Methods The methods defined in this interface are devised around flash calculations. The correct calling sequence should be that 1) define feed streams; 2) execute a proper flash calculation; 3) retrieve calculation results. The user can redefine feed stream if multiple streams need to be flashed. For a defined feed stream, the user can also call different flash calculations. After each flash calculation is converged, the calculated data (liquid and vapor stream, etc.) can only be retrieved once.
Before calling the methods, user need to declare component array in VBA macro. The lower bound of a component array has to be one, and the upper bound should be no less than the actual number of components. All the units of the arguments on the methods of this interface are CHEMCAD internal units.
Method GetNoOfComponents
Returns count of components in current job
Method DefineFeedStream
Returns number of flowrates received from compFlowLbmol_Hr
Argument |
Type |
Description |
tempR presPsia enthBtu_Hr compFlowLbmol_Hr |
float float float float[] |
Temperature (R) [in] Pressure (psia) [in] Enthalpy (Btu/hr) [in] Component flowrates (lbmol/hr) [in] |
HP flash at given enthalpy and pressure is carried out through the following method.
Method CalculateHPFlash
Return convergence of the flash routine (0 – converge, 1 – diverge)
Argument |
Type |
Description |
presPsia enthBtu_Hr |
float float |
Pressure (psia) [in] Enthalpy (Btu/hr) [in] |
TP flash at specified temperature and pressure is carried out by the next method.
Method CalculateTPFlash
Return convergence of the flash routine (0 – converge, 1 – diverge)
Argument |
Type |
Description |
tempR presPsia |
float float |
Temperature (R) [in] Pressure (psia) [in] |
VP flash at specified mole vapor fraction and pressure is called through CalculateVPFlash. This method can also calculate bubble point temperature if mole vapor fraction is 0, and dew point temperature if mole vapor fraction if 1.
Method CalculateVPFlash
Returns convergence of the flash routine (0 – converge, 1 – diverge)
Argument |
Type |
Description |
presPsia moleVapFrac |
float float |
Pressure (psia) [in] Mole vapor fraction [in] |
VT flash at specified mole vapor fraction and temperature is called in CalculateVTFlash. This method can also calculate bubble point pressure if mole vapor fraction is 0, and dew point pressure if mole vapor fraction if 1.
Method CalculateVTFlash
Returns convergence of the flash routine (0 – converge, 1 – diverge)
Argument |
Type |
Description |
tempR moleVapFrac |
float float |
Temperature (R) [in] Mole vapor fraction [in] |
After a flash calculation has converged, the following methods can be called to retrieve calculation data.
Method GetVaporStream / GetLiquidStream
Returns number of data items returned in array compFlowLbmol_Hr
Argument |
Type |
Description |
tempR presPsia enthBtu_Hr rateLbmol_Hr compFlowLbmol_Hr |
float float float float float[] |
Temperature (R) [out] Pressure (psia) [out] Enthalpy (Btu/hr) [out] Total mole rate (lbmol/hr) [out} Component flowrates (lbmol/hr) [out] |
Method GetKValues
Returns number of data items returned in array kValues
Argument |
Type |
Description |
kValues |
float[] |
Calculated k-values [out] |
Method GetIonRates
Returns number of data items returned in array ionFlowLbmol_Hr
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