West Control Solutions Pro-16 User Manual

Pro-16 Industrial Controller
Pro-16
Manual Part number: 59537-1
October 2013
© West Control Solutions
All rights reserved. No part of this document may be reproduced or published in any form or by any means without prior
written permission from the copyright owner.
A publication of West Control Solutions
P.O.Box 310229
D-34058 Kassel
Germany
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Table of contents
1.Mounting 6
2.Electrical connection 8
3.Operation 9
3.1 Front view 9
3.2 Operating structure 9
3.2.1 Operating Level 10
3.3 Behaviour after power-on 10
3.4 Operating level 11
3.5 Errorlist / Maintenance Manager 12
3.5.1 Error-List: 12
3.5.2 Error-Status (Self-tuning) 13
3.6 Function level 14
3.7 Self-tuning 15
3.7.1 Preparation before self-tuning 15
3.7.2 Optimization after start-up or at the set-point 16
3.7.3 Selecting the method ( ConF/ Cntr/ tunE) 16
3.7.4 Step attempt after start-up 17
3.7.5 Pulse attempt after start-up 17
3.7.6 Optimization at the set-point 17
3.7.7 Self-tuning start 20
3.7.8 Examples for self-tuning attempts 20
3.8 Help for manual tuning 22
3.9 Second PID parameter set 23
3.10 Alarm handling 24
4.Configuration level 26
4.1 Configuration overview 26
4.2 Configurations 27
4.3 Set-point processing 42
4.3.1 Set-point gradient / ramp 42
4.3.2 Cooling functions 42
4.3.3 Standard ( CyCl= 0 ) 42
4.3.4 Switching attitude linear ( CyCl=1) 43
4.3.5 Switching attitude non-linear ( CyCl= 2 ) 44
4.3.6 Heating and cooling with constant period ( CyCl=3 ) 45
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4.4 Configuration examples 46
4.4.1 On-Off controller / Signaller (inverse) 46
4.4.2 2-point and continuous controller (inverse) 47
4.4.3 3-point and continuous controller 48
4.4.4 3-point stepping controller (relay & relay) 49
4.4.5 - Y - Off controller / 2-point controller with pre-contact 50
4.4.6 KS 20-1 with measured value output 51
5.Parameter-Level 52
5.1 Parameter-Overview 52
5.2 Parameter 53
6.Input scaling 57
7.Calibration level 58
8.Programmer 61
8.1 Operation 61
8.1.1 Programmer display 62
8.1.2 Segment type 62
8.1.3 Bandwidth monitoring 63
8.1.4 Search run at programmer start 64
8.1.5 Behaviour after mains recovery or sensor error 64
8.2 Parameter overview 65
8.3 Parameter 66
8.4 Programmer description 68
8.4.1 General 68
8.4.2 Programmer set-up: 69
9.Special functions 71
9.1 Start-up circuit 71
9.2 Boost function 72
9.3 KS 20-1 as Modbus-Master 73
9.4 Linearization 74
9.5 Timer 75
9.5.1 Setting up the timer 75
9.5.2 Determining the timer run-time 76
9.5.3 Starting the timer 77
10.Ordering information 78
®
11.BlueControl
11.1 Configuration Port 80
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79
12.Technical Data 81
13.Safety notes 84
13.1 Resetting to factory setting 86
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1. Mounting
Mounting
CAUTION
Make sure that the inside of the mounting plate corresponds to the instrument operating temperature and that sufficient ventilation to prevent overheating is provided.
Please, DON’T remove the safety device/sealing of the mounting plate, in
The mounting plate must be solid and up to 6.0 mm thick. The required cut-out is shown
below. Several instruments with the following dimensions can be installed side by side: Instruments: (48n - 4) mm or (1.89n — 0.16) inches.
Fig. 1: Mounting dimensions
order to avoid jamming of the instrument in the mounting plate.
Mounting dimensions
The mounting depth with terminals plugged in is 110mm.
45mm
+0,5 - 0,0
45mm
+0,5 - 0,0
1. Insert instrument into the panel cut-out.
2. Hold front bezel firmly (without pressing on display area), and re-fit mounting clamp. Push clamp forward, using a tool if necessary, until gasket is compressedand instrument held firmly in position.
Mounting plate Housing Latching groove Seal
Fig. 2 : Orientation
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Mounting
Slip the mounting clip from
behind onto the housing until the spring tab snaps in the latch.
Fig. 3: Mounting clip
After installing the instrument in the mounting plate, it may be removed from its housing, if
necessary (see the information on fitting and removing the optional modules).
NOTE!
The flanges of the mounting clip lock in position on both sides or on the top and
g
bottom side of the instrument housing. For optimum performance it is important to use the latches on the sides of the instrument.
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Electrical connection
2. Electrical connection
Fig. 4: Electrical connection
Connection of input INP1 Input for variable x1 (process value) a thermocouple b resistance thermometer (Pt100/ Pt1000/ KTY/ ...) c potentiometer d voltage (0/2...10V) e current (0/4...20mA) f Transmitter Power Supply
Connection of input INP2 current (0/4…20mA and 0…30mA AC).
Connection of inputs di1/di2/di3 and di4 Digital inputs for switching functions, e.g. SP and SP.2/SP.e or programmer Run/Stop/Reset.
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3. Operation
3.1 Front view
Fig. 5: Front view
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.
3.2 Operating structure
Operation
1 Process value display 2 Set-point, controller output, parameter 3 Status of switching outputs 4 Gradient is active 5 Manual mode 6 Timer or programmer is running 7 Set-point SP.2 oder SP.e is effective
8 Function key 9 Changing the set-point or the controller
output value 0 Acknowledges alteration of a value or shows the next parameter/value
After supply voltage switch-on, the controller starts with the operating levels. The controller status is as before power off.
Fig. 6: Complete operating structure (depending on configuration)
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The setting in the function level or in BlueControl® (engineering tool), individual layers can be locked or made accessible by entering the password in.
Individual parameters accessible without password must be copied to the extended operating level via BlueControl
When supplied, all levels are fully accessible, Password PASS = OFF
3.2.1 Operating Level
Operation
®
.
See also chapter 3.4 Operating level
And chapter 3.6 Function level
3.3 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 before power-off, the controller starts with the last
correcting value after switching on again.
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3.4 Operating level
The operating level comprises two views for setpoint and controller output value. The operating level can be enhanced with two levels
Extended operating level Function level (see chapter 3.6)
The content of the extended operating level and the function level is determined by means of BlueControl (engineering tool). Parameters which are used frequently or the display of which is important can be copied to the extended operating level.
Operation
Fig. 7: Operating level and function level
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Operation
3.5 Errorlist / Maintenance Manager
The error list is visible only if an error entry is present. An active entry in the error list is displayed by a red/green blinking 2nd line and status LED’s in the display.
Err-Status Signification Proceed as follows
2. line blinks red
.. is red error
.. is green no error
All errors can be reset in the function level with Err È rSET (if configured).
3.5.1 Error-List:
Name Description
E.1
E.2
E.4
FBF. 1/2
Sht. 1/2
POL.1
HCA
SSR
existing error
- determine the error type in the error list via the error number
- remove error
- Acknowledge the alarm in the error list by pressing key
removed
È - The alarm entry is deleted.
Cause Possible remedial action
Internal error,
E.g. defective EEPROM Contact PMA service
cannot be removed
Internal error, can
e.g. EMC trouble -shortly separate the device from
be reset
Internal error, option modules
HW-Coding does not match the current recognized HW configuration
Sensor break INP1/2
Short circuit INP1/2
Sensor defectiveFaulty cabling
Sensor defectiveFaulty
cabling INP1 polarity error Faulty cabling Reverse INP1 polarity Heating current
alarm
- Heating current circuit interrupted, I <
or I >
HC.A
of configuration)
- Heater band defective
Heating current short circuit
- Current flow in heating
HC.A
(dependent
È - or
Send- in device
mains supply
- Keep measurement and power supply cables in separate runs
- Contact PMA service, send-in device or check option modules
Replace INP1/2 sensor Check INP1/2 connection
Replace INP1/2 sensor Check INP1/2 connection
-Check heating current circuit
- If necessary, replace heater band
-
Check heating current circuit
- If necessary, replace solid-
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Loop
AdA.H
Control loop alarm - Input signal defective
Self-tuning heating alarm (ADAH)
Ada.C
Self-tuning cooling alarm (ADAC)
Lim.
stored limit alarm adjusted limit value
1/2/3
Inf.1
time limit value message
Inf.2
duty cycle message (digital ouputs)
3.5.2 Error-Status (Self-tuning)
(error status 3 - 9 only with error AdA.H / AdA.C ):
Err-Status Description Behaviour
1
Stored error Delete the entry after acknowledgment
2
Existing error Change to error status 1 after error removal
3
Faulty control action Re-configure controller (inverse i direct)
4
No response of process variable
5
Low reversal point Let process cool down and start new adaptation attempt
6
Danger of exceeded set-point (parameter determined)
7
Output step change too small
8
Set-point reserve too small
9
Impulse tuning failed The control loop is perhaps not closed: check sensor,
Operation
circuit at controller off
state relay
- SSR defective
- Check heating or cooling circuit or not connected correctly
- Output not connected correctly
See Self-tuning heating error status
See Self-tuning cooling error status
- Check sensor and replace
it, if necessary
- Check controller and
switching device see Self-tuning heating error
status
See Self-tuning cooling error status
check process
1/2/3 exceeded
adjusted number of
application-specific
operating hours reached
adjusted number of duty
application-specific
cycles reached
The control loop is perhaps not closed: check sensor, connections and process
If necessary, increase (inverse) or reduce (direct) set­point
Let process cool down and start new adaptation attempt
Increase set-point (invers), reduce (direkt)
connections and process
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3.6 Function level
Switching functions via è key. The function level serves for the enhanced operation of the device. You can switch
functions such as manual / automatic, Sollwert/Sp.2/Sp.E, ... via the operation level on the controller are performed. It's content is determined by configuration ( LOGI ):
Err
Ereset
SP
SP.E
SP.2
Y
Y2
Y.ext
On
In the sequence above the list can be scrolled with the are adjusted, with Ù or latest 2 seconds after adjustment, the value is taken over.
Pressing key è returns to normal operation.
Operation
No reset of the error list
Resetting thr error list Internal setpoint active External setpoint active 2nd setpoint active Internal correcting variable
2. correcting variable External correcting variable
Controller/Signaller and Limit 1 are active
Off
Auto
Man
Bo.Off
Bo.On
Para.1
Para.2
Loc
rem
Controller/Signaller and Limit 1 are switched off
Automatic operation Manual operation Boost function not active Boost function aktive First parameter set aktive Second parameter set aktive Local-operation adjustment via front-
panel possible Remote-operation adjustment via
front-panel not
possible
Ù-key. With the keys ÌÈ values
Example (switching from internal setpoint to SP.2)
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3.7 Self-tuning
(automatic adaption of control parameters) For determination of optimum process parameters, self-tuning is possible. After starting by the operator, the controller makes an adaptation attempt, whereby 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
ti1
td1
t1
Pb2
ti2
td2
t2
Operation
Proportional band 1 (heating) in engineering units [e.g. °C] Integral time 1 (heating) in [s] r only, unless set to OFF Derivative time 1 (heating) in [s] r only, unless set to OFF Minimum cycle time 1 (heating) in [s]. This parameter is optimized only, unless
parameter Cntr/Adt0 was configured for “no self-tuning” using BlueControl
®
Proportional band 2 (cooling) in engineering units [e.g. °C] Integral time 2 (cooling) in [s] r only, unless set to OFF Derivative time 2 (cooling) in [s] r only, unless set to OFF Minimum cycle time 2 (cooling) in [s]. This parameter is optimized only, unless
parameter Cntr/Adt0 was configured for “no self-tuning”using BlueControl
®
Parameterset 2: according to Parameterset 1 (see page 23)
3.7.1 Preparation before self-tuning
o The limits of the control range must be adjusted for the controller operating range, i.e.
rnG.L and rnG.H must be adjusted to the limits within which control must take place ConfigurationrControllerrspan start and end of control range)
ConFrCntrrrnG.L and rnG.H
o Determine which parameter set must be optimized.
- The currently effective parameter set is optimized. r activate the corresponding parameter set (1 or 2).
o Determine which parameter must be optimized (see the list given above) o Select the method for self-tuning (See Chapter 3.7.616)
- Step attempt after start-up
- Pulse attempt after start-up
- Optimization at the set-point
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Operation
3.7.2 Optimization after start-up or at the set-point
There are two methods of optimization; either after start-up or at the set-point. As control parameters are always optimal only for a limited process range, various methods can be selected dependent of requirements. If the process behavior is very different after start-up and directly at the set-point, parameter sets 1 and 2 can be optimized using different methods. page 23).
Switch-over between parameter sets dependent of process status is possible (see
Optimization after start-up: (see page 17)
Optimization after start-up requires a certain separation between process value and set­point. This separation enables the controller to determine the control parameters by evaluation of the process whilst progressing 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 then recommend a
“Pulse attempt after start-up”.
Optimization at the set-point: (see page 17)
For optimizing at the set-point, the controller outputs a disturbance variable to the process. This is done by briefly changing the output variable. 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 set­point. The advantage is in the small control deviation during optimization.
3.7.3 Selecting the method ( ConF/ Cntr/ tunE)
Selection criteria for the optimization method:
tunE Step attempt
after start-up
= 0 sufficient set-point
reserve is provided
= 1 sufficient set-point
= 2 Only step attempt after
Pulse attempt after start-up
Optimization at the set-point
sufficient set-point
reserve is not provided sufficient set-point
reserve is provided
reserve is not provided
start-up required
Sufficient set-point reserve: inverse controller: process value is (10% of rnGH - rnGL) below the set-point direct controller: process value is (10% of rnGH - rnGL) above the set-point
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3.7.4 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 15). Subsequently, a correcting variable step change to 100% or Y.Hi is output.
The controller attempts to calculate the optimum control parameters from the process 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% or Y.Lo (100% cooling energy) is output from the set-point. After successful determination of the
“cooling parameters”, the controller will proceed to the setpoint using the optimized parameters.
3.7.5 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 15) Subsequently, a short pulse of 100% or Y.Hi 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 stabilized to the set-point.
With a 3-point controller, this is followed by “cooling”. After completing the 1st step as described and stabilized 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 parameters”, the optimized parameters are used for stabilized to the set-point.
Operation
3.7.6 Optimization at the set-point
Conditions:
A sufficient set-point reserve is not provided at self-tuning start (see page 16). tunE is 0 or 1 With Strt = 1 configured and detection of a process value oscillation by 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
9499-040-93811 / 59537-1 Page 17 of 88 Pro-16
Operation
with active gradient function ( PArA/ SETP/ r.SP OFF), the set-point
gradient is started from the process value and there isn't a sufficient set-point reserve.
Optimization-at-the-set-point procedure:
The controller uses its instantaneous parameters for control to the set-point. In stable condition, the controller makes a pulse attempt. This pulse reduces the correcting variable by max. 20% 1, to generate a slight process value undershoot. The changing process is analyzed and the parameters thus calculated are recorded in the controller. The optimized parameters are used for stabilized to the set-point.
Optimization at the set-point
With a 3-point controller, optimization for the “heating“ or “cooling” parameters occurs dependent of the instantaneous condition.
While the controller is in the "heating-phase" the heating-parameters are determined. If the controller is in the "cooling-phase" the cooling-parameters are determined.
1 If the correcting variable is too low for reduction in stable condition it is increased by max. 20%.
9499-040-93811 / 59537-1 Page 18 of 88 Pro-16
t
Operation
Optimization at the set-point for 3-point stepping controller
As position feedback is not provided, the controller calculates the actuator position internally by adjusting 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 voltage 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 real position
Internal calculation
t
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 self­tuning start, it will occur automatically by closing the actuator once.
Unless the positioning limits were reached within 10 hours, a significant deviation between simulation and actual position may have occurred. In this case, the controller would realize minor internal calculation, i.e. the actuator would be closed by 20 %, and re-opened by 20 % subsequently. As a result, the controller knows that there is a 20% reserve for the attempt.
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3.7.7 Self-tuning start
The operator can start self-tuning at any time. For this, keys simultaneously. With blinking in the second row the active adaptation is displayed Ad:PIR. The controller outputs 0%, waits until the process is at rest and starts self­tuning: Ad:Stp
The self-tuning attempt is started when the following prerequisite is met:
The difference between process value i set-point must be 10% of the set-point
range ( SP.Hi - SP.LO) (with inverse action: process value smaller than set­point, with direct action: process value higher than set-point).
After successful self-tuning, the AdA-LED is off and the controller continues operating with the new control parameters.
Self-tuning cancellation by the operator:
Self-tuning can always be cancelled by the operator. For this, press simultaneously. The controller continues operating with the old parameters in automatic mode in the first case and in manual mode in the second case.
Self-tuning cancellation by the controller:
An error detected during self-tuning means that the technical conditions prevent successful self-tuning.
In this case, self-tuning was cancelled by the controller. The controller switches off its outputs (controller output 0%), to avoid exceeding the setpoint.
The user has two possibilities to acknowledge a failed adaptation:
1. Press keys The controller continues controlling using the old parameters in automatic mode. The self-tuning error must be acknowledged in the error list.
2. Press key 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 13: "Error status"
Operation
Ù and È simultaneously:
Ù :
Ù and È must be pressed
Ù and È key
Acknowledgement of failed self-tuning
When pressing the
Ù key, the controller switches over to correcting variable display
(Y ....). After pressing the key again, the controller goes to the error list of the extended
operating level. The error message can be acknowledged by switching the message to 0 using the Ì - or the È key. After acknowledging the error message, the controller continues operating in the automatic mode, using the parameters valid prior to self-tuning start.
3.7.8 Examples for self-tuning attempts
(controller inverse, heating or heating/cooling)
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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 attempt 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), 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).
Three-point controller a The parameter for heating and cooling are
determined in two attempts. The heating power is switched on (1). Heating parameters Pb1, ti1, td1 and t1 are determined at the reversal point. The process is controlled to the set­point (2). With constant control deviation, the controller provides a cooling correcting variable pulse (3). After determining its cooling parameters Pb2, ti2, td2 and t2 (4) from the process characteristics , control operation is started using the new parameters (5).
Operation
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During phase 3, heating and cooling are done simultaneously!
3-point-stepping controller After the start (1) the controller closes the
actuator (2 Out.2). When the difference between process value and set-point is big enough (3), the changing of the process value is monitored for 1 min. (4). Afterwards the actuator is opened (5 Out.1). If the reversal point is reached (6) or there are made enough measurements, the parameters are detected and are adopted.
3.8 Help for manual tuning
The optimization aid should 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 variable 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.
100%
X
max
0%
Values T be used to determine the maximum rate of increase v
y
Y
h
x
and x
g
Tu
(step change from 0 to 100 %) or t and x (partial step response) can
max
Tg
{X
{t
Operation
max
W X
1 min
1
2
5
6
4
3
.
t
t
y = correcting variable Yh = control range Tu = delay time (s) Tg = recovery time (s) X
= maximum process value
max
t
V
max
X
=
Tg
max. rate of increase of process value
x
Δmax
=
= max.
t
Δ
The control parameters can be determined from the values calculated for delay time Tu , maximum rate of
t
increase v according to the formulas given below. Increase Pb, if
, control range Xh and characteristic K
max
stabilized to the set-point oscillates.
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Pb1
td1
ti1
OFF
OFF
OFF
Parameter adjustment effects
Parameter Control Stabilized of disturbances Start-up behaviour
higher increased damping slower stabilized slower reduction of duty cycle
lower reduced damping faster stabilized faster reduction of duty cycle
higher reduced damping faster response to disturbances faster reduction of duty cycle
lower increased damping slower response to disturbances slower reduction of duty cycle
higher increased damping slower stabilized slower reduction of duty cycle
lower reduced damping faster stabilized faster reduction of duty cycle
Formulas
K = Vmax * Tu
With 2-point and 3-point controllers, the cycle time must be adjusted to
t1 / t2 ß 0,25 * Tu
3.9 Second PID parameter set
Operation
controller behaviour PID 1,7 * K 2 * Tu 2 * Tu
PD 0,5 * K Tu OFF PI 2,6 * K P K 3-point-stepping 1,7 * K Tu 2 * Tu
Pb [phys. units] td [s] ti [s]
6 * Tu
The process characteristic is frequently affected by various factors such as process value, correcting variable and material differences.
To comply with these requirements, the controller can be switched over between two parameter sets. Parameter sets PArA and PAr.2 are provided for heating and cooling.
Dependent of configuration, switch-over to the second parameter set (ConF/LOG/Pid.2) is via key
or interface (OPTION).
Self-tuning is always done using the active parameter set, i.e. the second
g
parameter set must be active for optimizing.
9499-040-93811 / 59537-1 Page 23 of 88 Pro-16
è , one of digital inputs di1…di4
O
3.10 Alarm handling
Max. three alarms can be configured and assigned to the individual outputs. Generally, 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 limit 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 of each limit value is adjustable.
Ü Operaing principle absolute alarm L.1 = OFF
Operation
¡ Operating principle relative alarm
L.1 =
FF
H.1 = OFF
H.1 = OFF
Normally open: See examples (ConF / Out.x / O.Act = 0) Normally closed: The output relay action is inverted (ConF/ Out.x / O.Act = 1)
The alarm LED always shows the threshold violation on (out of limits, switching point). If several alarms are used can be checked at the operating level, which alarm is active (
Ù …r Lim.1 Ù … Lim.3)
The variable to be monitored can be selected separately per configuration for each
g
alarm.
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The following variables are available ( ConF / Lim / Src .x ): Variable (Src .x) Remark Alarm type
Process value Absolute Control deviation xw Process value - effective set-point. The effective
Control deviation xw + suppression after start­up or set-point change with time limit
Effective set-point Weff
Correcting variable y y = controller output signal Absolute Deviation from SP
internal
Control deviation xw + suppression after start­up or set-point change without time limit
g
Function (Fnc.x) Remark Switched off No limit value monitoring.
Measured value Process value monitoring. When exceeding the limit, an alarm is
Measured value + latch Process value monitoring + latching of the alarm condition. When
During alarm configuration, the following functions can be selected ( ConF / Lim / Fnc.x ):
Operation
Relative set-point Weff is used. E.g with a ramp, this is the changing set-point rather than the target set-point.
The alarm output is suppressed after switch-on or after a set-point change, until the process value is within the limits for the first time. At the latest after elapse of time 10 x ti1 the alarm is activated (ti1 = integral time 1; parameter r Cntr). If ti1 is switched off (ti1 = OFF), this is considered as Î , i.e. the alarm is not activated before the process value was within the limits once.
The effective set-point Weff for control. Absolute
Process value - internal set-point. The internal set­point is used. E.g. with a ramp, this is the target set-point instead of the varying effective set-point Weff.
After switch-on or after a set-point change, the alarm output is suppressed , until the process value is within the limits for the first time.
generated.The alarm is reset automatically, when the process value is "within the limits" (including hysteresis) again.
exceeding the limit value, an alarm is output. A latched alarm persists, until it is reset manually.
Relative
Relative
Relative
9499-040-93811 / 59537-1 Page 25 of 88 Pro-16
4. Configuration level
4.1 Configuration overview
Configuration level
ConF Configuration level
È Ì
Cntr Control and self-tuning
ProG Programmer
InP.1 Input 1
InP.2 Input 2
Lim Limit value functions
SP.Fn t.bAS StYP I.Fnc Fnc.1 O.tYP O.Act
b.ti S.Lin StYP Src.1 O.Act Y.1 SP.2 Addr
C.Fnc Corr Fnc.2 Y.1 Y.2 SP.E PrtY
mAn Src.2 Y.2 Lim.1
C.Act Fnc.3 Lim.1 Lim.2
FAIL Src.3 Lim.2 Lim.3
Ù
rnG.L HC.AL Lim.3 LP.AL
rnG.H LP.AL LP.AL HC.AL
Sp2C HC.AL HC.SC boos
CyCL HC.SC TimE Pid.2
tunE TimE t.End
Strt t.End P.End
FAi.2 PrG.1
PrG2 PrG3
PrG4 CALL
OuT.0
out1 Output 1
P.End FAi.1
FAi.1 FAi.2
PrG.1 PrG2
PrG3 PrG4
CALL
Out.1
O.Src
ut3 Output 3
Out2 Output 2
O
See output 2
Out4 Output 4
out5 Output 5
See output 2
See output 1
out6 Output 6
Logi Digital inpu ts
L_r bAud
Y.2 dELY
y.E Unit
See output 2
mAn dP
C.oFF Led
Err.r C.dEl
P.run
P.oFF
di.Fn
othr Display, operation,
interface
End
quit
9499-040-93811 / 59537-1 Page 26 of 88 Pro-16
LOGI
E
SP.E
2
Configuration
level
Adjustment: To access the configuration level, press the key
Ì to select the ConF-Menu item. Press Ù to confirm.
Ù for 3 seconds and then the key
If the password function is activated, a prompt for PASS is displayed. The configuration values can be adjusted using the ÌÈ keys. Press the
Ù key to save the value. The next configuration value is shown.
After the last configuration value of a group, donE is displayed, followed by
automatic changing to the next group
g Return to the beginning of a group, by pressing the Ù key for 3 sec g Press menu item quit to close/cancel configuration
4.2 Configurations
Cntr
Name Value range Description Default
SP.Fn
b.ti 0…9999 Timer tolerance band 5 C.Fnc
Basic configuration of setpoint processing 0
0 set-point controller can be switched over to external set-point
(->
/ SP.
1 program controller 2 timer, mode 1 (bandwidth-controlled, switched off at the end) 3 timer, mode 2 (bandwidth-controlled, set-point remains active
at the end) 4 timer, mode 3 (switched off at the end) 5 timer, mode 4 (set-point remains active at the end) 6 timer, mode 5 (switch-on delay) 7 timer, mode 6 (set-point switch-over)
10 controller with start-up circuit (see page 71) 11
Fixpoint /
Control behaviour (algorithm) 1 0 on/off controller or signaller with one output 1 PID controller (2-point and continuous)
)
/ SP.
controller with start-up circuit (see page 71)
9499-040-93811 / 59537-1 Page 27 of 88 Pro-16
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