West Control Solutions Pro-4 User Manual

West Pro-4 user manual – 59559
û
BlueControl
More efficiency in engineering,
more overview in operating:
The projecting environment for the BluePort
controllers
Description of symbols:
g General information a General warning l Attention: ESD sensitive devices
© PMA Prozeß- und Maschinen-Automation GmbH Printed in Germany
All rights reserved. No part of this document may bereproduced or published in any form
or by any means without prior written permission from the copyright owner.
A publication of PMA Prozeß- und Maschinen Automation
P.O.Box 310229
D-34058 Kassel
Contents
1 Mounting ..............................5
2 Electrical connections .......................6
2.1 Connecting diagram .......................6
2.2 Terminal connection.........................7
3 Operation .............................11
3.1 Front view ............................11
3.2 Behaviour after power-on .....................12
3.3 Operating level ...........................12
3.4 Error list / Maintenance manager .................13
3.5 Self-tuning .............................16
3.5.1 Preparation for self-tuning .......................16
3.5.2 Optimization after start-up or at the set-point ..............17
3.5.3 Selecting the method ( ConF/ Cntr/ tunE).............17
3.5.4 Step attempt after start-up ......................18
3.5.5 Pulse attempt after start-up .......................18
3.5.6 Optimization at the set-point ......................18
3.5.7 Optimization at the set-point for 3-point stepping controller ......20
3.5.8 Self-tuning start .............................21
3.5.9 Self-tuning cancellation ........................21
3.5.10 Acknowledgement procedures in case of unsuccessful self-tuning . 22
3.5.11 Examples for self-tuning attempts ..................23
3.6 Manual self-tuning .........................24
3.7 Second PID parameter set .....................25
3.8 Alarm handling...........................26
3.9 Operating structure.........................28
4 Configuration level ........................29
4.1 Configuration survey ....................29
4.2 Configuration parameters ....................30
4.3 Set-point processing ........................43
4.3.1 Set-point gradient / ramp ........................43
4.4 Switching behaviuor ........................44
4.4.1 Standard ( CyCl= 0 ) .........................44
4.4.2 Switching attitude linear ( CyCl= 1 ).................44
KS 90-1 / KS 92-1 3
4.4.3 Switching attitude non-linear ( CyCl= 2 )...............45
4.4.4 Heating and cooling with constant period ( CyCl= 3 )........46
4.5 Configuration examples ......................47
4.5.1 On-Off controller / Signaller (inverse) .................47
4.5.2 2-point controller (inverse) .......................48
4.5.3 3-point controller (relay & relay) ....................49
4.5.4 3-point stepping controller (relay & relay) ...............50
4.5.5 Continuous controller (inverse) .....................51
4.5.6 ∆ - Y - Off controller / 2-point controller with pre-contact ......52
4.5.7 Continuous controller with position controller .............53
4.5.8 Measured value output .........................54
5 Parameter setting level ......................55
5.1 Parameter survey ........................55
5.2 Parameters .............................56
5.3 Input scaling ............................59
5.3.1 Input Inp.1 and InP.3 .............60
5.3.2 Input InP.2...............................60
6 Calibration level .........................61
7 Special functions .........................64
7.1 DAC®– motor actuator monitoring ...............64
7.2 O2measurement ..........................66
7.2.1 Connection ...............................66
7.2.2 Configuration: ..............................67
7.3 Linearization ............................68
7.4 Loop alarm .............................69
7.5 Heating current input / heating current alarm ...........69
7.6 KS90-1 as Modbus master .....................70
7.7 Back-up controller (PROFIBUS) .................70
8 BlueControl ............................71
9 Versions ..............................72
10 Technical data ..........................73
11 Safety hints ............................77
11.1 Resetting to factory setting, ....................78
4 KS 90-1 / KS 92-1
1 Mounting
9
min.48 (1.89")
92
Mounting
+0,8
10
(3.78")
96
48 (1.89")
max.
(0.4")
118
1199
1199
°C
°C
°F
°F
para
para
func
func
Ada
Ada
Err
Err
F
F
è
KS 92-1 advanced
KS 90-1
60°C
0°Cmin.
(4.65")
123
1234
1200
1200
SP.E
SP.2
SP.E
SP.2
advanced
+0.03
+0,8
1..10
92
(0.04..0.4")
4
(3.62" )
2
1
3
4
+0,8
2
920.1
+0,6
45
(1.77" )
+0.02
Loc
security switch
Ü
or:
96
para func
Ada
Err
F
KS 92-1 advanced
o
C
921.2
run
SP.E
SP.2
run
SP.E
SP.2
96
118
10
max. 95% rel.
l
Ü
%
*
*
Safety switch:
For access to the safety switch, the controller must be withdrawn from the hou sing. Squeeze the top and bottom of the front bezel between thumb and forefinger and pull the controller firmly from the housing.
Loc open Access to the levels is as adjusted by means of BlueControl (engineering tool) 2
closed 1 all levels accessible wihout restriction
1 Factory setting 2 Default setting: display of all levels
suppressed, password PASS = OFF
Caution! The unit contains ESD-sensitive components.
-
KS 90-1 / KS 92-1 5
Electrical connections
6
2 Electrical connections
2.1 Connecting diagram
3
1
2
90...250V 24VUC
OUT1
OUT2
OUT3
KS90-1. -4 ... KS90-1. -5 ...
OUT4
KS90-1. -25...
!
V
V
d b
c
e
8
9
0
RGND
DATA B
DATA A
RS485 RS422
Modbus RTU
1 2 3
4 5 6
7 8 9
10 11 12
13 14 15
a
+24V DC
OUT5 OUT6
24V GND
RXD-B
RXD-A
TXD-B
TXD-A
GND
di2
di3
U
1 2 3
di1
7
di2
4 5 6
7
g
HC
mA
INP2
f
5
8 9
10 11
(mV)
0%
100%
mA
INP3
KS90-1..-.1...
12 13
14 15
mA
Volt
INP1
4
(16)
Option
1
(2)
3
4
5
10
11
12
13
14
15
(16)
17
6
7
8
9
VP (5V)
DGND
RxD/TxD-N
RxD/TxD-P
Schirm/ Screen
T
17
PROFIBUS-DP
(mV)
a
b
390 [
220 [
Adapter
390 [
cd
DGND
9
8
7
VP (5V)
6
Profibus DP
e
max.
1200m
5
4
3
2
1
5
9
4
8
3
7
2
6
1
g
Dependent of order, the controller is fitted with :
flat-pin terminals 1 x 6,3mm or 2 x 2,8mm to DIN 46 244 or
w
screw terminals for 0,5 to 2,5mm²
w
On instruments with screw terminals, the insulation must be stripped by min. 12 mm. Choose end crimps accordingly!
Connecting diagram 6 KS 90-1 / KS 92-1
2.2 Terminal connection
Power supply connection 1
See chapter "Technical data"
Electrical connections
Connection of outputs OUT1/2 2
2 OUT1/2 heating/cooling
Relay outputs (250V/2A), potential-free changeover contact
L
Connection of outputs OUT3/4 3
a relay (250V/2A), potential-free
changeover contact
universal output
b current (0/4...20mA) c voltage (0/2...10V) d transmitter supply e logic (0..20mA / 0..12V)
Connection of input INP1 4
N
Input mostly used for variable x1 (pro­cess value)
a thermocouple b resistance thermometer (Pt100/ Pt1000/ KTY/ ...) c current (0/4...20mA) d voltage (0/2...10V)
1
2
3
4
5
6
7
8
9
10 11 12
13 14 15
10 11 12
13 14
(16)
1 2 3
4 5 6 7 8 9
15
17
+
Connection of input INP2 5
f heating current input (0..50mA AC)
or input for ext. set-point (0/4...20mA) g potentiometer input for position feedback
Connection of input INP2 5
a Heating current input (0...50mA AC)
or input for ext. Set-point (0/4...20mA) b Potentiometer input for position
feedback
Connection of input INP3 6
As input INP1, but without voltage
Connection of inputs di1, di2 7
Digital input, configurable as switch or push-button
5 INP2 current tansformer
L
1 2
3 4
5 6
7 8
N
Logik
9
10 11 12
13 14 15
10 11 12
13 14 15
(16)
17
1 2 3
4 5
6 7
8 9
SSR
_
+
KS 90-1 / KS 92-1 7 Terminal connection
Electrical connections
Connection of inputs di2/3 8 (option)
Digital inputs (24VDC external), galvanically isolated, configurable as switch or push-button
Connection of output U
9 (option)
T
Supply voltage connection for external energization
Connection of outputs OUT5/6 0 (option)
Digital outputs (opto-coupler), galvanic isolated, common positive control volta ge, output rating: 18...32VDC
Connection of bus interface ! (option)
PROFIBUS DP or RS422/485 interface with Modbus RTU protocol
89 di2/3, 2-wire transmitter supply
OUT3
J
10 11
12
13 14 15
Option
15
(16)
17
13 14
-
+
-
g
+24VDC
3
0V
+
1
2
-
17,5V 22mA
K
5mA
5mA
+
-
1
(2)
3
4
5
6
7
8
9
10
11
12
13
14
15
(16)
17
J
Analog outputs OUT3 or OUT4 and transmitter supply UTare connected to different voltage potentials. Therefore, take care not to make an external galvanic connection between OUT3/4 and U
with analog outputs!
T
Terminal connection 8 KS 90-1 / KS 92-1
3 OUT3 transmitter supply
Electrical connections
3
13V
22mA
1
K
2
-
+
10 11
12
13 14 15
11 12
15
(16)
17
13 14
+
-
9 RS485 interface (with RS232-RS485 interface converter) *
R = 120...200 OhmT
RT
RGND connection optional
RGND
DATA B
DATA A
option
1
(2)
3
4
5
6
7
8
9
10
11
12
13
14
15
(16)
17
J
10
11
12
13
14
15
RGND
DATA B
DATA A
option
1
(2)
3
4
5
6
7
8
9
10
11
12
13
14
15
(16)
17
10
11
12
13
14
15
max. 1000m
"Twisted Pair” cable
RGND
DATA B
DATA A
R=100 Ohm
option
1
(2)
3
4
5
6
7
8
9
10
11
12
13
14
15
(16)
17
RT
R = 120...200 OhmT
10
11
12
13
14
15
PC
RS485-RS232
converter
* Interface description Modbus RTU in speperate manual: see page 71.
KS 90-1 / KS 92-1 9 Terminal connection
Electrical connections
3 OUT3 as logic output with solid-state relay (series and parallel connection)
Series connection
SSR
I =22mA
max
_
4V
+
SSR
_
4V
+
SSR
_
4V
+
12V
10 11
12
Logic
SSR
SSR
Parallel connection
I =22mA
max
_
12V
+
_
+
10 11
12
KS90-1 connecting example:
L1
L2
Fuse
1 2
3 4
5 6
7 8 9
10 11
12
13 14 15
KS90-1
Logik
10 11 12
13 14
(16)
1 2 3
4 5 6 7 8 9
SSR
_
+
15
17
Contactor
+
Fuse
Heating
1 TB 40-1 Temperaturelimiter
Standard-version (3 Relays): TB40-100-0000D-000
further versions on requestr
1
2
3
4
1
TB 40-1
Temperaturelimiter
5
6
7
8
9
10
11
12
13
14
15
+
Reset­key
Fuse
N1
N2
a
CAUTION: Using a temperature limiter is recommendable in systems where overtemperature implies a fire hazard or other risks.
Terminal connection 10 KS 90-1 / KS 92-1
3 Operation
1 2 3
4
F
SP.E
SP.2
920.1
921.2
C
para
func
Ada
Err
SP.E
SP.2
o
1200
1199
°C °F
SP.2
SP.E
para func
Ada
Err
F
123
4
1
2
3
4
5 6
$
7 8
%
&
(
/
p
9
0
SP
§"
!
92
4
C
9
0
!
§"
7 8
$
%
&
/
(
5 6
1
2
3
3.1 Front view
Operation
1 Statuses of switching outputs OuT.1... 6 2 Process value display 3 Setpoint or correcting variable display 4 °C or °F display signalling 5 Signals ConF- and PArA level 6 Signals activated function key 7 Selft-tuning active 8 Entry into the error list 9 Bargraph or plain text display 0 Setpoint SP.2 is effective ! Setpoint SP.E is effective " Setpoint gradient is effective
§ Manual-automatic switchover: Off: automatic On: manual mode (adjustment possible) Blinks: manual mode (adjustment not possible (r ConF/ Cntr/ MAn))
$ Enter key: call up extented operating level / error list % Up/ down keys: changing setpoint or correcting variable & automatic/manual or other functions ( r ConF /LOGI) / freely configurable function key with pure controller operation ( PC connection for BlueControl (engineering tool)
g
LED colours: LED 1, 2, 3, 4: yellow, Bargraph: red, other LEDs: red
In the upper display line, the process value is always displayed. At parameter, configuration, calibration as well as extended operating level, the bottom display line changes cyclically between parameter name and parameter value.
KS 90-1 / KS 92-1 11 Front view
Operation
A
M
l
3.2 Behaviour after power-on
After supply voltage switch-on, the unit starts with the operating level. The unit is in the condition which was active before power-off. If the controller was in manual mode at supply voltage switch-off, the controller will re-start with the last output value in manual mode at power-on.
3.3 Operating level
The content of the extended operating level is determined by means of BlueCon trol (engineering tool). Parameters which are used frequently or the display of which is important can be copied to the extended operating level.
time
out
utomatic
1199
1200
È Ì
Ù
1199
Y21
i
Ò
Ò
i
anua
1199
Y21
È Ì
Ù
1199
1200
time
out
-
È
Ù
only
display
Ù
Ì
Extended operating level
time
out
Error list (if error exists)
126
FbF.1
Err
Display
switching
126
2
Err
Behaviour after power-on 12 KS 90-1 / KS 92-1
3.4 Error list / Maintenance manager
Operation
With one or several errors, the extended operating level al
­ways starts with the error list. Signalling an actual entry in the error list (alarm, error) is done by the Err LED in the display. To reach the error list press Ù twice.
Err LED status Signification Proceed as follows
blinks
(status 2)
lit
(status 1)
off
(status 0)
Alarm due to existing error
Error removed, alarm not acknowledged
No error, all alarm entries deleted
Determine the error type in the error list
­After error correction the unit changes to status 1
­Acknowledge the alarm in the error list pressing key ÈorÌ
­The alarm entry was deleted (status 0).
-
-Not visible except when acknowledging
-
Error list:
Name
E.1
E.2
E.3
E.4
FbF.1
Sht.1
POL.1 FbF.2
Sht.2
POL.2 FbF.3
Sht.3
POL.3
Description Cause Possible remedial action
Internal error, cannot be removed
Internal error, can be reset
- E.g. defective EEPROM - Contact PMA service
- Return unit to our factory
- e.g. EMC trouble - Keep measurement and power supply cables in separate runs
- Ensure that interference suppression of contactors is provided
Configuration error, can be reset
- wrong configuration
- missing configuration
Hardware error - Codenumber and
hardware are not identical
Sensor break INP1
-
Sensor defective
-
Faulty cabling
Short circuit INP1-Sensor defective
-
Faulty cabling
INP1polarity error
-
Faulty cabling
Sensor break INP2-Sensor defective
-
Faulty cabling
Short circuit INP2-Sensor defective
-
Faulty cabling
INP2 polarity
-
Faulty cabling
Sensor break INP3-Sensor defective
-
Faulty cabling
Short circuit INP3-Sensor defective
-
Faulty cabling
INP3 polarity
-
Faulty cabling
- Check interaction of configuration / parameters
- Contact PMA service
- Elektronic-/Optioncard must be exchanged
-
Replace INP1 sensor
-
Check INP1 connection
-
Replace INP1 sensor
-
Check INP1 connection
-
Reverse INP1 polarity
-
Replace INP2 sensor
-
Check INP2 connection
-
Replace sensor INP2
-
Check INP2 connection
-
Reverse INP2 polarity
-
Replace INP3 sensor
-
Check INP3 connection
-
Replace sensor INP3
-
Check INP3 connection
-
Reverse INP3 polarity
1199
°C
°F
1200
para func
Ada
Err
SP.E
SP.2
KS 90-1 / KS 92-1 13 Error list / Maintenance manager
Operation
Name
HCA
SSr
LooP
AdA.H
AdA.C
LiM.1
Lim.2
Lim.3
Inf.1
Inf.2
E.5
dp.1
dp.2
dp.3
Description Cause Possible remedial action
Heating current alarm (HCA)
Heating current circuit
­interrupted, I< HC.A or
Check heating current circuit
­If necessary, replace heater band
-
I> HC.A (dependent of configuration) Heater band defective
-
Heating current short circuit (SSR)
Current flow in heating
­circuit with controller
Check heating current circuit
­If necessary, replace solid-state relay
-
off SSR defective
-
Control loop alarm (LOOP)
Input signal defective or
­not connected correctly Output not connected
­correctly
Check heating or cooling circuit
­Check sensor and replace it, if
­necessary Check controller and switching
­device
Self-tuning heating alarm
See Self-tuning heating
­error status
see Self-tuning heating error status
-
(ADAH) Self-tuning heating
alarm cooling (ADAC)
stored limit alarm 1 - adjusted limit value 1
See Self-tuning cooling
­error status
see Self-tuning cooling error status
-
- check process
exceeded
stored limit alarm 2 - adjusted limit value 2
- check process
exceeded
stored limit alarm 3 - adjusted limit value 3
- check process
exceeded
time limit value message
duty cycle message (digital ouputs)
Internal error in DP module
- adjusted number of operating hours reached
- adjusted number of duty cycles reached
-
self-test error
-
internal communication
- application-specific
- application-specific
-
Switch on the instrument again
-
Contact PMA service
interrupted
No access by bus master
-
bus error
-
connector problem
-
no bus connection
Faulty configuration-Faulty DP
configuration telegram
Inadmissible parameter setting telegram sent
-
Faulty DP parameter setting telegram
-
Check cable
-
Check connector
-
Check connections
-
Check DP configuration telegram in master
-
Check DP parameter setting telegram in master
No data
dp.4
Error list / Maintenance manager 14 KS 90-1 / KS 92-1
communication
-
Bus error
-
Address error
-
Master stopped
-
Check cable connection
-
Check address
-
Check master setting
Operation
g
g
Saved alarms (Err-LED is lit) can be acknowledged and deleted with the digital input di1/2/3, the è-key or the Ò-key. Configuration, see page 37: ConF / LOGI / Err.r
If an alarm is still valid that means the cause of the alarm is not removed so far (Err-LED blinks), then other saved alarms can not be acknowledged and deleted.
Self-tuning heating ( ADA.H) and cooling ( ADA.C) error status:
Error
status
Description Behaviour
0
No error
3
Faulty control action Re-configure controller (inverse i direct)
4
No response of process variable
5
Low reversal point Increase ( ADA.H) max. output limiting Y.Hi or decrease (
The control loop is perhaps not closed: check sensor, connections and process
ADA.C) min. output limiting Y.Lo
6
Danger of exceeded
If necessary, increase (inverse) or reduce (direct) set-point set-point (parameter determined)
7
Output step change too small (dy > 5%)
8
Set-point reserve too small
Increase ( ADA.H) max. output limiting Y.Hi or reduce (
ADA.C) min. output limiting Y.Lo
Acknowledgment of this error message leads to switch-over to
automatic mode.If self-tuning shall be continued,
increase set-point (invers), reduce set-point (direct)
or decrease set-point range
(r PArA / SEtp / SP.LO and SP.Hi )
9
Impulse tuning failed The control loop is perhaps not closed: check sensor, connections
and process
DAC function ( DAC) error status:
Error status
0 3 4 5 6
KS 90-1 / KS 92-1 15 Error list / Maintenance manager
No error Output is blocked Check the drive for blockage Wrong method of operation Wrong phasing, defect motor capacitor Fail at Yp measurement Check the connection to the Yp input Calibration error Manual calibration necessary
Description Behaviour
Operation
3.5 Self-tuning
For determination of optimum process parameters, self-tuning is possible.
After starting by the operator, the controller makes an adaptation attempt, where by the process characteristics are used to calculate the parameters for fast line-out to the set-point without overshoot.
The following parameters are optimized when self-tuning: Parameter set 1:
Pb1 - Proportional band 1 (heating) in engineering units [e.g. °C] ti1 - Integral time 1 (heating) in [s]r only, unless set to OFF td1 - Derivative time 1 (heating) in [s]r only, unless set to OFF t1 - Minimum cycle time 1 (heating) in [s]r only, unless Adt0 was
set to “no self-tuning” during configuration by means of BlueControl
®
.
Pb2 - Proportional band 2 (cooling) in engineering units [e.g. °C] ti2 - Integral time 2 (cooling) in [s]r only, unless set to OFF td2 - Derivative time 2 (cooling) in [s]r only, unless set to OFF t2 - Minimum cycle time 2 (cooling) in [s] r only, unless Adt0
was set to “no self-tuning” during configuration by means of BlueControl
®
.
-
Parameter set 2: analogous to parameter set 1 (see page 25)
3.5.1 Preparation for self-tuning
Adjust the controller measuring range as control range limits. Set values
w
rnG.L and rnG.H to the limits of subsequent control. (ConfigurationrControllerrlower and upper control range limits) ConFrCntrr rnG.L and rnG.H
Determine which parameter set shall be optimized.
w
-The instantaneously effective parameter set is optimized. r Activate the relevant parameter set (1 or 2).
Determine which parameter set shall be optimized (see tables above).
w
Select the self-tuning method
w
see chapter 3.5.3
-Step attempt after start-up
-Pulse attempt after start-up
-Optimization at the set-point
Self-tuning 16 KS 90-1 / KS 92-1
3.5.2 Optimization after start-up or at the set-point
The two methods are optimization after start-up and at the set-point. As control parameters are always optimal only for a limited process range, vari ous methods can be selected dependent of requirements. If the process behaviour is very different after start-up and directly at the set-point, parameter sets 1 and 2 can be optimized using different methods. Switch-over between parameter sets dependent of process status is possible (see page ).
Optimization after start-up: (see page 4) Optimization after start-up requires a certain separation between process value and set-point. This separation enables the controller to determine the control pa rameters by evaluation of the process when lining out to the set-point. This method optimizes the control loop from the start conditions to the set-point, whereby a wide control range is covered. We recommend selecting optimization method “Step attempt after start-up” with tunE = 0 first. Unless this attempt is completed successfully, we recom mend a “Pulse attempt after start-up”.
Operation
-
-
-
Optimization at the set-point: (see page 18) For optimizing at the set-point, the controller outputs a disturbance variable to the process. This is done by changing the output variable shortly. The process value changed by this pulse is evaluated. The detected process parameters are conver­ted into control parameters and saved in the controller. This procedure optimizes the control loop directly at the set-point. The advantage is in the small control deviation during optimization.
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 tunE =1 tunE =2
sufficient set-point reserve is
provided
sufficient set-point reserve is
provided
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)
sufficient set-point reserve is not
provided
sufficient set-point reserve is not
provided
KS 90-1 / KS 92-1 17 Self-tuning
Operation
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.
3.5.6 Optimization at the set-point
Conditions:
A sufficient set-point reserve is not provided at self-tuning start (see page 17).
w
tunE is0or1
w
With Strt = 1 configured and detection of a process value oscillation by
w
more than ± 0,5% of (rnG.H - rnG.L) by the controller, the control parameters are preset for process stabilization and the controller realizes an optimization at the set-point (see figure “Optimization at the set-point”). when the step attempt after power-on has failed
w
with active gradient function ( PArA/ SETP/ r.SPOFF), the set-point
w
gradient is started from the process value and there isn't a sufficient set-point reserve.
-
Self-tuning 18 KS 90-1 / KS 92-1
Operation
Optimization-at-the-set-point procedure:
The controller uses its instantaneous parameters for control to the set-point. In li ned out condition, the controller makes a pulse attempt. This pulse reduces the correcting variable by max. 20% 1, to generate a slight process value unders hoot. The changing process is analyzed and the parameters thus calculated are re corded in the controller. The optimized parameters are used for line-out to theset-point.
Optimization at the set-point
-
set-point
process value
-
-
correcting variable
With a 3-point controller, optimization for the “heating“ or “cooling” parameters occurs dependent of the instantaneous condition. These two optimizations must be started separately.
1 If the correcting variable is too low for reduction in lined out condition it is increased by max. 20%.
KS 90-1 / KS 92-1 19 Self-tuning
Operation
3.5.7 Optimization at the set-point for 3-point stepping controller
With 3-point stepping controllers, the pulse attempt can be made with or without position feedback. Unless feedback is provided, the controller calculates the mo tor actuator position internally by varying an integrator with the adjusted actuator travel time. For this reason, precise entry of the actuator travel time (tt), as time between stops is highly important. Due to position simulation, the controller knows whether an increased or reduced pulse must be output. After supply volta ge switch-on, position simulation is at 50%. When the motor actuator was varied by the adjusted travel time in one go, internal calculation occurs, i.e. the position corresponds to the simulation:
Simulation actual position
-
-
Internal calculation
tt
Internal calculation always occurs, when the actuator was varied by travel time
tt in one go
, independent of manual or automatic mode. When interrupting the variation, internal calculation is cancelled. Unless internal calculation occurred already after self-tuning start, it will occur automatically by closing the actuator once.
Unless the positioning limits were reached within 10 hours, a significant deviati
­on between simulation and actual position may have occurred. In this case, the controller would realize minor internal calculation, i.e. the actuator would be clo
­sed by 20 %, and re-opened by 20 % subsequently. As a result, the controller knows that there is a 20% reserve for the attempt.
Self-tuning 20 KS 90-1 / KS 92-1
3.5.8 Self-tuning start
Start condition:
For process evaluation, a stable condition is required. Therefore, the
w
controller waits until the process has reached a stable condition after self-tuning start. The rest condition is considered being reached, when the process value
oscillation is smaller than ± 0,5% of (rnG.H - rnG.L). For self-tuning start after start-up, a 10% difference from (SP.LO ... SP.Hi)
w
is required.
Operation
g
Self-tuning start can be blocked via BlueControl®(engineering tool) ( P.Loc).
Strt = 0 Only manual start by pressing keys Ù and È
simultaneously or via interface is possible.
Strt = 1 Manual start by press keys Ù and È simultaneously
via interface and automatic start after power-on and detection of process oscillations.
Ada LED status Signification
blinks Waiting, until process
calms down
lit Self-tuning is running
off Self-tuning not activ
or ended
3.5.9 Self-tuning cancellation
By the operator:
Self-tuning can always be cancelled by the operator. For this, press Ù and È key simultaneously.With controller switch-over to manual mode after self-tuning start, self-tuning is cancelled. When self-tuning is cancelled, the controller will continue operating using the old parameter values.
1199
°C
°F
1200
para func
Ada
Err
SP.E
SP.2
By the controller:
If the Err LED starts blinking whilst self-tuning is running, successful self-tuning is prevented due to the control conditions. In this case, self-tuning was cancelled by the controller. The controller continues operating with the old parameters in automatic mode. In manual mode it continues with the old controller output va
-
lue.
KS 90-1 / KS 92-1 21 Self-tuning
Operation
3.5.10 Acknowledgement procedures in case of unsuccessful self-tuning
1. Press keys Ù and È simultaneously:
The controller continues controlling using the old parameters in automatic mode. The Err LED continues blinking, until the self-tuning error was acknowledged in the error list.
2. Press key Ò (if configured):
The controller goes to manual mode. The Err LED continues blinking, until the self-tuning error was acknowleged in the error list.
3. Press key Ù :
Display of error list at extended operating level. After acknowledgement of the error message, the controller continues control in automatic mode using the old parameters.
Cancellation causes:
r page 15: "Error status self-tuning heating ( ADA.H) and cooling ( ADA.C)"
Self-tuning 22 KS 90-1 / KS 92-1
3.5.11 Examples for self-tuning attempts
(controller inverse, heating or heating/cooling)
Operation
Start: heating power switched on
Heating power Y is switched off (1). When the change of process value X was constant during one minute (2), the power is switched on (3). At the reversal point, the self-tuning at
­tempt is finished and the new parameter are used for controlling to set-point W.
Start: heating power switched off
The controller waits 1,5 minutes (1). Heating power Y is switched on (2). At the reversal point, the self-tuning attempt is finished and control to the set-point is using the new parameters.
Self-tuning at the set-point a
The process is controlled to the set-point. With the control deviation constant during a defined time (1) (i.e. constant separation of process value and set-point), the controller outputs a reduced correcting variable pulse (max. 20%) (2). After determination of the control parameters using the process characteristic (3), control is started using the new parameters (4).
100%
100%
X
W
100%
0%
Start r
X
W
Y
0%
Star t r
X
W
Y
0%
Y
start r
1
blinks
1
blinks
2
r
1
blinks
t
3
2
2
3
4
t
t reversal point
t
t reversal point
t
Three-point controller a
The parameter for heating and cooling are
X
W
3
rt
determined in two attempts. The heating power is switched on (1). Heating para meters Pb1, ti1, td1 and t1 are de termined at the reversal point. Control to the set-point occurs(2). With constant control deviation, the controller provides a cooling correcting variable pulse (3). Af
-
-
+100%
Y0%
-100%
Start r
1
t reversal
point
2
4
t
5
-
ter determining its cooling parameters Pb2, ti2, td2 and t2 (4) from the process characteristics , control operation is started using the new parameters (5).
a
KS 90-1 / KS 92-1 23 Self-tuning
During phase 3, heating and cooling are done simultaneously!
Operation
y
3.6 Manual self-tuning
The optimization aid can be used with units on which the control parameters shall be set without self-tuning.
For this, the response of process variable x after a step change of correcting varia ble y can be used. Frequently, plotting the complete response curve (0 to 100%) is not possible, because the process must be kept within defined limits. Values T
and x be used to determine the maximum rate of increase v
(step change from 0 to 100 %) or t and x (partial step response) can
max
.
max
100%
Y
h
0%
x
t
Tg
X
max
-
g
{X
{t
Tu
y = correcting variable
Y
h
Tu = delay time (s) Tg = recovery time (s) X
max
V
max
The control parameters can be determined from the values calculated for delay time T according to the formulas given below. Increase Xp, if line-out to the set-point oscillates.
= control range
= maximum process value
Xmax
=
Tg
, maximum rate of increase v
u
{{x
=
= max. rate of increase of process value
t
, control range Xhand characteristic K
max
t
Manual self-tuning 24 KS 90-1 / KS 92-1
Operation
Parameter adjustment effects
Parameter Control Line-out of disturbances Start-up behaviour
Pb1 higher increased damping slower line-out slower reduction of duty cycle
lower reduced damping faster line-out faster reduction of duty cycle
td1 higher reduced damping faster response to disturbances faster reduction of duty cycle
lower increased damping slower response to disturbances slower reduction of duty cycle
ti1 higher increased damping slower line-out slower reduction of duty cycle
lower reduced damping faster line-out faster reduction of duty cycle
Formulas
K = Vmax * Tu controller behavior Pb1 [phy. units] td1 [s] ti1 [s]
PID 1,7*K 2*Tu 2*Tu With 2-point and 3-point controllers,
the cycle time must be adjusted to
t1 / t2 ≤ 0,25 * Tu
PD 0,5 * K Tu OFF
PI 2,6 * K OFF 6*Tu
PKOFF OFF
3-point-stepping 1,7 * K Tu 2 * Tu
3.7 Second PID parameter set
The process characteristic is frequently affected by various factors such as pro­cess value, correcting variable and material differences. To comply with these requirements, KS 90-1 can be switched over between two parameter sets. Parameter sets PArA and PAr.2 are provided for heating and cooling.
Dependent of configuration ( ConF/LOG/Pid.2), switch-over to the second pa­rameter set ( ConF/LOG/Pid.2) is via one of digital inputs di1, di2, di3, key è or interface (OPTION).
g
Self-tuning is always done using the active parameter set, i.e. the second parameter set must be active for optimizing.
KS 90-1 / KS 92-1 25 Second PID parameter set
Operation
3.8 Alarm handling
Max. three alarms can be configured and assigned to the individual outputs. Ge nerally, outputs OuT.1... OuT.6 can be used each for alarm signalling. If more than one signal is linked to one output the signals are OR linked. Each of the 3 li mit values Lim.1 Lim.3 has 2 trigger points H.x (Max) and L.x (Min), which can be switched off individually (parameter = “OFF”). Switching difference HYS.x and delay dEl.x of each limit value is adjustable.
Ü Operaing principle absolut alarm
L.1 = OFF
InL.1
H.1
HYS.1
LED
InH.1
* Operating principle relative alarm
L.1 = OFF
SP
InL.1
H.1
HYS.1
-
-
InH.1
LED
H.1 = OFF
InL.1
InL.1
H.1
L.1
LED
L.1
HYS.1
LED
HYS.1 HYS.1
InH.1
InH.1
LED
H.1 = OFF
InL.1
InL.1
2
LED
LED
HYS.1
HYS.1
L.1
SP
InH.1
L.1
SP
InH.1
H.1
HYS.1
LED
2
1: normally closed ( ConF/ Out.x/O.Act=1 ) (see examples in the drawing) 2: normally open ( ConF/ Out.x/O.Act= 0 )(inverted output relay action)
Alarm handling 26 KS 90-1 / KS 92-1
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