Evaluating Response Performance
Engineers and technicians must be able to evaluate the performance of control
loops. Quantitative measures of performance are needed. These measures can also
be used to measure "good" response in order to select the tuning parameters of
controllers.
What is "good response"? The answer naturally varies depending on the function
and objectives of the system. In general, though, a good response will display
as many of these characteristics as possible:
- Response has constant size and magnitude
- Stable
- Fast
- Maximum disturbance rejection
- Minimum delay
- No offset
- Limited control action (manipulation cost)
- "Robust" -- insensitive to process changes and model mismatch
Usually, it is not possible to satisfy all these points equally, but
understanding of the process should help you decide which get priority.
Time Domain Performance Specifications
Most performance specifications are based upon an underdamped response, since
most common processes under feedback control show underdamped behavior.
Speed of Response
Several values can be used to examine the speed of response.
- Rise Time (tr) The time for the process to first cross
it's new steady state value.
- Time to First Peak (tp) The time for the process to
reach its maximum value.
- Settling Time (ts, a.k.a. Response Time) The time required for the process
to become "nearly constant", that is the time required for the output to reach
and remain inside a fixed error band about the steady state. We will
use a band of 5 percent, although sometimes 1 and 3 percent are also
used. The settling time may also be described as the "95% response time", etc.
Acceptable Oscillation
Various measures are available for the extent of oscillation.
- Damping coefficient Often in tuning controllers, a target
damping coefficient of 0.4 is used.
- Overshoot The fraction of the final steady state change by which
the first peak exceeds that change. Expressed as a ratio or as a percent, given
by
- Decay Ratio The ratio by which the oscillation is reduced
during one complete cycle, or the ratio of successive peak heights. A
"one quarter" decay ratio is a traditional standard. The ratio can be
calculated from
- Period (T) (or frequency (f)) of oscillation. The time between successive
peaks. The frequency is the reciprocal of the period. (Note that control
calculations often require frequency in terms of radians/second, not in Hz.)
When the system is undamped, it oscillates without attenuation. Under these
circumstances,
the natural frequency of the system. Consequently,
Performance Specifications -- Second Order Step Response
If a particular system is specified, many of the performance
specification values can be determined analytically.
Since the majority of process systems can be approximated by a first
order model, a second order underdamped system is probably the most
commonly analyzed closed-loop response. With that in mind, consider the
second order underdamped system given by
forced by a unit step input
to obtain the time response
The formulas which follow are derived for this case
only.
Speed of Response
The period can be shown to be
The frequency is
The rise time will be about one-fourth of the period, or can be found
from
The settling time for a 1% limit will be
Acceptable Oscillation
Two formulas are available for calculating the overshoot:
Choices are also available for finding the decay ratio:
Both the overshoot and the decay ratio are readily measured and
calculated from an output response plot, the formulas can be used with
the measured value to determine an estimated value of the damping
coefficient.
These expressions are useful -- but remember! they only apply to a true
second order step response with defined initial conditions.
References:
- Coughanowr, D.R. and L.B. Koppel, Process Systems Analysis and
Control, McGraw-Hill, 1965, pp. 88-90.
- Luyben, W.L., Process Modeling, Simulation, and Control for Chemical
Engineers (2nd Edition), McGraw-Hill, 1990, pp. 226- 227.
- Marlin, T.E., Process Control: Designing Processes and Control
Systems for Dynamic Performance, McGraw-Hill, 1995, pp. 242-245.
- Riggs, J.B., Chemical Process Control (2nd Edition),
Ferret, 2001, pp. 186-189.
- Smith, C.A. and A.B. Corripio, Principles and Practice of Automatic
Process Control (2nd Edition), John Wiley, 1997, pp. 53-56.
R.M. Price
Original: 11/18/93
Modified: 2/28/97, 4/13/98, 5/26/2003, 7/8/2003
Copyright 1998, 2003 by R.M. Price -- All Rights Reserved