void Init()
{
Padding = new Padding(10);
var mslist = flowsheet.SimulationObjects.Values.Where((x) => x.GraphicObject.ObjectType == ObjectType.MaterialStream).Select((x2) => x2.GraphicObject.Tag).ToList();
mslist.Insert(0, "");
this.CreateAndAddLabelRow("Setup");
this.CreateAndAddDescriptionRow("The True Critical Point utility calculates the True Critical Point of a mixture using the Peng-Robinson or Soave-Redlich-Kwong EOS.");
var spinner = this.CreateAndAddDropDownRow("Material Stream", mslist, 0, (arg3, arg2) => { });
var button = this.CreateAndAddButtonRow("Calculate", null, (arg3, arg2) => { });
this.CreateAndAddLabelRow("Results");
var txtResults = this.CreateAndAddMultilineMonoSpaceTextBoxRow("", 150, true, null);
button.Click += (sender, e) =>
{
if (spinner.SelectedIndex > 0)
{
var ms = (MaterialStream)flowsheet.GetFlowsheetSimulationObject(mslist[spinner.SelectedIndex]);
var calc = new DWSIM.Thermodynamics.ShortcutUtilities.Calculation(ms);
calc.CalcType = DWSIM.Thermodynamics.ShortcutUtilities.CalculationType.CriticalPoint;
DWSIM.Thermodynamics.ShortcutUtilities.CalculationResults results = null;
Task.Factory.StartNew(() =>
{
results = calc.Calculate();
}).ContinueWith((t) =>
{
Application.Instance.Invoke(() =>
{
if (results.ExceptionResult == null)
{
txtResults.Text = results.TextOutput;
}
else
{
txtResults.Text = results.ExceptionResult.Message;
}
});
});
}
};
}
void Init()
{
Padding = new Padding(10);
var su = flowsheet.FlowsheetOptions.SelectedUnitSystem;
var nf = flowsheet.FlowsheetOptions.NumberFormat;
var mslist = flowsheet.SimulationObjects.Values.Where((x) => x.GraphicObject.ObjectType == ObjectType.MaterialStream).Select((x2) => x2.GraphicObject.Tag).ToList();
mslist.Insert(0, "");
this.CreateAndAddDescriptionRow("The Phase Envelope utility calculates various VLE envelopes for mixtures.");
var spinner = this.CreateAndAddDropDownRow("Material Stream", mslist, 0, (arg3, arg2) => { });
var spinnerPE = this.CreateAndAddDropDownRow("Envelope Type", Shared.StringArrays.envelopetype().ToList(), 0, null);
var button = this.CreateAndAddButtonRow("Build Envelope", null, null);
var chart = new Eto.OxyPlot.Plot {
Height = 400, BackgroundColor = Colors.White
};
this.CreateAndAddControlRow(chart);
var txtResults = this.CreateAndAddMultilineMonoSpaceTextBoxRow("", 400, true, null);
button.Click += (sender, e) =>
{
if (spinnerPE.SelectedIndex >= 0 && spinner.SelectedIndex > 0)
{
var ms = (MaterialStream)flowsheet.GetFlowsheetSimulationObject(mslist[spinner.SelectedIndex]);
var calc = new DWSIM.Thermodynamics.ShortcutUtilities.Calculation(ms);
switch (spinnerPE.SelectedIndex + 1)
{
case 1:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopePT;
break;
case 2:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopePH;
break;
case 3:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopePS;
break;
case 4:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeTH;
break;
case 5:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeTS;
break;
case 6:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeVP;
break;
case 7:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeVT;
break;
}
DWSIM.Thermodynamics.ShortcutUtilities.CalculationResults results = null;
Task.Factory.StartNew(() =>
{
Application.Instance.Invoke(() => txtResults.Text = "Please wait...");
results = calc.Calculate();
}).ContinueWith((t) =>
{
Application.Instance.Invoke(() =>
{
if (results.ExceptionResult == null)
{
if (results.PlotModels.Count > 0)
{
chart.Model = (OxyPlot.PlotModel)results.PlotModels[0];
chart.Invalidate();
txtResults.Text = results.TextOutput;
}
else
{
chart.Model = null;
txtResults.Text = "Invalid result";
}
}
else
{
txtResults.Text = results.ExceptionResult.Message;
}
});
});
}
};
}
void Init()
{
Spacing = new Size(5, 5);
DynamicLayout p1;
TableLayout p2;
p1 = UI.Shared.Common.GetDefaultContainer();
p2 = new TableLayout()
{
Spacing = new Size(5, 5), Padding = new Padding(15)
};
Rows.Add(new TableRow(p1, p2));
p1.Width = 420;
var l1 = p1.CreateAndAddLabelRow("Envelope Setup");
var tabcontainer = new TabControl();
Eto.OxyPlot.Plot chart = null;
var su = flowsheet.FlowsheetOptions.SelectedUnitSystem;
var nf = flowsheet.FlowsheetOptions.NumberFormat;
var complist = flowsheet.SelectedCompounds.Values.Select((x2) => x2.Name).ToList();
complist.Insert(0, "");
p1.CreateAndAddDescriptionRow("The Binary Envelope utility calculates Temperature and Pressure VLE/VLLE envelopes for binary mixtures.");
var spinnerComp1 = p1.CreateAndAddDropDownRow("Compound 1", complist, 0, null);
var spinnerComp2 = p1.CreateAndAddDropDownRow("Compound 2", complist, 0, null);
var spinnerPE = p1.CreateAndAddDropDownRow("Envelope Type", Shared.StringArrays.binaryenvelopetype().ToList(), 1, null);
var tval = p1.CreateAndAddTextBoxRow(nf, "Temperature (" + su.temperature + ")", cv.ConvertFromSI(su.temperature, 298.15f), null);
var pval = p1.CreateAndAddTextBoxRow(nf, "Pressure (" + su.pressure + ")", cv.ConvertFromSI(su.pressure, 101325.0f), null);
bool vle = true, lle = false, sle = false, critical = false, areas = false;
p1.CreateAndAddLabelRow("Display Options");
p1.CreateAndAddCheckBoxRow("VLE", vle, (arg1a, arg2a) => { vle = arg1a.Checked.GetValueOrDefault(); });
p1.CreateAndAddDescriptionRow("VLE calculation works on all diagram types.");
p1.CreateAndAddCheckBoxRow("LLE", lle, (arg1a, arg2a) => { lle = arg1a.Checked.GetValueOrDefault(); });
p1.CreateAndAddDescriptionRow("LLE calculation works on T-x/y and P-x/y diagrams if the selected Property Package is associated with a Flash Algorithm which supports Liquid-Liquid equilibria.");
p1.CreateAndAddCheckBoxRow("SLE", sle, (arg1a, arg2a) => { sle = arg1a.Checked.GetValueOrDefault(); });
p1.CreateAndAddDescriptionRow("SLE calculation works on T-x/y diagrams only.");
p1.CreateAndAddCheckBoxRow("Critical Line", critical, (arg1a, arg2a) => { critical = arg1a.Checked.GetValueOrDefault(); });
p1.CreateAndAddDescriptionRow("Critical Line calculation works on T-x/y diagrams only.");
p1.CreateAndAddCheckBoxRow("Highlight Regions", areas, (arg1a, arg2a) => { areas = arg1a.Checked.GetValueOrDefault(); });
p1.CreateAndAddDescriptionRow("Highlights the different phase regions in the envelope.");
var pplist = flowsheet.PropertyPackages.Values.Select((x2) => x2.Tag).ToList();
pplist.Insert(0, "");
var spinnerpp = p1.CreateAndAddDropDownRow("Property Package", pplist, 0, null);
var button = p1.CreateAndAddButtonRow("Build Envelope", null, null);
chart = new Eto.OxyPlot.Plot {
BackgroundColor = Colors.White
};
var txtResults = new TextArea()
{
ReadOnly = true, Font = Fonts.Monospace(GlobalSettings.Settings.ResultsReportFontSize)
};
tabcontainer.Pages.Add(new TabPage(new TableRow(chart))
{
Text = "Chart"
});
tabcontainer.Pages.Add(new TabPage(new TableRow(txtResults))
{
Text = "Data"
});
p2.CreateAndAddLabelRow("Results");
p2.CreateAndAddControlRow(tabcontainer);
button.Click += (sender, e) =>
{
if (spinnerPE.SelectedIndex >= 0 && spinnerComp1.SelectedIndex > 0 && spinnerComp2.SelectedIndex > 0 && spinnerpp.SelectedIndex > 0)
{
var comp1 = flowsheet.SelectedCompounds[complist[spinnerComp1.SelectedIndex]];
var comp2 = flowsheet.SelectedCompounds[complist[spinnerComp2.SelectedIndex]];
var ms = new MaterialStream("", "");
ms.SetFlowsheet(flowsheet);
ms.PropertyPackage = (PropertyPackage)flowsheet.PropertyPackages.Values.Where(x => x.Tag == spinnerpp.SelectedValue.ToString()).First();
ms.SetFlowsheet(flowsheet);
foreach (var phase in ms.Phases.Values)
{
phase.Compounds.Add(comp1.Name, new DWSIM.Thermodynamics.BaseClasses.Compound(comp1.Name, ""));
phase.Compounds[comp1.Name].ConstantProperties = comp1;
phase.Compounds.Add(comp2.Name, new DWSIM.Thermodynamics.BaseClasses.Compound(comp2.Name, ""));
phase.Compounds[comp2.Name].ConstantProperties = comp2;
}
double val;
if (Double.TryParse(tval.Text, out val))
{
ms.Phases[0].Properties.temperature = cv.ConvertToSI(su.temperature, Double.Parse(tval.Text));
}
if (Double.TryParse(pval.Text, out val))
{
ms.Phases[0].Properties.pressure = cv.ConvertToSI(su.pressure, Double.Parse(pval.Text));
}
var calc = new DWSIM.Thermodynamics.ShortcutUtilities.Calculation(ms);
calc.DisplayEnvelopeAreas = areas;
calc.BinaryEnvelopeOptions = new object[] { "", 0, 0, vle, lle, sle, critical, false };
switch (spinnerPE.SelectedIndex)
{
case 0:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.BinaryEnvelopePxy;
break;
case 1:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.BinaryEnvelopeTxy;
break;
}
DWSIM.Thermodynamics.ShortcutUtilities.CalculationResults results = null;
var token = new System.Threading.CancellationTokenSource();
var pg = ProgressDialog.ShowWithAbort(this, "Please Wait", "Calculating Envelope Lines...", false, "Abort/Cancel", (s, e1) => {
token.Cancel();
});
Task.Factory.StartNew(() =>
{
Application.Instance.Invoke(() =>
{
txtResults.Text = "Please wait...";
});
results = calc.Calculate();
}, token.Token).ContinueWith((t) =>
{
Application.Instance.Invoke(() =>
{
pg.Close();
pg = null;
if (results.ExceptionResult == null)
{
if (results.PlotModels.Count > 0)
{
chart.Model = (OxyPlot.PlotModel)results.PlotModels[0];
chart.Model.Padding = new OxyPlot.OxyThickness(5, 5, 20, 5);
chart.Invalidate();
txtResults.Text = results.TextOutput;
}
else
{
chart.Model = null;
txtResults.Text = "Invalid result";
}
}
else
{
txtResults.Text = results.ExceptionResult.Message;
}
});
});
}
};
}
void Init()
{
Spacing = new Size(5, 5);
DynamicLayout p1;
TableLayout p2;
p1 = UI.Shared.Common.GetDefaultContainer();
p2 = new TableLayout()
{
Spacing = new Size(5, 5), Padding = new Padding(15)
};
Rows.Add(new TableRow(p1, p2));
p1.Width = 420;
var su = flowsheet.FlowsheetOptions.SelectedUnitSystem;
var nf = flowsheet.FlowsheetOptions.NumberFormat;
var mslist = flowsheet.SimulationObjects.Values.Where((x) => x.GraphicObject.ObjectType == ObjectType.MaterialStream).Select((x2) => x2.GraphicObject.Tag).ToList();
mslist.Insert(0, "");
p1.CreateAndAddLabelRow("Setup");
p1.CreateAndAddDescriptionRow("The Phase Envelope utility calculates various VLE envelopes for mixtures.");
var spinner = p1.CreateAndAddDropDownRow("Material Stream", mslist, 0, (arg3, arg2) => { });
var spinnerPE = p1.CreateAndAddDropDownRow("Envelope Type", Shared.StringArrays.envelopetype().ToList(), 0, null);
var EnvelopeOptions = new PhaseEnvelopeOptions();
var ft = new List <string>()
{
"PVF", "TVF"
};
var tabcontainer0 = new TabControl()
{
};
var c1 = UI.Shared.Common.GetDefaultContainer();
var c3 = UI.Shared.Common.GetDefaultContainer();
var c2 = UI.Shared.Common.GetDefaultContainer();
c1.CreateAndAddCheckBoxRow("Quality Line", EnvelopeOptions.QualityLine, (arg3, arg1) => { EnvelopeOptions.QualityLine = arg3.Checked.GetValueOrDefault(); });
c1.CreateAndAddDescriptionRow("Includes a Quality Line in the chart (TP only).");
c1.CreateAndAddTextBoxRow("G6", "Quality Value", EnvelopeOptions.QualityValue, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.QualityValue = arg3.Text.ToDoubleFromCurrent();
}
});
c1.CreateAndAddDescriptionRow("Vapor Phase Mole Fraction for Quality Line, between 0.0 and 1.0.");
c1.CreateAndAddCheckBoxRow("Stability Curve", EnvelopeOptions.StabilityCurve, (arg3, arg1) => { EnvelopeOptions.StabilityCurve = arg3.Checked.GetValueOrDefault(); });
c1.CreateAndAddDescriptionRow("Includes the Stability Curve in the chart (TP only). Works with PR and SRK Property Packages.");
c1.CreateAndAddCheckBoxRow("Phase Identification Curve", EnvelopeOptions.PhaseIdentificationCurve, (arg3, arg1) => { EnvelopeOptions.PhaseIdentificationCurve = arg3.Checked.GetValueOrDefault(); });
c1.CreateAndAddDescriptionRow("Calculates the PI curve (TP only), where the region above the curve is for a liquid-like phase and the region beyond the curve is for a vapor-like phase. Calculated using the PR EOS.");
c1.CreateAndAddCheckBoxRow("Operation Point", EnvelopeOptions.OperatingPoint, (arg3, arg1) => { EnvelopeOptions.OperatingPoint = arg3.Checked.GetValueOrDefault(); });
c1.CreateAndAddDescriptionRow("Includes the operating point in the chart.");
c2.CreateAndAddCheckBoxRow("Custom Initialization", EnvelopeOptions.BubbleUseCustomParameters, (arg3, arg1) => { EnvelopeOptions.BubbleUseCustomParameters = arg3.Checked.GetValueOrDefault(); });
c2.CreateAndAddDescriptionRow("Use the custom initialization options if the generated curve for bubble points has invalid points.");
c2.CreateAndAddDropDownRow("Initial Flash", ft, 0, (arg3, arg1) => { EnvelopeOptions.BubbleCurveInitialFlash = ft[arg3.SelectedIndex]; });
c2.CreateAndAddTextBoxRow("G6", "Initial Pressure (" + su.pressure + ")", EnvelopeOptions.BubbleCurveInitialPressure, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.BubbleCurveInitialPressure = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.pressure);
}
});
c2.CreateAndAddTextBoxRow("G6", "Initial Temperature (" + su.temperature + ")", EnvelopeOptions.BubbleCurveInitialTemperature, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.BubbleCurveInitialTemperature = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.pressure);
}
});
c2.CreateAndAddTextBoxRow("G6", "Maximum Temperature (" + su.temperature + ")", EnvelopeOptions.BubbleCurveMaximumTemperature, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.BubbleCurveMaximumTemperature = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.pressure);
}
});
c2.CreateAndAddTextBoxRow("G6", "Pressure Step (" + su.deltaP + ")", EnvelopeOptions.BubbleCurveDeltaP, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.BubbleCurveDeltaP = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.deltaP);
}
});
c2.CreateAndAddTextBoxRow("G6", "Temperature Step (" + su.deltaT + ")", EnvelopeOptions.BubbleCurveDeltaT, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.BubbleCurveDeltaT = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.deltaT);
}
});
c2.CreateAndAddTextBoxRow("N0", "Maximum Points", EnvelopeOptions.BubbleCurveMaximumPoints, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.BubbleCurveMaximumPoints = int.Parse(arg3.Text);
}
});
c3.CreateAndAddCheckBoxRow("Custom Initialization", EnvelopeOptions.DewUseCustomParameters, (arg3, arg1) => { EnvelopeOptions.DewUseCustomParameters = arg3.Checked.GetValueOrDefault(); });
c3.CreateAndAddDescriptionRow("Use the custom initialization options if the generated curve for dew points has invalid points.");
c3.CreateAndAddDropDownRow("Initial Flash", ft, 0, (arg3, arg1) => { EnvelopeOptions.DewCurveInitialFlash = ft[arg3.SelectedIndex]; });
c3.CreateAndAddTextBoxRow("G6", "Initial Pressure (" + su.pressure + ")", EnvelopeOptions.DewCurveInitialPressure, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.DewCurveInitialPressure = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.pressure);
}
});
c3.CreateAndAddTextBoxRow("G6", "Initial Temperature (" + su.temperature + ")", EnvelopeOptions.DewCurveInitialTemperature, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.DewCurveInitialTemperature = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.pressure);
}
});
c3.CreateAndAddTextBoxRow("G6", "Maximum Temperature (" + su.temperature + ")", EnvelopeOptions.DewCurveMaximumTemperature, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.DewCurveMaximumTemperature = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.pressure);
}
});
c3.CreateAndAddTextBoxRow("G6", "Pressure Step (" + su.deltaP + ")", EnvelopeOptions.DewCurveDeltaP, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.DewCurveDeltaP = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.deltaP);
}
});
c3.CreateAndAddTextBoxRow("G6", "Temperature Step (" + su.deltaT + ")", EnvelopeOptions.DewCurveDeltaT, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.DewCurveDeltaT = arg3.Text.ToDoubleFromCurrent().ConvertToSI(su.deltaT);
}
});
c3.CreateAndAddTextBoxRow("N0", "Maximum Points", EnvelopeOptions.DewCurveMaximumPoints, (arg3, arg1) => { if (arg3.Text.IsValidDouble())
{
EnvelopeOptions.DewCurveMaximumPoints = int.Parse(arg3.Text);
}
});
tabcontainer0.Pages.Add(new TabPage(new TableRow(c1))
{
Text = "Envelope Options"
});
tabcontainer0.Pages.Add(new TabPage(new TableRow(c2))
{
Text = "BP Initialization"
});
tabcontainer0.Pages.Add(new TabPage(new TableRow(c3))
{
Text = "DP Initialization"
});
p1.CreateAndAddControlRow(tabcontainer0);
var button = p1.CreateAndAddButtonRow("Build Envelope", null, null);
p1.CreateAndAddEmptySpace();
p1.CreateAndAddEmptySpace();
var tabcontainer = new TabControl()
{
Height = 400
};
var chart = new Eto.OxyPlot.Plot {
BackgroundColor = Colors.White
};
var txtResults = new TextArea()
{
ReadOnly = true, Font = Fonts.Monospace(GlobalSettings.Settings.ResultsReportFontSize)
};
tabcontainer.Pages.Add(new TabPage(new TableRow(chart))
{
Text = "Chart"
});
tabcontainer.Pages.Add(new TabPage(new TableRow(txtResults))
{
Text = "Data"
});
p2.CreateAndAddLabelRow("Results");
p2.CreateAndAddControlRow(tabcontainer);
button.Click += (sender, e) =>
{
if (spinnerPE.SelectedIndex >= 0 && spinner.SelectedIndex > 0)
{
var ms = (MaterialStream)flowsheet.GetFlowsheetSimulationObject(mslist[spinner.SelectedIndex]);
var calc = new DWSIM.Thermodynamics.ShortcutUtilities.Calculation(ms);
switch (spinnerPE.SelectedIndex + 1)
{
case 1:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopePT;
break;
case 2:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopePH;
break;
case 3:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopePS;
break;
case 4:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeTH;
break;
case 5:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeTS;
break;
case 6:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeVP;
break;
case 7:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.PhaseEnvelopeVT;
break;
}
calc.PhaseEnvelopeOptions = EnvelopeOptions;
DWSIM.Thermodynamics.ShortcutUtilities.CalculationResults results = null;
var token = new System.Threading.CancellationTokenSource();
var pg = ProgressDialog.ShowWithAbort(this, "Please Wait", "Calculating Envelope Lines...", false, "Abort/Cancel", (s, e1) => {
token.Cancel();
});
Task.Factory.StartNew(() =>
{
Application.Instance.Invoke(() => txtResults.Text = "Please wait...");
results = calc.Calculate();
}, token.Token).ContinueWith((t) =>
{
Application.Instance.Invoke(() =>
{
pg.Close();
pg = null;
if (results.ExceptionResult == null)
{
if (results.PlotModels.Count > 0)
{
chart.Model = (OxyPlot.PlotModel)results.PlotModels[0];
chart.Model.Padding = new OxyPlot.OxyThickness(5, 5, 20, 5);
chart.Invalidate();
txtResults.Text = results.TextOutput;
}
else
{
chart.Model = null;
txtResults.Text = "Invalid result";
}
}
else
{
txtResults.Text = results.ExceptionResult.Message;
}
});
});
}
};
}
void Init()
{
Padding = new Padding(10);
var su = flowsheet.FlowsheetOptions.SelectedUnitSystem;
var nf = flowsheet.FlowsheetOptions.NumberFormat;
var complist = flowsheet.SelectedCompounds.Values.Select((x2) => x2.Name).ToList();
complist.Insert(0, "");
this.CreateAndAddLabelRow("Setup");
this.CreateAndAddDescriptionRow("The Binary Envelope utility calculates Temperature and Pressure VLE/VLLE envelopes for binary mixtures.");
var spinnerComp1 = this.CreateAndAddDropDownRow("Compound 1", complist, 0, null);
var spinnerComp2 = this.CreateAndAddDropDownRow("Compound 2", complist, 0, null);
var spinnerPE = this.CreateAndAddDropDownRow("Envelope Type", Shared.StringArrays.binaryenvelopetype().ToList(), 0, null);
var tval = this.CreateAndAddTextBoxRow(nf, "Temperature (" + su.temperature + ")", cv.ConvertFromSI(su.temperature, 298.15f), null);
var pval = this.CreateAndAddTextBoxRow(nf, "Pressure (" + su.pressure + ")", cv.ConvertFromSI(su.pressure, 101325.0f), null);
var pplist = flowsheet.PropertyPackages.Values.Select((x2) => x2.Tag).ToList();
pplist.Insert(0, "");
var spinnerpp = this.CreateAndAddDropDownRow("Property Package", pplist, 0, null);
var button = this.CreateAndAddButtonRow("Build Envelope", null, null);
var tabcontainer = new TabControl()
{
Height = 400
};
var chart = new Eto.OxyPlot.Plot {
BackgroundColor = Colors.White
};
var txtResults = new TextArea()
{
ReadOnly = true, Font = Fonts.Monospace(GlobalSettings.Settings.ResultsReportFontSize)
};
tabcontainer.Pages.Add(new TabPage(new TableRow(txtResults))
{
Text = "Data"
});
tabcontainer.Pages.Add(new TabPage(new TableRow(chart))
{
Text = "Chart"
});
this.CreateAndAddLabelRow("Results");
this.CreateAndAddControlRow(tabcontainer);
button.Click += (sender, e) =>
{
if (spinnerPE.SelectedIndex >= 0 && spinnerComp1.SelectedIndex > 0 && spinnerComp2.SelectedIndex > 0 && spinnerpp.SelectedIndex > 0)
{
var comp1 = flowsheet.SelectedCompounds[complist[spinnerComp1.SelectedIndex]];
var comp2 = flowsheet.SelectedCompounds[complist[spinnerComp2.SelectedIndex]];
var ms = new MaterialStream("", "");
ms.SetFlowsheet(flowsheet);
ms.PropertyPackage = (PropertyPackage)flowsheet.PropertyPackages.Values.Where(x => x.Tag == spinnerpp.SelectedValue.ToString()).First();
ms.SetFlowsheet(flowsheet);
foreach (var phase in ms.Phases.Values)
{
phase.Compounds.Add(comp1.Name, new DWSIM.Thermodynamics.BaseClasses.Compound(comp1.Name, ""));
phase.Compounds[comp1.Name].ConstantProperties = comp1;
phase.Compounds.Add(comp2.Name, new DWSIM.Thermodynamics.BaseClasses.Compound(comp2.Name, ""));
phase.Compounds[comp2.Name].ConstantProperties = comp2;
}
double val;
if (Double.TryParse(tval.Text, out val))
{
ms.Phases[0].Properties.temperature = cv.ConvertToSI(su.temperature, Double.Parse(tval.Text));
}
if (Double.TryParse(pval.Text, out val))
{
ms.Phases[0].Properties.pressure = cv.ConvertToSI(su.pressure, Double.Parse(pval.Text));
}
var calc = new DWSIM.Thermodynamics.ShortcutUtilities.Calculation(ms);
switch (spinnerPE.SelectedIndex)
{
case 0:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.BinaryEnvelopePxy;
break;
case 1:
calc.CalcType = Thermodynamics.ShortcutUtilities.CalculationType.BinaryEnvelopeTxy;
break;
}
DWSIM.Thermodynamics.ShortcutUtilities.CalculationResults results = null;
Task.Factory.StartNew(() =>
{
Application.Instance.Invoke(() => txtResults.Text = "Please wait...");
results = calc.Calculate();
}).ContinueWith((t) =>
{
Application.Instance.Invoke(() =>
{
if (results.ExceptionResult == null)
{
if (results.PlotModels.Count > 0)
{
chart.Model = (OxyPlot.PlotModel)results.PlotModels[0];
chart.Invalidate();
txtResults.Text = results.TextOutput;
}
else
{
chart.Model = null;
txtResults.Text = "Invalid result";
}
}
else
{
txtResults.Text = results.ExceptionResult.Message;
}
});
});
}
};
}
