Minor fixes

chaos-polymtl · Nov 21, 2024 · c62eb5d · c62eb5d
1 parent 18740ac
commit c62eb5d
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Showing 2 changed files with 17 additions and 15 deletions.
diff --git a/...olved-cfd-dem/gas-solid-spouted-cylinder-bed/gas-solid-spouted-cylinder-bed.rst b/...olved-cfd-dem/gas-solid-spouted-cylinder-bed/gas-solid-spouted-cylinder-bed.rst
@@ -44,15 +44,15 @@ In this example, we are simulating a cylinder shaped spouted bed. We introduce t
     :name: geometry
     :height: 15cm 
 
-The geometry of the bed was created using `Pointiwise <../../../tools/pointwise/pointowise.html>`_. An overview of the mesh is:
+The geometry of the bed was created using `Pointwise <../../../tools/pointwise/pointwise.html>`_. An overview of the mesh is:
 
 .. image:: images/mesh.png
     :alt: The geometry and boundary conditions
     :align: center
     :name: mesh_ver
     :height: 10cm
 
-In unresolved CFD-DEM, the averaging volume used to calculate the void fraction needs to be large enough to contain several particles (>10). Since the averaging volume used in the quadrature-centred method is generally related to the cell volume, this introduces a limitation on the cell size. In general, the averaging volume, which in this case is controlled by the cell size, should be approximately three time larger than the diameter of the particles in order to get stable calculation.
+In unresolved CFD-DEM, the averaging volume used to calculate the void fraction needs to be large enough to contain several particles (>10). Since the averaging volume used in the quadrature-centred method is generally related to the cell volume, this introduces a limitation on the cell size. In general, the averaging volume, which in this case is controlled by the cell size, should be approximately three times larger than the diameter of the particles in order to get stable calculation.
 
 .. code-block:: text
 
@@ -189,8 +189,7 @@ We set the inlet velocity to 2.5 m/s, and the background velocity to 0.5 m/s on
   subsection boundary conditions
     set time dependent = false
     set number         = 5
-
-
+    
     subsection bc 0 #outlet
       set id   = 3
       set type = outlet

diff --git a/...ples/unresolved-cfd-dem/gas-solid-spouted-cylinder-bed/gas-solid-spouted-cylinder-bed.prm b/...ples/unresolved-cfd-dem/gas-solid-spouted-cylinder-bed/gas-solid-spouted-cylinder-bed.prm
@@ -11,12 +11,12 @@ set dimension = 3
 #---------------------------------------------------
 
 subsection simulation control
-  set method               = bdf2
-  set number mesh adapt    = 0
-  set output frequency     = 50
-  set time end             = 5
-  set time step            = 0.001
-  set output path          = output/
+  set method            = bdf2
+  set number mesh adapt = 0
+  set output frequency  = 50
+  set time end          = 5
+  set time step         = 0.001
+  set output path       = output/
 end
 
 #---------------------------------------------------
@@ -39,6 +39,10 @@ subsection FEM
   set pressure order = 1
 end
 
+#---------------------------------------------------
+# Timer
+#---------------------------------------------------
+
 subsection timer
   set type = iteration
 end
@@ -118,7 +122,6 @@ end
 # Boundary Conditions
 #---------------------------------------------------
 
-
 subsection boundary conditions
   set time dependent = false
   set number         = 5
@@ -144,16 +147,16 @@ subsection boundary conditions
   end
 
   subsection bc 2 #wall
-    set id = 6
+    set id   = 6
     set type = slip
   end
 
   subsection bc 3 #channel_wall
-    set id = 5
+    set id   = 5
     set type = slip
   end
-    
-  subsection bc 4   #bed_wall_bottom
+
+  subsection bc 4 #bed_wall_bottom
     set id   = 4
     set type = function
     subsection u