further electrochemical oxidation,which in turn produce eitherluminol radicals or excited3-amino-phthalate molecules.The luminescence is most likely caused by the interaction of luminol radicals with superoxide radicals formed from dissolved oxygen. Thesensitivity of our sensor was determinedtobe 170.58 mM@1 and 16.23 mM@1 for urea concentrations from 2to5.82 mM and from 5.82 to 30 mM, respectively, coveringthe normal urea level in human blood.
Carbon-based nanomaterials in biomass-based fuel-fed fuel cells (2017)
Le, Quynh Hoa ; Vestergaard, M.C. ; Tamiya, E
Environmental and sustainable economical concerns are generating a growing interest in biofuels predominantly produced from biomass. It would be ideal if an energy conversion device could directly extract energy from a sustainable energy resource such as biomass. Unfortunately, up to now, such a direct conversion device produces insufficient power to meet the demand of practical applications. To realize the future of biofuel-fed fuel cells as a green energy conversion device, efforts have been devoted to the development of carbon-based nanomaterials with tunable electronic and surface characteristics to act as efficient metal-free electrocatalysts and/or as supporting matrix for metal-based electrocatalysts. We present here a mini review on the recent advances in carbon-based catalysts for each type of biofuel-fed/biofuel cells that directly/indirectly extract energy from biomass resources, and discuss the challenges and perspectives in this developing field
Effect of CO2 gas on carbon steel corrosion in an acidic-saline based geothermal fluid (2019)
Aristia, Gabriela ; Le, Quynh Hoa ; Bäßler, Ralph
Geothermal energy is one of the most promising energy resources to replace fossil fuel. To extract this energy, hot fluids of various salts and gases are pumped up from a geothermal well having a certain depth and location. Geothermal wells in volcanic regions often contain highly corrosive CO2 and H2S gases that can be corrosive to the geothermal power-plants, which are commonly constructed of different steels, such as carbon steel. This research focuses on the corrosion behaviour of carbon steel exposed to an artificial geothermal fluid containing CO2 gas, using an artificial acidic-saline geothermal brine as found in Sibayak, Indonesia. This medium has a pH of 4 and a chloride content of 1,500 mg/L. Exposure tests were conducted for seven days at 70 °C and 150 °C to simulate the operating temperatures for low and medium enthalpy geothermal sources. Surface morphology and cross-section of the specimens from the above experiments were analysed using scanning electron microscope (SEM) and energy dispersive X-ray (EDX). Electrochemical tests via open circuit potential (OCP) and electrochemical impedance spectroscopy (EIS) were performed to understand the corrosion processes of carbon steel in CO2-containing solution both at 70 °C and 150 °C. Localized corrosion was observed to a greater extent at 70 °C due to the less protectiveness of corrosion product layer compared to that at 150 °C, where FeCO3 has a high corrosion resistance. However, a longer exposure test for 28 days revealed the occurrence of localized corrosion with deeper pits compared to the seven-day exposed carbon steel. In addition, corrosion product transformation was observed after 28 days, indicating that more Ca2+ cations incorporate into the FeCO3 structure.
Rezension: Röntgenfluoreszenzanalyse in der Laborpraxis (2018)
Le, Quynh Hoa
Dieses Buch ist definitiv eine Empfehlung an alle, die mit RFA arbeiten müssen. Außerdem bietet es nützliche und praktische Informationen für Forscher, die an einem bestimmten Thema arbeiten, das im Antragsteil erwähnt wird. Dies wird ihnen während ihrer Forschung helfen, Proben vorzubereiten sowie Fehler in der RFA-Analyse zu erkennen und somit zu vermeiden. Die Stärken des Buches liegen im verständlichen Text und darin, dass alle notwendigen Schritte der Analysenverfahren Punkt für Punkt aufgeführt sind. Obwohl die Autoren eine unglaubliche Arbeit geleistet haben, um den Leser auf den neuesten Stand zu bringen, sind einige Teile ziemlich kurz gehalten. Die Auflistung von weiterführender Literatur, einschließlich wichtiger Normen und Gesetze, verringert dieses Manko etwas und verweist die interessierten Leser auf ergänzende Quellen.
Corrosion of Carbon Steel in Artificial Geothermal Brine: Influence of Carbon Dioxide at 70 °C and 150 °C (2019)
Aristia, Gabriela ; Le, Quynh Hoa ; Bäßler, Ralph
This study focuses on the corrosion mechanism of carbon steel exposed to an artificial geothermal brine influenced by carbon dioxide (CO2) gas. The tested brine simulates a geothermal source in Sibayak, Indonesia, containing 1500 mg/L of Cl-, 20 mg/L of SO4 2-, and 15 mg/L of HCO3-with pH 4. To reveal the temperature effect on the corrosion behavior of carbon steel, exposure and electrochemical tests were carried out at 70 °C and 150 °C. Surface analysis of corroded specimens showed localized corrosion at both temperatures, despite the formation of corrosion products on the surface. After 7 days at 150 °C, SEM images showed the formation of an adherent, dense, and crystalline FeCO3 layer. Whereas at 70 °C, the corrosion products consisted of chukanovite (Fe2(OH)2CO3) and siderite (FeCO3), which are less dense and less protective than that at 150 °C. Control experiments under Ar-environment were used to investigate the corrosive effect of CO2. Free corrosion potential (Ecorr) and electrochemical impedance spectroscopy (EIS) confirm that at both temperatures, the corrosive effect of CO2 was more significant compared to that measured in the Ar-containing solution. In terms of temperature effect, carbon steel remained active at 70 °C, while at 150 °C, it became passive due to the FeCO3 formation. These results suggest that carbon steel is more susceptible to corrosion at the near ground surface of a geothermal well, whereas at a deeper well with a higher temperature, there is a possible risk of scaling (FeCO3 layer). A longer exposure test at 150 °C with a stagnant solution for 28 days, however, showed the unstable FeCO3 layer and therefore a deeper localized corrosion compared to that of seven-day exposed specimens.
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