Natural convection for nanofluids in a square cavity. Nusselt number graph is not according to Attached Figure. Your help will be highly appreciated.

조회 수: 13 (최근 30일)
function ADI_Nat_nan
mx=15; my=15;
nx=mx+1; ny=my+1;
lx=1; ly=1;
x=linspace(0,lx,nx); y=linspace(0,ly,ny);
%Nanofluid part
cpf=4179; cps=385; kf=0.613; ks=401; rhof=997.1; rhos=8933; bf=21e-5; bs=1.67e-5; muf=9.09e-4;
phi=0.2;
rhonf=(1-phi)*rhof+phi*rhos;
rcpnf=(1-phi)*rhof*cpf+phi*rhos*cps;
rbnf=(1-phi)*rhof*bf+phi*rhos*bs;
munf=muf/((1-phi)^2.5);
A=ks+2*kf; B=phi*(kf-ks); knf=kf*((A-2*B)/(A+B));
af=kf/(rhof*cpf); anf=knf/rcpnf; nuf=muf/rhof; Pr=nuf/af;
Ray_C=[1e+1 1e+2 1e+3 1e+4 1e+5]
for tt=1:length(Ray_C)
Ra=Ray_C(tt)
dx=lx/mx; dy=ly/my; dxx=dx*dx; dyy=dy*dy; dxxV=munf/(rhonf*af*dxx); dyyV=munf/(rhonf*af*dyy);
dxxT=anf/(af*dxx); dyyT=anf/(af*dyy); beta2=dxx/dyy;
S(1:nx,1:ny)=1; W=zeros(nx,ny); T=zeros(nx,ny); T(:,1)=1; S(1,1:ny)=0; S(nx,1:ny)=0; S(1:nx,1)=0; S(1:nx,ny)=0;
errtol=1e-6; errpsi=2*errtol; errome=2*errtol; errtem=2*errtol; iter=0; itermax=40000;
Siter=S; Snew_iter=S; Witer=W; Wnew_iter=W; Titer=T; Tnew_iter=T;
while((errpsi>errtol||errome>errtol||errtem>errtol)&&iter<itermax)
%Solving for the streamline
%Horizontal sweep
a(1:nx)=1;
b(1:nx)=-2*(1+beta2);
c(1:nx)=1;
d(1:nx)=0;
for j=2:ny-1
for i=2:nx-1
d(i)=-(beta2*(Siter(i,j-1)+Siter(i,j+1))+dxx*Witer(i,j));
end
a(1)=0; b(1)=1; c(1)=0; %Dirichlet B.C
a(nx)=0; b(nx)=1; c(nx)=0; %Dirichlet B.C
d(1)=S(1,j);
d(nx)=S(nx,j);
Snew_iter(1:nx,j)=solver_tdma(nx,a,b,c,d);
end
Siter=Snew_iter;
%Vertical sweep
for i=2:nx-1
a(1:ny)=beta2;
b(1:ny)=-2*(1+beta2);
c(1:ny)=beta2;
d(1:ny)=0;
for j=2:ny-1
d(j)=-(Siter(i-1,j)+Siter(i+1,j)+dxx*Witer(i,j));
end
a(1)=0; b(1)=1; c(1)=0; %Dirichlet B.C
a(ny)=0; b(ny)=1; c(ny)=0; %Dirichlet B.C
d(1)=S(i,1);
d(ny)=S(i,ny);
Snew_iter(i,1:ny)=solver_tdma(ny,a,b,c,d);
end
errpsi=sum(sum(abs(Snew_iter-Siter)))/sum(sum(abs(Snew_iter)));
Siter=Snew_iter;
%Velocity components calculation for internal nodes
u=zeros(nx,ny); v=zeros(nx,ny);
u(2:nx-1,2:ny-1)=(Snew_iter(2:nx-1,3:ny)-Snew_iter(2:nx-1,1:ny-2))/(2*dy);
v(2:nx-1,2:ny-1)=-(Snew_iter(3:nx,2:ny-1)-Snew_iter(1:nx-2,2:ny-1))/(2*dx);
%Solving for the vorticity
%Declaring B.Cs for vorticity
W(1:nx,1)=2*(Snew_iter(1:nx,1)-Snew_iter(1:nx,2))/dyy; %Bottom
W(1:nx,ny)=2*(Snew_iter(1:nx,ny)-Snew_iter(1:nx,ny-1))/dyy; %Top
W(1,1:ny)=2*(Snew_iter(1,1:ny)-Snew_iter(2,1:ny))/dxx; %Left
W(nx,1:ny)=2*(Snew_iter(nx,1:ny)-Snew_iter(nx-1,1:ny))/dxx; %Right
%Horizontal sweep
a(1:nx)=0;
b(1:nx)=0;
c(1:nx)=0;
d(1:nx)=0;
for j=2:ny-1
for i=2:nx-1
%Upwind
if(u(i,j)>0), sigu=1;
else if(u(i,j)<0), sigu=-1;
else sigu=0;
end;
end;
if(v(i,j)>0), sigv=1;
else if(v(i,j)<0), sigv=-1;
else sigv=0;
end;
end;
%Coeffiticents for vorticity equation
ap=2*dxxV+2*dyyV+sigu*u(i,j)/dx+sigv*v(i,j)/dy;
ae=0.5*(1-sigu)*u(i+1,j)/dx-dxxV;
aw=-0.5*(1+sigu)*u(i-1,j)/dx-dxxV;
an=0.5*(1-sigv)*v(i,j+1)/dy-dxxV;
as=-0.5*(1+sigv)*v(i,j-1)/dy-dxxV;
a(i)=aw;
b(i)=ap;
c(i)=ae;
d(i)=-(as*Witer(i,j-1)+an*Witer(i,j+1))+0.5*Ra*Pr*rbnf*(Titer(i+1,j)-Titer(i-1,j))/(dx*bf*rhonf);
end
a(1)=0; b(1)=1; c(1)=0; %Dirichlet B.C
a(nx)=0; b(nx)=1; c(nx)=0; %Dirichlet B.C
d(1)=W(1,j);
d(nx)=W(nx,j);
Wnew_iter(1:nx,j)=solver_tdma(nx,a,b,c,d);
end
Witer=Wnew_iter;
%Vertical sweep
for i=2:nx-1
for j=2:ny-1
%Upwind
if(u(i,j)>0), sigu=1;
else if(u(i,j)<0), sigu=-1;
else sigu=0;
end;
end;
if(v(i,j)>0), sigv=1;
else if(v(i,j)<0), sigv=-1;
else sigv=0;
end;
end;
%Coeffiticents for vorticity equation
ap=2*dxxV+2*dyyV+sigu*u(i,j)/dx+sigv*v(i,j)/dy;
ae=0.5*(1-sigu)*u(i+1,j)/dx-dxxV;
aw=-0.5*(1+sigu)*u(i-1,j)/dx-dxxV;
an=0.5*(1-sigv)*v(i,j+1)/dy-dxxV;
as=-0.5*(1+sigv)*v(i,j-1)/dy-dxxV;
a(j)=as;
b(j)=ap;
c(j)=an;
d(j)=0;
d(j)=-(aw*Witer(i-1,j)+ae*Witer(i+1,j))+0.5*Ra*Pr*rbnf*(Titer(i+1,j)-Titer(i-1,j))/(dx*bf*rhonf);
end
a(1)=0; b(1)=1; c(1)=0; %Dirichlet B.C
a(ny)=0; b(ny)=1; c(ny)=0; %Dirichlet B.C
d(1)=W(i,1);
d(ny)=W(i,ny);
Wnew_iter(i,1:ny)=solver_tdma(ny,a,b,c,d);
end
errome=sum(sum(abs(Wnew_iter-Witer)))/sum(sum(abs(Wnew_iter)));
Witer=Wnew_iter;
%Solving energy equation
%Horizontal sweep
for j=2:ny-1
for i=2:nx-1
%Upwind
if(u(i,j)>0), sigu=1;
else if(u(i,j)<0), sigu=-1;
else sigu=0;
end;
end;
if(v(i,j)>0), sigv=1;
else if(v(i,j)<0), sigv=-1;
else sigv=0;
end;
end;
%Coeffiticents for energy equation
ap=2*dxxT+2*dyyT+sigu*u(i,j)/dx+sigv*v(i,j)/dy;
ae=0.5*(1-sigu)*u(i+1,j)/dx-dxxT;
aw=-0.5*(1+sigu)*u(i-1,j)/dx-dxxT;
an=0.5*(1-sigv)*v(i,j+1)/dy-dxxT;
as=-0.5*(1+sigv)*v(i,j-1)/dy-dxxT;
a(i)=aw;
b(i)=ap;
c(i)=ae;
d(i)=0;
d(i)=-(as*Titer(i,j-1)+an*Titer(i,j+1));
end
a(1)=0; b(1)=1; c(1)=0; %Dirichlet B.C
a(nx)=0; b(nx)=1; c(nx)=0; %Dirichlet B.C
d(1)=T(1,j);
d(nx)=T(nx,j);
Tnew_iter(1:nx,j)=solver_tdma(nx,a,b,c,d);
end
Titer=Tnew_iter;
%Vertical sweep
for i=2:nx-1
for j=2:ny-1
%Upwind
if(u(i,j)>0), sigu=1;
else if(u(i,j)<0), sigu=-1;
else sigu=0;
end;
end;
if(v(i,j)>0), sigv=1;
else if(v(i,j)<0), sigv=-1;
else sigv=0;
end;
end;
%Coeffiticents for energy equation
ap=2*dxxT+2*dyyT+sigu*u(i,j)/dx+sigv*v(i,j)/dy;
ae=0.5*(1-sigu)*u(i+1,j)/dx-dxxT;
aw=-0.5*(1+sigu)*u(i-1,j)/dx-dxxT;
an=0.5*(1-sigv)*v(i,j+1)/dy-dxxT;
as=-0.5*(1+sigv)*v(i,j-1)/dy-dxxT;
a(j)=as;
b(j)=ap;
c(j)=an;
d(j)=0;
d(j)=-(aw*Titer(i-1,j)+ae*Titer(i+1,j));
end
a(1)=0; b(1)=1; c(1)=0; %Dirichlet B.C
a(ny)=-1; b(ny)=1; c(ny)=0; %Neumann B.C
d(1)=T(i,1);
d(ny)=0;
Tnew_iter(i,1:ny)=solver_tdma(ny,a,b,c,d);
end
errtem=sum(sum(abs(Tnew_iter-Titer)))/sum(sum(abs(Tnew_iter)));
Titer=Tnew_iter;
iter=iter+1;
end
maxpsi=max(max(abs(Siter)));
disp(maxpsi);
aL=NuVL(dx,Titer); % I am getting error here
aB=NuB(dy,Titer); % I am getting error here
Nu=(knf/kf)*aL;
Nu1=-(knf/kf)*aB;
i=0.1/dx+1; j=0.9/dx+1;
result=[y(i:j)' Nu(i:j)'];
result1=[x(i:j)' Nu1(i:j)'];
dlmwrite('NuL_Ra_100k_f.txt',result,'delimiter','\t','precision',3,'newline','pc');
dlmwrite('NuB_Ra_100k_f.txt',result1,'delimiter','\t','precision',3,'newline','pc');
figure(1); plot(x(i:j),Nu(i:j));
AB=Titer';
figure(tt);
contourf(x,y,AB,9,'k-');
hold on
contourf(x,y,v',9,'b*');
colormap;
% clabel(C,H,'LabelSpacing',500);
title(sprintf('Iteration %d and Rayleigh Number %0.2g, errpsi %0.2g, errome %0.2g, errtem %0.2g',iter, Ra, errpsi, errome, errtem));
end

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