sandbox/M1EMN/Exemples/siloaxi.c

    Bagnold flow in cylindrical silo

    #include "axi.h"
    #include "navier-stokes/centered.h"
    #define LEVEL 8
    double mumax,dg,P0,R0,Q;
    scalar mu_eq[];

    Bagnold solution for comparison,

    double Uba( double r){
        double dmu=.26,mu0=.38,I0=.3;
        //double rgs2=1;//
        double rgs2=1./2;
        double rs=mu0*P0/rgs2;
        double uu = 30*2*I0*((1 - r)*rgs2 + dmu*P0*log(rgs2*(rs-1) + dmu*P0 ) - 
           dmu*P0*log(dmu*P0 + rgs2*(rs-r) ));
    
        double uup = 30*2*I0*((1 - rs)*rgs2 + dmu*P0*log(rgs2*(rs-1) + dmu*P0 ) - 
           dmu*P0*log(dmu*P0 + rgs2*(rs-rs) ));
         return (r < rs? uup:uu ); }

    Main with parameters

     int main() {
      L0 = 1.;

    ‘Jansen’ pressure, but in fact any pressure gives almost the same ‘Q’

      P0 = 1./2/.38;
      DT = 0.01/2;
      R0 = 0.1 ; 
    
      // P0 =2;2D

    the regularisation value of viscosity

      mumax=1000;

    Boundary conditions are periodic

    no slip at the top, confinment pressure P_0

        u.t[top] = dirichlet(0);
        u.n[top] = dirichlet(0);
        p[left] =  dirichlet( (t < 1 )? P0 : P0);
        p[right] = (y <= R0 ? dirichlet(0) : neumann(0) );
        u.n[right] =  (y<= R0 ? neumann(0) :dirichlet(0));
        u.t[right] =  (y <= R0 ? neumann(0) :dirichlet(0));
        u.n[left] =  neumann(0);
        u.t[left] = neumann(0);

    symmetry at the bottom

        u.n[bottom] = dirichlet(0);
        u.t[bottom] = neumann(0); 
     
      run(); 
    }
    
    
    face vector muv[];
    
    event init (t = 0) {

    prepare viscosity

      mu = muv;

    equivalent gravity acceleration

        const face vector grav[] = {1,0};

    note that in “accceleration” in “navier-stokes/centered.h” there is the fmmetric term in front.

    event acceleration (i++,last)

    uf.x[] = fm.x[]*(face_value (u.x, 0) + dt*a.x[]);

    will be the same for alphav.x[] = fm.x[]/rho(ff); next…

      a = grav;

    Initialy at rest

      foreach() {
        u.x[] = 0;
        u.y[] = 0;
        p[]=P0;
      }
    }

    We check the number of iterations of the Poisson and viscous problems.

    //event logfile (i++)
    // fprintf (stderr, "%d %g %d %d\n", i, t, mgp.i, mgu.i);

    old value of the velocity is saved

    scalar un[];
    event init_un (i = 0) {
        foreach()
        un[] = u.x[];
    }

    so that when it does not more change we are converged

    event conv (t += 1; t < 150) {
        double du = change (u.x, un);
        fprintf(stdout,"t= %g %g %g %g \n",t,interpolate (u.x, L0/2, 0),interpolate (p, L0/2, 0),du);
        if (i > 0 && du < 1.0e-6)
            return 1; /* stop */
    }

    Implementation of the \mu(I) viscosity

    event nonnewviscosity(i++) {
        scalar eta_eq[];

    computation of the second invariant as defined by Darby -II_2 = 2 D:D and D_2=\sqrt{D:D} \displaystyle 2 D:D = (2 [(\frac{\partial v}{\partial y})^2 + (\frac{ v}{ y})^2) +(\frac{\partial u}{\partial x})^2] + [\frac{\partial v}{\partial x} + \frac{\partial u}{\partial y}]^2) Note that y is r

    so viscosity is \displaystyle \eta_{eq} = \mu(I)P/(\sqrt(2.)D2) with regularisation

        scalar shear[];
        foreach()
        shear[] = fabs((u.x[0,1] - u.x[0,-1])/(2.*Delta));
        boundary ({shear});
    
     foreach() { 
          double mI2 = 0.,D2 = 0,In = 0, muI = 0;
          dg = 1./30;
          double duxx = (u.x[1,0] - u.x[-1,0])/(2 * Delta);
          double duxy = (u.x[0,1] - u.x[0,-1])/(2 * Delta);
          double duyx = (u.y[1,0] - u.y[-1,0])/(2 * Delta);
          double duyy = (u.y[0,1] - u.y[0,-1])/(2 * Delta); 
    	    mI2 =  sq(duyx+duxy) + 2*(sq(duyy) + sq(duxx) + sq(u.y[]/ max(y, 1e-20)));
          D2 = sqrt(mI2/2.);
          In = sqrt(2.)*dg*D2/sqrt(fabs(p[])+1e-10);
          //In =  dg*shear[]/sqrt(fabs(P0));
          muI = .38 + (.26)*In/(.3 + In);
          if(D2>0){
            eta_eq[] = min(muI*fabs(p[])/(sqrt(2.)*D2) , mumax );}
           else {
            eta_eq[]=mumax;	
           }
        }   
          boundary ({eta_eq});
    
     
        boundary ({mu_eq});
        foreach_face() {
            muv.x[] = fm.x[]*(eta_eq[] + eta_eq[-1,0])/2.;
        }
        boundary ((scalar *){muv});
    }

    Save profiles computed, shear and exact

    event profiles (t += 1)
    {
        FILE * fp = fopen("xprof", "w");
        scalar shear[];
        foreach()
        shear[] = (u.x[0,1] - u.x[0,-1])/(2.*Delta);
        boundary ({shear});
        for (double y = 0.; y < 1.0; y += 1./pow(2.,LEVEL))
            fprintf (fp, "%g %g %g %g %g  %g \n", y, interpolate (u.x, L0/2, y), interpolate (u.y, L0/2, y),
            	   interpolate (shear, L0/2, y),interpolate (p, L0/2, y),
                      Uba(y));
        fclose (fp);
    
    
    
    }
    
     event interface (  t += .25  ) {
      char s[80];
      //sprintf (s, "field-%g.txt", t);
      sprintf (s, "field.txt");
      FILE * fp = fopen (s, "w");
      output_field ({p,u,uf,pf}, fp, linear = true);
      fclose (fp);
    }

    We adapt according to the error on the velocity field.

    event adapt (i++) {
          Q=0;
        double dy=1./pow(2.,LEVEL);
        for (double y = 0.; y < 1.0; y += dy)
            Q+=interpolate (u.x, L0-dy, y);
        Q=Q*dy;
    	 fprintf (stderr," %6.4g  %g \n",t,Q);
    	  // adapt_wavelet ({u}, (double[]){3e-3,3e-3}, 8, 6);
    }
    
    event profile (t = end) {
      foreach()
        printf ("%g %g %g %g %g\n", x, y, u.x[], u.y[], p[]);
    }

    Compilation

    ln -s siloaxi.c.page siloaxi.c              
    make siloaxi.tst;
    make siloaxi/plots;
    make siloaxi.c.html;

    Results and plots

    Plot of the exact and computed velocities.

    set ylabel "u(y)";set xlabel "y" 
    p'field.txt' u ($4+$1*3):2 w l
    profiles (script)

    profiles (script)

    reset
    set pm3d; set palette rgbformulae 22,13,-31;unset surface;
    set ticslevel 0;
    unset border;
    unset xtics;
    unset ytics;
    unset ztics;
    unset colorbox; 
    set view 0,0
    sp'field.txt' u 1:2:3 not
    (script)

    (script)

    Bibliography

    • mu(I) and silo and Co