using "stage_separators/tank";

FlowSheet tank_Test
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp	as Integer;
	SET
	PP.Components = ["ethane", "propane", "propylene", "1-butene", "n-hexane"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	
	DEVICES
	t as tank;
	s as stream_therm;
	
	CONNECTIONS
	s to t.Inlet;
	
	SPECIFY
	s.P = 480 * "kPa";
	s.T = 310 * "K";
	s.F = 180 * "kmol/h";
	s.z = 1.0/NComp; 
	s.v = 0.698; 
	t.Q = 0 * "J/s";
	t.Outlet.F = 179 * "kmol/h";
	
	SET
	t.Across = 2.20 * "m^2";
	
	INITIAL
	t.Outlet.T = 305 *"K";
	t.Level = 0.5 * "m";
	t.Outlet.z([1:4]) = 1.0/NComp;
	
	OPTIONS
	relativeAccuracy = 1e-5;
	outputLevel = "medium";
	time = [0:100:1000];
end

FlowSheet tank_cylindrical_Test
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp	as Integer;
	SET
	PP.Components = ["propane", "propylene", "1-butene","1,3-butadiene", "n-hexane"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	
	DEVICES
	t as tank_cylindrical;
	s as stream_therm;
	
	CONNECTIONS
	s to t.Inlet;
	
	SPECIFY
	s.F = 500 * "kmol/h";
	s.T = 300 * "K";
	s.P = 400 * "kPa";
	s.z = 1/NComp;
	s.v = 0.368;

	t.Q = 0 * "J/s";
	t.Outlet.F = 490 * "kmol/h";
	
	SET
	t.radius = 0.9 * "m";
	t.L = 7.12 * "m";
	
	INITIAL
	t.Outlet.T = 280*"K";
	t.Level = 1 * "m";
	t.Outlet.z([1:4]) = 1.0/NComp;
	
	OPTIONS
	relativeAccuracy = 1e-5;
	outputLevel = "medium";
	time = [0:100:1000];
end