TY - CONF A1 - Bork, Claus-Peter A1 - Wolf, Marcus A1 - Pfennig, A. A1 - Trenner, S. A1 - Wiegand, Reiner T1 - Comparison between X5CrNiCuNb16-4 and X46Cr13 under corrosion fatigue T2 - Corrosion 2014 N2 - In geothermal power plants materials e.g. pumps are exposed to extremely corrosive thermal water. This results in corrosion fatigue and so inevitably the reduction of the lifetime of these components. Also in the field of the carbon dioxide storage technology (carbon capture and storage CCS) components are exposed to a corrosive environment and mechanical stress. In order to gain knowledge upon the corrosion fatigue strength of materials a corrosion chamber for "in situ" conditions was designed and successfully applied.Two different steels X46Cr13 and X5CrNiCuNb16-4 have been tested and their corrosion fatigue behavior was compared. To simulate the frequency of operating pumps (30 – 40 Hz) a resonant testing machine was used. In addition technical CO2 was introduced into the closed system at a rate close to 9 L/h to keep stable environmental conditions. The samples have a surface roughness of Rz = 4 to simulate technical machined surfaces. The calculated tensile strength of X46Cr13 with soft annealed microstructure (coagulated cementite in ferrite-perlite matrix) is about 680 MPa and the yield strength is about 345 MPa. The tensile strength of X5CrNiCuNb16-4 is about 1078 MPa and the yield strength about 928 MPa. Testing parameters are: corrosion media: saline aquifer water (Stuttgart Aquifer) temperature of the brine at 60 °C and load ratio of R=-1. For X46Cr13 a stress amplitude between 160 MPa to 270 MPa and for X5CrNiCuNb16-4 a stress amplitude between 150 to 500 was chosen. Cycles until crack initiation differ strongly and were found to start at 5 x 104 up to 12.5 x 106 cycles.X46Cr13 has reached a maximum number of cycles (12.5 x 106) at a stress amplitude of 173 MPa. X5CrNiCuNb16-4 has reached the maximum number of cycles (10 x 106) at a stress amplitude of 150 MPa. The range of scatter for X5CrNiCuNb16-4 is very high (1:34) in comparison the range of scatter for X46Cr13 (1:3.5). T2 - Corrosion 2014 CY - San Antonio, TX, USA DA - 09.03.2014 KW - Steel KW - Corrosion chamber KW - Geothermal power KW - CCS KW - Corrosion fatigue PY - 2014 SP - Paper 3776, 1 EP - 6 PB - NACE AN - OPUS4-31085 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Bork, Claus-Peter A1 - Wolf, Marcus T1 - Design of a high pressure system for in-situ tests on the corrosion fatigue of metallic materials T2 - Corrosion 2014 N2 - In geothermal power plants pumps are exposed to corrosive and oscillating loads. This leads to corrosion fatigue and reduces the lifetime of certain components. Usually underwater power pumps are placed inside the borehole. In this case an installation depth of 600 to 800 meters below ground level is typical. In these depths an additional load due to high pressure and high temperature is introduced which is based on geothermal brine. Therefore the material which is used for the pump is steel.For fatigue testing at loads existing in deep geological layers an appropriate system for fatigue tests under in-situ conditions was set up. The requirements of the design are: temperature of the corrosion medium of 200 °C pressure of 200 bars and the complete immersion of the specimen in flowing corrosion medium containing mixtures of corrosive gasses during the entire test period.The test system has three main components the corrosion chamber the heating module and the reservoir. It is important that the corrosion chamber is only fixed onto the specimen which allows for highest flexibility of the test system operational in many different test machines. The heating module heats the corrosion medium up to 200 °C. The reservoir make sure that the volume of the corrosion medium satisfies requirements of the DIN 50905 Part 1 is conformed providing minimum required corrosive medium of 10 ml/cm² in relation to the sample surface.This innovative fatigue test system aims at performing in- situ fatigue corrosion tests simultaneously at high pressure and high temperature in liquid and gaseous corrosive environment. Results from the tests will allow determining the fatigue life of several materials influenced by pressure and temperature under corrosive conditions. T2 - Corrosion 2014 CY - San Antonio, TX, USA DA - 09.03.2014 KW - High pressure KW - Corrosion fatigue KW - Corrosion chamber PY - 2014 SP - Paper 3775, 1 EP - 6 AN - OPUS4-31086 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Gröber, A. A1 - Kranzmann, Axel T1 - The Role of Surface Texture on the Corrosion Behavior of High Alloyed Steel Exposed to Saline Aquifer Water Environments N2 - Coupons of X5CrNiCuNb16-4 that may be used as injection pipe with 16% Chromium and 0.05% Carbon (1.4542, AISI 630) were exposed for 3000 h to CO2-saturated saline aquifer water similar to the conditions in the Northern German Basin at ambient pressure and 60 °C. Surface corrosion layers and pits reveal carbonate corrosion products on the surface such as FeCO3 and FeOOH as the main precipitation phases with no dependence on the original surface roughness. Corrosion rates for polished and technical surfaces were below 0.005 mm/year compared to corrosion rates of 0.035 mm/year after shot peening. T2 - 14th Greenhouse Gas Control Technologies Conference CY - Melbourne, Australia DA - 21.10.2018 KW - High alloyed steel KW - Pitting KW - Surface KW - Roughness KW - CO2 PY - 2019 SP - 1 EP - 8 PB - Elsevier Ltd. AN - OPUS4-50375 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Kranzmann, Axel T1 - Effect of CO2, atmosphere and pressure on the stability of C35CrMo17 stainless steel in laboratory CCS-environment N2 - During carbon sequestration the CO2-induced corrosion of injection pipe steels is a relevant safety issue when emission gasses are compressed into deep geological layers. The reliability of the high alloyed steel X35CrMo17 suitable as injection pipe for the geological onshore CCS-site (Carbon Capture and Storage) in the Northern German Basin, is demonstrated in laboratory experiments in equivalent corrosive environment (T = 60 °CC, p = 1–100 bar, aquifer water, CO2-flow rate of 9 L/h, 700–8000 h exposure time). Corrosion kinetics and microstructure were characterized and compared to other potential injection pipe steels (42CrMo4, X46Cr13, X20Cr13 and X5CrNiCuNb16-4). T2 - 14th Greenhouse Gas Control Technologies Conference CY - Melbourne, Australia DA - 21.10.2018 KW - Steel KW - Supercritical CO2 KW - Pipeline KW - Corrosion KW - CO2-storage PY - 2019 SP - 1 EP - 9 PB - Elsevier Ltd. AN - OPUS4-50382 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Linke, B. A1 - Schulz, Sabrina A1 - Kranzmann, Axel T1 - CO2-corrosion of steels exposed to saline water environment T2 - TMS 2011 - 140th Annual Meeting & Exhibition (Proceedings) N2 - With CO2 being one reason for climate change carbon capture and storage (CCS) is discussed to mitigate climate change. When emission gases are compressed into deep geological layers CO2-corrosion can easily cause failure of injection pipes. Different steels 42CrMo4, X46Cr13 and X20Cr13 were tested as well as X35CrMo17 and X5CrNiCuNb16-4 in a laboratory Environment similar to the conditions of the CCS engineering site at the Northern German Bassin. Samples were exposed to synthetic aquifer water saturated with technical CO2 at a flow rate of 3 NL/h. Corrosion rates obtained via mass loss vary in a wide range (0,005 to 2.5 mm/year). The precipitations within the corrosion scale revealed a complicated multiphase layer containing siderite FeCO3, goethite α-FeOOH, lepidocrocite γ-FeOOH, mackinawite FeS and akaganeite Fe8O8(OH)8Cl1,34 and spinelphases of various compositions. T2 - TMS 2011 - 140th Annual Meeting & Exhibition CY - San Diego, CA, USA DA - 27.02.2011 KW - CCS KW - Steel KW - Corrosion KW - Carbon Capture and Storage PY - 2011 DO - https://doi.org/10.1002/9781118062173.ch102 VL - 3 IS - 0807 SP - 807 EP - 814 AN - OPUS4-23472 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Simkin, Roman A1 - Kranzmann, Axel T1 - Construction of an adiabatic calorimeter for investigation of high tempertarue salt - based phase change material T2 - International Proceedings of Chemical, Biological and Environmental Engineering N2 - The commercial usage of latent thermal energy storages primarily depends on the development of a suitable phase change material (PCM). For industrial high temperature applications above 400 °C multicomponent chloride eutectics are promising and therefore discussed seriously. The profound thermodynamic investigation of such eutectics requires a much greater amount of specimen material than conventional calorimeter can handle. Therefore, a special adiabatic calorimeter was developed and designed. With a specimen mass of > 100 g the typical thermodynamic measurements with a commercial calorimeter can be extended by cycle stability measurements, which are often decisive for practical application of PCM. Furthermore, by implementing corrosion specimens inside the calorimeter high temperature corrosion experiments according to ISO 21608 can be performed inside the calorimeter. Adiabatic measuring conditions can be provided by using two separate heating systems. Therefore, the outer “protective system” follows the temperature curve of the inner “measuring system” minimizing the temperature difference between the heating systems and simultaneously preventing heat losses from the measuring systems. T2 - 10th International Conference on Chemical, Biological and Environmental Engineering ICBEE 2018 CY - Berlin, Germany DA - 27.09.2018 KW - Adiabatic calorimeter KW - Thermal energy storage KW - Phase change material KW - Salt eutectics PY - 2018 DO - https://doi.org/10.7763/IPCBEE.2018.V103.6 VL - 103 SP - 21 EP - 28 AN - OPUS4-50363 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Wolf, M. A1 - Kranzmann, Axel T1 - In-situ testing of corrosion and corrosion fatigue behavior of stainless steels in geothermal environment T2 - International Proceedings of Chemical, Biological and Environmental Engineering IPCBEE N2 - In CCS environment (carbon capture and storage) pipes are loaded statically and/or cyclically and at the same time exposed constantly to the highly corrosive hot thermal water. Experimental procedures such as ambient pressure immersions tests, in-situ corrosion fatigue experiments using a flexibly designed corrosion chamber at ambient pressure and a specially designed corrosion chamber at high pressure. Experimental set-ups for push/pull and rotation bending load are introduced. The corrosion behavior and lifetime reduction of high alloyed steels (X46Cr13, 1.4043), (X5CrNiCuNb16-4, 1.4542) and (X2CrNiMoN22-5-3, 1.4462) is demonstrated (T=60 °C, geothermal brine: Stuttgart Aquifer flow rate: 9 l/h, CO2 ). T2 - 10th International Conference on Chemical, Biological and Environmental Engineering ICBEE 2018 CY - Berlin, Germany DA - 27.09.2018 KW - Adiabatic calorimeter KW - Thermal energy storage KW - Phase change material KW - Salt eutectics PY - 2018 DO - https://doi.org/10.7763/IPCBEE.2018.V103.5 VL - 103 SP - 13 EP - 20 AN - OPUS4-50364 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Wolf, Marcus T1 - High-temperature-high pressure stress-strain testing of materials in CO2-containing saline solutions T2 - TMS 2015 - 144th annual meeting and exhibition supplemental proceedings N2 - In-situ stress-strain testing under corrosive environment, such as corrosive gasses (e.g. CO2) and highly saline water, is a challenge in testing corrosion fatigue of materials, e.g. for geothermal application or CCS (carbon capture and storage). The first corrosion chamber system was designed for performance at ambient pressure up to 100 °C. The second allows for corrosion fatigue testing at high pressure up to 200 bar and 400 °C. The highly flexible corrosion chambers allow for fast changing and easy alignment of test samples, visual monitoring, CAD-camera monitoring electrochemical measurements, O2-partial pressure or gas partial pressure measurement. Novelty is the fixing of the corrosion chamber directly onto the specimen, that guarantees best fitting and enables the test system to be modified easily suiting a variety of fatigue test machines. All parts of the test system are conforming to the technical rules. T2 - TMS 2015 annual meeting and exhibition CY - Orlando, FL, USA DA - 15.03.2015 PY - 2015 SN - 1-11-908241-2 SN - 978-1-119-08241-5 DO - https://doi.org/10.1002/9781119093466.ch123 SP - 1015 EP - 1022 PB - Wiley CY - Hoboken, NJ AN - OPUS4-35270 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Wolf, Marcus A1 - Wiegand, Reiner A1 - Bork, Claus-Peter T1 - New in-situ measurement technique to determine corrosion fatigue in components and pipes under cyclic load T2 - MWWD & IEMES 2012 (Proceedings) N2 - In the field of water pipelines, geothermal energy production as well as carbon capture and storage technology (CCS) materials have to provide a high resistance to corrosion and mechanical stress. The combination of cyclic load and corrosive aqueous environment leads to corrosion fatigue of pipes and components (e.g. pumps) and thus inevitably to the reduction of the lifetime of these components. To estimate the reliability of components from adjusted in-situ-laboratory experiments a corrosion chamber was designed and tested with CO2 saturated corrosive aqueous media flowing at a steady rate. Unique feature of this special chamber is its installation directly onto the sample and thus providing flexible usability in almost every testing machine. This allows simultaneous mechanical loading of the sample, operation at temperatures up to 100 °C and exposure to fluid flow of corrosive liquids and gases. The lifetime reduction of AISI 420C (X46Cr13, 1.4034) is demonstrated at T=60 °C, geothermal brine: Stuttgart Aquifer flow rate: 9 l/h, CO2. S-N plots, micrographic-, phase-, fractographic- and surface analysis were applied to obtain sustainable information on the corrosion fatigue behavior. Maximum number of cycles (here 12.5 x 106 cycles to failure) is reached at σa =173 MPa. No typical fatigue strength exists and passive corrosion fatigue may be identified as failure cause. T2 - MWWD & IEMES 2012 CY - Budva, Montenegro DA - 22.10.2012 KW - Corrosion fatigue KW - Corrosion chamber KW - S-N-plots KW - Steel KW - In-situ experiment PY - 2012 SN - 978-9944-5566-6-8 SP - 1 EP - 8 AN - OPUS4-28569 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Pfennig, A. A1 - Wolthusen, Helmut A1 - Wolf, Marcus A1 - Kranzmann, Axel T1 - Effect of heat treatment of injection pipe steels on the reliability of a saline aquifer water CCS-site in the Northern German basin T2 - GHGT-12 - Greenhouse gas control technologies conference N2 - Samples of differently heat treated high alloyed stainless injection-pipe steels AISI 420 X46Cr13, AISI 420J X20Cr13 as well as X5CrNiCuNb16-4 AISI 630 were kept at T=60 °C and ambient pressure as well as p=100 bar for 700 h - 8000 h in a CO2- saturated synthetic aquifer environment similar to possible geological on-shore CCS-sites in the northern German Basin. Corrosion rates and scale growth are lowest after long term exposure for steels hardened and tempered at 600 to 670 °C and pits - indicating local corrosion- decrease in diameter but increase in number as a function of carbon content of the steel. Martensitic microstructure is preferred with respect to this particular CCS-site. T2 - GHGT-12 - Greenhouse gas control technologies conference CY - Austin, TX, USA DA - 05.10.2014 KW - Steel KW - Supercritical CO2 KW - Pipeline KW - Corrosion KW - CCS KW - CO2-storage PY - 2014 UR - https://nbn-resolving.org/urn:nbn:de:kobv:b43-319433 DO - https://doi.org/10.1016/j.egypro.2014.11.609 SN - 1876-6102 N1 - Serientitel: Energy Procedia – Series title: Energy Procedia VL - 63 SP - 5762 EP - 5772 PB - Elsevier Ltd. AN - OPUS4-31943 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -