Temperature effect and alloying elements impact on the corrosion behaviour of the alloys exposed to molten carbonate environments for CSP application

  1. de Miguel, M.T.
  2. Lasanta, M.I.
  3. García-Martín, G.
  4. Díaz, R.
  5. Pérez, F.J.
Revista:
Corrosion Science

ISSN: 0010-938X

Año de publicación: 2022

Volumen: 201

Páginas: 110274

Tipo: Artículo

DOI: 10.1016/J.CORSCI.2022.110274 GOOGLE SCHOLAR lock_openAcceso abierto editor

Otras publicaciones en: Corrosion Science

Resumen

This investigation assesses the effect of the alloy composition and temperature in the corrosivity of the ternary carbonate eutectic, 32% Li2CO3, 33% Na2CO3, 35% K2CO3. To this end, an iron-based alloy, coded as 51Fe-24Cr-20Ni, and a nickel-based alloy, coded as 5Fe–23Cr-58Ni-8Mo, were exposed to the carbonate mixture for 500 h at 700 ºC, 750 ºC and 800 ºC under static atmospheric air. The results revealed that corrosion extension does not have a linear dependence on temperature. There are changes in the corrosion mechanism that depend on the temperature, but, in turn, they are directly influenced by the alloying elements of the material. The performance of the nickel-based substrate proved to be catastrophic at all the studied temperatures. The order from worst to best was 700 ºC > 750 ºC > 800 ºC. The presence of a high molybdenum concentration in the carbonate mixture in contact with this nickel-based alloy suggested that this element dissolution contributes to increasing the corrosivity of the mixture. By contrast, the iron-based alloy showed improved corrosion resistance, with an estimated corrosion rate in the order of hundreds of microns at the three temperatures. The best performance of the 51Fe-24Cr-20Ni alloy was achieved at 700 ºC, followed by that at 800 ºC, while the highest degradation was registered at 750 ºC. This investigation reinforced the idea of the complexity of the corrosion processes in molten carbonate. The equilibrium of corrosive species is very sensitive to an important number of parameters, meaning that modifications in the system conditions have a great impact on corrosivity. Hence, it is critical not to make assumptions when considering potential materials for carbonate containment in CSP technology.

Información de financiación

Financiadores

Referencias bibliográficas

  • Achkari, (2020), Appl. Therm. Eng., 167, 10.1016/j.applthermaleng.2019.114806
  • International Energy Agency, Concentrating Solar Power (CSP). 2020, Paris. 〈https://www.iea.org/reports/concentrated-solar-power-csp〉.
  • Fereres, (2018), Sol. Energy Mater. Sol. Cells, 188, pp. 119, 10.1016/j.solmat.2018.08.028
  • Fernández, (2019), Renew. Energy, 140, pp. 152, 10.1016/j.renene.2019.03.049
  • M..Mehos, C. Turchi., J. Vidal, M. Wagner, Z. Ma, C. Ho, W. Kolb,C. Andraka, A. Kruizenga, Concentrating Solar Power Gen3 Demonstration Roadmap, ( Ed.), N.R.E. Laboratory. 2017.
  • González-Roubaud, (2017), Renew. Sustain. Energy Rev., 80, pp. 133, 10.1016/j.rser.2017.05.084
  • Wu, (2011), Sol. Energy, 85, pp. 1957, 10.1016/j.solener.2011.05.004
  • Turchi, (2018), Sol. Energy, 164, pp. 38, 10.1016/j.solener.2018.01.063
  • Viswanathan, (2001), J. Mater. Eng. Perform., 10, pp. 81, 10.1361/105994901770345394
  • Javanshir, (2018), Energy, 157, pp. 65, 10.1016/j.energy.2018.05.137
  • Turchi, (2012), Energy Sustain., 44816, pp. 375
  • Padilla, (2015), Appl. Energy, 148, pp. 348, 10.1016/j.apenergy.2015.03.090
  • Ahn, (2015), Nucl. Eng. Technol., 47, pp. 647, 10.1016/j.net.2015.06.009
  • R.J. Petri, T.D. Claar, L.G. Marianowski, Evaluation of molten carbonates as latent heat thermal energy storage materials, in: Proceedings of the Conference, Fourteenth Intersociety Energy Conversion Conference, Boston, MA, USA, 5 Aug 1979, Institute of Gas Technology, Chicago, IL,None. Medium, X, Size, 7.
  • R.W. Mar, R.W. Carling, The application of molten salts to large solar power systems., in: Proceedings of the Third International Molten Salt Symposium in the 158th Meeting of The Electrochemical Society, T.E. Society, Editor, The Electrochemical Society, Hollywood, Florida, 1981.
  • Frangini, (2016), Int. J. Hydrog. Energy, 41, pp. 18739, 10.1016/j.ijhydene.2015.12.073
  • Spiegel, (1997), Corros. Sci., 39, pp. 1193, 10.1016/S0010-938X(97)00020-6
  • Vossen, (1995), J. Electrochem. Soc., 142, pp. 3327, 10.1149/1.2049983
  • Biedenkopf, (1997), Mater. Corros., 48, pp. 477, 10.1002/maco.19970480803
  • Biedenkopf, (2000), Mater. Corros., 51, pp. 287, 10.1002/(SICI)1521-4176(200005)51:5<287::AID-MACO287>3.0.CO;2-8
  • Gonzalez-Rodriguez, (2007), J. Power Sources, 172, pp. 799, 10.1016/j.jpowsour.2007.05.010
  • D.A. Shores, P. Singh, Molten carbonate fuel cell technology, in: Proceedings of the Electrochemical Society Serie, Pennington, New Jersey, 1984.
  • S. Frangini, Corrosion of Structural Materials in Molten Carbonate Fuel Cells: an Overview, in High Temperature Corrosion in Molten Salts, C.A.C. Sequeira, Editor, 2003.
  • Gomez-Vidal, (2016), Sol. Energy Mater. Sol. Cells, 157, pp. 517, 10.1016/j.solmat.2016.07.029
  • A. Kruizenga, Corrosion Mechanisms in Chloride and Carbonate Salts, in: SANDIA Report, 2012, SANDIA National Laboratories.
  • de Miguel, (2016), Sol. Energy Mater. Sol. Cells, 157, pp. 966, 10.1016/j.solmat.2016.08.014
  • Sarvghad, (2017), Sol. Energy Mater. Sol. Cells, 172, pp. 220, 10.1016/j.solmat.2017.07.036
  • Sarvghad, (2017), Sol. Energy Mater. Sol. Cells, 170, pp. 48, 10.1016/j.solmat.2017.05.063
  • Sarvghad, (2018), Sol. Energy, 172, pp. 198, 10.1016/j.solener.2018.03.053
  • Encinas-Sánchez, (2018), Sol. Energy, 171, pp. 286, 10.1016/j.solener.2018.06.091
  • Gallardo-González, (2018), Sol. Energy Mater. Sol. Cells, 186, pp. 1, 10.1016/j.solmat.2018.06.003
  • Sah, (2018), Corros. Sci., 133, pp. 310, 10.1016/j.corsci.2018.01.031
  • Fernández, (2019), Renew. Energy, 140, pp. 227, 10.1016/j.renene.2019.03.087
  • Sah, (2020), Corros. Sci., 169, 10.1016/j.corsci.2020.108535
  • Luo, (2020), Sol. Energy Mater. Sol. Cells, 217, 10.1016/j.solmat.2020.110679
  • Liu, (2019), Sol. Energy, 191, pp. 435, 10.1016/j.solener.2019.09.015
  • Zhuang, (2019), Sol. Energy, 189, pp. 254, 10.1016/j.solener.2019.07.065
  • Fernández, (2014), Sol. Energy, 109, pp. 125, 10.1016/j.solener.2014.07.027
  • Zimnol, (1997), Solid State Ion., 101–103, pp. 667, 10.1016/S0167-2738(97)00321-4
  • Paik, (2005), Thermochim. Acta, 425, pp. 131, 10.1016/j.tca.2004.06.012
  • Zhang, (2013), Int. J. Greenh. Gas Control, 12, pp. 351, 10.1016/j.ijggc.2012.11.013
  • Pérez, (2002), Surf. Coat. Technol., 161, pp. 293, 10.1016/S0257-8972(02)00417-6
  • Audigié, (2018), Surf. Coat. Technol., 349, pp. 1148, 10.1016/j.surfcoat.2018.05.081
  • Devereux, (1983), Corros. Sci., 23, pp. 205, 10.1016/0010-938X(83)90103-8
  • Vossen, (1996), J. Electrochem. Soc., 143, pp. 58, 10.1149/1.1836387
  • Pérez, (2000), Oxid. Met., 53, pp. 375, 10.1023/A:1004501606718
  • Tzvetkoff, (2003), Mater. Chem. Phys., 82, pp. 897, 10.1016/j.matchemphys.2003.08.001
  • Vossen, (1996), J. Electrochem. Soc., 143, pp. 66, 10.1149/1.1836388
  • Biedenkopf, (1997), Mater. Corros., 48, pp. 731, 10.1002/maco.19970481103
  • Uchida, (1986), J. Electroanal. Chem. Interfacial Electrochem., 209, pp. 125, 10.1016/0022-0728(86)80191-7
  • Pérez, (2006), Mater. Sci. Forum, 522–523, pp. 531, 10.4028/www.scientific.net/MSF.522-523.531
  • Al Omer, (1978), Thermochim. Acta, 24, pp. 97, 10.1016/0040-6031(78)85138-7
  • Li, (1999), J. Electrochem. Soc., 146, pp. 2449, 10.1149/1.1391954