Function setupControls.m
Set up the controlsThere are two types of controls:
The controls locations have been hard coded here, but they can be changed. We have chosen a set of four cells on the western side for the injection and a face on the eastern side where we impose pressure. function bc = setupControls(G, fluid, param)
system.R = getR();
system.k = getHenryCoef();
system.Temp = param.Temp;
system.vp = vaporPressure(system.Temp);
system.fluid = fluid;
nComp = 3; % 3 components (He, Ne, CO_{2})
system.nComp = nComp;
influx_p = param.influx_p;
outflux_p = param.outflux_p;
We assume injection fluid is only composed of (ideal) gas influx_C = param.influx_C*influx_p/(system.R*system.Temp); We assume the output fluid is only composed of liquid (typically same composition as initial state). This assumption should actually not be used if there is only outflow on this faces. Indeed, in this case, the boundary values of the concentrations are not used due to upwinding face evaluation. omega = cell2mat(omega_l(outflux_p, system)); outflux_C = 1/(omega'*param.outflux_C)*param.outflux_C; outflux_C = outflux_C(1:nComp); Given pressure on eastern face of the cell 411, which is the most eastern cell of the reservoir. east_cell = 411; east_faces = G.cells.faces(G.cells.facePos(east_cell):G.cells.facePos(east_cell + 1)  ... 1 , :); bc.dirichlet.faces = east_faces(east_faces(:, 2) == 2 , 1); bc.dirichlet.pressure = outflux_p; bc.dirichlet.C = arrayfun(@(x)(x), outflux_C, 'uniformoutput', false); [cg, cl, cw, s, Cw] = flash_calculation(outflux_C', outflux_p, system); bc.dirichlet.cg = arrayfun(@(x)(x), cg, 'uniformoutput', false); bc.dirichlet.cl = arrayfun(@(x)(x), cl, 'uniformoutput', false); bc.dirichlet.cw = cw; bc.dirichlet.s = s; bc.dirichlet.Cw = Cw; Given influx on a set of 4 cells on the western side of the reservoir. west_cells = [4527; 4528; 4451; 4452]; nwc = numel(west_cells); bc.influx_cells = west_cells; influx_C = repmat(influx_C', nwc, 1); influx_p = repmat(influx_p, nwc, 1); [cg, cl, cw, s, Cw] = flash_calculation(influx_C, influx_p, system); bc.dirichlet.C = cell(nComp, 1); for ic = 1:nComp bc.C_influx{ic} = param.influx_rate*influx_C(:, ic); end bc.water_influx = param.influx_rate*Cw; end
