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boundary.c
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///////////////////////////////////////////////////////////////////////////////
///
/// \file boundary.c
///
/// \brief Set the boundary conditions
///
/// \author Mingang Jin, Qingyan Chen
/// Purdue University
/// Jin55@purdue.edu, YanChen@purdue.edu
/// Wangda Zuo
/// University of Miami
/// W.Zuo@miami.edu
///
/// \date 8/3/2013
///
/// This file provides functions that are used for setting the boundary
/// conditons.
/// It starts with \c set_bnd(). Then different subroutines are called
/// according to the properties of variables.
///
///////////////////////////////////////////////////////////////////////////////
#include "boundary.h"
///////////////////////////////////////////////////////////////////////////////
/// Entrance of setting boundary conditions
///
/// Specific boundary conditions will be selected according to the variable
/// type.
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param var_type The type of variable
///\param index Index of trace substances or species
///\param psi Pointer to the variable needing the boundary conditions
///\param BINDEX Pointer to boundary index
///
///\return 0 if no error occurred
///////////////////////////////////////////////////////////////////////////////
int set_bnd(PARA_DATA *para, REAL **var, int var_type, int index, REAL *psi,
int **BINDEX) {
int flag;
switch(var_type) {
case VX:
flag = set_bnd_vel(para, var, VX, psi, BINDEX);
if(flag!=0)
ffd_log("set_bnd(): Could not set boundary condition for X-velocity.",
FFD_ERROR);
break;
case VY:
flag = set_bnd_vel(para, var, VY, psi, BINDEX);
if(flag!=0)
ffd_log("set_bnd(): Could not set boundary condition for Y-velocity.",
FFD_ERROR);
break;
case VZ:
flag = set_bnd_vel(para, var, VZ, psi, BINDEX);
if(flag!=0)
ffd_log("set_bnd(): Could not set boundary condition for Z-velocity.",
FFD_ERROR);
break;
case TEMP:
flag = set_bnd_temp(para, var, TEMP, psi, BINDEX);
if(flag!=0)
ffd_log("set_bnd(): Could not set boundary condition for temperature.",
FFD_ERROR);
break;
case TRACE:
flag = set_bnd_trace(para, var, index, psi, BINDEX);
if(flag!=0)
ffd_log("set_bnd(): Could not set boundary condition for trace.",
FFD_ERROR);
break;
default:
flag = 1;
sprintf(msg,
"set_bnd(): boundary condition for variable type %d is not defined.",
var_type);
ffd_log(msg, FFD_ERROR);
}
return flag;
} // End of set_bnd()
///////////////////////////////////////////////////////////////////////////////
/// Set boundary conditions for velocity
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param var_type The type of variable
///\param psi Pointer to the variable needing the boundary conditions
///\param BINDEX Pointer to boundary index
///
///\return 0 if no error occurred
///////////////////////////////////////////////////////////////////////////////
int set_bnd_vel(PARA_DATA *para, REAL **var, int var_type, REAL *psi,
int **BINDEX) {
int i, j, k;
int it;
int imax = para->geom->imax, jmax = para->geom->jmax;
int kmax = para->geom->kmax;
int index= para->geom->index;
int IMAX = imax+2, IJMAX = (imax+2)*(jmax+2);
REAL *aw = var[AW], *ae = var[AE], *as = var[AS], *an = var[AN];
REAL *af = var[AF], *ab = var[AB];
REAL *flagp = var[FLAGP];
switch(var_type) {
/* --------------------------------------------------------------------------
| VX
-------------------------------------------------------------------------- */
case VX:
for(it=0; it<index; it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
// Inlet
if(flagp[IX(i,j,k)]==0) {
psi[IX(i,j,k)] = var[VXBC][IX(i,j,k)];
if(i!=0) psi[IX(i-1,j,k)] = var[VXBC][IX(i,j,k)];
}
// Solid wall
if(flagp[IX(i,j,k)]==1) {
psi[IX(i,j,k)] = 0;
if(i!=0) psi[IX(i-1,j,k)] = 0;
}
// Outlet
if(flagp[IX(i,j,k)]==2) {
// West
if(i==0) {
psi[IX(i,j,k)] = psi[IX(i+1,j,k)];
aw[IX(i+1,j,k)] = 0;
}
// East
if(i==imax+1) {
psi[IX(i-1,j,k)] = psi[IX(i-2,j,k)];
ae[IX(i-2,j,k)] = 0;
}
// South
if(j==0) as[IX(i,j+1,k)] = 0;
// North
if(j==jmax+1) an[IX(i,j-1,k)] = 0;
// Floor
if(k==0) ab[IX(i,j,k+1)] = 0;
// Ceiling
if(k==kmax+1) af[IX(i,j,k-1)] = 0;
}
} // End of setting VX
break;
/* --------------------------------------------------------------------------
| VY
-------------------------------------------------------------------------- */
case VY:
for(it=0;it<index;it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
// Inlet
if(flagp[IX(i,j,k)]==0) {
psi[IX(i,j,k)] = var[VYBC][IX(i,j,k)];
if(j!=0) psi[IX(i,j-1,k)] = var[VYBC][IX(i,j,k)];
}
// Solid wall
if(flagp[IX(i,j,k)]==1) {
psi[IX(i,j,k)] = 0;
if(j!=0) psi[IX(i,j-1,k)] = 0;
}
// Outlet
if(flagp[IX(i,j,k)]==2) {
// West
if(i==0) aw[IX(i+1,j,k)]=0;
// East
if(i==imax+1) ae[IX(i-1,j,k)]=0;
// South
if(j==0) {
as[IX(i,j+1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j+1,k)];
}
// North
if(j==jmax+1) {
an[IX(i,j-2,k)] = 0;
psi[IX(i,j-1,k)] = psi[IX(i,j-2,k)];
}
// Floor
if(k==0) ab[IX(i,j,k+1)] = 0;
if(k==kmax+1) af[IX(i,j,k-1)] = 0;
}
} // End of setting VY
break;
/* --------------------------------------------------------------------------
| VZ
-------------------------------------------------------------------------- */
case VZ:
for(it=0;it<index;it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
// Inlet
if(flagp[IX(i,j,k)]==INLET) {
psi[IX(i,j,k)] = var[VZBC][IX(i,j,k)];
if(k!=0) psi[IX(i,j,k-1)] = var[VZBC][IX(i,j,k)];
}
if(flagp[IX(i,j,k)]==SOLID) {
psi[IX(i,j,k)] = 0;
if(k!=0) psi[IX(i,j,k-1)] = 0;
}
if(flagp[IX(i,j,k)]==OUTLET) {
// West
if(i==0) aw[IX(i+1,j,k)] = 0;
// East
if(i==imax+1) ae[IX(i-1,j,k)] = 0;
//South
if(j==0) as[IX(i,j+1,k)] = 0;
// North
if(j==jmax+1) an[IX(i,j-1,k)] = 0;
// Floor
if(k==0) {
ab[IX(i,j,k+1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k+1)];
}
// Ceiling
if(k==kmax+1) {
af[IX(i,j,k-2)] = 0;
psi[IX(i,j,k-1)] = psi[IX(i,j,k-2)];
}
}
} // End of setting VZ
break;
} // End of switch case
return 0;
}// End of set_bnd_vel( )
///////////////////////////////////////////////////////////////////////////////
/// Set the boundary condition for temperature
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param var_type The type of variable
///\param psi Pointer to the variable needing the boundary conditions
///\param BINDEX Pointer to boundary index
///
///\return 0 if no error occurred
///////////////////////////////////////////////////////////////////////////////
int set_bnd_temp(PARA_DATA *para, REAL **var, int var_type, REAL *psi,
int **BINDEX) {
int i, j, k;
int it;
int index=para->geom->index;
int imax = para->geom->imax, jmax = para->geom->jmax;
int kmax = para->geom->kmax;
int IMAX = imax+2, IJMAX = (imax+2)*(jmax+2);
REAL *aw = var[AW], *ae = var[AE], *as = var[AS], *an = var[AN];
REAL *af = var[AF], *ab = var[AB], *b=var[B],
*qflux = var[QFLUX], *qfluxbc = var[QFLUXBC];
REAL axy, ayz, azx; // Area of surfaces
REAL h;
REAL rhoCp_1 = 1/ (para->prob->rho * para->prob->Cp);
REAL D;
REAL *flagp = var[FLAGP];
/****************************************************************************
| Go through all the boundary cells
****************************************************************************/
for(it=0; it<index; it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
axy = area_xy(para, var, i, j, k);
ayz = area_yz(para, var, i, j, k);
azx = area_zx(para, var, i, j, k);
/*-------------------------------------------------------------------------
| Inlet boundary
| 0: Inlet, -1: Fluid, 1: Solid Wall or Block, 2: Outlet
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==INLET) psi[IX(i,j,k)] = var[TEMPBC][IX(i,j,k)];
/*-------------------------------------------------------------------------
| Solid wall or block
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==SOLID) {
/*......................................................................
| Constant temperature
......................................................................*/
if(BINDEX[3][it]==1) {
psi[IX(i,j,k)] = var[TEMPBC][IX(i,j,k)];
// West boundary wall and eastern neighbor cell is fluid
if(i==0) {
if(flagp[IX(i+1,j,k)]==FLUID) {
D = 0.5 * length_x(para,var,i+1,j,k);
h = h_coef(para,var,i+1,j,k,D);
aw[IX(i+1,j,k)] = h * rhoCp_1 * ayz;
qflux[IX(i,j,k)] = h * (psi[IX(i+1,j,k)]-psi[IX(i,j,k)]);
}
} // End of if(i==0)
// East boundary wall and western neigbor cell is fluid
else if(i==imax+1) {
if(flagp[IX(i-1,j,k)]==FLUID) {
D = 0.5 * length_x(para,var,i-1,j,k);
h = h_coef(para,var,i-1,j,k,D);
ae[IX(i-1,j,k)] = h * rhoCp_1 * ayz;
qflux[IX(i,j,k)] = h * (psi[IX(i-1,j,k)]-psi[IX(i,j,k)]);
}
} // End of else if(i==imax+1)
// Between West and East
else {
// Eastern neighbor cell is fluid
if(flagp[IX(i+1,j,k)]==FLUID) {
D = 0.5 * length_x(para,var,i+1,j,k);
h = h_coef(para,var,i+1,j,k,D);
aw[IX(i+1,j,k)] = h * rhoCp_1 * ayz;
qflux[IX(i,j,k)] = h * (psi[IX(i+1,j,k)]-psi[IX(i,j,k)]);
}
// Western neigbor cell is fluid
if(flagp[IX(i-1,j,k)]==FLUID) {
D = 0.5 * length_x(para,var,i-1,j,k);
h = h_coef(para,var,i-1,j,k,D);
ae[IX(i-1,j,k)] = h * rhoCp_1 * ayz;
qflux[IX(i,j,k)] = h * (psi[IX(i-1,j,k)]-psi[IX(i,j,k)]);
}
} // End of 0<i<imax+1
// South wall boundary and northern neighbor is fluid
if(j==0) {
if(flagp[IX(i,j+1,k)]==FLUID) {
D = 0.5 * length_y(para,var,i,j+1,k);
h = h_coef(para,var,i,j+1,k,D);
as[IX(i,j+1,k)] = h * rhoCp_1 * azx;
qflux[IX(i,j,k)] = h * (psi[IX(i,j+1,k)]-psi[IX(i,j,k)]);
}
}
// North wall boundary and southern neighbor is fluid
else if(j==jmax+1) {
if(flagp[IX(i,j-1,k)]==FLUID) {
D = 0.5 * length_y(para,var,i,j-1,k);
h = h_coef(para,var,i,j-1,k,D);
an[IX(i,j-1,k)] = h * rhoCp_1 * azx;
qflux[IX(i,j,k)] = h * (psi[IX(i,j-1,k)]-psi[IX(i,j,k)]);
}
}
// Between South and North
else {
// Southern neighbor is fluid
if(flagp[IX(i,j-1,k)]==FLUID) {
D = 0.5 * length_y(para,var,i,j-1,k);
h = h_coef(para,var,i,j-1,k,D);
an[IX(i,j-1,k)] = h * rhoCp_1 * azx;
qflux[IX(i,j,k)] = h * (psi[IX(i,j-1,k)]-psi[IX(i,j,k)]);
}
// Northern neighbor is fluid
if(flagp[IX(i,j+1,k)]==FLUID) {
D = 0.5 * length_y(para,var,i,j+1,k);
h = h_coef(para,var,i,j+1,k,D);
as[IX(i,j+1,k)] = h * rhoCp_1 * azx;
qflux[IX(i,j,k)] = h * (psi[IX(i,j+1,k)]-psi[IX(i,j,k)]);
}
}
// Floor and ceiling neighbor is fluid
if(k==0) {
if(flagp[IX(i,j,k+1)]==FLUID) {
D = 0.5 * length_z(para,var,i,j,k+1);
h = h_coef(para,var,i,j,k+1,D);
ab[IX(i,j,k+1)] = h * rhoCp_1 * axy;
qflux[IX(i,j,k)] = h * (psi[IX(i,j,k+1)]-psi[IX(i,j,k)]);
}
}
// Ceilling and floor neighbor is fluid
else if(k==kmax+1) {
if(flagp[IX(i,j,k-1)]==FLUID) {
D = 0.5 * length_z(para,var,i,j,k-1);
h = h_coef(para,var,i,j,k-1,D);
af[IX(i,j,k-1)] = h * rhoCp_1 * axy;
qflux[IX(i,j,k)] = h * (psi[IX(i,j,k-1)]-psi[IX(i,j,k)]);
}
}
// Between Floor and Ceiling
else {
// Ceiling neighbor is fluid
if(flagp[IX(i,j,k+1)]==FLUID) {
D = 0.5 * length_z(para,var,i,j,k+1);
h = h_coef(para,var,i,j,k+1,D);
ab[IX(i,j,k+1)] = h * rhoCp_1 * axy;
qflux[IX(i,j,k)] = h * (psi[IX(i,j,k+1)]-psi[IX(i,j,k)]);
}
// Floor neighbor is fluid
if(flagp[IX(i,j,k-1)]==FLUID) {
D = 0.5 * length_z(para,var,i,j,k-1);
h = h_coef(para,var,i,j,k-1,D);
af[IX(i,j,k-1)] = h * rhoCp_1 * axy;
qflux[IX(i,j,k)] = h * (psi[IX(i,j,k-1)]-psi[IX(i,j,k)]);
}
}
} // End of contant temperature wall
/*.......................................................................
| Constant heat flux
.......................................................................*/
if(BINDEX[3][it]==0) {
// West wall boundary and eastern neighbor is fluid
if(i==0) {
if(flagp[IX(i+1,j,k)]==FLUID) {
aw[IX(i+1,j,k)] = 0;
D = 0.5 * length_z(para,var,i+1,j,k);
h = h_coef(para,var,i+1,j,k,D);
b[IX(i+1,j,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * ayz;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i+1,j,k)];
}
} // End of if(i==0)
// East wall bounary and western neighbor is fluid
else if(i==imax+1) {
if(flagp[IX(i-1,j,k)]==FLUID) {
ae[IX(i-1,j,k)] = 0;
D = 0.5 * length_z(para,var,i-1,j,k);
h = h_coef(para,var,i-1,j,k,D);
b[IX(i-1,j,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * ayz;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i-1,j,k)];
}
} // End of else if(i==imax+1)
// Between West and East
else {
// Eastern neighbor is fluid
if(flagp[IX(i+1,j,k)]==FLUID) {
aw[IX(i+1,j,k)] = 0;
D = 0.5 * length_z(para,var,i+1,j,k);
h = h_coef(para,var,i+1,j,k,D);
b[IX(i+1,j,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * ayz;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i+1,j,k)];
}
// Western neighbor is fluid
if(flagp[IX(i-1,j,k)]==FLUID) {
ae[IX(i-1,j,k)] = 0;
D = 0.5 * length_z(para,var,i-1,j,k);
h = h_coef(para,var,i-1,j,k,D);
b[IX(i-1,j,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * ayz;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i-1,j,k)];
}
} // End of else
// South wall boundary and northern neighbor is fluid
if(j==0) {
if(flagp[IX(i,j+1,k)]==FLUID) {
as[IX(i,j+1,k)] = 0;
D = 0.5 * length_z(para,var,i,j+1,k);
h = h_coef(para,var,i,j+1,k,D);
b[IX(i,j+1,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * azx;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j+1,k)];
}
}
// North wall boundary and southern neighbor is fluid
else if(j==jmax+1) {
if(flagp[IX(i,j-1,k)]==FLUID) {
an[IX(i,j-1,k)] = 0;
D = 0.5 * length_z(para,var,i,j-1,k);
h = h_coef(para,var,i,j-1,k,D);
b[IX(i,j-1,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * azx;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j-1,k)];
}
}
// Between South and North
else {
// Southern neighbor is fluid
if(flagp[IX(i,j-1,k)]==FLUID) {
an[IX(i,j-1,k)] = 0;
D = 0.5 * length_z(para,var,i,j-1,k);
h = h_coef(para,var,i,j-1,k,D);
b[IX(i,j-1,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * azx;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j-1,k)];
}
// Northern neighbor is fluid
if(flagp[IX(i,j+1,k)]==FLUID) {
as[IX(i,j+1,k)] = 0;
D = 0.5 * length_z(para,var,i,j+1,k);
h = h_coef(para,var,i,j+1,k,D);
b[IX(i,j+1,k)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * azx;
// get the temperature of solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j+1,k)];
}
}
// Floor boundary and ceiling neighbor is fluid
if(k==0) {
if(flagp[IX(i,j,k+1)]==FLUID) {
ab[IX(i,j,k+1)] = 0;
D = 0.5 * length_z(para,var,i,j,k+1);
h = h_coef(para,var,i,j,k+1,D);
b[IX(i,j,k+1)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * axy;
// Get the temperature on the solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j,k+1)];
}
}
// Ceiling boundary and floor neighbor is fluid
else if(k==kmax+1) {
if(flagp[IX(i,j,k-1)]==FLUID) {
af[IX(i,j,k-1)] = 0;
D = 0.5 * length_z(para,var,i,j,k-1);
h = h_coef(para,var,i,j,k-1,D);
b[IX(i,j,k-1)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * axy;
// Get the temperature on the solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j,k-1)];
}
}
// Between Floor and Ceiling
else {
// Ceiling neighbor is fluid
if(flagp[IX(i,j,k+1)]==FLUID) {
ab[IX(i,j,k+1)] = 0;
D = 0.5 * length_z(para,var,i,j,k+1);
h = h_coef(para,var,i,j,k+1,D);
b[IX(i,j,k+1)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * axy;
// Get the temperature on the solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j,k+1)];
}
// Floor neighbor is fluid
if(flagp[IX(i,j,k-1)]==FLUID) {
af[IX(i,j,k-1)] = 0;
D = 0.5 * length_z(para,var,i,j,k-1);
h = h_coef(para,var,i,j,k-1,D);
b[IX(i,j,k-1)] += rhoCp_1 * qfluxbc[IX(i,j,k)] * axy;
// Get the temperature on the solid surface
psi[IX(i,j,k)] = qfluxbc[IX(i,j,k)]/h + psi[IX(i,j,k-1)];
}
}
} // End of constant heat flux
} // End of wall boundary
/*-------------------------------------------------------------------------
| Outlet boundary
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==OUTLET) {
// West
if(i==0) {
aw[IX(i+1,j,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i+1,j,k)];
}
// North
if(i==imax+1) {
ae[IX(i-1,j,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i-1,j,k)];
}
// South
if(j==0) {
as[IX(i,j+1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j+1,k)];
}
// North
if(j==jmax+1) {
an[IX(i,j-1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j-1,k)];
}
// Floor
if(k==0) {
ab[IX(i,j,k+1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k+1)];
}
// Ceiling
if(k==kmax+1) {
af[IX(i,j,k-1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k-1)];
}
} // End of boundary for outlet
} // End of for() loop for go through the index
return 0;
} // End of set_bnd_temp()
///////////////////////////////////////////////////////////////////////////////
/// Set the boundary condition for trace substance
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param trace_index Index of the trace substance
///\param psi Pointer to the variable needing the boundary conditions
///\param BINDEX Pointer to boundary index
///
///\return 0 if no error occurred
///////////////////////////////////////////////////////////////////////////////
int set_bnd_trace(PARA_DATA *para, REAL **var, int trace_index, REAL *psi,
int **BINDEX) {
int i, j, k, it, id;
int index=para->geom->index;
int imax = para->geom->imax, jmax = para->geom->jmax;
int kmax = para->geom->kmax;
int IMAX = imax+2, IJMAX = (imax+2)*(jmax+2);
REAL *aw = var[AW], *ae = var[AE], *as = var[AS], *an = var[AN];
REAL *af = var[AF], *ab = var[AB], *b=var[B];
REAL *flagp = var[FLAGP];
/****************************************************************************
| Go through all the boundary cells
****************************************************************************/
for(it=0; it<index; it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
/*-------------------------------------------------------------------------
| Inlet boundary
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==INLET) {
id = BINDEX[4][it];
psi[IX(i,j,k)] = para->bc->XiPort[id][trace_index];
}
/*-------------------------------------------------------------------------
| Solid wall or block
-------------------------------------------------------------------------*/
else if(flagp[IX(i,j,k)]==SOLID) {
/*.......................................................................
| Neumann B.C.
.......................................................................*/
// Eastern neighbor is fluid
if(i!=imax+1 && flagp[IX(i+1,j,k)]==FLUID) {
aw[IX(i+1,j,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i+1,j,k)];
}
// Western neighbor is fluid
if(i=!0 && flagp[IX(i-1,j,k)]==FLUID) {
ae[IX(i-1,j,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i-1,j,k)];
}
// Northern neighbor is fluid
if(j!=jmax+1 && flagp[IX(i,j+1,k)]==FLUID) {
as[IX(i,j+1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j+1,k)];
}
// Southern neighbor is fluid
if(j!=0 && flagp[IX(i,j-1,k)]==FLUID) {
an[IX(i,j-1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j-1,k)];
}
// Ceiling neighbor is fluid
if(k!=kmax+1 && flagp[IX(i,j,k+1)]==FLUID) {
ab[IX(i,j,k+1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k+1)];
}
// Floor neighbor is fluid
if(k==kmax+1 && flagp[IX(i,j,k-1)]==FLUID) {
af[IX(i,j,k-1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k-1)];
}
} // End of wall boundary
/*-------------------------------------------------------------------------
| Outlet boundary
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==OUTLET) {
// West
if(i==0) {
aw[IX(i+1,j,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i+1,j,k)];
}
// North
if(i==imax+1) {
ae[IX(i-1,j,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i-1,j,k)];
}
// South
if(j==0) {
as[IX(i,j+1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j+1,k)];
}
// North
if(j==jmax+1) {
an[IX(i,j-1,k)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j-1,k)];
}
// Floor
if(k==0) {
ab[IX(i,j,k+1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k+1)];
}
// Ceiling
if(k==kmax+1) {
af[IX(i,j,k-1)] = 0;
psi[IX(i,j,k)] = psi[IX(i,j,k-1)];
}
} // End of boundary for outlet
} // End of for() loop for go through the index
return 0;
} // End of set_bnd_trace()
///////////////////////////////////////////////////////////////////////////////
/// Set the boundary condition for pressure
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param p Pointer to pressure variable
///\param BINDEX Pointer to boundary index
///
///\return 0 if no error occurred
///////////////////////////////////////////////////////////////////////////////
int set_bnd_pressure(PARA_DATA *para, REAL **var, REAL *p, int **BINDEX) {
int i, j, k, it;
int imax = para->geom->imax, jmax = para->geom->jmax;
int kmax = para->geom->kmax;
int index=para->geom->index;
int IMAX = imax+2, IJMAX = (imax+2)*(jmax+2);
REAL *aw = var[AW], *ae = var[AE], *as = var[AS], *an = var[AN];
REAL *af = var[AF], *ab = var[AB];
REAL *flagp = var[FLAGP];
for(it=0;it<index;it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
/*-------------------------------------------------------------------------
| For X direction
-------------------------------------------------------------------------*/
if(i>0) {
if(flagp[IX(i-1,j,k)]<0) {
p[IX(i,j,k)] = p[IX(i-1,j,k)];
ae[IX(i-1,j,k)] = 0;
}
}
if(i<imax+1) {
if(flagp[IX(i+1,j,k )]<0) {
p[IX(i,j,k)] = p[IX(i+1,j,k)];
aw[IX(i+1,j,k)] = 0;
}
}
/*-------------------------------------------------------------------------
| For Y direction
-------------------------------------------------------------------------*/
if(j>0) {
if(flagp[IX(i,j-1,k)]<0) {
p[IX(i,j,k)] = p[IX(i,j-1,k )];
an[IX(i,j-1,k)] = 0;
}
}
if(j<jmax+1) {
if(flagp[IX(i,j+1,k)]<0) {
p[IX(i,j,k )] = p[IX(i,j+1,k )];
as[IX(i,j+1,k)] = 0;
}
}
/*-------------------------------------------------------------------------
| For Z direction
-------------------------------------------------------------------------*/
if(k>0) {
if(flagp[IX(i,j,k-1)]<0) {
p[IX(i,j,k)] = p[IX(i,j,k-1)];
af[IX(i,j,k-1)] = 0;
}
}
if(k<kmax+1) {
if(flagp[IX(i,j,k+1 )]<0) {
p[IX(i,j,k)] = p[IX(i,j,k+1)];
ab[IX(i,j,k+1)] = 0;
}
}
}
return 0;
} // End of set_bnd_pressure()
///////////////////////////////////////////////////////////////////////////////
/// Enforce the mass conservation by adjusting the outlet flow rate
///
/// The detailes was published in the paper
/// "W. Zuo, J. Hu, Q. Chen 2010.
/// Improvements on FFD modeling by using different numerical schemes,
/// Numerical Heat Transfer, Part B Fundamentals, 58(1), 1-16."
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param BINDEX Pointer to boundary index
///
///\return 0 if no error occurred
///////////////////////////////////////////////////////////////////////////////
int mass_conservation(PARA_DATA *para, REAL **var, int **BINDEX) {
int i, j, k;
int it;
int imax = para->geom->imax, jmax = para->geom->jmax;
int kmax = para->geom->kmax;
int index= para->geom->index;
int IMAX = imax+2, IJMAX = (imax+2)*(jmax+2);
REAL *u = var[VX], *v = var[VY], *w = var[VZ];
REAL dvel;
REAL *flagp = var[FLAGP];
dvel = adjust_velocity(para, var, BINDEX); //(mass_in-mass_out)/area_out
/*---------------------------------------------------------------------------
| Adjust the outflow
---------------------------------------------------------------------------*/
for(it=0;it<index;it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
// Fixme: Adding or substracting velocity may cause change in flow direction
if(flagp[IX(i,j,k)]==2) {
if(i==0) u[IX(i,j,k)] -= dvel;
if(i==imax+1) u[IX(i-1,j,k)]+= dvel;
if(j==0) v[IX(i,j,k)] -= dvel;
if(j==jmax+1) v[IX(i,j-1,k)] += dvel;
if(k==0) w[IX(i,j,k)] -= dvel;
if(k==kmax+1) w[IX(i,j,k-1)] += dvel;
}
}
return 0;
} // End of mass_conservation()
///////////////////////////////////////////////////////////////////////////////
/// Get the mass flow difference divided by outflow area
///
/// The detailes was published in the paper
/// "W. Zuo, J. Hu, Q. Chen 2010.
/// Improvements on FFD modeling by using different numerical schemes,
/// Numerical Heat Transfer, Part B Fundamentals, 58(1), 1-16."
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param BINDEX Pointer to boundary index
///
///\return Mass flow difference divided by the outflow area
///////////////////////////////////////////////////////////////////////////////
REAL adjust_velocity(PARA_DATA *para, REAL **var, int **BINDEX) {
int i, j, k;
int it;
int imax = para->geom->imax, jmax = para->geom->jmax;
int kmax = para->geom->kmax;
int index= para->geom->index;
int IMAX = imax+2, IJMAX = (imax+2)*(jmax+2);
REAL *u = var[VX], *v = var[VY], *w = var[VZ];
REAL mass_in = (REAL) 0.0, mass_out = (REAL) 0.00000001;
REAL area_out=0;
REAL *flagp = var[FLAGP];
REAL axy, ayz, azx;
// Go through all the inelt and outlets
for(it=0; it<index; it++) {
i = BINDEX[0][it];
j = BINDEX[1][it];
k = BINDEX[2][it];
axy = area_xy(para, var, i, j, k);
ayz = area_yz(para, var, i, j, k);
azx = area_zx(para, var, i, j, k);
/*-------------------------------------------------------------------------
| Compute the total inflow
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==0) {
// West
if(i==0) mass_in += u[IX(i,j,k)] * ayz;
// East
if(i==imax+1) mass_in += (-u[IX(i,j,k)]) * ayz;
// South
if(j==0) mass_in += v[IX(i,j,k)] * azx;
// North
if(j==jmax+1) mass_in += (-v[IX(i,j,k)]) * azx;
// Floor
if(k==0) mass_in += w[IX(i,j,k)] * axy;
// Ceiling
if(k==kmax+1) mass_in += (-w[IX(i,j,k)]) * axy;
}
/*-------------------------------------------------------------------------
| Compute the total outflow
-------------------------------------------------------------------------*/
if(flagp[IX(i,j,k)]==2) {
// West
if(i==0) {
mass_out += (-u[IX(i,j,k)]) * ayz;
area_out += ayz;
}
// East
if(i==imax+1) {
mass_out += u[IX(i-1,j,k)] * ayz;
area_out += ayz;
}
// South
if(j==0) {
mass_out += (-v[IX(i,j,k)]) * azx;
area_out += azx;
}
// North
if(j==jmax+1) {
mass_out += v[IX(i,j-1,k)] * azx;
area_out += azx;
}
// Floor
if(k==0) {
mass_out += (-w[IX(i,j,k)]) * axy;
area_out += axy;
}
// Ceiling
if(k==kmax+1) {
mass_out += w[IX(i,j,k-1)] * axy;
area_out += axy;
}
} // End of computing outflow
} // End of for loop for going through all the inlets and outlets
/*---------------------------------------------------------------------------
| Return the adjusted velocuty for mass conservation
---------------------------------------------------------------------------*/
return (mass_in-mass_out)/area_out;
} // End of adjust_velocity()
///////////////////////////////////////////////////////////////////////////////
/// Calculate convective hrat transfer coefficient divided by
///
///\param para Pointer to FFD parameters
///\param var Pointer to FFD simulation variables
///\param i I-index of the cell
///\param j J-index of the cell
///\param k K-index of the cell
///\param D distance from the cell center to the wall
///
///\return Mass flow difference divided by the outflow area
///////////////////////////////////////////////////////////////////////////////
REAL h_coef(PARA_DATA *para, REAL **var, int i, int j, int k, REAL D) {
REAL h, kapa;
REAL nu = para->prob->nu;
switch(para->prob->tur_model) {
case LAM:
kapa = nu;
break;
case CONSTANT:
kapa = (REAL)101.0 * nu;
break;
case CHEN:
kapa = nu + nu_t_chen_zero_equ(para, var, i, j, k);
break;
default:
sprintf(msg, "h_coef(): Value (%d) for para->prob->tur_model"
"was not correct.", para->prob->tur_model);
ffd_log(msg, FFD_ERROR);
}
h = para->prob->Cp * para->prob->rho * para->prob->alpha * kapa
/ (nu * D);
return h;
} // End of h_coef()