private double CalculateSpecificEnthalpyLiquidOutlet(double massConcentration)
{
double retValue = 0;
if (inlet is DryingMaterialStream)
{
DryingMaterialStream dmsLiquidOutlet = liquidOutlet as DryingMaterialStream;
retValue = dmsLiquidOutlet.GetBubblePointEnthalpy(dmsLiquidOutlet.Pressure.Value, (1.0 - massConcentration));
}
return(retValue);
}
private double CalculateSpecificEnthalpyVaporOutlet(double tBoilingPointOutlet)
{
//SteamTable steamTable = SteamTable.GetInstance();
//SubstanceStatesAndProperties props = steamTable.GetPropertiesFromPressureAndTemperature(vaporOutlet.Pressure.Value, tBoilingPointOutlet);
//return props.enthalpy;
double hValue = 0;
if (inlet is DryingMaterialStream)
{
DryingMaterialStream dmsVaporOutlet = vaporOutlet as DryingMaterialStream;
double pValue = vaporOutlet.Pressure.Value;
double hBubble = dmsVaporOutlet.GetBubblePointEnthalpy(pValue, 1.0);
double tBoilingPoint = dmsVaporOutlet.GetBoilingPoint(pValue, 0);
double evapHeat = vaporOutlet.GetEvaporationHeat(tBoilingPoint);
SteamTable steamTable = SteamTable.GetInstance();
SubstanceStatesAndProperties props = steamTable.GetPropertiesFromPressureAndVaporFraction(pValue, 1.0);
double hVapor1 = props.enthalpy;
props = steamTable.GetPropertiesFromPressureAndTemperature(pValue, tBoilingPointOutlet + 1.0e-6);
double hVapor2 = props.enthalpy;
hValue = hBubble + evapHeat + (hVapor2 - hVapor1);
}
return(hValue);
}
