protected override void OnCalculate()
{
//
//Get input Thermo Material Object and its properties
//
double zTemperature = InputPort.Temperature;
double zPressure = InputPort.Pressure;
double zEnthalpy = InputPort.Enthalpy;
double zTotalFlow = InputPort.TotalFlow;
double[] zFraction = InputPort.Fraction;
//
//Get output Thermo Material Object and set its properties
//
OutputPort.Temperature = zTemperature;
OutputPort.Pressure = zPressure;
OutputPort.Enthalpy = zEnthalpy;
OutputPort.TotalFlow = zTotalFlow;
OutputPort.Fraction = zFraction;
try
{
OutputPort.CalculateEquilibrium(CapeOpenFlashType.PH);
}
catch
{
//Error Handling
}
}
protected override void OnCalculate()
{
//
//Check Components Number and their IDS
//
int zComponentNumber;
zComponentNumber = InputPort.ComponentsCount;
string[] zIds;
zIds = InputPort.Ids;
//
//Input Port properties
//
double zTemperature = InputPort.Temperature;
double zPressure = InputPort.Pressure;
double zTotalFlow = InputPort.TotalFlow;
//Volume is to Calculate...
InputPort.CalculateProperty(CapeOpenThermoMaterialPropertyType.Volume, CapeOpenPhaseType.Overall, CapeOpenCalculationType.Pure);
double zVolume = InputPort.Volume;
double zEnthalpy = InputPort.Enthalpy;
double[] zFraction = InputPort.Fraction;
//
//Units of Measure changing
//
double dTotmod = zTotalFlow * 3.6;
double dTempmod = zTemperature - 273.15;
double dPresmod = zPressure / 100000.0;
//Calc. Partial Pressure
double[] partial_pressure = new double[zComponentNumber];
for (int i = 0; i < zComponentNumber; i++)
{
partial_pressure[i] = zFraction[i] * zPressure;
}
//Reaction Speed
double R = 1.98578;
double r1;
double r2;
double r3;
//Reaction Temperature
double Treaction = zTemperature + 119.0;
r1 = K1Value * Math.Exp(-E1Value / (R * Treaction)) * (partial_pressure[0] / 1000.0) * (partial_pressure[2] / 1000.0);
r2 = K2Value * Math.Exp(-E2Value / (R * Treaction)) * (partial_pressure[0] / 1000.0) * (partial_pressure[2] / 1000.0);
r3 = K3Value * Math.Exp(-E3Value / (R * Treaction)) * (partial_pressure[0] / 1000.0) * (partial_pressure[2] / 1000.0);
//display the output pressure
double pressureout = zPressure - 80000.0;
//define the reactor volume
double vol = 101.78;
double propene1;
double propene2;
double propene3;
double k1tot;
double k2tot;
double k3tot;
k1tot = K1Value * Math.Exp(-E1Value / (R * Treaction));
k2tot = K2Value * Math.Exp(-E2Value / (R * Treaction));
k3tot = K3Value * Math.Exp(-E3Value / (R * Treaction));
propene1 = 0.00199 * vol * r1;
propene2 = 0.00199 * vol * r2;
propene3 = 0.00199 * vol * r3;
double propene_final = zFraction[0] * zTotalFlow * 3.6 - (propene1 + propene2 + propene3);
double water_final = zFraction[1] * zTotalFlow * 3.6 + (propene1 + propene2 + 3.0 * propene3);
double oxygen_final = zFraction[2] * zTotalFlow * 3.6 - (1.5 * propene1 + 2.5 * propene2 + 4.5 * propene3);
double nitrogen_final = zFraction[3] * zTotalFlow * 3.6;
double acetic_final = zFraction[4] * zTotalFlow * 3.6 + propene2;
double acrylic_final = zFraction[5] * zTotalFlow * 3.6 + propene1;
double CO2_final = zFraction[6] * zTotalFlow * 3.6 + (propene2 + 3.0 * propene3);
//Calculate outputstream
double sum = propene_final + water_final + oxygen_final + nitrogen_final + acetic_final + acrylic_final + CO2_final;
//mole fractions for output stream
double fr_propene_final = propene_final / sum;
double fr_water_final = water_final / sum;
double fr_oxygen_final = oxygen_final / sum;
double fr_nitrogen_final = nitrogen_final / sum;
double fr_acetic_final = acetic_final / sum;
double fr_acrylic_final = acrylic_final / sum;
double fr_CO2_final = CO2_final / sum;
double[] fractionout = new double[8];
fractionout[0] = fr_propene_final;
fractionout[1] = fr_water_final;
fractionout[2] = fr_oxygen_final;
fractionout[3] = fr_nitrogen_final;
fractionout[4] = fr_acetic_final;
fractionout[5] = fr_acrylic_final;
fractionout[6] = fr_CO2_final;
//Define Enthalpy
double deltaH = -3590030.0;
double enthalpyOut = zEnthalpy - deltaH;
//
//Output Thermo Material Object
//
double suma = sum / 3.6;
OutputPort.Temperature = Treaction;
OutputPort.Pressure = pressureout;
OutputPort.TotalFlow = suma;
OutputPort.Enthalpy = enthalpyOut;
OutputPort.Volume = zVolume;
OutputPort.Fraction = fractionout;
OutputPort.CalculateEquilibrium(CapeOpenFlashType.TP);
}
protected override void OnCalculate()
{
double zTemperature = InputPort.Temperature;
double zPressure = InputPort.Pressure;
double zEnthalpy = InputPort.Enthalpy;
double zTotalFlow = InputPort.TotalFlow;
double[] zFraction = InputPort.Fraction;
// totalflow ii inmultit cu 3.6 pt. ca CO il citeste in mol/s si tie iti trebuie in kmol/hr
double zTotmod = zTotalFlow * 3.6;
string[] zIds = InputPort.Ids;
string[] zPropertyValue = new string[1];
zPropertyValue[0] = "casRegistryNumber";
string[] zPropVal = null;
object[] zObj;
zObj = (object[])InputPort.ConnectedObject.GetComponentConstant(zPropertyValue, zIds);
zPropVal = new string[zObj.GetLength(0)];
for (int i = 0; i < zObj.GetLength(0); i++)
{
zPropVal[i] = (string)zObj[i];
}
//Volume
InputPort.CalculateProperty(CapeOpenThermoMaterialPropertyType.Volume, CapeOpenPhaseType.Overall, CapeOpenCalculationType.Pure);
double zVolume = InputPort.Volume;
Dictionary <string, double> zComponentsList = new Dictionary <string, double>();
DataAccessHelper zAccessoDati = new DataAccessHelper();
foreach (string zCas in zPropVal)
{
double zSumIndexNorm = 0;
try
{
zSumIndexNorm = zAccessoDati.GetSumIndexNorm(zCas);
}
catch
{
return;
}
zComponentsList.Add(zCas, zSumIndexNorm);
}
double zInCP;
double zInEP;
double zOutCP;
double zOutEP;
double MM;
MM = 0;
double[] zMolecularWeights;
zObj = (object[])InputPort.ConnectedObject.GetComponentConstant("molecularWeight", zIds);
zMolecularWeights = new double[zObj.GetLength(0)];
for (int i = 0; i < zObj.GetLength(0); i++)
{
zMolecularWeights[i] = (double)zObj[i];
}
//calculate of molecular weight of the stream
for (int i = 0; i < InputPort.ComponentsCount; i++)
{
MM = MM + zFraction[i] * zMolecularWeights[i];
}
double[] zFractionMasses = new double[InputPort.ComponentsCount];
for (int i = 0; i < InputPort.ComponentsCount; i++)
{
zFractionMasses[i] = zFraction[i] * zMolecularWeights[i] / MM;
}
StreamWriter zWriter;
if (ProcessTypeValue == 0.0)
{ //for process_type=0 calc impact
if (CapePositionValue == 0.0)
{ // ' if the stream is the begin of process
zInCP = 0;
double zIndividual0;
for (int r0 = 0; r0 < InputPort.ComponentsCount; r0++)
{
zIndividual0 = zTotmod * MM * zFraction[r0] * zComponentsList[zPropVal[r0]];
zInCP = zInCP + zIndividual0;
}
zWriter = new StreamWriter("WAR.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("value:" + zInCP.ToString());
zWriter.Close();
//' write the mass flow results
zWriter = new StreamWriter("stream.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
//' write all results
zWriter = new StreamWriter("results.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine(" value:" + zInCP.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
}
else if (CapePositionValue == 1.0)
{
double zIndividual1;
zOutCP = 0;
zWriter = new StreamWriter("stream_name_and_composition.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
for (int g0 = 0; g0 < InputPort.ComponentsCount; g0++)
{
zIndividual1 = zTotmod * MM * zFractionMasses[g0] * zComponentsList[zPropVal[g0]];
zOutCP = zOutCP + zIndividual1;
double zCompFlowRateWasteCp = zTotmod * MM * zFractionMasses[g0];
zWriter.WriteLine(zIds[g0]);
zWriter.WriteLine("comp.mass flow-rates=" + zCompFlowRateWasteCp.ToString());
}
zWriter.Close();
zWriter = new StreamWriter("WAR.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("value:" + zOutCP.ToString());
zWriter.Close();
//' write the mass flow results
zWriter = new StreamWriter("stream.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
zWriter = new StreamWriter("results.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine(" value:" + zOutCP.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
}
else if (CapePositionValue == 2.0)
{ //if the stream is the end of the process
zWriter = new StreamWriter("stream_name_and_composition.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
for (int u0 = 0; u0 < InputPort.ComponentsCount; u0++)
{
double zCompFlowRateWasteCp = zTotmod * MM * zFractionMasses[u0];
zWriter.WriteLine(zIds[u0]);
zWriter.WriteLine("comp.mass flow-rates=" + zCompFlowRateWasteCp.ToString());
}
zWriter.Close();
zWriter = new StreamWriter("WAR.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("value:output stream of the chemical process");
zWriter.Close();
//' write the mass flow results
zWriter = new StreamWriter("stream.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
zWriter = new StreamWriter("results.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine(" value:0");
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
}
else if (CapePositionValue == 3.0)
{ //if the stream is internal
zWriter = new StreamWriter("WAR.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("value:internal stream of the chemical process");
zWriter.Close();
//' write the mass flow results
zWriter = new StreamWriter("stream.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
zWriter = new StreamWriter("results.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine(" value:0");
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
}
}
if (ProcessTypeValue == 1.0)
{ //' for process_type=1 calc. the impactof process of generation of energy
if (CapePositionValue == 0.0)
{ // ' beginning of the process
zInEP = 0;
double zIndividual2;
for (int r1 = 0; r1 < InputPort.ComponentsCount; r1++)
{
zIndividual2 = zTotmod * MM * zFraction[r1] * zComponentsList[zPropVal[r1]];
zInEP = zInEP + zIndividual2;
}
zWriter = new StreamWriter("WAR.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("value:" + zInEP.ToString());
zWriter.Close();
//' write the mass flow results
zWriter = new StreamWriter("stream.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
//' write all results
zWriter = new StreamWriter("results.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine(" value:" + zInEP.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
}
else if (CapePositionValue == 1.0)
{//end of process
zWriter = new StreamWriter("stream_name_and_composition.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
for (int k0 = 0; k0 < InputPort.ComponentsCount; k0++)
{
double zCompFlowRateWasteEp = zTotmod * MM * zFractionMasses[k0];
zWriter.WriteLine(zIds[k0]);
zWriter.WriteLine("comp.mass flow-rates=" + zCompFlowRateWasteEp.ToString());
}
zWriter.Close();
//calculaction of the energy
StreamReader zReader = new StreamReader("ENERGY.txt");
string s = null;
while (!zReader.EndOfStream)
{
s = zReader.ReadLine();
}
zReader.Close();
s = s.Substring(s.Length - 15);
double zHProcess = Convert.ToDouble(s.Trim());
if (zHProcess < 0)
{
zOutEP = 0;
for (int g1 = 0; g1 < InputPort.ComponentsCount; g1++)
{
double zIndividual3 = zTotmod * MM * zFraction[g1] * zComponentsList[zPropVal[g1]];
zOutEP = zOutEP + zIndividual3;
}
zWriter = new StreamWriter("WAR.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("value:" + zOutEP.ToString());
zWriter.Close();
//' write the mass flow results
zWriter = new StreamWriter("stream.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
zWriter = new StreamWriter("results.txt", true, Encoding.UTF8);
zWriter.WriteLine(" ");
zWriter.WriteLine(" type:" + ProcessTypeValue.ToString());
zWriter.WriteLine(" name:CO" + CapeIDValue.ToString());
zWriter.WriteLine(" ind:" + CapePositionValue.ToString());
zWriter.WriteLine(" value:" + zOutEP.ToString());
zWriter.WriteLine("mass flow-rate:" + Convert.ToString(zTotmod * MM));
zWriter.Close();
}
else
{
}
}
}
//
//Output thermo material object
//
OutputPort.Temperature = zTemperature;
OutputPort.Pressure = zPressure;
OutputPort.Enthalpy = zEnthalpy;
OutputPort.TotalFlow = zTotalFlow;
OutputPort.Volume = zVolume;
OutputPort.Fraction = zFraction;
try
{
OutputPort.CalculateEquilibrium(CapeOpenFlashType.PH);
}
catch
{
}
}