/// <summary>
/// set property
/// </summary>
/// <param name="propName">property name, defined in CO reference</param>
/// <param name="phases">empty means overall, if it's vapor and liquid, will be combined to "vaporliquid", otherwise, just add the names</param>
/// <returns></returns>
protected void SetPropList(string propName, PropertyBasis basis, IEnumerable <double> value, Phases[] phases = null)
{
CasterLogger.Debug($"Set property for {propName}: {value}");
double[] temp = value as double[] ?? value.ToArray();
if (phases == null || phases.Length == 0) // overall
{
CasterLogger.Debug($"Set property {propName} for overall phase");
_capeThermoMaterialObject.SetProp(propName, "Overall", null, "mixture", basis.ToString(), temp);
}
else if (phases.Length == 1) // one phase
{
CasterLogger.Debug($"Set property {propName} for {phases[0]}");
_capeThermoMaterialObject.SetProp(propName, phases[0].Value, null, null, basis.ToString(), temp);
}
else if (phases.Length == 2) // two phases
{
CasterLogger.Debug($"Set property {propName} for {phases[0]} and {phases[1]}");
string phaseName = null;
if (phases.Contains(Phases.Vapor) && phases.Contains(Phases.Liquid))
{
phaseName = Phases.Vapor.Value + Phases.Liquid.Value; // vapor in front
}
else
{
phaseName = phases[0].Value + phases[1].Value;
}
_capeThermoMaterialObject.SetProp(propName, phaseName, null, "mixture", basis.ToString(), temp);
}
else
{
CasterLogger.Error($"Only support overall, 1 phase or 2 phases");
throw new ArgumentOutOfRangeException($"Only support overall, 1 phase or 2 phases");
}
//_alreadyFlashed = false;
CasterLogger.Debug($"Set property completed");
}
/// <summary>
/// Calculation method for the MixerExample unit operation.
/// </summary>
/// <remarks>
/// A mixer unit operation combined the material flows from two inlet ports into the flow of a single outlet port.
/// In order to do this calculation, the mixer unit obtains flow information from each inlet port,
/// the adds the flows to obtain the flow of the outlet port. In the case of the mixer below, it is assumed that the
/// components are the same in each material object and that the components are listed in the same order.
/// After the combined flow is calculated at the values set to the outlet port, along with the
/// enthalpy of the stream calculated from an energy balance and the pressure determined from
/// the inlet pressures, the outlet stream can be flahsed to determine equilibrium conditions.
/// The last task is releasing any duplicate material objects obtained.
/// </remarks>
/// <example>
/// <para>An example of how to calculate a unit operation. This method obtains material objects
/// from each of ports using the <see cref = "PortCollection"/> class. The <see cref = "ICapeThermoMaterialObject"/>
/// interface is used to obtain the names using the CompIds() method, flows of each of the
/// components present in the material object, overall pressure and overall enthalpy are
/// obtained using the <see cref = "ICapeThermoMaterialObject.GetProp"/> method. The overall enthalpy of the stram is
/// calculated using <see cref = "ICapeThermoMaterialObject.CalcProp"/> method. The unit then combines the flows,
/// calculates the output stream enthalpy, and determines output pressure from the lower of
/// the two streams' pressure and pressure drop parameter. Lastly, the results of the
/// calculations are applied to the output material object using the <see cref = "ICapeThermoMaterialObject.SetProp"/>
/// method. The last method of the calculate method is to call the material's
/// <see cref = "ICapeThermoMaterialObject.CalcEquilibrium"/> method.</para>
/// <para>
/// In this case, the inlet materials need to be released. This is accomplished using the
/// <see cref = "System.Runtime.InteropServices.Marshal.ReleaseComObject"/> method.
/// Using this method to release the outlet material object would result in an null object reference error.
/// </para>
/// <para>
/// The method also documents use of the <see cref = "CapeObjectBase.throwException"/> method to provide
/// CAPE-OPEN compliant error handling.
/// </para>
/// <code>
/// protected override void Calculate()
/// {
/// // Log a message using the simulation context (pop-up message commented out.
/// if (this.SimulationContext != null)
/// ((ICapeDiagnostic)this.SimulationContext).LogMessage("Starting Mixer Calculation");
/// //(CapeOpen.ICapeDiagnostic)(this.SimulationContext).PopUpMessage("Starting Mixer Calculation");
///
/// // Get the material Object from Port 0.
/// ICapeThermoMaterialObject in1 = null;
/// ICapeThermoMaterialObject tempMO = null;
/// try
/// {
/// tempMO = (ICapeThermoMaterialObject)this.Ports[0].connectedObject;
/// }
/// catch (System.Exception p_Ex)
/// {
/// this.OnUnitOperationEndCalculation("Error - Material object does not support CAPE-OPEN Thermodynamics 1.0.");
/// CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Material object does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
/// this.throwException(ex);
/// }
///
/// // Duplicate the port, its an input port, always use a duplicate.
/// try
/// {
/// in1 = (ICapeThermoMaterialObject)tempMO.Duplicate();
/// }
/// catch (System.Exception p_Ex)
/// {
/// this.OnUnitOperationEndCalculation("Error - Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.");
/// CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
/// this.throwException(ex);
/// }
/// // Arrays for the GetProps and SetProps call for enthaply.
/// String[] phases = { "Overall" };
/// String[] props = { "enthalpy" };
///
/// // Declare variables for calculations.
/// String[] in1Comps = null;
/// double[] in1Flow = null;
/// double[] in1Enthalpy = null;
/// double[] pressure = null;
/// double totalFlow1 = 0;
///
/// // Exception catching code...
/// try
/// {
/// // Get Strings, must cast to string array data type.
/// in1Comps = (String[])in1.ComponentIds;
///
/// // Get flow. Arguments are the property; phase, in this case, Overall; compound identifications
/// // in this case, the null returns the property for all components; calculation type, in this case,
/// // null, no calculation type; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
/// in1Flow = (double[])in1.GetProp("flow", "Overall", null, null, "mole");
///
/// // Get pressure. Arguments are the property; phase, in this case, Overall; compound identifications
/// // in this case, the null returns the property for all components; calculation type, in this case, the
/// // mixture; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
/// pressure = (double[])in1.GetProp("Pressure", "Overall", null, "Mixture", null);
///
/// // The following code adds the individual flows to get the total flow for the stream.
/// for (int i = 0; i < in1Flow.Length; i++)
/// {
/// totalFlow1 = totalFlow1 + in1Flow[i];
/// }
///
/// // Calculates the mixture enthalpy of the stream.
/// in1.CalcProp(props, phases, "Mixture");
///
/// // Get the enthalpy of the stream. Arguments are the property, enthalpy; the phase, overall;
/// // a null pointer, required as the overall enthalpy is desired; the calculation type is
/// // mixture; and the basis is moles.
/// in1Enthalpy = (double[])in1.GetProp("enthalpy", "Overall", null, "Mixture", "mole");
/// }
/// catch (System.Exception p_Ex)
/// {
/// // Exception handling, wraps a COM exception, shows the message, and re-throws the excecption.
/// if (p_Ex is System.Runtime.InteropServices.COMException)
/// {
/// System.Runtime.InteropServices.COMException comException = (System.Runtime.InteropServices.COMException)p_Ex;
/// p_Ex = CapeOpen.COMExceptionHandler.ExceptionForHRESULT(in1, p_Ex);
/// }
/// this.throwException(p_Ex);
/// }
/// IDisposable disp = in1 as IDisposable;
/// if (disp != null)
/// {
/// disp.Dispose();
/// }
///
///
/// // Get the material Object from Port 0.
/// ICapeThermoMaterialObject in2 = null;
/// tempMO = null;
/// try
/// {
/// tempMO = (ICapeThermoMaterialObject)this.Ports[1].connectedObject;
/// }
/// catch (System.Exception p_Ex)
/// {
/// this.OnUnitOperationEndCalculation("Error - Material object does not support CAPE-OPEN Thermodynamics 1.0.");
/// CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Material object does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
/// this.throwException(ex);
/// }
///
/// // Duplicate the port, its an input port, always use a duplicate.
/// try
/// {
/// in2 = (ICapeThermoMaterialObject)tempMO.Duplicate();
/// }
/// catch (System.Exception p_Ex)
/// {
/// this.OnUnitOperationEndCalculation("Error - Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.");
/// CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
/// this.throwException(ex);
/// }
///
/// // Declare variables.
/// String[] in2Comps = null;
/// double[] in2Flow = null;
/// double[] in2Enthalpy = null;
/// double totalFlow2 = 0;
///
/// // Try block.
/// try
/// {
/// // Get the component identifications.
/// in2Comps = in2.ComponentIds;
///
/// // Get flow. Arguments are the property; phase, in this case, Overall; compound identifications
/// // in this case, the null returns the property for all components; calculation type, in this case,
/// // null, no calculation type; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
/// in2Flow = in2.GetProp("flow", "Overall", null, null, "mole");
///
/// // Get pressure. Arguments are the property; phase, in this case, Overall; compound identifications
/// // in this case, the null returns the property for all components; calculation type, in this case, the
/// // mixture; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
/// double[] press = in2.GetProp("Pressure", "Overall", null, "Mixture", null);
/// if (press[0] < pressure[0]) pressure[0] = press[0];
///
/// // The following code adds the individual flows to get the total flow for the stream.
/// for (int i = 0; i < in2Flow.Length; i++)
/// {
/// totalFlow2 = totalFlow2 + in2Flow[i];
/// }
///
/// // Calculates the mixture enthalpy of the stream.
/// in2.CalcProp(props, phases, "Mixture");
///
/// // Get the enthalpy of the stream. Arguments are the property, enthalpy; the phase, overall;
/// // a null pointer, required as the overall enthalpy is desired; the calculation type is
/// // mixture; and the basis is moles.
/// in2Enthalpy = in2.GetProp("enthalpy", "Overall", null, "Mixture", "mole");
/// }
/// catch (System.Exception p_Ex)
/// {
/// System.Runtime.InteropServices.COMException comException = (System.Runtime.InteropServices.COMException)p_Ex;
/// if (comException != null)
/// {
/// p_Ex = CapeOpen.COMExceptionHandler.ExceptionForHRESULT(in2, p_Ex);
/// }
/// this.throwException(p_Ex);
/// }
/// // Release the material object if it is a COM object.
/// disp = in2 as IDisposable;
/// if (disp != null)
/// {
/// disp.Dispose();
/// }
///
///
/// // Get the outlet material object.
/// ICapeThermoMaterialObject outPort = (ICapeThermoMaterialObject)this.Ports[2].connectedObject;
///
/// // An empty, one-member array to set values in the outlet material stream.
/// double[] values = new double[1];
///
/// // Use energy balanace to calculate the outlet enthalpy.
/// values[0] = (in1Enthalpy[0] * totalFlow1 + in2Enthalpy[0] * totalFlow2) / (totalFlow1 + totalFlow2);
/// try
/// {
/// // Set the outlet enthalpy, for the overall phase, with a mixture calculation type
/// // to the value calculated above.
/// outPort.SetProp("enthalpy", "Overall", null, "Mixture", "mole", values);
///
/// // Set the outlet pressure to the lower of the to inlet pressures less the value of the
/// // pressure drop parameter.
/// pressure[0] = pressure[0] - (((RealParameter)(this.Parameters[0])).SIValue);
///
/// // Set the outlet pressure.
/// outPort.SetProp("Pressure", "Overall", null, null, null, pressure);
///
/// // Resize the value array for the number of components.
/// values = new double[in1Comps.Length];
///
/// // Calculate the individual flow for each component.
/// for (int i = 0; i < in1Comps.Length; i++)
/// {
/// values[i] = in1Flow[i] + in2Flow[i];
/// }
/// // Set the outlet flow by component. Note, this is for overall phase and mole flows.
/// // The component Identifications are used as a check.
/// outPort.SetProp("flow", "Overall", in1Comps, null, "mole", values);
///
/// // Calculate equilibrium using a "pressure-enthalpy" flash type.
/// outPort.CalcEquilibrium("PH", null);
///
/// // Release the material object if it is a COM object.
/// if (outPort.GetType().IsCOMObject)
/// {
/// System.Runtime.InteropServices.Marshal.FinalReleaseComObject(outPort);
/// }
/// }
/// catch (System.Exception p_Ex)
/// {
/// System.Runtime.InteropServices.COMException comException = (System.Runtime.InteropServices.COMException)p_Ex;
/// if (comException != null)
/// {
/// p_Ex = CapeOpen.COMExceptionHandler.ExceptionForHRESULT(outPort, p_Ex);
/// }
/// this.throwException(p_Ex);
/// }
///
/// // Log the end of the calculation.
/// if (this.SimulationContext != null)
/// ((CapeOpen.ICapeDiagnostic)this.SimulationContext).LogMessage("Ending Mixer Calculation");
/// //(CapeOpen.ICapeDiagnostic)(this.SimulationContext).PopUpMessage("Ending Mixer Calculation");
/// }
///
/// </code>
/// </example>
/// <see cref="ICapeThermoMaterialObject"/>
/// <see cref="COMExceptionHandler"/>
protected override void Calculate()
{
// Log a message using the simulation context (pop-up message commented out.
if (this.SimulationContext != null)
{
((ICapeDiagnostic)this.SimulationContext).LogMessage("Starting Mixer Calculation");
}
//(CapeOpen.ICapeDiagnostic>(this.SimulationContext).PopUpMessage("Starting Mixer Calculation");
// Get the material Object from Port 0.
ICapeThermoMaterialObject in1 = null;
ICapeThermoMaterialObject tempMO = null;
try
{
tempMO = (ICapeThermoMaterialObject)this.Ports[0].connectedObject;
}
catch (System.Exception p_Ex)
{
this.OnUnitOperationEndCalculation("Error - Material object does not support CAPE-OPEN Thermodynamics 1.0.");
CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Material object does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
this.throwException(ex);
}
// Duplicate the port, its an input port, always use a duplicate.
try
{
in1 = (ICapeThermoMaterialObject)tempMO.Duplicate();
}
catch (System.Exception p_Ex)
{
this.OnUnitOperationEndCalculation("Error - Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.");
CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
this.throwException(ex);
}
// Arrays for the GetProps and SetProps call for enthaply.
String[] phases = { "Overall" };
String[] props = { "enthalpy" };
// Declare variables for calculations.
String[] in1Comps = null;
double[] in1Flow = null;
double[] in1Enthalpy = null;
double[] pressure = null;
double totalFlow1 = 0;
// Exception catching code...
try
{
// Get Strings, must cast to string array data type.
in1Comps = (String[])in1.ComponentIds;
// Get flow. Arguments are the property; phase, in this case, Overall; compound identifications
// in this case, the null returns the property for all components; calculation type, in this case,
// null, no calculation type; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
in1Flow = (double[])in1.GetProp("flow", "Overall", null, null, "mole");
// Get pressure. Arguments are the property; phase, in this case, Overall; compound identifications
// in this case, the null returns the property for all components; calculation type, in this case, the
// mixture; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
pressure = (double[])in1.GetProp("Pressure", "Overall", null, "Mixture", null);
// The following code adds the individual flows to get the total flow for the stream.
for (int i = 0; i < in1Flow.Length; i++)
{
totalFlow1 = totalFlow1 + in1Flow[i];
}
// Calculates the mixture enthalpy of the stream.
in1.CalcProp(props, phases, "Mixture");
// Get the enthalpy of the stream. Arguments are the property, enthalpy; the phase, overall;
// a null pointer, required as the overall enthalpy is desired; the calculation type is
// mixture; and the basis is moles.
in1Enthalpy = (double[])in1.GetProp("enthalpy", "Overall", null, "Mixture", "mole");
}
catch (System.Exception p_Ex)
{
// Exception handling, wraps a COM exception, shows the message, and re-throws the excecption.
if (p_Ex is System.Runtime.InteropServices.COMException)
{
System.Runtime.InteropServices.COMException comException = (System.Runtime.InteropServices.COMException)p_Ex;
p_Ex = CapeOpen.COMExceptionHandler.ExceptionForHRESULT(in1, p_Ex);
}
this.throwException(p_Ex);
}
IDisposable disp = in1 as IDisposable;
if (disp != null)
{
disp.Dispose();
}
// Get the material Object from Port 0.
ICapeThermoMaterialObject in2 = null;
tempMO = null;
try
{
tempMO = (ICapeThermoMaterialObject)this.Ports[1].connectedObject;
}
catch (System.Exception p_Ex)
{
this.OnUnitOperationEndCalculation("Error - Material object does not support CAPE-OPEN Thermodynamics 1.0.");
CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Material object does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
this.throwException(ex);
}
// Duplicate the port, its an input port, always use a duplicate.
try
{
in2 = (ICapeThermoMaterialObject)tempMO.Duplicate();
}
catch (System.Exception p_Ex)
{
this.OnUnitOperationEndCalculation("Error - Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.");
CapeOpen.CapeInvalidOperationException ex = new CapeOpen.CapeInvalidOperationException("Object connected to Inlet Port 1 does not support CAPE-OPEN Thermodynamics 1.0.", p_Ex);
this.throwException(ex);
}
// Declare variables.
String[] in2Comps = null;
double[] in2Flow = null;
double[] in2Enthalpy = null;
double totalFlow2 = 0;
// Try block.
try
{
// Get the component identifications.
in2Comps = in2.ComponentIds;
// Get flow. Arguments are the property; phase, in this case, Overall; compound identifications
// in this case, the null returns the property for all components; calculation type, in this case,
// null, no calculation type; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
in2Flow = in2.GetProp("flow", "Overall", null, null, "mole");
// Get pressure. Arguments are the property; phase, in this case, Overall; compound identifications
// in this case, the null returns the property for all components; calculation type, in this case, the
// mixture; and lastly, the basis, moles. Result is cast to a double array, and will contain one value.
double[] press = in2.GetProp("Pressure", "Overall", null, "Mixture", null);
if (press[0] < pressure[0])
{
pressure[0] = press[0];
}
// The following code adds the individual flows to get the total flow for the stream.
for (int i = 0; i < in2Flow.Length; i++)
{
totalFlow2 = totalFlow2 + in2Flow[i];
}
// Calculates the mixture enthalpy of the stream.
in2.CalcProp(props, phases, "Mixture");
// Get the enthalpy of the stream. Arguments are the property, enthalpy; the phase, overall;
// a null pointer, required as the overall enthalpy is desired; the calculation type is
// mixture; and the basis is moles.
in2Enthalpy = in2.GetProp("enthalpy", "Overall", null, "Mixture", "mole");
}
catch (System.Exception p_Ex)
{
System.Runtime.InteropServices.COMException comException = (System.Runtime.InteropServices.COMException)p_Ex;
if (comException != null)
{
p_Ex = CapeOpen.COMExceptionHandler.ExceptionForHRESULT(in2, p_Ex);
}
this.throwException(p_Ex);
}
// Release the material object if it is a COM object.
disp = in2 as IDisposable;
if (disp != null)
{
disp.Dispose();
}
// Get the outlet material object.
ICapeThermoMaterialObject outPort = (ICapeThermoMaterialObject)this.Ports[2].connectedObject;
// An empty, one-member array to set values in the outlet material stream.
double[] values = new double[1];
// Use energy balanace to calculate the outlet enthalpy.
values[0] = (in1Enthalpy[0] * totalFlow1 + in2Enthalpy[0] * totalFlow2) / (totalFlow1 + totalFlow2);
try
{
// Set the outlet enthalpy, for the overall phase, with a mixture calculation type
// to the value calculated above.
outPort.SetProp("enthalpy", "Overall", null, "Mixture", "mole", values);
// Set the outlet pressure to the lower of the to inlet pressures less the value of the
// pressure drop parameter.
pressure[0] = pressure[0] - (((RealParameter)(this.Parameters[0])).SIValue);
// Set the outlet pressure.
outPort.SetProp("Pressure", "Overall", null, null, null, pressure);
// Resize the value array for the number of components.
values = new double[in1Comps.Length];
// Calculate the individual flow for each component.
for (int i = 0; i < in1Comps.Length; i++)
{
values[i] = in1Flow[i] + in2Flow[i];
}
// Set the outlet flow by component. Note, this is for overall phase and mole flows.
// The component Identifications are used as a check.
outPort.SetProp("flow", "Overall", in1Comps, null, "mole", values);
// Calculate equilibrium using a "pressure-enthalpy" flash type.
outPort.CalcEquilibrium("PH", null);
// Release the material object if it is a COM object.
if (outPort.GetType().IsCOMObject)
{
System.Runtime.InteropServices.Marshal.FinalReleaseComObject(outPort);
}
}
catch (System.Exception p_Ex)
{
System.Runtime.InteropServices.COMException comException = (System.Runtime.InteropServices.COMException)p_Ex;
if (comException != null)
{
p_Ex = CapeOpen.COMExceptionHandler.ExceptionForHRESULT(outPort, p_Ex);
}
this.throwException(p_Ex);
}
// Log the end of the calculation.
if (this.SimulationContext != null)
{
((CapeOpen.ICapeDiagnostic) this.SimulationContext).LogMessage("Ending Mixer Calculation");
}
//(CapeOpen.ICapeDiagnostic>(this.SimulationContext).PopUpMessage("Ending Mixer Calculation");
}