Aerosol Production in Lead-protected and Flibe-protected Chambers

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Presentation transcript:

Aerosol Production in Lead-protected and Flibe-protected Chambers J.P. Sharpe INEEL Fusion Safety Program Discussion Topics Improvements to Models Comparison of Lead and Initial Flibe Results What’s Next? (to pass the Continuing Resolution!!!)

Model Improvements: Analysis: Wall thermal response model (including volumetric heating from penetrating x-rays) is now fully incorporated into the code; surface vaporization and condensation are solved consistently with other parts of code Flibe bulk properties added to perform initial look at flibe nucleation; calculations for dissociation of flibe and condensation of component species has NOT been performed Analysis: Average values of aerosol properties in four chamber regions were determined; a spherical chamber with a 6.5 m radius was used Values of interest are mass concentration and particle size distribution in Region 1; these quantities are important for their impact on beam and target propagation

Model Results: Liquid Wall Chambers Simulations were performed for liquid-covered walls exposed to the energy from a 458 MJ indirect-drive target. X-rays carry 115 MJ for this target; only the x-ray flux was considered to deposit energy on the wall surface. Initial chamber conditions for both cases: Twall = 800 K, and the chamber pressure equal to the material’s equilibrium vapor pressure at the wall temperature. Chamber radius is 6.5 m. Flow Model Results: Vapor Velocity Lead Flibe

Model Results: Liquid Wall Chambers, cont. Aerosol Model Results- Total Vapor and Aerosol Masses: Lead Flibe Regional Mass Concentrations: Lead Flibe

Model Results: Liquid Wall Chambers, cont. Regional Particle Size Distributions (for flibe only): Region 1 Region 2 Region 3 Region 4

Model Results: Liquid Wall Chambers, cont. Region 1 Particle Size Distributions: Region 1 Region 1 Lead Flibe Results indicate that flibe gives a smaller mass concentration near the chamber center (10 mg/m3 versus 20 mg/m3 for lead). The size distribution of flibe is more narrow.

Summary of results: What’s Next??? add other particle sources to model (e.g. melt-layer ejection and spry droplet injection) fix radiative/plasma part of gas-dynamic model to better simulate the behavior of evaporated vapor (e.g. ion heating) extend to model to multi-component aerosols to allow more realistic simulation of Flibe condensation