#
NUMBER_OF_MODULES 
1
#
# 1st module
#
MODULE_NAME
Convection Diffusion Equation
MODULE_ID
0
APPLICATION
poisson
# Number of variables
# Name of variables
VARIABLES
1
c
# Number of data
# Number of coefficients; tag in outputfile; Name in window; name of coeffs; default values
EQUATION_DATA
4
2;CONVECTIVE VELOCITIES;Convective Velocities;U =;0.0;V =;0.0 
3;CONDUCTIVITY;Diffusion coefficients:;k11 = ;1.0;k12 = ;0.0;k22 = ;1.0 
1;ABSORTION;Absorbtion coefficient:;a = ;0.0
1;RIGHT HAND SIDE;Source term:;f = ;0.0
#
# Boundary conditions
#
BOUNDARY_CONDITIONS
2
Dirichlet Boundary Condition;%s = 
Neumann Boundary Condition;grad(%s).n = 
BOUNDARY_TAGS
D;N;F;Z;N;F;Q
#
# 2nd module
#
MODULE_NAME
Incompressible Navier-Stokes
MODULE_ID
1
APPLICATION
nsfem
VARIABLES
2
u;v
# Number of data
# Number of coefficients; tag in outputfile; Name in window; name of coeffs;
EQUATION_DATA
3
1;REYNOLDS; Reynolds number; Re = ;100
1;TIME STEP; Time step:; dt = ;0.1
1;TIME TOL; Time tolerance:; tol = ;0.001
#
# Boundary conditions
#
BOUNDARY_CONDITIONS
2
Dirichlet Boundary Condition;%s = 
Neumann Boundary Condition;grad(%s).n = 
BOUNDARY_TAGS
D;N;F;Z;N;F;Q
#
# 3d module
#
MODULE_NAME
Navier-Stokes & Energy equation
MODULE_ID
2
APPLICATION
nsefem
VARIABLES
3
u;v;T
# Number of data
# Number of coefficients; tag in outputfile; Name in window; name of coeffs;
EQUATION_DATA
5
1;TIME STEP; Time step:; dt = ;0.1
1;TIME TOL; Time tolerance:; tol = ;0.001
1;REYNOLDS; Reynolds number; Re = ;100
1;RAYLEIGH; Rayleigh number:; Ra = ;27
1;PRANDTL; Prandtl number:; Pr = ;27
#
# Boundary conditions
#
BOUNDARY_CONDITIONS
3
Dirichlet Boundary Condition;%s = 
Neumann Boundary Condition;grad(%s).n = 
Thermocapillary Condition; (ignored)%s = 
BOUNDARY_TAGS
D;N;F;T;Y;W;T;W;W;W;W;W;
#
# 4th module
#
MODULE_NAME
Transient Diffusion Equation
MODULE_ID
3
APPLICATION
transi
# Number of variables
# Name of variables
VARIABLES
1
c
# Number of data
# Number of coefficients; tag in outputfile; Name in window; name of coeffs; default values
EQUATION_DATA
3
3;CONDUCTIVITY;Diffusion coefficients:;k11 = ;1.0;k12 = ;0.0;k22 = ;1.0 
1;RIGHT HAND SIDE;Source term:;f = ;0.0
1;TIME INTERVAL; Time interval:; T = ;1.0
#
# Boundary conditions
#
BOUNDARY_CONDITIONS
2
Dirichlet Boundary Condition;%s = 
Neumann Boundary Condition;grad(%s).n = 
BOUNDARY_TAGS
D;N;F;Z;N;F;Q
END