Abstract

Modifications to the Computational Fluid Dynamic (CFD) software ANSYS Fluent were done to quantify and characterize tritium transport in gas-liquid contactors (GLCs). A double-slit, Ergun-like equation was employed for the porous media model, with Ergun coefficients validated with Sulzer's Sulcol software. Tritium transport from PbLi within the GLC was verified against analytical models. The geometry of the CFD model was based on the MELODIE GLC experiment. The hydrodynamic CFD pressure drop results align well with Sulcol estimations and fall between the predictions of the analytical Delft-Olujić and Billet and Schultes models. In terms of mass transfer efficiency, traditional mass transfer models showed a significant deviation from experimental results when using varying values of H solubility in PbLi. A saturation phenomenon occurred when utilizing high solubility values for hydrogen in PbLi. A modified film theory mass transfer coefficient incorporating either the Delft-Olujić or Billet and Schultes wettability model yielded CFD-predicted extraction efficiencies that closely matched experimental measurements.

Department(s)

Nuclear Engineering and Radiation Science

Publication Status

Full Text Access

Comments

Office of Science, Grant DE-SC0023674

Keywords and Phrases

Computational fluid dynamics, Porous media approach, Eulerian-Eulerian, Ergun; Fusion; Gas-liquid contactor (GLC); Tritium extraction from Pbli

International Standard Serial Number (ISSN)

0920-3796

Document Type

Article - Journal

Document Version

Citation

File Type

text

Language(s)

English

Rights

© 2026 Elsevier, All rights reserved.

Publication Date

01 Jan 2026

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