#*----------------------------------------------
* FlowSheet generated automaticaly by EMSO-GUI
*----------------------------------------------*#

using "streams.mso";
using "pressure_changers/valve.mso";
using "controllers/PIDs.mso";
using "stage_separators/tank.mso";

FlowSheet Sample_TankL_PID
	PARAMETERS
	PP as Plugin(Brief="Physical Properties",
		Type="PP",
		Components = ["n-butane","benzene","n-octane"],
		LiquidModel = "SRK",
		VapourModel = "SRK"
	);
	NComp as Integer;
	SET
	NComp = PP.NumberOfComponents;

	DEVICES
	Feed as simple_source;
	valve_liquid as valve_flow;
	PID_LC as PID;
	LiquidProduct as simple_sink;
	Heat_Duty as energy_source2;
	TankL_1 as TankL;

	CONNECTIONS
	PID_LC.Output to valve_liquid.FlowFraction;
	valve_liquid.Outlet to LiquidProduct.Inlet;
	Feed.Outlet to TankL_1.Inlet;
	Heat_Duty.OutletQ to TankL_1.InletQ;
	TankL_1.OutletLiquid to valve_liquid.Inlet;
	TankL_1.LI to PID_LC.Input;

	SET
	PID_LC.PID_Select = "Parallel_AWBT" ;
	PID_LC.Action = "Direct" ;
	PID_LC.Mode = "Automatic" ;
	PID_LC.Clip = "Clipped" ;
	PID_LC.alpha = 1 ;
	PID_LC.beta = 1 ;
	PID_LC.bias = 0.5 ;
	PID_LC.derivTime = 19 * 's' ;
	PID_LC.intTime = 76 * 's' ;
	PID_LC.gain = 1.1776 ;
	PID_LC.gamma = 1 ;
	PID_LC.tau = 1 * 's' ;
	PID_LC.tauSet = 1 * 's' ;
	PID_LC.MinInput = 0 ;
	PID_LC.MaxInput = 2 ;
	PID_LC.MinOutput = 0 ;
	PID_LC.MaxOutput = 1 ;
	TankL_1.Levelpercent_Initial = 0.80 ;

	SPECIFY
	Feed.MolarComposition(1) = 0.3 ;
	Feed.MolarComposition(2) = 0.3 ;
	Feed.MolarComposition(3) = 0.4 ;
	Feed.F = 500 * 'kmol/h' ;
	Feed.T = 338 * 'K' ;
	Feed.P = 5 * 'atm' ;
	PID_LC.SetPoint = 0.7 ;
	Heat_Duty.OutletQ = 0 * 'kW' ;

	INITIAL

	GUESS

	OPTIONS
	Dynamic = true;
	TimeStep = 0.2;
	TimeEnd = 12;
	TimeUnit = 'h';
	Integration = "original";
	NLASolver(
		File = "sundials",
		RelativeAccuracy = 1e-3,
		AbsoluteAccuracy = 1e-3,
		MaxIterations = 100
	);
	DAESolver(
		File = "sundials",
		RelativeAccuracy = 1e-2,
		AbsoluteAccuracy = 1e-6,
		EventAccuracy = 1e-2
	);
end