source: branches/gui/sample/stage_separators/sample_batch_dist_PID.mso @ 554

#*-------------------------------------------------------------------
* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
*
* This LIBRARY is free software; you can distribute it and/or modify
* it under the therms of the ALSOC FREE LICENSE as available at
* http://www.enq.ufrgs.br/alsoc.
*
* EMSO Copyright (C) 2004 - 2007 ALSOC, original code
* from http://www.rps.eng.br Copyright (C) 2002-2004.
* All rights reserved.
*
* EMSO is distributed under the therms of the ALSOC LICENSE as
* available at http://www.enq.ufrgs.br/alsoc.
*
*--------------------------------------------------------------------
* Sample file for batch distillation with controllers
*--------------------------------------------------------------------
* 
* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
* Author: 
* $Id: sample_batch_dist_PID.mso 318 2007-07-19 04:23:31Z arge $
*--------------------------------------------------------------------*#
using "stage_separators/batch_dist";
using "controllers/PIDs";

FlowSheet TesteBatch_PID
        
        PARAMETERS
        PP              as Plugin(Brief="Physical Properties",
                Type="PP", Components = [ "isobutane", "benzene" ],
                LiquidModel = "PR", VapourModel = "PR");
        NComp   as Integer;
        P_max   as pressure(Brief="Maximum Pressure on distillator");
        P_min   as pressure(Brief="Minimum Pressure on distillator");
        
        VARIABLES
        P_ad    as fraction(Brief="Dimensionless pressure");
        P_set   as pressure(Brief="Minimum Pressure on distillator");

        SET
        NComp = PP.NumberOfComponents;
        
        DEVICES
        batch   as Diff_Dist;
        reflux  as liquid_stream;
        feed    as source;
        pidP    as PID;
        Q               as energy_source;
        
        CONNECTIONS
        reflux to batch.InletL;
        feed.Outlet to batch.Inlet;
        Q.OutletQ to batch.InletQ;

        EQUATIONS
        if batch.Level > 1E-3 then
                Q.OutletQ.Q = 3.7743e6 * 'kJ/h';
        else
                Q.OutletQ.Q = 0 * 'kJ/h';
        end

    "Pressure Controller"
        pidP.Parameters.tau = 0*'s';    
        pidP.Parameters.tauSet = 0*'s'; 
        pidP.Parameters.alpha = 0.3;
        pidP.Parameters.bias = 0;       
        pidP.Parameters.gamma = 1;
        pidP.Parameters.beta = 1;
        pidP.Options.action = -1;
        pidP.Options.clip = 1;
        pidP.Options.autoMan = 0;
        pidP.Parameters.intTime = 0.1*'min';
        pidP.Parameters.gain = 1;
        pidP.Parameters.derivTime = 0.02*'min';
        pidP.Ports.setPoint = (P_set-P_min)/(P_max-P_min);
        pidP.Ports.input = P_ad;
        P_ad = (batch.P-P_min)/(P_max-P_min);
        batch.OutletV.F = 500 * 'kmol/h' * pidP.Ports.output;

        SPECIFY
        reflux.F = 0 * 'kmol/h';
        reflux.T = 328 * 'K';
        reflux.P = 180 * 'kPa';
        reflux.z = [0.5, 0.5];
        
        feed.Outlet.F = 0 * 'kmol/h';
        feed.Outlet.T = 328 * 'K';
        feed.Outlet.P = 180 * 'kPa';
        feed.Outlet.z = [0.5, 0.5];

        P_set = 300 * 'kPa';

        SET
        pidP.PID_Select = "Ideal_AWBT";
        batch.V = 3 * 'm^3';
        batch.Across = 1 * 'm^2';
        P_max = 500 * 'kPa';
        P_min = 100 * 'kPa';
        
        INITIAL
        batch.T = 298 *'K';
        batch.Level = 2.5 * 'm';
        batch.x(2) = 0.2;
        
        OPTIONS
        TimeEnd = 6;
        TimeStep = 0.01;
        TimeUnit = 'min';
end