source: branches/gui/sample/reconciliation/flash_rec.mso

using "stage_separators/flash";

# exemplo baseado nos dados do artigo do Gani 1985.
FlowSheet flash_Test
        PARAMETERS
        PP as Plugin(Brief="Physical Properties",
                Type="PP",
                Components = ["1,3-butadiene", "isobutene", "n-pentane",
                        "1-pentene", "1-hexene", "benzene"],
                LiquidModel = "PR",
                VapourModel = "PR"
        );
        NComp as Integer;

        VARIABLES
        Q       as energy_source (Brief="Heat supplied");
        
        SET
        NComp = PP.NumberOfComponents;
        
        DEVICES
        fl as flash_steady;
        s1 as source;
        
        CONNECTIONS
        s1.Outlet to fl.Inlet;
        Q.OutletQ to fl.InletQ;
        
        SPECIFY
        s1.F = 496.3 * 'kmol/h';
        s1.T = 338 * 'K';
        s1.P = 507.1 * 'kPa';
        s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283];
        
        fl.OutletLiquid.P = 2.5 * 'atm';

        #Q.OutletQ.Q = 0 * 'kJ/h';
        fl.OutletLiquid.T = 315.06 * 'K';
        
        OPTIONS
        Dynamic = false;
end

Reconciliation flash_rec as flash_Test

        RECONCILE
        s1.F; fl.OutletLiquid.F; fl.OutletVapour.F;
        
        FREE
        s1.F;

        EXPERIMENTS
        # FILE            WEIGTH
        "flash.dat"       1;
        

        OPTIONS
        Filter = "mean";
        Significance = 0.95;
        ObjectiveFunction = "Normal";
        
        GrossErrorTests(
                Global = true,
#               Nodal = true,
                Measurements = true
        );
        
        NLPSolver(
                MaxIterations=1000,
                File = "complex"
                #File = "ipopt_emso"
        );
        Dynamic = false;
end