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| author | Claudius "keldu" Holeksa <mail@keldu.de> | 2025-11-12 15:46:07 +0100 |
|---|---|---|
| committer | Claudius "keldu" Holeksa <mail@keldu.de> | 2025-11-12 15:46:07 +0100 |
| commit | d8640dc3c4f971d577a27c0f848892a1657f112c (patch) | |
| tree | 07abfff74d98b0eed8f186d7a617f2aaa0e5c4a2 /typst | |
| parent | 7386b497a25658d67cfe67dc455f227a7ea3ad7b (diff) | |
| download | phd-fluid_mechanics_report-d8640dc3c4f971d577a27c0f848892a1657f112c.tar.gz | |
progress
Diffstat (limited to 'typst')
| -rw-r--r-- | typst/main.typ | 12 |
1 files changed, 10 insertions, 2 deletions
diff --git a/typst/main.typ b/typst/main.typ index 6944755..e47c56c 100644 --- a/typst/main.typ +++ b/typst/main.typ @@ -170,9 +170,9 @@ These forces diverge the smaller $h$ becomes. This is due to the viscous stress increasing on small films of fluid which then in turn dominate the interaction. -== Volume Averaged Navier-Stokes(VANS) +== Volume Averaged Navier-Stokes (VANS) -For the suspension of multiple particles Laurez et al suggests the use of a volume averaged Navier-Stokes equation where +For the suspension of multiple particles Laurez et al@MAYA2024 suggests the use of a volume averaged Navier-Stokes equation where the a porostiy field $epsilon$ is introduced and defined as #math.equation( @@ -195,6 +195,14 @@ $ delta (epsilon rho_f) / (delta t) + nabla ( epsilon rho_f v^f) = 0 $ ) +with a fluid momentum balance equation + +#math.equation( +block:true, +$ delta(epsilon rho_f v^f) / (delta t) + nabla (epsilon rho_f v^f v^f ) = - epsilon rho_f g + epsilon nabla\ +(mu_f (nabla v^f + (nabla v^f)^T) - epsilon^2 mu_f ( v^f - v^p) / K). $ +) + == Clogging of porous structures |
