Différences

Ci-dessous, les différences entre deux révisions de la page.

--- datasetmeca:flow2dpastheadtedcylinder1 [2021/12/15 14:55] – [Database organisation] yann
+++ datasetmeca:flow2dpastheadtedcylinder1 [2023/05/26 18:54] (Version actuelle) – yann
@@ Ligne 5: / Ligne 5: @@
 </note>
+**Author** :  Y. Fraigneau, LISN, UMR CNRS 9015 (yann.fraigneau@lisn.fr) \\
-**Author** :  Y. Fraigneau  CNRS-LIMSI (yann.fraigneau@limsi.fr) \\
 **Date**   :  June 2019\\
-**Simulation type** : DNS ([[https://sunfluidh.limsi.fr|Sunfluidh code]]) \\
+**Simulation type** : DNS (code Sunfluidh -- [[https://sunfluidh.lisn.upsaclay.fr|Sunfluidh code]]) \\
 **Location** : /DATABASE_2DFLOW_AROUND_HEATED_SQUARECYLINDER_DNS \\
-**Status** : Free access \\
+**Status** : Free access for laboratory members, on request for external members \\
-**Data size** : ~ 3 Gb \\
+**Data size** : ~ 1 Gb \\
 {{ :datasetmeca:snapshot_heatcyl_snap.png?900 |}}
-[[https://sunfluidh.limsi.fr/sunfluidh:sunfluidh_gallery| A video is available here ]]
+[[https://sunfluidh.lisn.upsaclay.fr/doku.php?id=sunfluidh:sunfluidh_gallery#d_flow_past_a_heated_square-cylinder| A video is available here ]]
 [[:start|Come back to first page]]
@@ Ligne 24: / Ligne 23: @@
 === 2D sketch ===
-{{ :datasetmeca:sketch_config_heatcyl.jpg?800 |}}
+{{ :datasetmeca:sketch_config_heatcyl.jpg?600 |}}
-\\
 === Referential : cartesian geometry ===
@@ Ligne 44: / Ligne 40: @@
    * Dynamic viscosity : dynamic viscosity of the fluid ($\mu_0$)
    * thermal diffusivity :  ($\kappa_0$)
-   * Reynolds number   : $Re_H= \frac{\rho_0.U_0.h}{\mu_0}= 50$
+   * Reynolds number   : $Re_h= \frac{\rho_0.U_0.h}{\mu_0}= 50$
-   * Rayleigh number   : $Ra=  \frac{\rho_0.\beta.g\Delta T.H_u^3}{\mu_0 \kappa_0}= 5\;10^6$
+   * Rayleigh number   : $Ra_{Hu}=  \frac{\rho_0.\beta.g\Delta T.H_u^3}{\mu_0 \kappa_0}= 5\;10^6$
 === Non-dimensionalised data ===
@@ Ligne 51: / Ligne 47: @@
    * density    : $\rho^*= \rho/\rho_0= 1$
    * coordinates : $x*=\frac{x}{h}$, $y^*=\frac{y}{h}$
-   * temperature : $T^*=\frac{T-T_c}{T_h-T_c}$ ($T_h$ and $T_c$ are respectively the temperature imposed at the cylender's walls and the temperature at the inlet and channel's walls)
+   * temperature : $T^*=\frac{T-T_c}{T_h-T_c}$ ($T_h$ and $T_c$ are respectively the temperature imposed at the cylinder's walls and the temperature at the inlet and channel's walls)
 === Computational domain ===
@@ Ligne 116: / Ligne 112: @@
     /SNAPSHOTS       : snapshots binary files res_xxxxx_yyyyyyy.d
-    /SNAPSHOTS_MPI4  : snapshots ressulting from a domain decomposition with 4 MPI processes
+    /SNAPSHOTS_MPI4  : snapshots resulting from a domain decomposition with 4 MPI processes
     /TIMESERIES      : ASCII files