Abstract

In the development of concentrated solar power systems (CSPs), the high-temperature corrosion of alloys in receivers and heat exchangers can affect the performance on CSPs and influence the apparent durability. [1-4] The extent to which high-temperature corrosion is reversible may improve the commercialization. To understand corrosion mechanisms and their impact on alloys, experimental coupon (1.2mm×12mm×30mm) studies were conducted to the 700-1000°C within halide and fluoride salts in a thermosiphon. The thermosiphon reactor was designed to allow exposure the coupons to the both isothermal and non-isothermal condition. That is, the thermal gradients between top and bottom of the reactor could induce natural convection of the salts. The corrosion experiments such as coupon test and post mortem analysis highlighted main corrosion mechanisms of Cr depletion and diffusion along the grain boundaries. [5-6] A multi-physics corrosion model that include the main corrosion mechanism of Cr oxidation along with diffusion-limited corrosion as the limiting step allow to predict corrosion rates (i.e., current density) and corrosion potentials. Also, a CFD model has shown that temperatures and fluid flows can be accurately predicted in molten salt heat transfer systems including coupons. The CFD predictions allow to characterize natural convection flows in the reactor by analyzing engineering parameters such as Rayleigh number, Nutssel number, and Grashof number, etc. As the temperature and mass transports are coupled in the natural convection system, the analysis of these dimensionless numbers helps to correlate different physics to understand the system better and to reduce complication to solve the problem. These dimensionless numbers around coupons incorporated into the corrosion model allow to predict mass transfer coefficients and boundary layer thickness that determine corrosion rates (i.e., current density). The model predictions and experiment results suggest that the use of thicker materials to improve the lifetime may not be a good strategy in molten salt systems due to the localized nature of the corrosion. Acknowledgements The authors gratefully acknowledge the support for this work by the DOE EERE SunShot Initiative under a subcontract from SRNL to the University of Alabama and to the University of South Carolina. R eferences [1] C. Forsberg, Progress in Nuclear Energy, 47, 32-43, 2005.[2] C. Forsberg, P.F. Peterson, and H.H. Zhao, J. Sol. Energy Eng. Trans.-ASME, 129, 141-146, 2007.[3] D. Ludwig, L. Olson, K. Sridahran, M. Anderson, and T. Allen, Corrosion Engineering Science and Technology, 46, 360-364, 2011.[4] P. Sabharwall, Matt Ebner, Manohar Sohal, Phil Sharpe, Mark Anderson, Kumar Sridharan, James Ambrosek, Luke Olson, Paul Brooks, Molten Salts for High Temperature Reactors: University of Wisconsin Molten Salt Corrosion and Flow Loop Experiments – Issues Identified and Path Forward, 2010. [5] B. L. Garcia-Diaz, L. Olson, M. Martinez-Rodriguez, R. Fuentens, J. Gray, “Electrochemical study of corrosion in high temperature molten salts,” paper #741, 2014 ECS and SMEQ Joint International Meeting, Cancun, Mexico, Oct. 08, 2014. [6] R. Fuentens, L. Olson, M. Martinez-Rodriguez, J. Gray, B. L. Garcia-Diaz, “Corrosion of high temperature materials in fluoride and chloride molten salts,” paper #743, 2014 ECS and SMEQ Joint International Meeting, Cancun, Mexico, Oct. 08, 2014.

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