PHOTON USE p phi up z mirror y msg Oil concentration con oil x 1 sh;int 300 msg Pressto continue pause msg Temperature contours con tem1 x 1 fil;0.01 msg Press to continue pause msg Velocity vectors vec x 1 sh msg Press e to END ENDUSE Text(Oil tanker rupture; warm-water layer effect TITLE DISPLAY This case simulates an oil tanker rupture. The purpose of this calculation is to show how a higher temperature in the layer near the sea surface affect the asending plume of the water-oil mixture. The buoyancy force is modelled as a linear function of both oil concentration and the temperature; and is set by In-Form. This calculation focuses on the top layer near the surface and the output from a separate parabolic calculation of the turbulent plume is used as guidance to the input at the lower surface. The profiles of inflow velocity is therefore represented as a sine curve. The results show that the presence of a warm-water layer near the sea surface causes the water-oil liquid to spread laterally, beneath the hot layer, perhaps never reaching the surface. ENDDIS NX=1; NY=40; NZ=40 xulast=0.01;yvlast=2000;zwlast=1000 grdpwr(y,ny,yvlast,1.1) grdpwr(z,nz,zwlast,1.1) CARTES=F GROUP 7. Variables stored, solved & named SOLUTN(P1,Y,Y,Y,P,P,P); OUTPUT(P1,Y,Y,Y,Y,Y,Y) SOLUTN(V1,Y,Y,Y,P,P,P); OUTPUT(V1,Y,Y,Y,Y,Y,Y) SOLUTN(W1,Y,Y,Y,P,P,P); OUTPUT(W1,Y,Y,Y,Y,Y,Y) store(tem1) solutn(tem1,y,y,y,p,p,p);output(tem1,y,y,y,y,y,y) solve(oil) store(enut,len1) turmod(kemodl) rho1=1000. ** density difference between water and oil real(dendif) dendif=0.03 ** solve an equation for residence time solve(rest) terms(rest,n,y,n,p,p,p) patch(elapse,phasem,1,nx,1,ny,1,nz,1,lstep) coval(elapse,rest,fixflu,1.0) enul=1.e-6 patch(ini1,inival,1,nx,1,ny,1,35,1,lstep) (initial of tem1 at ini1 is 4.0) patch(ini2,inival,1,nx,1,ny,35+1,nz,1,lstep) (initial of tem1 at ini2 is 10.0) ** buoyancy force is a linear function of both oil concentration and temperature at the warm-water layer patch(upper,phasem,1,nx,1,ny,35+1,nz,1,lstep) (source of w1 at upper is 9.81*(oil*:dendif:+1000.*1.e-4*(tem1-10.)$ )) patch(lower,phasem,1,nx,1,ny,1,35,1,lstep) (source of w1 at lower is 9.81*:dendif:*oil) ** Sine curve profile at the lower surface patch(leak,low,1,1,1,12,1,1,1,1) ! with density = 1000 and ! maximum velocity 0.03 (source of p1 at leak is 1000*0.03*sin((532-yg)/338.7) with fixflu) (source of w1 at leak is 0.03*sin((532-yg)/338.7) with onlyms) coval(leak,oil,onlyms,1.e-3) coval(leak,ke,onlyms,0.01**2) coval(leak,ep,onlyms,fiinit(ep)) coval(leak,tem1,onlyms,4.0) patch(bottom,cell,1,1,12+1,ny,1,1,1,1) coval(bottom,p1,1.e3,0.0) coval(bottom,oil,0.0,0.0) coval(bottom,tem1,0.0,4.0) patch(north1,cell,1,1,ny,ny,1,35,1,lstep) coval(north1,p1,1.e3,0.0) coval(north1,tem1,onlyms,4.0) patch(north2,cell,1,1,ny,ny,35+1,nz,1,lstep) coval(north2,p1,1.e3,.0) coval(north2,tem1,onlyms,10.) (stored var logo is log10(oil)) relax(p1,linrlx,0.2) relax(oil,linrlx,0.5) relax(v1,falsdt,0.1) relax(w1,falsdt,0.1) relax(tem1,falsdt,10.) fiinit(ke)=0.01**2 fiinit(ep)=0.164*fiinit(ke)**1.5/10.0 relax(ke,linrlx,0.5) relax(ep,linrlx,0.5) lsweep=2000 tstswp=-1 idispa=50;csg1=t izmon=25 nyprin=1;nzprin=1 iyprl=5;izprl=5 LIBREF=401 STOP