1 / 12

Corrosion in Liquid Metal MHD flow

Corrosion in Liquid Metal MHD flow. By S. Saeidi Contribution from: S. Smolentsev, S. Malang University of Los Angeles August, 2009. Outline. Introduction Motivation/Goals Problem Definition Mathematical model Numerical Code Test Results Conclusion and Future Investigation.

june
Download Presentation

Corrosion in Liquid Metal MHD flow

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. Corrosion in Liquid Metal MHD flow By S. Saeidi Contribution from: S. Smolentsev, S. Malang University of Los Angeles August, 2009

  2. Outline • Introduction • Motivation/Goals • Problem Definition • Mathematical model • Numerical Code • Test Results • Conclusion and Future Investigation

  3. Introduction • Liquid metal, such as PbLi has so many advantages using as heat transfer fluid • Corrosion behavior of ferritic steel exposed to PbLi is not well understood • Maintaining acceptable limits for material loss is an important goal in blanket development • For ferritic steel/PbLi, corrosion is controlled by convection, diffusion and dissolution at the solid-liquid interface • Mass, heat and momentum transfer are coupled • The main purpose is to develop a numerical code to access corrosion of ferritic steel in PbLi under either experimental or real blanket conditions

  4. Motivation/Goals • There are no commercial codes available for corrosion analysis under fusion blanket conditions • Experimental data are available on ferritic steel/PbLi corrosion, but no good interpretation exists • We need a code, which would help us to perform some initial corrosion analysis under blanket conditions • We want to help experimentalists to understand the data, and to understand the corrosion phenomenon itself • Use of code for benchmarking with more sophisticated software, which is planned to be developed in future (HIMAG)

  5. Problem Definition for Ferritic Steel/PbLi Corrosion/Deposition • Corrosion is a result of dissolution of wall material, which is then transported by the flow • Transport mechanism are convection and diffusion • Flow is either laminar or turbulent. MHD effects should be included • We consider only one component (Fe) diffusing into PbLi • We also consider deposition phenomenon, which occurs in the cold part of the loop • Heat, mass and momentum transfer are coupled. The mathematical model should include energy equation, flow equations (including MHD effects), and mass transfer equation • The boundary condition at the solid-liquid interface assumes saturation concentration at given wall temperature

  6. Mathematical Model: governing equations m=0 – plane geometry m=1 – pipe t, kt, Dt=0 – laminar t, kt, Dt>0 – turbulent Turbulence closures are used to calculate t, kt, Dt MHD effects are included through jxB, P/x, t, kt, Dt More equationsare used to introduce MHD effects • Flow • Heat Transfer: • Mass Transfer:

  7. Mathematical Model:Input Data Saturation concentration Csat of iron atoms in PbLi as function of temperature Mass diffusion coefficient plotted as a function of the wall temperature Borgstedt, H.U and Rohrig, H.D:1991, Journal of Nuclear Materials 181-197 • Saturation concentration equation expressed in mole fraction (percentage)

  8. Numerical Code • Velocity distribution can be calculated for both laminar and turbulent flow regimes for simple geometries (pipe, rectangular duct, parallel channel) with or without a magnetic field • Finite-difference computer code • Non-uniform meshes with clustering points near the walls • Implicit method for solving equations (Tri-diagonal solver)

  9. Test Results, 1 Plot of Nusselt number along x direction in Plane channel with parabolic velocity profile The comparisons have been made for a laminar flow

  10. Test results, 2 Temperature profile Concentration profile Flow Length: 2m Channel Width: 20cm Twall= 500 C Laminar flow= U=3 cm/s Cwall=0.01 Kg/m3

  11. Test Results, 3 Rate of mass transfer along the X direction: Plot of Sherwood number along the X direction: • Sh decreases along the x until the flow become fully developed

  12. Conclusion and Future Investigations • Initials steps towards a mathematical model and numerical code for modeling of corrosion/deposition processes have been performed • We will keep working on the code and use it to analyze the effect of the flow regime, MHD, flow geometry, inlet conditions, etc. on corrosion/deposition of ferritic steel in PbLi under either experimental or real blanket conditions • We will look for experimental data and run the code trying to reproduce the experimental data • In the future, the code will be used for benchmarking with more sophisticated software (HIMAG)

More Related