PRESSURE CONTROL LOOP TRAINER
OVERALL SYSTEM CAPABILITY:
Unitech
Scales and Measurements Pvt. Ltd, Bangalore proudly announces the introduction
of PRESSURE LOOP CONTROL training system for the Instrumentation and process
control students and Industrial Technicians. This system is the outcome of our
production team effort, which mainly suits to the syllabi of the
Instrumentation courses.
Typically,
the training system is comprised by four independent process (like temperature,
pressure, level and flow). Each work process is individually supported by a
100% compatible for the common PC which acts as the PID controller. This helps
the student to visualize the process graphically on the screen.
Each
individual Process can equip the instrumentation and control laboratory to
train students and industrial technicians on how to inspect, hands on
experiment and tuning and the process control systems.
Each
process trainer is provided with one latest PC based software for independent
operation. All the parameters of the process trainer are controlled by the
software. ON-OFF, Proportional, Integral and Derivative control (PID control)
are done by software. Since each process station is based on the PC.
Introduction:
Proportional,
integral, and Derivative controller or PID is a standard feedback loop
component in industrial control applications. It measures an “output” of a
process and controls an “input”, with a goal of maintaining the output at a
target value, which is called the “setpoint”. An example of a PID application
is the control of a process temperature, although it can be used to control any
measurable variable which can be affected by manipulating some other process
variable.
The
Controller compares a measured value from a process (typically and industrial
process) are as follows
Industrial processes are procedures involving chemical or
mechanical steps to aid in the manufacture of an item or items, usually carried
out on a large scale.
Industrial processes are the key
components of heavy industry.
Most
processes make the production of an otherwise rare material vastly cheaper,
thus changing it into a commodity i.e. the process makes it economically
feasible for society to use the material on a large scale. One of the best
examples of this is the change in aluminum from prices more expensive than
silver to its use in recyclable/disposable beverage containers.
An
industrial process differs from a craft, workshop or laboratory process by the
scale or investment required. Most of the processes are complex and require
large capital investments in machinery, or a substantial amount of raw
materials, in comparison to batch or processes. Production of a specific
material may involve more than one type of process.
The
difference (or “error” signal) is then used to calculate a new value for a
manipulatable input to the process that brings the process’ measured value back
to its desired setpoint. Unlike simpler control algorithm, the PU) controller
can adjust process outputs based on the history and of change of the error
signal, which gives more accurate and stable control. (It can be shown
mathematically that a PID loop will produce accurate, stable control in cases
where a simple proportional control would either have a steady state error or
would cause the process to oscillates). PD controllers do not require advanced
mathematics to design and can be easily adjusted (or “tuned”) to the desired
application, unlike more complicated control algorithms based on optimal
control theory.
Theory:
PROPORTONAL BAND
The
control algorithm that generates a linear control output proportional to
deviation is called proportional action. in proportional action the amount of
change in the measured valve (Or deviation) is expressed in percent of span
that is required to cause the control output to change from 0 to 100% is called
the proportional band.
INTEGRAL TIME
With
P action the measured valve will not necessarily become equal to the set the
point, and a deviation will usually be present. The control algorithm that
applies changes in output as long as a deviation exits, so as to bring the
deviation to zero, is called integral action.
When integral action is used, the parameter that determines
how fast the output will in correspondence to some amount of deviation is
referred to as integral time, and shorter the integral time, stronger the
integral action (the greater the output rate of change). I action is usually
used together with P action as P1 action, and due only to I became equal to
that due only to P action.
DERIVATIVE TIME:
If
the controlled object has a large time constant or dead time, with P or P1
action alone there will be cases where the response will be slow, overshoot
will occur, and the control system will be unstable. In order to achieve faster
response and more stable operation cases one uses derivation action (D action)
to apply an output component proportional to the input (deviation) rate of
change.
D
action must always be used with P action time required with PD action. If a
ramp input (constant rate of change input) is applied, for the output due to P
action alone to become equal to that due to D action alone. The longer the
derivation time, the stronger the derivation action.
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