using "stage_separators/condenser";
using "mixers_splitters/splitter";

# condenser with splitter dividing liquid outlet
FlowSheet condenser_Test
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp	as Integer;

	VARIABLES
	Q	as heat_rate (Brief="Heat supplied");
	
	SET
	PP.Components = [ "isobutane", "n-pentane"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	
	DEVICES
	c1 as condenser;
	sp as splitter;
	s1 as stream_therm;
	
	CONNECTIONS
	s1 to c1.InletV;
	c1.OutletL to sp.Inlet;
	Q to c1.Q;
	
	SPECIFY
	s1.P = 152 * "kPa";
	s1.T = 298.6 * "K";
	s1.F = 153 * "kmol/h";
	s1.z = [0.664, 0.336];
	s1.v = 1.0;
	
	sp.frac = 0.444445;
	c1.OutletV.F = 0 * "kmol/h";
	c1.OutletL.F = 153 * "kmol/h";

	Q = -3.71e6 * "kJ/h";

	SET
	c1.V = 2 * "m^3";
	c1.Across = 1 * "m^2";

	INITIAL
	c1.OutletL.T = 280 *"K";
	c1.Level = 1 * "m";
	c1.OutletL.z(1) = 0.65;
	
	OPTIONS
	time = [0:20:1000];
end

FlowSheet condenserSteady_Test
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp	as Integer;

	VARIABLES
	Q	as heat_rate (Brief="Heat supplied");
	
	SET
	PP.Components = [ "isobutane", "n-pentane"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	
	DEVICES
	c1 as condenserSteady;
	s1 as stream_therm;
	
	CONNECTIONS
	s1 to c1.InletV;
	Q to c1.Q;
	
	SPECIFY
	s1.P = 152 * "kPa";
	s1.T = 298.6 * "K";
	s1.F = 153 * "kmol/h";
	s1.z = [0.664, 0.336];
	s1.v = 1.0;
	Q = 3.71e6 * "kJ/h";

	SET
	c1.DP = 100 * "kPa";

	OPTIONS
	mode = "steady";
	time = [0:20:1000];
end