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authorClaudius "keldu" Holeksa <mail@keldu.de>2025-11-12 15:46:07 +0100
committerClaudius "keldu" Holeksa <mail@keldu.de>2025-11-12 15:46:07 +0100
commitd8640dc3c4f971d577a27c0f848892a1657f112c (patch)
tree07abfff74d98b0eed8f186d7a617f2aaa0e5c4a2 /typst
parent7386b497a25658d67cfe67dc455f227a7ea3ad7b (diff)
downloadphd-fluid_mechanics_report-d8640dc3c4f971d577a27c0f848892a1657f112c.tar.gz
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Diffstat (limited to 'typst')
-rw-r--r--typst/main.typ12
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