TY - JOUR A1 - Pfennig, Anja A1 - Linke, Barbara A1 - Kranzmann, Axel T1 - Corrosion behaviour of pipe steels exposed for 2 years to CO2 -saturated saline aquifer environment similar to the CCS-site Ketzin, Germany N2 - When emission gasses are compressed into deep geological layers (CCS) CO2-corrosion of injection pipe steels is a relevant safety issue. The reliability of the steels used at the geological onshore CCS-site at Ketzin, Germany, is demonstrated in 2 years laboratory experiments under an equivalent corrosive environment at ambient pressure (T=60 °C, aquifer water, CO2-flow rate of 3 l/h). Corrosion kinetics and microstructures were characterized using samples of the heat treated steel 42CrMo4 (casing), and samples of the martensitic stainless steel X46Cr13 (injection). KW - Steel KW - Pipeline KW - Corrosion KW - CCS KW - CO2-storage PY - 2011 SN - 1876-6102 VL - 4 SP - 5122 EP - 5129 PB - Elsevier CY - Amsterdam AN - OPUS4-23621 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Pfennig, Anja A1 - Kranzmann, Axel ED - Roland Span, ED - Ingo Weber, T1 - Effect of CO2 on the stability of steels with 1% and 13% Cr in saline water T2 - 15th International Conference on the Properties of Water and Steam (ICPWS XV), "Water, Steam, and Aqueous Solutions - Advances in Science and Technology for Power Generation" CY - Berlin, Germany DA - 2008-09-07 KW - Steel KW - Corrosion KW - Injection tube KW - Carbonate scale KW - CO2-storage KW - CO2-injection PY - 2008 SN - 978-3-931384-64-7 IS - Session 06: Electro-12 SP - 1 EP - 11 AN - OPUS4-17869 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Pfennig, Anja A1 - Kranzmann, Axel T1 - Effects of saline aquifere water on the corrosion behaviour of injection pipe steels 1.4034 and 1.7225 during exposure to CO2 environment N2 - CO2-corrosion of injection pipe steels is a relevant safety issue when emission gasses are compressed in deep geological layers (CCS). The reliability of the steels used at the geological onshore CCS-site at Ketzin, Germany, is demonstrated in laboratory experiments under an equivalent corrosive environment (T=60 °C,p=1-60 bar, aquifer water, CO2-flow rate of 3 l/h, 700 h–8000 h heat treatment). Corrosion kinetics and microstructures were characterized using samples of the heat treated steel 1.7225 (AISI 4140, 42CrMo4) used for casing, and samples of the martensitic stainless injection-pipe steel 1.4034 (AISI 420, X46Cr13). KW - Steel KW - Pipeline KW - Corrosion KW - Carbonate layer KW - CCS KW - CO2-injection KW - CO2-storage PY - 2009 DO - https://doi.org/10.1016/j.egypro.2009.02.080 SN - 1876-6102 VL - 1 IS - 1 SP - 3023 EP - 3029 PB - Elsevier CY - Amsterdam AN - OPUS4-19393 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Pfennig, Anja A1 - Wojtas, P. A1 - Spengler, I. A1 - Linke, B. A1 - Kranzmann, Axel ED - Villacampa, V. ED - Brebbia, C.A. ED - Mammoli, A.A. T1 - Influence of heat treatment on the corrosion behavior of steels exposed to CCS environment N2 - The influence of heat treatment on pit corrosion needs to be considered to guarantee reliability and safety during the injection of compressed emission gasses – mainly containing CO2 – into deep geological layers (CCS-technology, Carbon Capture and Storage). In laboratory experiments different heat treated steels used as injection pipe with 13% Chromium and 0.46% Carbon (X46Cr13, 1.4034) as well as 0.2% Carbon (X20Cr13, 1.4021) were tested. Also X5CrNiCuNb16-4 (1.4542) was investigated as typical steel used for geothermal pumps. Keeping stable environmental conditions in laboratory experiments the samples were exposed to the distinct synthetic aquifer environment saturated with technical CO2 at a flow rate of 3 l/h for up to 6 months. Independent of the exposure time the least amount of pits is found on hardened steels with martensitic microstructure where X5CrNiCuNb16-4 shows fewer pits than X46Cr13 and X20Cr13. Regarding steels with similar Cr-content the higher Ccontent in 1.4034 results in fewer pits compared to 1.4021. KW - Steel KW - Heat treatment KW - Pit corrosion KW - CCS KW - CO2-injection KW - CO2-storage PY - 2011 SN - 978-1-84564-508-3 DO - https://doi.org/10.2495/ESUS110411 SN - 1746-448X SN - 1743-3541 SP - 487 EP - 498 PB - WIT Press CY - Southampton, UK AN - OPUS4-23840 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Hünert, Daniela A1 - Kranzmann, Axel T1 - Impact of oxyfuel atmospheres H2O/CO2/O2 and H2O/CO2 on the oxidation of ferritic-martensitic and austenític steels N2 - In future power plant technologies, oxyfuel, steels are subjected to steam rich and carbon dioxide rich combustion gases. The effect of simulated combustion gases H2O/CO2/O2 (30/69/1 mol%) and H2O/CO2 (30/70 mol%) on the corrosion behavior of low alloyed steels, 9-12% chromium steels and an austenitic steel were studied. It was discovered that the formation of protective chromium rich oxides is hampered due to the carburization of the base material and the formation of chromium rich carbides. The kinetics of corrosion and carburization are quantified. The effect of temperature and the effect of gas pressure are analyzed statistically. KW - A. Steel KW - C. Oxidation KW - C. Carburization KW - C. High temperature corrosion PY - 2011 DO - https://doi.org/10.1016/j.corsci.2011.03.015 SN - 0010-938X VL - 53 IS - 6 SP - 2306 EP - 2317 PB - Elsevier CY - Orlando, Fla. AN - OPUS4-23833 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Kranzmann, Axel T1 - COORETEC - technischer Überblick T2 - Fachkongress "Innovative Technologien zur Stromerzeugung - auf dem Weg zu CO2-freien Kohle- und Gaskraftwerken" CY - Berlin, Germany DA - 2004-05-10 PY - 2004 AN - OPUS4-7077 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Ritter, Martin A1 - Dziomba, T. A1 - Hemmleb, M. A1 - Koenders, L. A1 - Kranzmann, Axel T1 - A 3D-Calibration Method for the Quantitative SPM Measurement of Hardness Indenters KW - 3D Calibration KW - SPM KW - Hardness Indenter PY - 2007 SN - 0970-3950 VL - 22 IS - 3 SP - 167 EP - 175 PB - Metrology Society of India CY - New Delhi AN - OPUS4-16357 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Ritter, Martin A1 - Dziomba, T. A1 - Kranzmann, Axel A1 - Koenders, L. T1 - A landmark-based 3D calibration strategy for SPM N2 - We present a new method for the complete three-dimensional (3D) calibration of scanning probe microscopes (SPM) and other high-resolution microscopes, e.g., scanning electron microscopes (SEM) and confocal laser scanning microscopes (CLSM), by applying a 3D micrometre-sized reference structure with the shape of a cascade slope-step pyramid. The 3D reference structure was produced by focused ion beam induced metal deposition. In contrast to pitch featured calibration procedures that require separate lateral and vertical reference standards such as gratings and step height structures, the new method includes the use of landmarks, which are well established in calibration and measurement tasks on a larger scale. However, the landmarks applied to the new 3D reference structures are of sub-micrometre size, the so-called 'nanomarkers'. The nanomarker coordinates are used for a geometrical calibration of the scanning process of SPM as well as of other instrument types such as SEM and CLSM. For that purpose, a parameter estimation routine involving three scale factors and three coupling factors has been developed that allows lateral and vertical calibration in only one sampling step. With this new calibration strategy, we are able to detect deviations of SPM lateral scaling errors as well as coupling effects causing, e.g., a lateral coordinate shift depending on the measured height position of the probe. KW - Scanning probe microscopy KW - Focused ion beam KW - Calibration KW - 3D standards KW - Parameter estimation KW - Spatial coupling KW - Distortions KW - SPM KW - Landmarks KW - Nanomarker KW - Coupling KW - 3D calibration PY - 2007 DO - https://doi.org/10.1088/0957-0233/18/2/S12 SN - 0957-0233 SN - 1361-6501 VL - 18 SP - 404 EP - 414 PB - IOP Publ. Ltd. CY - Bristol AN - OPUS4-16358 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Ritter, Martin A1 - Dziomba, T. A1 - Xu, M. A1 - Koenders, L. A1 - Kranzmann, Axel T1 - Eine neue 3D Kalibrierstrategie für Mikro- und Nanomessverfahren T2 - Tagung "Messtechnik für Mikro- und Nano-Engineering" CY - Erlangen, Deutschland DA - 29.11.2006 KW - 3D Kalibrierung KW - Rastermikroskopie KW - Nanomarker PY - 2006 SN - 3-18-091950-7 IS - 1950 SP - 15 EP - 24 AN - OPUS4-16359 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Kranzmann, Axel A1 - Hünert, Daniela T1 - Influence of pressure and chromium content on corrosion reactions at 600 C in a CO2-H2O atmosphere T2 - NACE CORROSION 2008 Conference and Expo CY - New Orleans, LA, USA DA - 2008-03-16 PY - 2008 AN - OPUS4-16450 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Kranzmann, Axel T1 - Transport von CO2 in Pipelines - Anforderungen an das CO2 in Rauchgasen T2 - DBI-Fachforum CO2 - Carbon Capture and Storage CY - Berlin, Germany DA - 2011-05-10 PY - 2011 AN - OPUS4-24634 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Pfennig, Anja A1 - Kranzmann, Axel T1 - Reliability of pipe steels with different amounts of C and Cr during onshore carbon dioxide injection N2 - During the compression of emission gasses into deep geological layers (Carbon Dioxide Capture and Storage, CCS) CO2-corrosion will become a relevant safety issue. The reliability of the steels used at a geological onshore CCS-site in the Northern German Bassin 42CrMo4 (1.7225, AISI 4140) used for casing, and the injection pipe steels X46Cr13 (1.4034, AISI 420 C), X20Cr13 (1.4021, AISI 420 J) as well as X35CrMo17 (1.4122) is demonstrated in laboratory experiments. Samples were kept in a synthetic aquifer environment at T = 60 °C. This corrosive environment is then saturated with technical CO2 at a flow rate of 3 l/h. Microstructures were characterized by X-ray diffraction, light microscopy, scanning electron microscopy, and energy dispersive X-ray analysis, after a series of heat treatments (700 h to 2 years). The non-linear isothermal surface corrosion behaviour of the steels reveals surface corrosion rates around 0.1–0.8 mm/year, when obtained by mass gain. Severe pit corrosion (pit heights ca. 4.5 mm) are only located on the injection pipe steels. Main phases of the continuous scales are siderite FeCO3 and goethite α-FeOOH. The formation of the non-protective layer is likely to form via a transient Fe(OH)2-phase. KW - Steel KW - Pipe KW - Corrosion KW - Carbonate layer KW - CO2-injection KW - CO2-storage CCS PY - 2011 DO - https://doi.org/10.1016/j.ijggc.2011.03.006 SN - 1750-5836 VL - 5 IS - 4 SP - 757 EP - 769 PB - Elsevier CY - New York, NY [u.a.] AN - OPUS4-25533 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, Anja A1 - Schulz, Sabrina A1 - Linke, Barbara A1 - Kranzmann, Axel T1 - Supercritical CO2-corrosion in pipe steels during carbon capture and storage CCS N2 - The CCS technique involves the compression of emission gasses in deep geological layers. To guarantee the safety of the site, C02-corrosion of the injection pipe steels has to be given special attention when engineering CCSsites. To get to know the corrosion behaviour samples of the heat treated Steel 1.72252CrMo4, used for casing, and the stainless injection-pipe Steel 1.4034 X46Cr 13 were kept at T=60 °C and ambient pressure as well as p=100 bar for 700 h - 8000 h in a C02-saturated synthetic aquifer environment similar to possible geological on-shore CCS-sites in the northern German Basin. The isothermal corrosion behaviour obtained by mass gain of the steels in the gas phase, the liquid phase and the intermediate phase gives surface corrosion rates around 0.1 to 0.8 mm/year at ambient pressure and much lower about 0.02 to 0.2 mm/year at 100 bar where the C02 is in its supercritical state. Severe pit corrosion with pit heights around 4.5 mm are only located on the 42CrMo4 Steel. Main phase of the continuous complicated multi-layered carbonate/oxide structure is siderite FeCO} in both types of Steel. T2 - 4th International conference on sustainable energy and environment (SEE 2011) - A paradigm shift to low carbon society CY - Bangkok, Thailand DA - 23.11.2011 KW - Steel KW - Pipeline KW - Corrosion KW - Carbonate layer KW - CCS KW - Supercritical CO2- KW - CO2-storage PY - 2011 SP - 1 EP - 6 AN - OPUS4-25534 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, Anja A1 - Linke, Barbara A1 - Schulz, Sabrina A1 - Kranzmann, Axel T1 - Supercritical CO2-corrosion in pipe steels during carbon capture and storage CCS N2 - The CCS technique involves the compression of emission gasses in deep geological layers. To guarantee the safety of the site, CC>2-corrosion of the injection pipe steels has to be given special attention when engineering CCS-sites. To get to know the corrosion behaviour samples of the heat treated Steel 1.72252CrMo4, used for casing, and the stainless injection-pipe Steel 1.4034 X46Crl3 were kept at T=60 °C and ambient pressure as well as p=100 bar for 700 h - 8000 h in a CC>2-saturated synthetic aquifer environment similar to possible geological onshore CCS-sites in the northern German Basin. The isothermal corrosion behaviour obtained by mass gain of the steels in the gas phase, the liquid phase and the intermediate phase gives surface corrosion rates around 0.1 to 0.8 mm/year at ambient pressure and much lower about 0.02 to 0.2 mm/year at 100 bar where the CO2 is in its supercritical state. Severe pit corrosion with pit heights around 4.5 mm are only located on the 42CrMo4 Steel. Main phase of the continuous complicated multi-layered carbonate/oxide structure is siderite FeCCh in both types of Steel. T2 - 3rd International congress on green process engineering (GPE 2011) CY - Kuala-Lumpur, Malaysia DA - 06.12.2011 KW - Steel KW - Pipeline KW - Corrosion KW - Carbonate layer KW - CCS KW - Supercritical CO2- KW - CO2-storage PY - 2011 SP - 1 EP - 6 AN - OPUS4-25535 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, Anja A1 - Wojtas, P. A1 - Spengler, I. A1 - Kranzmann, Axel T1 - Effect of heat treatment of injection pipe steels on the formation of local corrosion in CCS-environment N2 - When engineering a Carbon Capture and Storage site (CCS) local corrosion (pitting) of the injection pipe steel may become an issue when emission gasses from oxyfuel power plants are compressed into deep geological layers. This highly corrosive environment arises when the flue gasses, mainly composed of CO2 , are injected into saline aquifer water. Immediately carbonic acid is formed causing corrosive attack of the injection steels. The influence of heat treatment on the local corrosion resistance was demonstrated in laboratory experiments at 60 °C and ambient pressure for three steels X46Cr13 (1.4034), X20Cr13 (1.4021) and X5CrNiCuNb16-4 (1.4543) under a similar liquid corrosive environment as found at a geological onshore CCS-site in the Northern German Bassin. T2 - 2nd Oxyfuel combustion conference CY - Yeppoon, Queensland, Australia DA - 12.09.2011 KW - Steel KW - Pipe KW - Corrosion KW - Heat treatment KW - CO2-injection KW - CO2-storage CCS KW - Carbonate KW - Ambient pressure KW - CCS KW - Steels PY - 2011 SP - 1 EP - 3 AN - OPUS4-25536 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Ruhl, Aki Sebastian A1 - Kranzmann, Axel T1 - Investigation of pipeline corrosion in pressurized CO2 containing impurities N2 - Transmission of captured CO2 in pipelines is an essential part of the carbon capture and sequestration process chain. Dependent of the fuel, the combustion process and the capture technology the resulting gas contains impurities that might cause corrosion effects in pipelines constructed of low alloyed steels. Corrosion testing under simulated conditions therefore is a prerequisite for the installation of reliable and safe CCS systems. Sulfur and nitrogen oxides together with water vapor form corrosive acids. Their behaviours and corrosive effects in static pressurized experiments were critically investigated in the present study. The results indicate that experimental limitations might influence the predictive capability of corrosion tests with sulfur dioxide. The limited supply of corrosive constituents in static test might lead to an underestimation of the corrosion risk. PY - 2013 DO - https://doi.org/10.1016/j.egypro.2013.06.199 SN - 1876-6102 VL - 37 SP - 3131 EP - 3136 PB - Elsevier Ltd. CY - Amsterdam AN - OPUS4-29163 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Schulz, Wencke A1 - Feigl, Michael A1 - Dörfel, Ilona A1 - Nofz, Marianne A1 - Kranzmann, Axel T1 - Influence of a sol-gel alumina coating on oxidation of X20CrMoV12-1 in air up to 650 °C N2 - The need for a more efficient coal power plant generation (e.g. oxyfuel technology) results in modified process parameters and enhanced corrosion. To reach the necessary service life of high temperature parts protective coatings may be a sufficient technical solution. A modified Yoldas sol (Al2O3 based) was used to coat X20CrMoV12-1 by spin coating. After appropriate heat treatments transition alumina coatings being about 400 nm thick were obtained. Oxidation studies were carried out in laboratory air at temperatures up to 650 °C for up to 500 h exposure time. In case of the uncoated sample a rough oxide layer formed on the surface and a remarkable weight gain (2.62 mg/cm²) were detected. The sol–gel alumina layer (mainly δ-Al2O3) demonstrated a high protection, i.e. a very low weight gain (0.05 mg/cm²). Diffusion of alloying elements into the coating was observed. No indication of spallation of the coating occurred. Local defects (2 µm–30 µm) in the coating led to the formation of iron-oxide islands. KW - X20CrMoV12-1 KW - Sol-gel deposition KW - Alumina KW - Air oxidation KW - Transmission electron microscopy KW - Chromium KW - Diffusion KW - Manganese PY - 2013 DO - https://doi.org/10.1016/j.tsf.2013.04.132 SN - 0040-6090 VL - 539 SP - 29 EP - 34 PB - Elsevier B.V. CY - Amsterdam AN - OPUS4-29162 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Pfennig, A. A1 - Zastrow, Philip A1 - Kranzmann, Axel T1 - Influence of heat treatment on the corrosion behaviour of stainless steels during CO2-sequestration into saline aquifer N2 - The appropriate strength of steels used for saline aquifer carbon capture and storage sites (CCS) is usually achieved by applying heat treatments. Thus, heat treatment influences the corrosion resistance for injection pipe steels with 13% chromium and different carbon content: 1.4034/X46Cr13 and 1.4021/X20Cr13 in CO2 saturated saline aquifer water at 60 °C, 1 and 100 bar. X46Cr13 shows better corrosion resistance with respect to corrosion rate, number of pits and maximum intrusion depth. Low corrosion rates are obtained for steels with martensitic microstructures exposed to supercritical CO2 at 100 bar, whereas normalized steels show better corrosion resistance at ambient pressure. KW - Steel KW - Heat treatment KW - CO2 injection KW - Carbon capture and storage (CCS) KW - Corrosion PY - 2013 DO - https://doi.org/10.1016/j.ijggc.2013.02.016 SN - 1750-5836 VL - 15 SP - 213 EP - 224 PB - Elsevier Ltd. CY - New York, NY [u.a.] AN - OPUS4-27994 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, Anja A1 - Linke, B. A1 - Schulze, S. A1 - Kranzmann, Axel T1 - Corrosion in pipe steels exposed to supercritical CO2 during carbon capture and storage CCS N2 - The CCS technique involves the compression of emission gasses in deep geological layers. To guarantee the safety of the site, CO2-corrosion of the injection pipe steels has to be given special attention when engineering CCS-sites. To get to know the corrosion behaviour samples of the heat treated steel 1.72252CrMo4, used for casing, and the stainless injection-pipe steel 1.4034 X46Cr13 were kept at T=60 °C and ambient pressure as well as p=100 bar for 700 h - 8000 h in a CC 2-saturated synthetic aquifer environment similar to possible geological on-shore CCS-sites in the northern German Basin. The isothermal corrosion behaviour obtained by mass gain of the steels in the gas phase, the liquid phase and the intermediate phase gives surface corrosion rates around 0.1 to 0.8 mm/year at ambient pressure and much lower about 0.02 to 0.2 mm/year at 100 bar where the CO 2 is in its supercritical state. Severe pit corrosion with pit heights around 4.5 mm are only located on the 42CrMo4 steel. Main phase of the continuous complicated multi-layered carbonate/oxide structure is siderite FeCO 3 in both types of steel. T2 - EUROCORR 2011 - Developing solutions for the global challenge CY - Stockholm, Sweden DA - 04.09.2011 KW - Steel KW - Pipeline KW - Corrosion KW - Carbonate layer KW - CCS KW - CO2-storage PY - 2011 SP - Paper 1044-1 EP - Paper 1044-8 AN - OPUS4-28008 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, Anja A1 - Linke, B. A1 - Schulze, S. A1 - Kranzmann, Axel T1 - Static and dynamic long term corrosion experiments in CCS-conditions N2 - Dealing with first corrosion screening experiments to predict the reliability and safety of Germanys first Carbon Capture and Storage site in the northern Bassin of Germany, northwest of the Capital Berlin, laboratory experiments have been established to simulate the particular conditions at T=60 °C, highly saline aquifer water similar to 'Stuttgart Aquifer', but only at ambient pressure. With mounting 2 independent full 2-grade titanium autoclave systems (running up to 250 bar and 300 °C) pressures up to p=100 bar are possible. In 2010 a specific corrosion chamber of 2-grade titanium working up to 100 °C, flowing aqui fer water with different gas mixtures was designed to fit to a high cycle fatigue testing machine. Long term fatigue experiments simulating fatigue crack growth under corrosive environments will soon start. These experiments may not only help engineering a CCS site, but results can be used to improve the maintenance of geothermal energy production sites, especially moved parts such as pumps and shafts. T2 - EUROCORR 2011 - Developing solutions for the global challenge CY - Stockholm, Sweden DA - 04.09.2011 KW - CO2 KW - Static corrosion KW - High cycle fatigue KW - Steel KW - CCS KW - CO2-storage KW - Corrosion PY - 2011 SP - 1 EP - 7 (Paper 1087) AN - OPUS4-28009 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Ruhl, Aki Sebastian A1 - Göbel, Artur A1 - Kühn, Hans-Joachim A1 - Kranzmann, Axel T1 - Materials testing under mechanical stress, pressure and turbulent flow of impure supercritical CO2 N2 - The climate change necessitates measures to reduce carbon dioxide (CO2) emissions in the atmosphere, one of which is carbon dioxide capture and storage (CCS). Transmission of pressurized liquid or supercritical CO2 containing residual flue gas constituents in pipelines is an important component of CCS systems. Material testing under conditions as close as possible to real conditions is a prerequisite for reliable and safe implementation of CCS. A novel pipeline corrosion test facility was developed, accounting for major mechanical, physical and chemical influencing factors: elastic deformation, pressure, temperature, gas composition and flow velocity can be independently adjusted. Radial and tangential stress distributions on a round sample were experimentally investigated, indicating a good accordance with expected theoretical values. In this contribution the idea of the novel corrosion test facility and the assembled equipment as well as first results are presented and discussed.----------------------------------------------------------------------------------------------------Die Klimaveränderung macht Maßnahmen zur Reduktion von Kohlendioxidemission (CO2) in die Atmosphäre erforderlich, Rückhalt und Speicherung in tiefen geologischen Formationen (carbon capture and storage (CCS)) stellt eine davon dar. Der Transport von verflüssigtem oder superkritischem CO2 mit Verunreinigungen in Pipelines stellt einen wichtigen Teil von CCS-Systemen dar. Die Materialprüfung unter möglichst realitätsnahen Bedingungen ist eine wichtige Voraussetzung für die Einrichtung zuverlässiger und sicherer CCS-Systeme. Hierzu wurde eine neue Versuchseinrichtung zur Korrosionsprüfung von Pipelinewerkstoffen entwickelt, die folgende wesentliche physikalische und chemische Einflussgrößen berücksichtigt: Elastische Verformung, Druck, Temperatur, Gaszusammensetzung, und Fließgeschwindigkeit können unabhängig voneinander eingestellt werden. Die Verteilung der Radial- und Tangentialspannungen wurden in einer Rundprobe untersucht, und die Ergebnisse zeigten gute Übereinstimmungen mit den theoretisch zu erwartenden Werten. In dem vorliegenden Beitrag werden die Idee zu der neuen Korrosionsprüfeinrichtung und erste Ergebnisse vorgestellt sowie diskutiert. PY - 2013 DO - https://doi.org/10.3139/120.110428 SN - 0025-5300 VL - 55 IS - 3 SP - 158 EP - 162 PB - Hanser CY - München AN - OPUS4-28283 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -