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Sommaire du brevet 1131327 

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  • lorsque la demande peut être examinée par le public;
  • lorsque le brevet est émis (délivrance).
(12) Brevet: (11) CA 1131327
(21) Numéro de la demande: 1131327
(54) Titre français: METHODE ET APPAREIL DE CONTROLE AVEC DISPOSITIF POUR EMPECHER LA REMISE A L'ETAT INITIAL
(54) Titre anglais: CONTROL METHOD AND APPARATUS WITH RESET WINDUP PREVENTION
Statut: Durée expirée - après l'octroi
Données bibliographiques
(51) Classification internationale des brevets (CIB):
  • G5B 11/06 (2006.01)
  • G5B 11/36 (2006.01)
(72) Inventeurs :
  • GANAWAY, FRANKLIN D. (Etats-Unis d'Amérique)
(73) Titulaires :
  • PHILLIPS PETROLEUM COMPANY
(71) Demandeurs :
  • PHILLIPS PETROLEUM COMPANY (Etats-Unis d'Amérique)
(74) Agent: OSLER, HOSKIN & HARCOURT LLP
(74) Co-agent:
(45) Délivré: 1982-09-07
(22) Date de dépôt: 1978-06-29
Licence disponible: S.O.
Cédé au domaine public: S.O.
(25) Langue des documents déposés: Anglais

Traité de coopération en matière de brevets (PCT): Non

(30) Données de priorité de la demande:
Numéro de la demande Pays / territoire Date
818,036 (Etats-Unis d'Amérique) 1977-07-22

Abrégés

Abrégé anglais


CONTROL METHOD AND APPARATUS
Abstract of the Disclosure
In a control method wherein a control signal is generated in
responsive to the deviation of a process variable signal from a setpoint
signal and the time integral over this deviation, the windup of the
respective controller is prevented by automatically modifying this deviation
by a signal representative of the difference between the control signal
and the process control signal such as to reduce the deviation of the
process variable signal from the setpoint signal by an amount represent-
ative of the difference mentioned.

Revendications

Note : Les revendications sont présentées dans la langue officielle dans laquelle elles ont été soumises.


The embodiments of the invention in which an exclusive
property or privilege is claimed are defined as follows:
1. A control method comprising
(a) automatically generating a control signal representative
of the deviation of a process variable signal from a setpoint signal and
of the time integral over said deviation,
(b) automatically generating a process control signal for
manipulation of a process parameter,
(c) automatically generating a difference signal representa-
tive of the difference between the process control signal and the control
signal,
(d) automatically reducing said deviation by a value
representative of said difference signal.
2. A method in accordance with claim 1 wherein said process
control signal is generated by automatically selecting one signal as said
process control signal from a group of signals conprising said control
signal.
3. A method in accordance with claim 2 wherein said group of
signals comprises at least one further control signal representative of
the deviation of a further process variable signal from a further
setpoint signal.
4. A method in accordance with claim 3 wherein the lowest
control signal of the group of signals is automatically selected as said
process control signal.
5. A method in accordance with claim 3 wherein the highest
of the group of signals is automatically selected as said process control
signal.
6. A method in accordance with claim 2 wherein said group of
signals consists of said control signal and a limit signal.

7. A method in accordance with claim 6 wherein the lower
of the two signals is selected as said process control signal.
8. A method in accordance with claim 6 wherein the higher
of the two signals is selected as said process control signal.
9. A method in accordance with claim 2 wherein said group of
signals consists of said control signal, a low limit signal and a high
limit signal and wherein said process control signal is automatically
selected so that its value is not higher than that of the high limit signal
and not lower than that of the low limit signal.
10. A method in accordance with claim 3 comprising
(a) automatically generating at least one further difference
signal representative of the difference between the process control signal
and the respective further control signal,
(b) automatically reducing the deviation of the respective
further process variable signal from the respective further setpoint
signal by a value representative of the respective further difference signal.
11. A method in accordance with claim 1 wherein said control
signal comprises a proportional component being the linear function for
said deviation and additively combines therewith an integral component
being the linear function of the time integral over said deviation.
12. An apparatus for generating a control signal comprising
(a) controller means for automatically converting an input
signal into a control signal representative of the deviation of a process
variable signal from a setpoint signal and of the time integral over this
deviation,
(b) generator means for generating a process control signal
connected to said controller means,
(c) anti-reset windup means comprising
21

(aa) difference means connected to said generator means
and to said controller means for generating a difference signal repre-
sentative of the difference between the process control signal and the
control signal,
(bb) reduction means connected to said difference
signal means and to said controller menas and adapted to reduce the
deviation of said process variable signal from said setpoint signal by a
value representative of said difference signal.
13. An apparatus in accordance with claim 12 wherein said
generator means comprise at least two inputs and one output,
wherein one of said inputs is connected to said controller means
receiving said control signal,
wherein at least one further input of said generator means
is connected to a further control signal source,
wherein said generator means further comprises a selector
adapted for automatically selecting one of the inputs and providing the
respective signal at the output as said process control signal.
14. An apparatus in accordance with claim 12 wherein the means
are composed of electrical analog circuits.
15. An apparatus in accordance with claim 14 wherein said
controller means are selected from the group consisting of PI and PID
controllers and wherein said generator means is selected from the group
consisting of high limit circuits, low limit circuits, high limit and low
limit circuits, high select circuits and low select circuits.
22

16. An apparatus in accordance with claim 12 wherein said
further signal source is a further control means adapted for converting
a further input signal into a further control signal representative of
the deviation of a further process variable signal from a further setpoint
signal, said further signal source being connected with the output furnishing
the further control signal to said generator means being selected from the
group consisting of high select and low select circuits and providing as
said process control signal at the output of said generator means a signal
representative of the higher or respective lower of the control signals
at the inputs of the generator means.
17. An apparatus in accordance with claim 12 wherein said
difference means comprise an operational amplifier receiving the control
signal and the process control signal of the controller means or respectively
the generator means at its inverting or respectively noninverting input
and adapted to generate an output signal representative of the difference
between the process control signal and the control signal and wherein said
reduction means comprise a further operational amplifier connected with
its respective input to the output of the difference signal operational
amplifier as well æ to a process variable signal input and wherein this
operational amplifier is adapted for changing the size of the process
variable signal by an amount corresponding to the output signal of the
difference means and in a direction such as to reduce the deviation of
the process variable signal from the respective setpoint signal.
23

CLAIMS SUPPORTED BY SUPPLEMENTARY DISCLOSURE
18. A method in accordance with claim 1 wherein said process
control signal is used to manipulate a process parameter so as to maintain
said process variable signal generally equal to said setpoint signal.
19. A method in accordance with claim 3 wherein the effect of a
change in said process variable signal on said control signal is delayed
for a time T representative of the time delay necessary to generally
reduce oscillations of said process variable signal about said setpoint
signal.
20. Apparatus in accordance with claim 14 wherein said reduction
means comprise:
means for combining said difference signals and said process
variable signal;
means for supplying said difference signal to said means for com-
bining said difference signal and said process variable signal;
delay means;
means for supplying said process variable signal to said delay
means; and
means for supplying said process variable signal from said delay
means to said means for combining said difference signal and said process
variable signal.
24

Description

Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.


3~t7
CONTROL METHOD AND APPARATUS
WITH RESET WINDUP PREVENTION
This invention relates to control methods. More specifically,
the invention relates to an anti-reset windup method by which the winding
up of 8 controller reset or a controller having an integral portion
representative of the time integral over the deviation of the process
variable signal from the set point is avoided. In accordance with a
further aspect, this invention relates to a circuit and apparatus for
carrying out the control method.
Background of the Invention
Automatic control system for the control of physical or
chemical procesæes have been known for a long time and are further
refined particularly by using digital or analog computer equipment. One
control system that has considerable advantages in many applications
involves so called PI or PID controllers. These controllers generate a
control signal composed of a first portion that is proportional to (P~, a
second portion that is the time integral of ~I~ and optionally a third
portion that is the time derivative of ~D~ the deviation of a process
variable signal from a setpoint.
In case where these PI or PID controllers are used in
connection with a circuitry that limits the size of the control signal or
in connection with a circuitry that selects among two or more of the
controllers described, the problem arises that the controller which is
not actually used does not have a "feedback" through the controlled
process. Therefore the integrator portion of the controller winds up
until the controller has reached the maximum output signal possible.
This is very undesirable because the control signal of the respective
windup controller then is not representative of the desired control
action anymore when the respective controller becomes active again.
-1- ..
,~

3~7
The Invention
It is thus one object of this invention to provide a control
method in which the windup of a controller is prevented. A further object
of this invention is to provide a control circuit or apparatus that does
not wind up while the control is achieved by a process control signal
different from the control signal generated by this control circuit.
Another object of this invention is to provide a control
method and apparatus having a controller with an anti-reset windup portion
that is equally useful in connection with select circuits and with limit
circuits without the necessity of switching off the controller while it
is not in active use.
A still further object of this invention is to provide means
of preventing reset windup of a controller when the controller output is
an input to a limiter circuit, to a high select circuit or to a low-select
circuit.
Furthermore, it is an object of this invention to provide a
control method and apparatus in which effective control of a process variable
is maintained while the operation is carried out near one or more fixed or
varying process constraints.
In accordance with this invention, there is now provided an
improved control method wherein a control signal is generated representative
- of a deviation of a process variable signal from the setpoint signal and
of the time integral over this deviation. The improvement in accordance
with this invention consists in automatically reducing the deviation men-
tioned by an amount representative of the difference between an actually
used process control signal and the control signal generated. In the
simplest and therefore preferred case this amount is proportional to the
difference, although other relationships can be- used. If this difference
is zero, the amount mentioned is zero also.

~3~ 7
More specifically, the control method of the present invention
comprises the following steps: A control signal representative of the
deviation of a process variable signal from a setpoint signal and of the
time integral over this deviation is automatically generated. In addition
to the control signal a process control signal for manipulating a process
parameter is automatically generated. This process control signal may
be the control signal or it Inay be another signal. A difference signal
representative of the difference between the process control signal and the
control signal is automatically generated. The value of this difference
signal is zero if the process control signal is the control signal.
The deviation of the process variable signal from the setpoint signal is
automatically reduced by an amount representative of the difference signal
mentioned. This reduction of the deviation is preferably done by summing
the process variable signal 180~ out of phase with the difference signal.
In the case when the amount by which the deviation is reduced is proportional
to the difference signal, the factor by which the difference signal is
multiplied or the gain given to the difference signal preferably is about
equal to the gain of the process control loop in which the control signal
mentioned is generated.
Summarizing, the function of the anti-reset windup circuit
of this invention is to prevent the windup of a controller having!reset
or integrator',means in the case where the controller output signal is
operated on by a nonlinear function such as a magnitude signal selector
or a fixed limiter. The anti-reset windup circuit provides a means of
measuring the potential differe~ce from the output of the controller
to the output of the nonlinear operator, to amplify this difference
signal and sum it with the controller process variable signal in such phase
as to reduce the error or deviation signal to the controller. The gain
of this anti-reset windup circuit which is in fact a second feedback

3~
loop is in most applications not critical but should always be at least
equal to or greater than the gain of the process in which the respective
controller is controlling. Preferably, the gain of the an'i~reset windup
circuit loop equals the gain of the corresponding process control loop.
The effect of the anti-reset windup circuit is to limit further reset action
of the controller when the controller output signal is no longer controlling
the process.
As the process variable changes so as to reverse the sign of
the "actual" controller error or deviation signal, the proportional offset
across the nonlinear operator achieved by the anti-reset windup circuit
is reduced to zero and the integrator portion of the controller is at the
same position as when the controller output became limited or deselected
by the nonlinear operator. In this control system, effective controller
action therefore can be maintained while the control operation is carried
out against a process constraint.
The method of this invention is particularly useful in control
situations where the process control signal is generated by automatically
selecting one signal as the process control signal from a group of
signals comprising the control signal. Such a group of signals can
consist of the control signal and at least one further control signal
which is representative of the deviation of a further process variable
signal from a further setpoint. This further control signal can also
be the output of a PI or PID controller. The selection of the process
control signal from the group of control signals can be a so-called high
select or a low select mode. In case of the high select mode, the higher
of two control signals or the highest of a number of control signals is
selected as the process control signal whereas in the case of the low select
mode the lower of the two control signals or the lowest of a number Qf
control signals is selected as said process control signal.

~L3~Z'~
In the last-mentioned case of having a plurality of control
signals generated by a PI or PID controller, i.e. in-cases-~h~re-each
one of the control signals is composed of a first portion proportional
to the deviation of the respective process variable signal from the
respective setpoint signal and of a second portion which is proportional
to the time integral over this deviation, it is particularly advantageous
and therefore preferred to modify the deviation of every controller that -
is not in active use by reducing the deviation by a value representative
of the difference signal obtained by subtracting the process variable
signal and the control signal generated by the respective controller.
In another embodiment of this invention, the process control
signal is selected from a group of signals consisting of the control
signal and a limit signal. This limit signal can be a lower limit or an
upper limit signal. In the first-mentioned case, the process control signal
will be the larger of the two signals whereas in the last-mentioned case
the process control signal will be the lower of the two signals. It is
also within the scope of this invention to select the process control
signal from a group of signals consisting of the control signal, an upper
limit and a lower limit signal with the provision that the process control
signal is neither higher than the high limit signal nor lower than the low
limit signal.
In the presently preferred control method of this invention,
the control signal comprises a proportional component being a linear
function of the deviation and additively combined therewith an integral
component being a linear function of the time over the deviation.
Mathematically, the relationship between the control signal cs, the process
variable signal pvs and the setpoint signal sps can be expressed by the
following formula:
cs = a(sps-pvs) ~ b ~ (sps-pvs)dt

3;2~
wherein a and b represent constants and wherein the time integral
symbol is employed in the usual manner.
In accordance with a further embodiment of this invention,
there is also provided an apparatus for generating a control signal.
This apparatus comprises controller means for automatically converting an
input signal into a control signal representative of the deviation of a
process variable signal from a setpoint signal and of the time integral
over this deviation. The apparatus further comprises generator means for
generating a process control signal. These generator means are connected
to the controller means and provide a process control signal at the
output of the generator means that either is the control signal or ifi_a-
process signal different from the control signal. In accordance with this
invention the apparatus comprises anti-reset windup means which in turn
comprise difference signal means and reduction means. The difference
signal means is connected to the controller means and to the generator
means and the difference signal means generates a difference signal which
is representative of the difference between the process control signal and
the control signal. The reduction means in turn are connected to the
difference signal means and the controller means in such a manner as to
reduce the deviation of the control signal from the input signal by an amount
representative of the difference signal generated by the difference signal
means.
More specifically and in accordance with a preferred
embodiment, the generator means comprise at least two inputs and one
output. One of the inputs of the generator means is connected to the
controller means receiving the control signal. At least one further input
is connected to a further signal source. The generator means comprises
a selector adapted for automatically selecting one of the input signals and
generating a process control signal corresponding to the selected input
~6~

1iL3~L3~
signal at the output of the generator. Among the process control signal
generator means, those are presently preferred that can be characterized
as belonging to the group consisting of high select modes, low select
modes, high limit modes, low limit modes and high and low limit modes. The
high select mode i5 a selector apparatus or circuit that automatically
selects among the input signals that one with the highest signal value and
furnishes this signal or a signal representative thereof to its output.
Oppositethereto the low select mode is an apparatus or circuit that selects
the input signals of the lowest value and transmits this input signal or
a signal representative thereof to its output. Among those high or respect-
ively low select circuits, those with two inputs in which the higher or
the lower of the two inputs, respectively, is furnished as the output
signal of the generator means or as the process control signal are
presently preferred.
The high or respectively low limit mode is a process control
signal generator that only has two inputs, one for receiving the control
signal and one for receiving either the high limit or the low limit signal
respectively. The generator means in this embodiment comprise a selector
which in case of the high limit mode furnishes the control signal at the
output as long as the control signal is below the high limit signal and
furnishes the high limit signal at the output whenever the control signal
is above the high limit signal; correspondingly, in case of the low limit
mode the selector furnishes the control signal at the output as the process
control signal whenever the control signal is above the low limit signal
and furnishes the low limit signal as the control signal at its output
whenever the control signal is below the low limit signal. The embodiment
of the high and low limit mode constitutes a combination of the high
limit mode and the low limit mode and thus comprises a selector circuit
that furnishes the low limit signal at its output as the process control
--7--

z~
signal when the control signal is below the low limit signal, furnishes
the control signal as the process control signal at its output whenever
the control signal is neither below the low limit signal nor above the
high limit signal and furnishes the high limit signal as the process control
signal at its output whenever the control signal is above the high limit
signal.
In the case of the generator being a high or low select
circuit it is preferred that this generator has at least two inputs and
one output. One of the inputs is connected to receive the control signal.
At least one further input is connected to receive at least one further
control signal which is representative of the deviation of a further process
variable signal from a further setpoint signal and of the time integral
over this deviation. This further control signal is provided by a further
controller means. In this embodiment, anti-reset windup means are preferably
provided for each controller means. Thus, at least one further anti-reset
windup means is connected to the generator means and to the further controller
means. The further anti-reset windup means comprises a further
difference signal means and a further reduction means. The further differ-
ence signal means is connected to receive the further control signal from
the further controller means and to receive the process control signal from
the generator means, and to generate a difference signal representative
of the difference between the process control signal and the further control
signal. The further reduction means is connected to the further difference
signal means and the further controller means is adapted to reduce the
deviaticn of the further process variable signal from the further setpoint
signal by an amount representative of the size of the difference signal.
Most preferably, two controller means as described, each being provided
with one PI controller and an anti-reset windup means are connected to the
generator means.

3;~7
The apparatus of this invention preferably is composed of
analog circuits. The controllers in the apparatus of this invention
preferably are PI and PID controllers. The generator means described are
preferably selected fromithe group consisting of high select circuits,
low select circuits, high limit circuits, low limit circuits, and high and
low limit circuits.
Among the apparatus embodiments of this invention, those in
which the individual means are analog electrical circuits composed
essentially of operational amplifiers are presently preferred.
The invention will yet be more fully understood from the
following description of the drawing, which is intended to illustrate
the preferred embodiments of this invention but not to unduly limit the
scope thereof.
In FIG~RE 1 a control system in accordance with this invention
is schematically illustrated. The process 1 and 1' show two sections of
two control loops of one and the same physical or chemical process.
These boxes may represent the sensing of different process variables or of
the same process variable. Depending upon the control system to be
described, different actions of manipulation are being taken. Thus the
process variable measured at 1 may be a temperature, the process variable
measured at 1' may be a flow rate; correspondingly, the process variable
that is manipulated in case of the control loop section 1 may be the heat
input and in control loop section 1' may be a catalyst circulation rate.
Thus whereas both control loop sections 1 and 1' relate to one and the same
chemical or physical process, the control dynamics of the respective
process loops can be and in most cases will be different from each other.
These process dynamics for the control loop section 1 are characterized
by Hpl and for the process control loop section 1' are characterized by
HP2 .

1~3~L~27
In the two control loops the different inputs and outputs of
the two systems are functionally the same and differ mainly in the
specific control constants. The various inputs and outputs therefore were
given the same letters or numerals and the description can therefore be
limited to one of the two control loops as well as the specific way of their
connection.
A controller 2 which preferably is a PI or a PID controller
is provided with one process variable input and a setpoint input E. The
setpoint input E receives a setpoint G in the form of a voltage from a
manual or variable setpoint source. The variable setpoint source may be
the output of a computation device. The process variable input F receives
correspondingly an input representative of the process variable from the
process control loop section 1. The controller 2 generates a control signal
at the output G, which is connected to the input H of a low select circuit
4. This low select circuit 4 also receives the control signal from the
second controller output G'. The low select circuit 4 selects the lower
of the two control signals received at its input H and K, respectively and
provides the lower of the two signals as the process control signal at its
output P. This process control signal manipulates a process variable in
order to bring the process variable signal at the input F or F' of the
controller 2 or respectively 2' back to the setpoint value at the input
E or respectively E' depending upon which one of the control signals at the
outputs G or G' the low select circuit 4 has selected as the process control
signal. Thus, depending upon the selection made in circuit 4, one of the
control loops is closed in the sense that the control signal provided
by the respective controller is the process control signal whereas the
other contr-ol loop is open in the sense that the control signal provided
by the respective controller is not used as the process control signal.
In the open control loop, no feedback via the process itself to the controller
--10--

1~3~3Z~
input F or respectively F' therefore exists and the danger of winding up of
the controller and more specifically of the reset or integrator portion
thereof exists. In accordance with this invention, such a windup is ef-
ficiently prevented by a circuit and method as will be described in the
following. Generically speaking, the reset windup prevention of the present
invention starts from a switching means (in the present example of the
drawing, a low select circuit 4) which selects between two signals that are
very similar in size in accordance with a given logic, e.g., it selects
the smaller or the larger of the two signals. The switch or selector cir-
cuit 4 also may be one that in case of all the input signals being the same
size selects one of them as the process control signal in accordance with
the direction or rate of change of the respective signal at a given move-
ment. Thus, the windup prevention of the present invention is not concerned
with a buntless transfer of different controllers into and out of the
respective control loop since at the point of transfer or switching or
selecting the respective signals are either the same or very nearly the
same size.
The reset windup prevention in accordance with this invention
is done by reducing the deviation of the process variable signal from the
setpoint signal in the controls loops that are open. The deviation men-
tioned is reduced by an amount that corresponds to the difference between
the respective control signal and the actually used process control signal.
Therefore, the anti-reset windup unit 3 (respectively 3') receives the
control signal from the output G or respectively G' at its input C or
respectively C' and also receives the process control signal from the
output P of the low select unit 4 at its input D or respectively D'. The
anti-reset windup units 3 or 3' in the simplest case modifies either the
setpoint signal or preferably the process variables such as to achieve
the reduction of the deviation between the process variable signal and
the setpoint signal as mentioned and as will be described in more detail
in connection with a special circuit later.
11--

327
FIGURE 2 shows an actual circuit being an analog electrical circuit
and comprising the controller 2 and the anti-reset windup circuit 3. Whereas
in FIGURE 1 a straight line was shown between the process variable input F
and the connecting point B between the controller 2 and the anti-reset wind-
up 3 in the specific embodiment shown in FIGURE 2 a zero span circuit 20 is
shown. This zero span circuit comprises one operational amplifier, a
constant voltage source and several resistors. The function of this zero
span circuit is merely to convert a milliampere signal at the input F into
a voltage signal at B. Thus, B can be thought of as the process variable
signal input.
Since the details and function of operational amplifiers are well
known and understood in the art, the operational amplifiers here are only
shown schematically as triangles with their inverting input characterized
by a minus sign and their noninverting input characterized by a plus sign.
All the resistors and the capicitor are shown in their sizes in either ohms,
kilohms or megohms and the capicitor is characterized in the yield weight by
the capacitance in microfarad.
The first operational amplifier 31 of the anti-reset windup circuit
receives, in the specific example, the control signal from the output G of
the controller 2 via the anti-reset windup input C. Via the input D of the
anti-reset windup circuit 3, this first operational amplifier 31 receives
the process control signal, e.g., from a low select circuit as shown in
FIGURE 3. Input D, in other words, is connected to the output P of
FIGURE 3.
-12-

The second operational amplifier 32 of the anti-reset windup
circuit receives at the inverting input thereof the signal from the
output b of the zero span circuit 20 as well as the output from the first
operational amplifier 31. The output of this second operational amplifier
32 therefore is corresponding to the process variable signal minus a
constant factor times the difference between the process control signal at
D and the control signal at C. This output of the second controller 32 of
the anti-reset windup circuit is referred to in the following as the
modified process variable signal. The third operational amplifier 33 of
the anti-reset windup circuit essentially has the function of reversing the
sign of the modified process variable signal. The output sign~l of this
third operational amplifier 33 is connected to the operational amplifier
21 of the controller circuit 2. This operational amplifier 21 also
receives the setpoint signal from the input F thereof. The output of the
operational amplifier 21 thus corresponds to the difference between the
modified process variable signal and the setpoint. The second operational
amplifier 22 of the controller 2 at its inverting input receives the
signal just mentioned. The output voltage at the output of the operational
amplifier 22 thus corresponds to the difference between the setpoint signal
and the modified process variable signal multiplied by a constant which
depends upon the proportional gain selected. This deviation signal at
the output of the operational amplifier 22 becomes a part of the ~Qntrol
signal at the output G of the controller 2. The output of the operational
amplifier 22 is connected to the inverting input of the operational amplifier
23. In addition to the portion that is proportional to the deviation signal,
the control signal at the output G also comprises integral part. This
integral part is supplied by an integrator circuit which comprises an
operational amplifier 24 having its output connected via a capacitor 25
-13-

~L~l3~ 7
to its input. The connection is achieved via a dual field effect transistor
and the size of the integral portion of the signal is determined by the
adjustable integral gain. For simplicity reasons, such portions of the
integrator as startup devices and switches have not been shown in the
drawing. The noninverting input of the operational amplifier 23 receives
the output of the operational amplifier 24 and the output of the operational
amplifier 23 thus is composed of a proportional portion which is proportional
to the deviation signal and an integral portion which is proportional to
the time integral over this deviation signal.
Summarizing again, the circuit shown in FIGURE 2 achieves a
modification of the process variable signal furnished via input F or
respectively B by an amount corresponding to the difference between the
actually used process control signal supplied to the input D and the control
signal generated by the oontroller 2 and supplied from its output G to the
input of the anti-reset windup unit C. The circuitry is such that the
modification of the process variable signal is accomplished to reduce
the difference between the process variable signal and the setpoint
signal furnished at the input E of the controller 2.
In FIGURE 3 a low select circuit 4 is schematically shown.
This low select circuit 4 has two inputs H and K. The input voltage
from the input H is added to the reference voltage by the operational
amplifier 41. The sum of the input voltage at H into the reference
voltage is positive. Consequently, the output of the operational amplifier
41 is negative, the diode D2 conducts and diode Dl does not conduct. Thus
the voltage at the reference point 42 is equal to the sum of the input
signal H and the reference voltage (with reversed polarity, of course).
-14-

~3~2~
In the operational amplifier 43, the voltage at point 42 and
the reference voltage are again added by means of connecting both to
the inverting input of operational amplifier 43. The output of the opera-
tional amplifier 43 therefore corresponds to the input voltage at H
(assuming that the diode D4 is not conducting) since the reference voltage
is cancelled out by this addition and the sign of the input at the inverting
input of operational amplifier 43 is reversed again. The input voltage
H from the output of operational amplifier 43 and the input voltage from
the second input K being reversed in operational amplifier 44 are both
connected to the inverting input of operational amplifier 45. The
output voltage of this operational amplifier 45 therefore is equal to the
difference of the input signal from the input K and the input signal from
the input H. Thus if the ~ignal K is larger than the signal H (both
signals seem to be positive), the output of the operational amplifier 45
will be positive. Thus, the diode D3 conducts and the diode D4 does not
.onduct. Therefore no signal is fed back from operational amplifier 45
to the noninverting input of operational amplifier 43 and the output of
the low select circuit 4 at the output P equals the smaller voltage H as
furnished by the operational amplifier 43.
If the input signal of the input K is smaller than the input
signal at H, the output of the operational amplifier 45 will be negative
and corresponding to the difference of the input signal K minus the input
signal at the input H. In this case the diode D3 does not conduct and
the diode D4 will conduct furnishing the difference of these two signals
to the noninverting input of operational amplifier 43. Therefore, the
output of the operationnl amplifier 43 will equal the input voltage at
the input K. At the output P of the low select circuit 4, the input
voltage of the input K this time appears which again is the lower of
the two input voltages.

113~3Z~7
The anti-reset windup circuit and method described above in
connection with a direct acting controller 2 is equally applicable to a
reverse acting controller. In~this case, it is only necessary to reverse
the input C and D of the anti-reset windup unit.
In the following, a specific example of a control system as
shown in FIGURE 1 is given for a rich oil distillation column.
EXAMPLE
A rich oil distillation column in which pentane and lighter hydro-
carbons are separated from the circulating oil is controlled by a process
and apparatus of this invention as described above. The first process
variable determined is the pentane content in the bottom of the distilla-
tion column. This determination is done by a commercially available gas
chromatographic analyzer. The second process variable is the temperature
in the bottom of the distillation column. This temperature is sensed by
a thermocouple and a signal is generated with commercially available equip-
ment.
The distillation column is heated by a fuel gas fired furnace.
The process control signal is used to control the flow of the fuel gas into
this furnace.
Under normal operating conditions, the controller associated to
the pentane content in the rich oil in the bottom of the distillation
column is operated to maintain the pentane concentration at the selected
setpoint. This is achieved by controlling the fuel gas flow into the fur-
nace. In the event that the temperature in the bottom of the distillation
column exceeds a preselected safe operating value, the controller associated
with the temperature in the bottom of the distillation column will generate a
control signal that is selected by the low select circuit as the process
control signal and will cause a fuel gas flow such that temperature in the
bottom of the distillation column will be reduced again to a value equal
to the setpoint.
-16-

~3~2'7
The anti-reset windup circuit of this invention prevents the
winding up of the deselected controller while the selected controller is in
operation and has control over the flow of the fuel gas to the furnace.
Reasonable variations and modifications which will become
apparent to those skilled in the art can be made in this invention without
departing from the spirit and scope thereof.
-17-

26162
~3~3~7
SUPPLEMENTARY DISCLOSURE
As is illustrated in FIGURE 2, the output G of the controller 2 is
directly related to the magnitude of the output A from the anti-reset windup
circuit 3. The output A from the anti-reset windup circuit 3 is directly
related to the magnitude of the input B which is a representation of the pro-
cess variable signal. Thus, a change in the process variable signal directly
affects the output G of the controller 2.
If a disturbance occurs which causes a change in the process var-
iable signal F or B, then the output G of the controller 2 is increased or
decreased so as to bring the process variable signal F or B back to the value
of the setpoint E.
If the output G of the controller 2 is increased or decreased too
quickly, in response to a change in the process variable signal F or B, the
process variable signal F or B will have a tendency to oscillate about the
setpoint E. The process is said to be unstable under these conditions, which
is highly undesirable.
In contrast, if the output G of the controller 2 is increased or
S decreased very slowly in response to a change in the process variable signal F
or B, the process will be operating off specification for a longer period of
time than necessary, which will result in economic loss.
It is thus desirable to operate the control system of the present
invention so as to prevent oscillation while still providing a fast control
response to a process disturbance. This is accomplished by lagging or delay-
ing the effect of the process variable signal only to the extent necessary to
prevent oscillations and instability.
Many different circuit configurations are available which could be
utilized to provide a lag Qr delay. In the present invention the parallel
combinations of the resistor and capacitor in the feedback loop of operational
amplifier 32 are utilized to delay the effect of a change in the process var-
iable signal F or B.
SDl

:~1313Z7
The lag or delay of five to fifteen minutes is considered optimal
for most processes. However delays as short as a few seconds may be used if
disturbances which come and go quickly are not encountered in a particular
process. The optimum lag for a particula~ process may be determined by moni-
toring the process variable signal F as a process disturbance occurs. Begin-
ning witb a small lag or delay, the lag or delay may be increased until there
is only limited oscillation of the process variable signal F about the set-
point E. A trade-off may be made between response time of the control system
and instability of the process if desired.
The delay may be calculated by the equation
(I) T = (R) (C)
where
T = delay in seconds;
R = resistance of the resistor in the feedback loop of
operational amplifier 32 in ohms;
C = capacitance of the capacitor in the feedback loop of
operational amplifier 32 in farads.
In a particular embodiment of the present invention the preferred size of the
resistor is 500 K~ and the preferred size of the capacitor is lOOO~f. Equa-
tion (I) gives a delay of 8.33 minutes for these values. Thus the output Gfrom the controller 2 will not be affected by a process disturbance, which
causes a change in the process variable signal F, for 8.33 minutes. This
results in a more stable operation of a process.
The 500 K~ resistor in the feedback loop of operational amplifier 32
and the 500 KQ resistor between B and the operational amplifier 32 may be
increased by equal amounts or decreased by equal amounts as desired. A value
of 1 M~ should not be exceeded since resistance values above 1 MQ may cause
deterioration of the amplification characteristics of operational amplifier 32.
.
19
SD2

Dessin représentatif

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États administratifs

2024-08-01 : Dans le cadre de la transition vers les Brevets de nouvelle génération (BNG), la base de données sur les brevets canadiens (BDBC) contient désormais un Historique d'événement plus détaillé, qui reproduit le Journal des événements de notre nouvelle solution interne.

Veuillez noter que les événements débutant par « Inactive : » se réfèrent à des événements qui ne sont plus utilisés dans notre nouvelle solution interne.

Pour une meilleure compréhension de l'état de la demande ou brevet qui figure sur cette page, la rubrique Mise en garde , et les descriptions de Brevet , Historique d'événement , Taxes périodiques et Historique des paiements devraient être consultées.

Historique d'événement

Description Date
Inactive : Périmé (brevet sous l'ancienne loi) date de péremption possible la plus tardive 1999-09-07
Accordé par délivrance 1982-09-07

Historique d'abandonnement

Il n'y a pas d'historique d'abandonnement

Titulaires au dossier

Les titulaires actuels et antérieures au dossier sont affichés en ordre alphabétique.

Titulaires actuels au dossier
PHILLIPS PETROLEUM COMPANY
Titulaires antérieures au dossier
FRANKLIN D. GANAWAY
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Description du
Document 
Date
(yyyy-mm-dd) 
Nombre de pages   Taille de l'image (Ko) 
Page couverture 1994-02-17 1 11
Abrégé 1994-02-17 1 12
Revendications 1994-02-17 5 142
Dessins 1994-02-17 3 42
Description 1994-02-17 19 651