function phi = fvm_soln_SS_adv_diff( X_edges, Z_edges, X_P, Z_P, K_P, ... rho, c, u_velo, w_velo, S_C, S_P, phi_u, phi_d, q_e, q_w ) %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %% find steady-state phi(x,z), for combined advection and diffusion %% with given heat sources S and conductivity K_P. %% %% div( rho u phi) = div( K grad(phi) ) + S %% %% Uses Patankar Finite Volume method. %% %% %% THIS CODE INCLUDES ADVECTIVE FLUX WITH CENTERED DIFFERENCE %% (NO UPWINDING SCHEME) %% *** DON'T USE THIS AT HOME FOR SERIOUS WORK!! *** %% %% EXTERNALLY SPECIFIED VELOCITY MUST SATISFY CONTINUITY, %% i.e. IS A CONSTANT %% %% Boundary Conditions: %% vector phi_u is fixed value of phi on upper boundary %% vector phi_d is fixed value of phi on lower boundary %% vector q_w is fixed flux on west boundary %% vector q_e is fixed flux on east boundary %% %% In this treatment, flux boundary conditions are applied on edges %% of finite volumes. This means that I don't have to use half-volumes. %% Function-value boundary conditions are applied on nodes, i.e. with %% half-volumes at Up and Down boundaries. %% %% THIS CODE APPLIES FLUX BOUNDARY CONDITIONS ON VOLUME INTERFACES %% on East and West %% APPLIES FIXED VALUE BOUNDARY CONDITIONS ON VOLUME CENTERS %% in Up and Down %% %% a_P = coefficient of phi_P at point P = (i,j) %% a_E = coefficient of phi_E at point east of (i,j) %% a_E, a_W, a_U, a_D for points East, West, Up, Down %% %% System of equations to be solved for phi %% %% big_A * phi = rhs %% %% big_A = matrix with coefficients a_E etc, modified to include BC %% phi = unknown values in Control-volumes %% rhs = right-hand-side column vector containing sources and BC terms %% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % % % get Finite-Volume dimensions % ------------------------------ [nz_P, nx_P] = size(X_P); % get dX, dZ - spacings between volume edges % ------------------------------------------- dX = diff(X_edges')'; dZ = diff(Z_edges); % % reduce dimensions where boundaries are at interfaces dX = dX(1:end-1,:); % get dX_E, dx_W, dZ_U, dZ_D - % - distances to adjacent volume centers % ----------------------------------------------- % if( size(X_P,2) == 1) dX_e = ones( size(X_P) ); dX_w = ones( size(X_P) ); else dX_e = diff(X_P')'; % add dummy row at eastern edge to maintain size [nx, nz] dX_e = [ dX_e dX_e(:,end) ]; % dX_w = diff(X_P')'; % add dummy row at western edge to maintain size [nx, nz] dX_w = [ dX_w(:,1) dX_w ]; end % dZ_u = diff(Z_P); % add dummy row at top edge to maintain size [nx, nz] dZ_u = [ dZ_u(1,:)' dZ_u' ]'; % dZ_d = diff(Z_P); % add dummy row at bottom edge to maintain size [nx, nz] dZ_d = [ dZ_d' dZ_d(end,:)' ]'; % % get f_e, f_w, f_u, f_d % - fractional distances to volume interfaces % --------------------------------------------------- f_e = 1 - (X_edges(1,2:end) - X_P(1,:))./ dX_e(1,:); f_e = repmat( f_e, nz_P, 1 ); f_w = 1 - (X_P(1,:) - X_edges(1,1:(end-1)) ) ./ dX_w(1,:); f_w = repmat( f_w, nz_P, 1 ); f_u = 1 - (Z_P(:,1) - Z_edges(1:(end-1),1 ))./ dZ_u(:,1); f_u = repmat( f_u, 1, nx_P ); % f_d = 1 - (Z_edges(2:end,1 ) - Z_P(:,1) )./ dZ_d(:,1); f_d = repmat( f_d, 1, nx_P ); % % set up b matrix - includes constant part of source matrix S % S = S_C + S_P * phi_P (units are W m^-3) % ---------------------------------------------------------- b = S_C.* dX.* dZ; % % % set up matrices for conductivities in adjacent volumes % ------------------------------------------------------ K_E = [ K_P(:,2:end) K_P(:, end) ]; K_W = [ K_P(:,1) K_P(:,1:end-1) ]; K_U = [ K_P(1,:)' K_P(1:end-1,:)' ]'; K_D = [ K_P(2:end,:)' K_P(end,:)' ]'; % % % set up interface conductivity matrices % -------------------------------------- K_e = 1./ ( (1 - f_e)./K_P + f_e./K_E ); K_w = 1./ ( (1 - f_w)./K_P + f_w./K_W ); K_u = 1./ ( (1 - f_u)./K_P + f_u./K_U ); K_d = 1./ ( (1 - f_d)./K_P + f_d./K_D ); % % % set up velocities at interfaces %% (this is quick and dirty because velocity is uniform) % ------------------------------------------------------ u_e = u_velo; u_w = u_velo; w_u = w_velo; w_d = w_velo; % % set up coefficients at adjacent points % --------------------------------------- a_E = ( K_e ./ dX_e - rho.* c.* u_e/2 ).* dZ; a_W = ( K_w ./ dX_w + rho.* c.* u_w/2 ).* dZ; a_U = ( K_u ./ dZ_u + rho.* c.* w_u/2 ).* dX; a_D = ( K_d ./ dZ_d - rho.* c.* w_d/2 ).* dX; % set up coefficient at central point P (incl source dependent on phi) % -------------------------------------------------------------------- a_P = a_E + a_W + a_U + a_D - S_P.* dX.* dZ; % % % set Boundary Conditions %%%%%%%%%%%%%%%%%%%%%%%%%%% % % specified flux boundaries % --------------------------- % East boundary - outward flux (q_w = 0) % use q_e = - K_e * (T_E - T_P)/dx (flux toward E) % i.e. T_E = T_P - dx * (q_e/K_e) to eliminate T_E a_P(:,end) = a_P(:,end) - a_E(:,end); b(:,end) = b(:,end) - dX_e.* (q_e./K_e(:,end)) .* a_E(:,end); a_E(:,end) = 0; % West boundary - zero inward flux (q_w = 0) % use q_w = - K_w * (T_P - T_W)/dx (flux from W) % i.e. T_W = T_P + dx * (q_w/K_w) to eliminate T_W a_P(:,1) = a_P(:,1) - a_W(:,1); b(:,1) = b(:,1) + dX_w.* (q_w./K_w(:,1)) .* a_W(:,1); a_W(:,1) = 0; % % % specified phi = phi_u on upper boundary % ------------------------------------------- a_P(1,:) = 1; b(1,:) = phi_u; a_U(1,:) = 0; a_D(1,:) = 0; a_E(1,:) = 0; a_W(1,:) = 0; % % specified phi = phi_d on lower boundary % ------------------------------------------- a_P(end,:) = 1; b(end,:) = phi_d; a_D(end,:) = 0; a_U(end,:) = 0; a_E(end,:) = 0; a_W(end,:) = 0; % %%%%%%%%%%%%%% % % Now call matrix solver %%%%%%%%%%%%%%%%%%%%%%%%%%%% phi = solver( a_E, a_W, a_U, a_D, a_P, b ); % % % %