3 selecting the method ( conf/ cntr/ tune) 17, 4 step attempt after start-up 17, 5 pulse attempt after start-up 17 – West Control Solutions KS 92-1 Programmer manual User Manual

Page 17: Operation

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3.5.3 Selecting the method (

ConF/ Cntr/ tunE)

Selection criteria for the optimization method:

Step attempt after start-up

Pulse attempt after start-up

Optimization at the set-point

tunE = 0

sufficient set-point reserve is

provided

sufficient set-point reserve is not

provided

tunE = 1

sufficient set-point reserve is

provided

sufficient set-point reserve is not

provided

tunE = 2

always step attempt after

start-up

Sufficient set-point reserve:
inverse controller:(with process value < set-point- (10% of

rnGH - rnGL)

direct controller: (with process value > set-point + (10% of

rnGH - rnGL)

3.5.4 Step attempt after start-up

Condition:

-

tunE = 0 and sufficient set-point reserve provided or

-

tunE = 2

The controller outputs 0% correcting variable or

Y.Lo and waits, until the process

is at rest (see start-conditions on page 8).
Subsequently, a correcting variable step change to 100% is output.
The controller attempts to calculate the optimum control parameters from the pro-
cess response. If this is done successfully, the optimized parameters are taken
over and used for line-out to the set-point.
With a 3-point controller, this is followed by “cooling”.
After completing the 1st step as described, a correcting variable of -100% (100%
cooling energy) is output from the set-point. After successfull determination of
the “cooling parameters”, line-out to the set-point is using the optimized parame-
ters.

3.5.5 Pulse attempt after start-up

Condition: -

tunE = 1 and sufficient set-point reserve provided.

The controller outputs 0% correcting variable or

Y.Lo and waits, until the process

is at rest (see start conditions page 8)
Subsequently, a short pulse of 100% is output (Y=100%) and reset.
The controller attempts to determine the optimum control parameters from the
process response. If this is completed successfully, these optimized parameters
are taken over and used for line-out to the set-point.
With a 3-point controller, this is followed by “cooling”.
After completing the 1st step as described and line-out to the set-point, correcting
variable "heating" remains unchanged and a cooling pulse (100% cooling energy)
is output additionally. After successful determination of the “cooling parame-
ters”, the optimized parameters are used for line-out to the set-point.

Operation

KS 90-1

p / KS 92-1

p

17

Self-tuning

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