Revision bdc080d3acb04ab5f1977c15aa2bda23299e7ea8 authored by Leif Strand on 23 July 2005, 09:02:47 UTC, committed by Leif Strand on 23 July 2005, 09:02:47 UTC
1 parent 5040de8
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Process_buoyancy.c
/*
 *~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
 * 
 *<LicenseText>
 *=====================================================================
 *
 *                              CitcomS
 *                 ---------------------------------
 *
 *                              Authors:
 *           Louis Moresi, Shijie Zhong, Lijie Han, Eh Tan,
 *           Clint Conrad, Michael Gurnis, and Eun-seo Choi
 *          (c) California Institute of Technology 1994-2005
 *
 *        By downloading and/or installing this software you have
 *       agreed to the CitcomS.py-LICENSE bundled with this software.
 *             Free for non-commercial academic research ONLY.
 *      This program is distributed WITHOUT ANY WARRANTY whatsoever.
 *
 *=====================================================================
 *
 *  Copyright June 2005, by the California Institute of Technology.
 *  ALL RIGHTS RESERVED. United States Government Sponsorship Acknowledged.
 * 
 *  Any commercial use must be negotiated with the Office of Technology
 *  Transfer at the California Institute of Technology. This software
 *  may be subject to U.S. export control laws and regulations. By
 *  accepting this software, the user agrees to comply with all
 *  applicable U.S. export laws and regulations, including the
 *  International Traffic and Arms Regulations, 22 C.F.R. 120-130 and
 *  the Export Administration Regulations, 15 C.F.R. 730-744. User has
 *  the responsibility to obtain export licenses, or other export
 *  authority as may be required before exporting such information to
 *  foreign countries or providing access to foreign nationals.  In no
 *  event shall the California Institute of Technology be liable to any
 *  party for direct, indirect, special, incidental or consequential
 *  damages, including lost profits, arising out of the use of this
 *  software and its documentation, even if the California Institute of
 *  Technology has been advised of the possibility of such damage.
 * 
 *  The California Institute of Technology specifically disclaims any
 *  warranties, including the implied warranties or merchantability and
 *  fitness for a particular purpose. The software and documentation
 *  provided hereunder is on an "as is" basis, and the California
 *  Institute of Technology has no obligations to provide maintenance,
 *  support, updates, enhancements or modifications.
 *
 *=====================================================================
 *</LicenseText>
 * 
 *~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
 */
/*  Here are the routines which process the results of each buoyancy solution, and call
    any relevant output routines. Much of the information has probably been output along
    with the velocity field. (So the velocity vectors and other data are fully in sync).
    However, heat fluxes and temperature averages are calculated here (even when they
    get output the next time around the velocity solver);
    */


#include "element_definitions.h"
#include "global_defs.h"



void post_processing(struct All_variables *E)
{
  return;
}



/* ===================
    Surface heat flux
   =================== */

void heat_flux(E)
    struct All_variables *E;
{
    int m,e,el,i,j,node,lnode;
    float *flux[NCS],*SU[NCS],*RU[NCS];
    float VV[4][9],u[9],T[9],dTdz[9],area,uT;
    float *sum_h;
    double rtf[4][9];

    struct Shape_function GN;
    struct Shape_function_dA dOmega;
    struct Shape_function_dx GNx;
    void get_global_shape_fn();
    void exchange_node_f();
    void velo_from_element();
    void sum_across_surface();
    void return_horiz_ave();
    void return_horiz_ave_f();

    const int dims=E->mesh.nsd,dofs=E->mesh.dof;
    const int vpts=vpoints[dims];
    const int ppts=ppoints[dims];
    const int ends=enodes[dims];
    const int nno=E->lmesh.nno;
    const int lev = E->mesh.levmax;
    const int sphere_key=1;


  sum_h = (float *) malloc((5)*sizeof(float));
  for(i=0;i<=4;i++)
    sum_h[i] = 0.0;

  for(m=1;m<=E->sphere.caps_per_proc;m++) {

    flux[m] = (float *) malloc((1+nno)*sizeof(float));

    for(i=1;i<=nno;i++)   {
      flux[m][i] = 0.0;
      }

    for(e=1;e<=E->lmesh.nel;e++) {
      get_global_shape_fn(E,e,&GN,&GNx,&dOmega,0,sphere_key,rtf,lev,m);

      velo_from_element(E,VV,m,e,sphere_key);

      for(i=1;i<=vpts;i++)   {
        u[i] = 0.0;
        T[i] = 0.0;
        dTdz[i] = 0.0;
        for(j=1;j<=ends;j++)  {
          u[i] += VV[3][j]*E->N.vpt[GNVINDEX(j,i)];
          T[i] += E->T[m][E->ien[m][e].node[j]]*E->N.vpt[GNVINDEX(j,i)];
          dTdz[i] += -E->T[m][E->ien[m][e].node[j]]*GNx.vpt[GNVXINDEX(2,j,i)];
          }
        }

      uT = 0.0;
      area = 0.0;
      for(i=1;i<=vpts;i++)   {
        uT += u[i]*T[i]*dOmega.vpt[i] + dTdz[i]*dOmega.vpt[i];
        }

      uT /= E->eco[m][e].area;

      for(j=1;j<=ends;j++)
        flux[m][E->ien[m][e].node[j]] += uT*E->TWW[lev][m][e].node[j];

      }             /* end of e */
    }             /* end of m */


  exchange_node_f(E,flux,lev);

  for(m=1;m<=E->sphere.caps_per_proc;m++)
     for(i=1;i<=nno;i++)
       flux[m][i] *= E->MASS[lev][m][i];

  if (E->parallel.me_loc[3]==E->parallel.nprocz-1)
    for(m=1;m<=E->sphere.caps_per_proc;m++)
      for(i=1;i<=E->lmesh.nsf;i++)
        E->slice.shflux[m][i]=2*flux[m][E->surf_node[m][i]]-flux[m][E->surf_node[m][i]-1];

  if (E->parallel.me_loc[3]==0)
    for(m=1;m<=E->sphere.caps_per_proc;m++)
      for(i=1;i<=E->lmesh.nsf;i++)
        E->slice.bhflux[m][i] = 2*flux[m][E->surf_node[m][i]-E->lmesh.noz+1]
                                - flux[m][E->surf_node[m][i]-E->lmesh.noz+2];

  for(m=1;m<=E->sphere.caps_per_proc;m++)
    for(e=1;e<=E->lmesh.snel;e++) {
         uT =(E->slice.shflux[m][E->sien[m][e].node[1]] +
              E->slice.shflux[m][E->sien[m][e].node[2]] +
              E->slice.shflux[m][E->sien[m][e].node[3]] +
              E->slice.shflux[m][E->sien[m][e].node[4]])*0.25;
         el = e*E->lmesh.elz;
         sum_h[0] += uT*E->eco[m][el].area;
         sum_h[1] += E->eco[m][el].area;

         uT =(E->slice.bhflux[m][E->sien[m][e].node[1]] +
              E->slice.bhflux[m][E->sien[m][e].node[2]] +
              E->slice.bhflux[m][E->sien[m][e].node[3]] +
              E->slice.bhflux[m][E->sien[m][e].node[4]])*0.25;
         el = (e-1)*E->lmesh.elz+1;
         sum_h[2] += uT*E->eco[m][el].area;
         sum_h[3] += E->eco[m][el].area;
         }

  sum_across_surface(E,sum_h,4);

  if (E->parallel.me_loc[3]==E->parallel.nprocz-1)   {
    sum_h[0] = sum_h[0]/sum_h[1];
/*     if (E->control.verbose && E->parallel.me==E->parallel.nprocz-1) fprintf(E->fp_out,"surface heat flux= %f %f\n",sum_h[0],E->monitor.elapsed_time); */
    if (E->parallel.me==E->parallel.nprocz-1) {
      fprintf(stderr,"surface heat flux= %f\n",sum_h[0]);
      //fprintf(E->fp,"surface heat flux= %f\n",sum_h[0]);
    }
  }

  if (E->parallel.me_loc[3]==0)    {
    sum_h[2] = sum_h[2]/sum_h[3];
/*     if (E->control.verbose && E->parallel.me==0) fprintf(E->fp_out,"bottom heat flux= %f %f\n",sum_h[2],E->monitor.elapsed_time); */
    if (E->parallel.me==0) {
      fprintf(stderr,"bottom heat flux= %f\n",sum_h[2]);
      fprintf(E->fp,"bottom heat flux= %f\n",sum_h[2]);
    }
  }


  for(m=1;m<=E->sphere.caps_per_proc;m++)
    free((void *)flux[m]);

  free((void *)sum_h);

  return;
  }

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