[SCM] Gerris Flow Solver branch, upstream, updated. b3aa46814a06c9cb2912790b23916ffb44f1f203

Stephane Popinet s.popinet at niwa.co.nz
Fri May 15 02:52:11 UTC 2009


The following commit has been merged in the upstream branch:
commit aca2f35a10b4b684382a6cc801ed0fc162b09775
Author: Stephane Popinet <s.popinet at niwa.co.nz>
Date:   Tue Jul 5 12:32:03 2005 +1000

    Replaced SourceViscosity with SourceDiffusion in examples for now
    
    darcs-hash:20050705023203-fbd8f-bb70b17ff9893f38ce4bb3b44591f28eedd47d00.gz

diff --git a/doc/examples/cylinder/cylinder.gfs b/doc/examples/cylinder/cylinder.gfs
index 0e4bce6..21d2892 100644
--- a/doc/examples/cylinder/cylinder.gfs
+++ b/doc/examples/cylinder/cylinder.gfs
@@ -69,7 +69,8 @@
   # Set a viscosity source term on the velocity vector with x-component U
   # The Reynolds number is Re = D*U/Nu = 0.125*1/0.00078125 = 160
   # where D is the cylinder diameter (as defined in cylinder.gts)
-  SourceViscosity {} U 0.00078125
+  SourceDiffusion {} U 0.00078125
+  SourceDiffusion {} V 0.00078125
 
   # Writes the time and timestep every 10 timesteps on standard output
   OutputTime { istep = 10 } stdout
diff --git a/doc/examples/cylinder/heated/heated.gfs b/doc/examples/cylinder/heated/heated.gfs
index 17171b9..90103e2 100644
--- a/doc/examples/cylinder/heated/heated.gfs
+++ b/doc/examples/cylinder/heated/heated.gfs
@@ -60,7 +60,8 @@
   # Set a viscosity source term on the velocity vector with x-component U
   # The Reynolds number is Re = D*U/Nu = 0.125*1/0.00078125 = 160
   # where D is the cylinder diameter (as defined in cylinder.gts)
-  SourceViscosity {} U 0.00078125
+  SourceDiffusion {} U 0.00078125
+  SourceDiffusion {} V 0.00078125
 
   # Writes the time and timestep every 10 timesteps on standard output
   OutputTime { istep = 10 } stdout
diff --git a/doc/examples/lid/lid.gfs b/doc/examples/lid/lid.gfs
index 7e38ffc..2812d5b 100644
--- a/doc/examples/lid/lid.gfs
+++ b/doc/examples/lid/lid.gfs
@@ -57,7 +57,8 @@
 
   # Set a viscosity source term on the velocity vector with x-component U
   # The Reynolds number is Re = L*U/Nu = 1*1/1e-3 = 1000
-  SourceViscosity {} U 1e-3
+  SourceDiffusion {} U 1e-3
+  SourceDiffusion {} V 1e-3
 
   # Writes the time and timestep every 10 timesteps on standard error
   OutputTime { istep = 10 } stderr

-- 
Gerris Flow Solver



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