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

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

FlowSheet Sample_TankVL_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;

	SET

	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';

	INITIAL

	GUESS

	DEVICES
	VaporProduct as sink;

	SET

	SPECIFY

	INITIAL

	GUESS

	DEVICES
	valve_liquid as valve_flow;

	SET

	SPECIFY

	INITIAL

	GUESS

	DEVICES
	valve_Vapour as valve_flow;

	SET

	SPECIFY

	INITIAL

	GUESS

	DEVICES
	PID_LC as PID;

	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;

	SPECIFY
	PID_LC.SetPoint = 0.7;

	INITIAL

	GUESS

	DEVICES
	PID_PC as PID;

	SET
	PID_PC.PID_Select = "Parallel_AWBT";
	PID_PC.Action = "Direct";
	PID_PC.Mode = "Automatic";
	PID_PC.Clip = "Clipped";
	PID_PC.alpha = 1;
	PID_PC.beta = 1;
	PID_PC.bias = 0.5;
	PID_PC.derivTime = 18 * 's';
	PID_PC.intTime = 72 * 's';
	PID_PC.gain = 0.9275;
	PID_PC.gamma = 1;
	PID_PC.tau = 1 * 's';
	PID_PC.tauSet = 1 * 's';
	PID_PC.MinInput = 0;
	PID_PC.MaxInput = 4;
	PID_PC.MinOutput = 0;
	PID_PC.MaxOutput = 1;

	SPECIFY
	PID_PC.SetPoint = 0.6;

	INITIAL

	GUESS

	DEVICES
	LiquidProduct as simple_sink;

	SET

	SPECIFY

	INITIAL

	GUESS

	DEVICES
	Heat_Duty as energy_source2;

	SET

	SPECIFY
	Heat_Duty.OutletQ = 0 * 'kW';

	INITIAL

	GUESS

	DEVICES
	V001 as TankVL;

	SET
	V001.Orientation = "horizontal";
	V001.Heads = "elliptical";
	V001.Diameter = 3.1 * 'm';
	V001.Lenght = 6 * 'm';
	V001.Levelpercent_Initial = 0.5;
	V001.Temperature_Initial = 300 * 'K';

	SPECIFY

	INITIAL

	GUESS

	CONNECTIONS
	valve_Vapour.Outlet to VaporProduct.Inlet;
	PID_LC.Output to valve_liquid.FlowFraction;
	PID_PC.Output to valve_Vapour.FlowFraction;
	valve_liquid.Outlet to LiquidProduct.Inlet;
	Feed.Outlet to V001.Inlet;
	V001.OutletVapour to valve_Vapour.Inlet;
	V001.PI to PID_PC.Input;
	V001.LI to PID_LC.Input;
	Heat_Duty.OutletQ to V001.InletQ;
	V001.OutletLiquid to valve_liquid.Inlet;

	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