PID Loop - Start Here

Topic: DMD0245

Help File Version: 2.9.4.37

Process Control Instruction Set

The Do-more environment utilizes what we refer to as the Tinker-Toy™ approach to providing options that can handle various Process Control requirements. Rather than embedding the alarm handlers and Ramp / Soak tables within the PID instruction itself, these are all handled by separate instructions, allowing the proper level of customization for whatever control algorithms are used. The Do-more controller provides a full complement of Process Control related instructions that includes:

Process Control Utilities

The Do-more Designer programming environment has several utility programs to assist in the configuration, tuning and monitoring of PID loops:

The PID View - is where the majority of the work related to configuring, tuning, and monitoring PID loops will be done. The PID View is opened by selecting Debug-> PID View from the Online Toolbar, or right-clicking on any PID instruction in a ladder diagram and select Trend Instruction from the pop-up menu, or double-clicking on the PID Overview graphic for that PID loop.

The PID View is broken into three sections: the PID Data form which displays the current configuration of the underlying PID Loop, and two trend graphs (one with the .PV and .SP fields, and one with the .Output and .Bias fields) to see the results of the configuration and tuning efforts.

Using Auto-tune - the Do-more controller provides an automatic tuning function to help in achieving optimal P, I, and D values. Any of the terms set incorrectly can cause the process to be unstable, or very slow to control.

The PID Overview - is a container that will display a boilerplate for each Closed Loop Controller (PID) instruction used in a Do-more Designer project. The boilerplate for each PID Loop displays the most commonly needed runtime values and alarming information (if available).

Using the PID Process Simulator - the Do-more Simulator includes a PID Process simulator that can be used to demonstrate the process control abilities of the controller, or for testing potential changes to existing control solutions by working with the process control instructions in a simulation environment before deploying the control solution to a Do-more controller. The PID Process simulator uses a first order filter and a dead time calculation to provide the simulated PID loop response.

PID Structure Fields

Each Closed Loop Controller (PID) in a project has an associated data structure that is used to store its data.

Each of these structures contains members ("dot" fields) that can be used elsewhere in your ladder program. These structure members are updated each time the PID instruction is executed. The syntax for using them in other places in the project is <PID structure>.< member field>.

The Input fields of a PID loop are used for writing configuration data to the PID loop, to manage the PID loop's mode, and to manage the Autotune process. The Output fields of a PID loop are used to monitor the loop's response to its configuration and the input values. These fields are updated each time the PID instruction is executed as part of the ladder logic scan. Refer to the following chart for complete lists of the input and output fields, their data types, and acceptable ranges:

The Input fields of a PID loop are used for writing configuration data to the PID loop, to manage the PID loop's mode, and to manage the Autotune process. The Output fields are calculated by the PID algorithm and can be used to monitor the loop's response to its configuration and the input values. These fields are updated each time the PID instruction is executed as part of the ladder logic scan.

The following is a list of the"dot" fields that are programmatically accessible for each Closed Loop Controller instruction:

Field	Field Type	Field Name	Data Type	Description
.PV	Input	Process Variable	Real	The Process Variable (PV) is the input value that is being measured, typically from an analog input.
.SP	Input	Setpoint	Real	The Set point is the target value that the PID loop wants the Process Variable (PV) to reach.
.Gain	Input	Proportional	Real	The Gain (P) value sets the output of the PID loop proportional to the change in the process variable (PV). Larger values mean a faster output response since the larger the error, the larger the proportional term compensation. But, an excessively large proportional gain can lead to process instability and oscillation.
.Reset	Input	Integral	Real	The Reset (I) value determines how the PID loop output will change based on the amount of time (in seconds) there is an error between set point (SP) and the process variable (PV). Larger values eliminate steady state errors more slowly. The trade-off is larger overshoot: any negative error integrated during transient response must be integrated away by positive error before reaching steady state. The time base is seconds, so a value of 1.0 = 1 Second, 0.5 = 500ms, etc. A value of 0 disables the effect of this term in the PID calculation.
.Rate	Input	Derivative	Real	The Rate (D) value determines how the PID loop will respond based on the rate of change in the process variable (PV). Larger values decrease overshoot, but slow down transient response and may lead to instability due to signal noise amplification in the differentiation of the error. The time base is value / second, so a value of 1.5 = 1.5 / second, 0.75 = 0.75 / second, etc.
.Bias	Output	Bias	Real	In some modes the Bias is used to provide bumpless transfer from automatic to manual mode, and vice versa. Bias is set equal to the actual output value (with consideration of the Error term) when the loop is switched from manual to automatic mode.
.Output	Output	Control Output	Real	The output value from the loop calculation.
.ErrorDB	Input	Error Deadband	Real	The Error Deadband designates the area around Error value where no action will occur. The error deadband is the same above and below the setpoint. If 'Enable Error Deadband' has been selected in the PID instruction, this is where the deadband value is entered.
.DGainLmt	Input	Derivative Gain Limit	Real	If the magnitude of the loop calculation exceeds the derivative gain limit, the derivative component will be clamped at the specified limit.
.SampleTime	Input	Loop Sample Time	Integer	The SampleTime value designates how often the loop calculation is performed. The value is specified in milliseconds.
.Mode	Output (read-only)	Loop More	Bit	0 = Manual Mode 1 = Automatic Mode
.AutoTuning	Output (read-only)	Autotune Mode	Bit	0 = No Autotune in progress 1 = Autotune in progress
.AutoTuneComp	Output (read-only)	Autotune Complete	Bit	0 = Autotune complete 1 = Autotune is running
.AutoTuningErr	Output (read-only)	Autotune Error	Bit	0 = Autotune completed successfully 1 = Autotune did not complete successfully, loop is not tuned.
.RanThisScan	Output	Loop calculation ran this scan		0 = Loop Calculation was not performed on the current PLC scan 1 = Loop Calculation was performed on the current PLC scan
.Tune	Input	Autotune	Bit	Initiates an Autotune: 0 = Stop Autotune 1 = Start Autotune
.TuningAlg	Input	Tuning Algorithm	Bit	Designates whether the Autotune should use an Open Loop or Closed loop algorithm: 0 = Closed Loop 1 = Open Loop
.TunedParms	Input	Tuning Parameters	Bit	Designates whether the Autotune should use a PI or PID calculation: 0 = PI 1 = PID
.LastError	Output (read-only)	Error value	Real	The Computed Error value, that is, the difference between a measured process variable (PV) and a desired setpoint (SP).

Process Control Instruction Set

Process Control Instruction Set

PID Calculation and Tuning Constants

Alarm Handlers

Input and Output Value Limiters

Noise Suppression

Ramp / Soak Profiles - up to 250 steps per Profile

Input and Output Scaling

Emulate Analog Level Control with a Discrete Output Device

Process Control Utilities

PID Structure Fields

See Also: