Component 39: Controller with internal target value

In This Topic

Component 39: Controller with internal target value

Specifications

Line connections
1	Actual value - process value
2	Controlled value

The colour indicates the type of activation of the controller (depending upon the flag FACT):

Dark purple: the controller starts immediately

Red: delayed start after 20, 30, 40 or 50 iterations

Pink: delayed start after 100 iterations

White: the controller is disabled

General User Input Values Characteristic Lines Physics Used Displays Example

General

Component 39 is the simplest controller in EBSILON^®Professional. It differs from component 12 by not having a connection for the target value. For this reason, component 39 can be used only when the target value is constant. Details of controlling are described in Component 12.

A start value has to be specified for the controlled value, either internally as the specification value or externally via the component 33 (start value).

The start value should be at least in the order of magnitude of the expected value and not several powers of ten off. The recommended procedure is to get the model running without a controller first, then you will get suitable start values.

Component 39 can also be used for simple optimization tasks. To do this, the field SCV (scheduled value) is left blank. The controller then assumes that this value should be as high as possible. However, this feature functions only when the defaults are selected very carefully. The controller thereby requires (as normal) a monotonous relationship between the actual value and the correction value. The controlling stops when this monotony is violated. Therefore, basically one can find only the next local maximum. This feature is implemented as follows: starting from the 11th iteration step, the scheduled value is set to the (1+CHL3)-times of the actual value. If the actual value now increases, the scheduled value increases further. If the actual value reduces, the controller is disabled (and then remains so).

Controllers can be dampened even more. For this, three more damping levels ("very very high", "higher", "extremely high") have been introduced.

The sequence of the specification values in the input screen has been sorted. First are the specification values that relate to the reference value, and then the values that relate to the correction variable. Then follow general controller parameters like characteristic, activation, start value specification, and damping or limitation of change.

Decoupling of turn-on/-off feature and delayed start
The flag FACT served both to turn a controller on and off, and to specify a delayed start. In order to be able to better expand the setting options, this feature has been distributed to the two flags FACT and FFU.
The flag FACT is used to specify at which iteration step the controller is to start (at the earliest). FACT=0 means that the controller is to start as early as possible. The previous variants FACT=-1 and FACT=-2 for deactivating the controller with (-1) and without (-2) start value setting respectively have been marked as “deprecated“, but they are still operational for reasons of compatibility. However, it is recommended to use the new flag FFU for this purpose.
The flag FFU offers various variants for activating and deactivating controllers in different load cases. There are the following setting options:

• Controller active
   - always: FFU=1
   - only in design case: FFU=4 or -4
   - only in off-design case: FFU=5 or -5
   - never: FFU=0 or -1

• Controller not active (i.e. does not control) but sets its start value
   - always: FFU=0
   - only in design case: FFU=5
   - only in off-design case: FFU=4

• Controller not active, without start value setting
   - always: FFU=-1
   - only in design case: FFU=-5
   - only in off-design case: FFU=-4

Alternative start value in the case of deactivated controller:
The start value one wants to set with deactivated controller is not always suitable as start value in the case of activated controller (e.g. 0 kg/s). Previously one had to set different start values in different profiles then. There is an alternative start value L2STARTOFF (Component 39) and L3STARTOFF (Components 12 and 69) respectively for this. It is used when the controller is deactivated but is to set its start value. If no value is entered here, L2START and L3START respectively will be used also in the case of deactivated controller.

Compliance with limits:

The limits L2MIN/L2MAX (Component 39) and L3MIN/L3MAX (Component 12, Component 69) respectively were not strictly adhered to, but only caused the controller to be deactivated when the respective limit was exceeded. This mainly served to prevent a drifting off in the course of the iteration. For the final result, however, this behaviour is unsatisfactory as the precise achieved value depends on the behaviour of the iteration.
For this reason, the limits are strictly complied with. For reasons of compatibility, however, it is possible to switch back to the old behaviour via the flag FLIM. For this, FLIM has to be set to 0 (“Shut off controller after limit was exceeded“). The standard setting is FLIM=1 (“Stop at limit“).

Functionality of the limits

The limits L3MIN/L3MAX (Component 12, Component 69) and L2MIN/L2MAX (Component 39) only become effective if numerical values are specified for them.

If that is the case, the flag FLIM checks according to the specification with
FLIM=0: the controller is switched off after the limit L3MIN/L3MAX is fallen below / transgressed
or with
FLIM=1: the controller stops on the limit L3MIN/L3MAX.

Deactivation of warnings:
A warning is issued by default when the controller cannot achieve its target value. In some cases, however, this is unnecessary, e.g. when, in the case of an injection, the inlet temperature is already below the set point temperature. In such cases it is possible to shut off the warning with the flag FWARN.
The flag FWARNOFF allows to activate or deactivate warnings for deactivated controllers. Here it is checked if the start value (in the case of component 69 also the off-value L3OFF) is within the range of validity.

Start Value Transfer In controllers (FMODE)

(Components 12, 39, and 69) it is possible to take over the result for the control variable as start value for the next calculation. As there is a certain analogy with respect to the transfer of the reference values for off-design calculations here, the flag for this has been named FMODE as well. The following settings exist:

FMODE=1: no transfer
FMODE=0: transfer for design calculation
FMODE=-1: transfer for every calculation

The transferred value is written onto the specification values L2START and L2STARTOFF. However, it only has an impact if FL2START is set to “internal start value specification“. Also, the transfer only takes place if a value was entered into L2START respectively before. If the field has been set to the “empty”, the field will remain empty. When adding new controllers, FMODE=1 will be set by default. This is consistent with the previous behaviour. In a good modeling, the final result should in fact not (or only slightly) depend on the start value, but a change of the start value may lead to convergence problems. An influence on the final result also arises from the interaction of controllers with threshold values and limit values if it depends on the convergence behaviour when a controller is activated and deactivated respectively.

Flag FWARN

In the controllers there is a flag FWARN that allows setting in which situations the controller is to output warnings. For this there is a new setting FWARN=3.
With this setting, a warning is only output if the controller has not reached its target but the control variable has not reached its limit value either.

This setting makes sense if reaching the limit value represents a “normal” condition, like e.g. in the case of an injection where a certain temperature is to be set downstream
of the injection. By the injection, however, only a reduction of the temperature can be effected. If the temperature is below this set point value, nothing needs to be injected.
FWARN=3 allows to set that in this case no warning is to be effected. The control variable of the controller then equals the lower limit value of 0 kg/s, and no warning is output
if the set point value of the temperature has not been reached.

It is possible to output an error message instead of a warning with the setting FWARN=4.

FWARN=5 allows to individually program in a Kernel expression EWARN under which circumstances a comment, a warning or an error message is to be output.

Set Point Specification via Kernel Expressions

For the controllers that have the option for an internal set point specification (target value or scheduled value, Components 39 and 69) a Kernel expression ESCV can be used as an alternative to the specification value SCV. The control is affected via the flag FSCV:

• FSCV=0: the specification value SCV is used as set point value

• FSCV=1: (only for Component 69)

• FSCV=2: the set point value is determined from the Kernel expression ESCV.

Please note: as the set point value is usually a variable with units and – in contrast to the simple specification value – no automatic unit conversion can be carried out in the case of Kernel expressions, the value must be calculated in standard Ebsilon units.

Control Precision

For the solution of an equation system, Ebsilon continues the iteration as long as the changes from one iteration step to the next are smaller than the specified iteration precision.
Here the termination of the iteration is independent of to what extent the controllers have reached their set point value. Only a warning will be output if the deviation between
actual value and set point value is too great.

In the case of strongly damped controllers in particular, the change from one iteration step to the next is relatively small, so that the convergence criterion is already fulfilled although
the control target has not been achieved yet. In these cases it would be desirable if the iteration were continued for another couple of steps in order to get closer to the specified target.
It was therefore created the possibility to prevent a termination of the iteration in the case of too great a deviation from the set point value has been created.

Inversely, there are also cases where the adjustment of an unimportant variable requires very many iteration steps and thus increases the computing time for the entire model. In such
cases it is desirable to be able to carry out the control with a greater fuzziness.

This option is available with the specification value TOL (for all controllers).

The specification value TOL is used for setting the control precision in both cases. Which one of the two cases is desired is set via the flag FTOL:

FTOL=1 (“TOL=lower bound“) serves to accelerate the control by means of a greater fuzziness. In this case, the controller terminates the control if the relative deviation between actual
value and set point value falls below the bound TOL.

FTOL=2 (“TOL=upper bound“) prevents the termination of the iteration as long as the relative deviation between actual value and set point value transgresses the bound TOL. However,
this does not apply if the correction variable has reached its lower or upper bound. As the controller does not continue operating in this case, carrying out further iteration steps does
not make sense.

For analyzing the convergence behaviour, in the case FTOL=2 you can see in the result value ITNOTCONV up to which iteration step the controller has prevented a termination of the
iteration. This allows to systematically find out the controllers that are responsible for a deterioration of the convergence behaviour and to improve their settings if necessary.

FTOL=0 is the default setting.

Zero point Shift

As in the case of controllers in Ebsilon the change of the actuating variable is effected via a change factor, controllers previously could not be operated in such a way that the actuating variable was able to change its algebraic sign. To enable this, there is now a specification value CZP that serves to shift the zero point of the controller internally. Shifting is effected in positive direction. If e.g. “100“ is entered, -100 will be mapped onto 0 and it will also be possible to control beyond 0 in the range >-100.

With great values of CZP, the internal actuating variable will become great accordingly so that this way, in the case of similar relative changes, the absolute change of the actuating variable will become very great too. This may lead to convergence problems. In this case, it is recommended to decrease the maximum change factor (CHL2respectively), and that from the beginning ( ITCHL2 = 0 respectively).

Kernel Expressions for Range Limits

Previously, only fixed values could be entered as range limits for the actuating variable. Now it is possible to use a Kernel expression as the limit. To do so, the corresponding flag (FL2MIN and FL2MAX respectively for Components 12 and 69) has to be set to “Kernel expression“, and an EbsScript that calculates the corresponding limit has to be created in EL2MIN and EL2MAX respectively for Components 12 and 69.

This feature was needed for the variation of the steam inlet pressure for a preheater in order to achieve a certain feed water outlet temperature. Without limitation, the controller decreased the pressure so far that the saturated water temperature dropped below the feed water inlet temperature and no condensation was possible anymore. A fixed limit, however, was not possible either as the feed water inlet temperature is not known in advance but only appears in the course of the calculation. For instance, the following Kernel expression allows to set the lower pressure limit to a reasonable value in each iteration step:

function evalexpr:REAL;

begin

evalexpr:=waterSteamTable(1006, Feedwater.T, 0.0);

end;

Note - Setting a relative humidity of 100% or super saturation in air and flue gas lines

To a relative humidity of z. For example, to set 100% or super saturation, a controller is required.

In the previous handling with the function "air humidity (rel.)", It could happen after iteration course that the air was supersaturated, i. Water contained in the liquid phase. The reason for this was that even with supersaturated air, the relative humidity remained at the value of 100% and the controller had thus reached its set point.

In order to allow a regulation to the saturation point (100%) or the setting of a certain super saturation, there is a function "saturation factor".

The saturation factor always refers to the maximum possible proportion of gaseous water. If the water content is higher, you get liquid water XH2OL. Humid air can only be considered approximately as an ideal gas. With increasing water content, the real proportion of gaseous water XH2OG decreases again. In the ideal approximation, the proportion of gaseous water would then simply remain constant, no matter how much liquid water would add to it. In reality, that's probably not the case
and therefore with supersaturated air:

XH2OG> X_SAT = f (p, t (air outlet line))

For values up to 100%, the results of the "Saturation factor" function are the same as those of the "Humidity (rel.)" Function.

Definition Saturation factor for "saturated air" 0 - 100%: The result values agree with the results of the "relative humidity" function.

Definition saturation factor for "supersaturated air"> 100% = corresponds to the ratio: total water content (XH2O) / maximum possible gaseous water content
(Water vapour saturation concentration x_sat = f (p, t (air, port 2))

Example: Application of saturation factor:

In the example circuit, the saturation factor is used for controlling the relative humidity. You can see in the controller input diagram that the red curve is above and below 1

Specification-Values "Water injection"

Specification-Values "Controller 39"

User Input Values

Controller Main Attributes
FFU	Flag for ON / OFF / SET-start-value Like in Parent Profile (Sub Profile option only) Expression =0: OFF: Controller not active, but start value set in all load cases =1: ON: Controller active in all load cases =4: ON: Controller active in design, OFF: (only set starting value ) in off-design =5: OFF: (only set starting value) in design, ON: Controller active in off-design =-1: OFF: Completely deactivated in all load cases =-4: ON: Controller active in design, OFF: completely deactivated in off-design =-5: OFF: Completely deactivated in design, ON: Controller active in off-design =-6: OFF: (only set starting value) in design, OFF: in off-design it isn't =-7: OFF: (only set starting value) in off-design, OFF: in design it isn't Note to -6/ - 7: In both cases, no controlling takes place. Actually the use of a controller is redundant in this case as the same effect could be achieved by means of a measured value input (Component 46) instead. The fact that a control can be activated on demand after all, however, facilitates a uniform design of several models or the creation of generally applicable macros.
FCHAR	Flag for controller characteristics Like in Parent Profile (Sub Profile option only) Expression =1: Positive (i.e. an increase in the correction value causes an increase of the actual value) =-1: Negative (i.e. an increase in the correction value causes a lowering of the actual value)
Process Variable
FL1SCV	Flag for the type of comparison between L1 (process value) and SCV (target value) Like in Parent Profile (Sub Profile option only) Expression =1: Pressure =2: Temperature =3: Enthalpy =4: Mass flow =5: Power/heat flow =6: Enthalpy of boiling liquid for given pressure =7: Enthalpy of saturated vapour for given pressure =8: Enthalpy of boiling liquid for given temperature =9: Enthalpy of saturated vapour for given temperature =10: Pressure of boiling liquid for given temperature =11: Oxygen-fraction in air-/flue gas line =12: Steam content (X) of water/steam =13: Composition of the mass ratio (use with FSUBST) =14: Net calorific value =15: Composition as mole ratio (use of FSUBST) of all substances =16: Composition as mole ratio (use of FSUBST) of the dry part (without water/steam) =17: Entropy =18: Volume flow =19: Specific volume =20: Degrees sub cooling (with WD-lines this value refers to the boiling point, when humid air to the dew point temperature) =21: Degrees super heating (with WD-lines this value refers to the boiling point, when humid air to the dew point temperature) =22: Relative Pressure =23: Exergy, Note: Regarding the exergy, however, please be aware that the solution may not be unambiguous as the exergy does not rise monotonously with the temperature in all temperature ranges. Depending on the starting conditions and the set characteristic, sometimes one and sometimes the other solution may be found. =24: Voltage =25: Current =26: Frequency
FSUBST	Value to be controlled (active with FL1SCV=composition) Like in Parent Profile (Sub Profile option only) Expression =0: nothing =-1: Humidity (rel.) =-2: Humidity (abs.) =0: Unused =1: Nitrogen (N2) =2: Oxygen (O2) =3: Carbon dioxide (CO2) =4: Water H2O =5: Sulphur dioxide SO2 =6: Argon (Ar) =7: Carbon monoxide CO =8: Carbonyl sulfide (COS) =9: Hydrogen (H2) =10: Hydrogen sulphide (H2S) =11: Methane (CH4) =12: Hydrogen chloride HCl =13: Ethane (C2H6) =14: Propane (C3H8) =15: Butane (C4H10) =16: n-Pentane (CH3-CH2-CH2-CH2-CH3) =17: Hexane (C6H14) =18: Heptane (C7H16) =19: Acetylene (C2H2) =20: Benzene (C6H6) =21: Elementary carbon (C) =22: Elementary hydrogen (H) =23: Elementary oxygen (O) =24: Elementary nitrogen (N) =25: Elementary Sulphur (S) =26: Elementary chlorine (Cl) =27: Ash =28: Calcium hydroxide (Ca(OH)2) =29: deprecated Water (liquid) (H2O) =30: Water bound (H2O) =31: Ash (gaseous) =32: Nitrogen monoxide (NO) =33: Nitrogen dioxide (NO2) =34: Ammonia NH3 =35: deprecated Ammonia (liquid) (NH3) =36: deprecated Carbon dioxide (liquid) (CO2) =37: Methanol (Ca3OH) =38: deprecated Water (H2O) =39: Neon (Ne) =40: Dry Air further material properties No. 41 - No. 2400 Further material values to be regulated for a composition can be found on the surface of the controller - default value "FSUBST" Obviously, or entering two to three significant letters of the desired material value is sufficient to obtain a targeted selection of material values.
Controller Output
FL2	Flag for controlled variable type Like in Parent Profile (Sub Profile option only) Expression =1: Pressure =3: Enthalpy =4: Mass flow =5: Power =24: Voltage =26: Frequency
FLIM	Flag for Handling of L2MIN and L2MAX Like in Parent Profile (Sub Profile option only) Expression =0: Shut controller off after limit was exceeded =1: Stop at limit,
FL2MIN	Source of minimum value of controlled variable Like in Parent Profile (Sub Profile option only) Expression =0:Specification value L2MIN =2: Kernel Expression EL2MIN
L2MIN	Minimum value controlled variable
EL2MIN	Function for minimum value
FL2MAX	Source of maximum value of controlled variable Like in Parent Profile (Sub Profile option only) Expression =0:Specification value L2MAX =2: Kernel Expression EL2MAX
L2MAX	Maximum value controlled variable
EL2MAX	Function for maximum value
FL2START	Flag for the type of start value default Like in Parent Profile (Sub Profile option only) Expression =0: internal default through the specification value L2START =1: external (Stricter plausibility checks:, There will be error messages if - FL3START respectively are set to “external start value specification“, but no corresponding start value or measured value exists on the respective line. - a value is used as actuating variable that cannot be modified at all but is determined by other components. )
L2START	Start value of controlled variable (if FL2START=0)
L2STARTOFF	Alternative start value with FFU=0 (optional)
Target value
FSCV	Source of target value Like in Parent Profile (Sub Profile option only) Expression =0: Specification value SCV =2: Kernel expression ESCV
SCV	target value
ESCV	Function for target value function evalexpr:REAL; begin evalexpr:=1.0; end;
Additional Attributes
FACT	Number of iterations after which the controller is activated Like in Parent Profile (Sub Profile option only) Expression =0: immediately =20: after 20 iterations =30: after 30 iterations =40: after 40 iterations =50: after 50 iterations =60: after 60 iterations =80: after 80 iterations =100: after 100 iterations =150: after 150 iterations =250: after 250 iterations =Deprecated: -1: controller deactivated, only setting the start value =Deprecated: -2: controller completely deactivated
FDAMP	Flag for strength of damping Like in Parent Profile (Sub Profile option only) Expression =1: Without =2: Very little =3: Little =4: Medium =5: Medium high =6: High =7: Very high =8: Very very high =9: Even higher =10: Extremely high
ITCHL2	Number of iterations after which the change factor becomes active (default value: 100)
CHL2	Maximum change factor of corrected value (set as constant 0.15 till ITCHL2 is reached, after ITCHL2 according to the default between the limits: 0 < CHL3 <= 0.15)
CZP	Controller zero point
STOPGRAD	Stop controlling if gradient is less than
ITSTEP	Controller is active every n-th step (default value: 1)
FSEQ	Flag to define the position in calling sequence Like in Parent Profile (Sub Profile option only) Expression =0: Parallel to other components =1: Late, after fluids are recalculated
FSTOP	Stop behaviour if controller has not started Like in Parent Profile (Sub Profile option only) Expression =0: Do not stop iteration before controller has started =1: Stop in case of convergence even if controller has not started
FTOL	Flag for meaning of TOL Like in Parent Profile (Sub Profile option only) Expression = 0: not used = 1: TOL= lower limit: controller is working only as long as relative deviation > TOL = 2: TOL= upper limit: relative deviation must be < TOL before iteration stops
TOL	Controller tolerance
FSTOP	Switch behaviour in achieving convergence Like in Parent Profile (Sub Profile option only) Expression =0: Do not stop iteration before controller has started =1: Stop in Case of convergency even if controller has not started
FMODE	Flag for transfer of calculated value of controlled variable to start value Like in Parent Profile (Sub Profile option only) Expression =0 : After calculation in design mode =1 : No =-1: After each calculation
Notification Options
FWARN	Notification in case of missed target Like in Parent Profile (Sub Profile option only) Expression =0: Not notification =1: Warning =3: Warning, unless correction value is at limit =4: Error =5: Notification according to EWARN FWARN=5 allows to individually program in a Kernel expression EWARN under which circumstances a comment, a warning or an error message is to be output.
EWARN	Function for notification function evalexpr:REAL; var target,actual,correction,errorlevel:real; diff:real; begin target:=keGetInternal("TARGET"); actual:=keGetInternal("ACTUAL"); correction:=keGetInternal("CORRECTION"); errorlevel:=keGetInternal("ERRORLEVEL"); if (abs(target)>0) then begin //use relative deviation diff:=abs(actual-target)/target; end else begin diff:=abs(actual-target); end; if (diff > errorlevel) then begin evalexpr := 3; //Error end else if (diff > 0.1errorlevel) then begin evalexpr := 2; //Warning end else if (diff > 0.01errorlevel) then begin evalexpr := 1; //Comment end else begin evalexpr := 0; //None end; end;
FWARNOFF	Plausibility check in case of inactive controller Like in Parent Profile (Sub Profile option only) Expression =0: No warning if range (L2MIN to L2MAX) is exceeded =1: Warning if range (L2MIN to L2MAX) is exceeded

Generally, all inputs that are visible are required. But, often default values are provided.

For more information on colour of the input fields and their descriptions see Edit Component\Specification values

For more information on design vs. off-design and nominal values see General\Accept Nominal values

Values for FL1SCV

Scheduled value

Actual value

Measured value

for comparison

Comparative value

Pressure

Temperature

Enthalpy

Mass flow

Heat flow

Pressure

Temperature

Enthalpy

Mass flow

Heat flow

Pressure

Temperature

Enthalpy

Mass flow

Heat flow

Pressure

Temperature

Enthalpy' (P)

Enthalpy'' (P)

Enthalpy' (T)

Enthalpy'' (T)

Pressure' (T)

Enthalpy

Pressure

O2-fraction in air / flue gas lines

Steam content X

Composition (by mass)

Net calorific value

Composition by mole

Composition by mole (dry)

Entropy

Volume flow

Specific volume

Degrees sub cooling

Degrees super heating

O2-content

Steam content X

Composition (by mass)

Net calorific value

Composition by mole

Composition by mole (dry)

Entropy

Volume flow

Specific volume

TS=f(P)

O2-content

Steam content X

Composition (by mass)

Net calorific value

Composition by mole

Composition by mole (dry)

Entropy

Volume flow

Specific volume

Degrees sub cooling:
(Water /Steam: Temp.Diff to boiling point;
wet air: Temp.Diff. to dew point)

Degrees super heating:
(Water /Steam: Temp.Diff above the boiling point;
wet air: Temp.Diff. above dew point)

Values for FDAMP

Boundary conditions for the change gradient GRi

Lower limit for GRi

Upper limit for GRi

Damping behaviour

0.3

0.75

0.2

0.1

0.05

99999.0

9999.0

2.0

1.25

1.0

0.6

0.3

Without

Very little

Little

Medium

Medium-high

High

Very high

Very very high

Even higher

Extremely high

Characteristic Lines

CCHL2 - correction factor for CHL2

This characteristic enables one to change the maximum change factor CHL2 continuously in the course of the iteration (ITCHL2 enables an abrupt change in the iteration step ITCHL2). Normally, one will be able to narrow down the permissible deviation at the end of the iteration, in order to achieve a faster convergence.

x-value: Iteration step

y-value: Correction factor (CHL2 used = default value CHL2 * y-value)

Physics Used

With component 39 an outlet can be modelled with the help of a self-learning characteristic, which reaches the scheduled value SCV at the connection, from where the input is coming.

relative scheduled-actual value difference

(Scheduled value-actual value)

Si = ---------------------------------------------

Scheduled value

relative change of the correction value Ki

| f(new) - f(old) |

Ki= | ------------------------ |

| f(old) |

Change gradient

GRi = -----

The controller has got a "self-learning" characteristic i.e. the best possible changing of the correction value of the following iteration step is taken from the analysis of the controlling success of the last iteration steps. Therefore, the change gradient is used, which has been defined before. The change gradient is a measure of the relative changing of the correction value as a function of the relative variance difference. A change gradient GRi=1.0 results in a relative variance difference of, for instance, 5% to a changing of the correction value of even this 5%. The change gradient set to GRi=0.5 results from this supposed variance difference to a changing of the correction value of 2.5 %.

The gradient calculated from the last two steps is used to determine a new correction value as per the following table.

Correction value

Df = f * GRi * Si

f(new) = f(old) * (1.0 + Df) * FCHAR

The change gradient has the following limits:

During the iteration steps 1 to 10, GRi will be set as follows:

from iteration 1 to 5: GRi = 0.95, and

from iteration 6 to 10: GRi = 0.90 .

Starting from iteration 11, the gradient GRi is calculated by interpreting the controlling success achieved.

The user must define the maximum and the minimum values for the GRi by using FDAMP (see list).

The value f(new) is bound via a sensitivity according to following regulations.

- If Ki is less than CHL2, f(new) is not considered,

- If Ki is higher than or equal to CHL2, f(new) is according to the following relationships:

f(new)=f(old)*(1 +/- CHL2)

positive sign,

if f(new) >= f(old)

negative sign,

if f(new) < f(old)

The following rules apply to the determination of CHL2:

If the number of iteration steps is less than ITCHL2, the sensitivity is set internally to 0.15.

If the number of iteration steps is higher than or equal to ITCHL2, the input value CHL2 is applicable, but the maximum value is 0.15.

Component Displays

Display Option 1

Example

Click here >> Component 39 Demo << to load an example.