WangHenkeMethod2Solve Method

public Object Solve(
	Column rc,
	int nc,
	int ns,
	int maxits,
	double[] tol,
	double[] F,
	double[] V,
	double[] Q,
	double[] L,
	double[] VSS,
	double[] LSS,
	double[][] Kval,
	double[][] x,
	double[][] y,
	double[][] z,
	double[][] fc,
	double[] HF,
	double[] T,
	double[] P,
	Columncondtype condt,
	int stopatitnumber,
	double[] eff,
	ColumnColType coltype,
	PropertyPackage pp,
	Dictionary<string, ColumnSpec> specs,
	bool IdealK,
	bool IdealH
)

Public Function Solve ( 
	rc As Column,
	nc As Integer,
	ns As Integer,
	maxits As Integer,
	tol As Double(),
	F As Double(),
	V As Double(),
	Q As Double(),
	L As Double(),
	VSS As Double(),
	LSS As Double(),
	Kval As Double()(),
	x As Double()(),
	y As Double()(),
	z As Double()(),
	fc As Double()(),
	HF As Double(),
	T As Double(),
	P As Double(),
	condt As Columncondtype,
	stopatitnumber As Integer,
	eff As Double(),
	coltype As ColumnColType,
	pp As PropertyPackage,
	specs As Dictionary(Of String, ColumnSpec),
	IdealK As Boolean,
	IdealH As Boolean
) As Object

Parameters

rc  Column

The rigorous column object being solved.

nc  Int32

Number of chemical components.

ns  Int32

Number of equilibrium stages (0-based).

maxits  Int32

Maximum number of outer iterations.

tol  Double

Convergence tolerance array.

F  Double

Feed molar flow rate for each stage (mol/s).

V  Double

Initial vapour molar flow rate profile (mol/s).

Q  Double

Stage heat duty profile (kW).

L  Double

Initial liquid molar flow rate profile (mol/s).

VSS  Double

Vapour side-stream draw-off rates (mol/s).

LSS  Double

Liquid side-stream draw-off rates (mol/s).

Kval  Double

Initial K-value matrix (stage × component).

x  Double

Initial liquid mole-fraction matrix (stage × component).

y  Double

Initial vapour mole-fraction matrix (stage × component).

z  Double

Feed composition matrix (stage × component).

fc  Double

Feed component molar flow matrix (stage × component).

HF  Double

Feed molar enthalpy for each stage (kJ/mol).

T  Double

Initial temperature profile (K).

P  Double

Pressure profile (Pa).

condt  Columncondtype

The condenser type (total, partial, or full reflux).

stopatitnumber  Int32

Iteration number at which to pause (0 = run to completion).

eff  Double

Murphree tray efficiency for each stage.

coltype  ColumnColType

The column type (distillation, absorption, etc.).

pp  PropertyPackage

Property package used for thermodynamic calculations.

specs  DictionaryString, ColumnSpec

Column specifications (condenser and reboiler specs).

IdealK  Boolean

If True, use ideal (Raoult) K-values.

IdealH  Boolean

If True, use ideal enthalpies.

Return Value

Reference