Information
-
Patent Grant
-
6517891
-
Patent Number
6,517,891
-
Date Filed
Tuesday, October 31, 200024 years ago
-
Date Issued
Tuesday, February 11, 200322 years ago
-
Inventors
-
Original Assignees
-
Examiners
Agents
- Wood, Herron & Evans, L.L.P.
-
CPC
-
US Classifications
Field of Search
US
- 427 8
- 427 421
- 427 424
- 222 63
-
International Classifications
-
Abstract
An apparatus for controlling a speed of a motor of a metering pump providing pressurized fluid at a dispensing gun. The dispensing gun is opened and closed to dispense fluid onto a substrate being carried by a conveyor past the dispensing gun. The apparatus has a pressure control producing first motor speed signals as a function of changing speeds of the conveyor and changing fluid pressures in the dispensing gun when the dispensing gun is open. A flow control produces second motor speed signals as a function of the changing speeds of the conveyor. During changes in conveyor velocity, a motor speed control provides the first motor speed signal to the pump motor which operates the motor at speeds causing the pump to provide fluid to the dispensing gun at pressures changing at a rate tracking a rate of change of the speed of the conveyor. When full conveyor speed is detected, the motor speed control provides the second motor speed signal to the pump motor which operates the motor at speeds determined by the full conveyor speed. In addition, there are methods for generating pressure related and conveyor speed related motor speed signals and automatically switching between those signals as a function of the conveyor speed.
Description
FIELD OF THE INVENTION
The present invention relates generally to an apparatus for dispensing viscous fluids and, more particularly, to an apparatus and method for supplying hot melt adhesives to a dispensing gun.
BACKGROUND OF THE INVENTION
The ability to precisely dispense viscous industrial materials, such as hot melt adhesives, is a necessity for manufacturers engaged in the packaging and plastics industries. Inconsistent application of adhesive onto a substrate translates into unusable and scrap product and increased costs. Therefore, the process of supplying adhesive to a fluid dispensing applicator or gun must be precisely controlled.
A typical fluid dispensing operation employs a dispensing gun to apply a fluid, for example, an adhesive, onto a substrate being moved past the dispensing gun by a conveyor. The speed of the conveyor, or line speed, is set according to such factors as the complexity of the dispensing pattern and the configuration of the gun. Fluid adhesive is normally supplied to the dispensing gun by flexible hoses. Adhesive is pumped from a reservoir by a metering pump, for example, a motor-driven positive displacement pump. A metering pump for purposes herein is a pump in which the output volume is directly proportional to the action or displacement of the pump independent of fluid viscosity, except for any fluid leakage within the pump. Therefore, with a metering pump, the flow rate of the adhesive being dispensed from the gun is a function of the speed of the motor driving the pump.
The proper application of fluid or adhesive onto a substrate requires that the flowrate of the fluid from the dispensing gun remain as constant as possible throughout the fluid dispensing process. Variations in the flowrate result in different quantities or volumes of fluid being applied at different locations across the substrate. Thus, with too little adhesive, a desired coating thickness is not achieved, and the quality of the adhesive capability is reduced. Similarly, with an excessive quantity of fluid being dispensed, the adhesive may subsequently be displaced to areas of the substrate where it is not wanted; and again, the quality of the substrate product is reduced. In either event scrap product is often the result.
In many applications, the speed of the conveyor carrying the substrate is controllable and changed in accordance with the production line's capability to produce a high quality product. For example, with a first time run of a product, a production line may be operated at a slower speed to ensure a high quality product. But over time, as the production line is tuned, it can operate at a higher conveyor speed and still produce a high quality product. Assume the fluid dispensing system is operating properly with the conveyor operating at a first constant speed. If the speed of the conveyor and the substrate is increased to a higher constant speed, the flowrate of fluid being dispensed through the gun must also be increased in order to maintain a consistent, high quality coating of fluid on the substrate. It is known to use a signal related to the conveyor speed to modify the speed of the pump motor. Hence, when the conveyor is adjusted to the higher constant speed, the speed of the pump motor increases; and the flow of fluid to the gun is increased, thereby causing the pressure within the gun to increase. The increased gun pressure causes the flowrate of fluid from the gun to increase, and thus, the flowrate of the fluid being dispensed is changed as a function of conveyor speed.
The above flow control system works relatively well while the conveyor is operating at a constant speed, however, the flow control system does not operate properly during periods when the conveyor is accelerating or decelerating. Such conveyor speed changes occur, for example, when the conveyor is initially started from rest. Known systems are unable to maintain the desired flowrate of the fluid through the dispensing gun during periods of conveyor acceleration and deceleration.
FIG. 5A
illustrates how the fluid pressure at the dispensing gun changes with respect to an acceleration and deceleration of the conveyor. When the conveyor is at a zero speed (
500
), with some systems, for example, those using a pressure relief recirculation valve, the recirculation pressure is higher (
502
) than a desired operating pressure (
504
) of the dispensing gun. Therefore, when the conveyor line is initially started (
506
) and is accelerating, the fluid dispensing occurs at an excessive pressure, thereby depositing excessive fluid and producing scrap product. The production of scrap product will continue as the pressure decreases (
508
) and the conveyor accelerates until both the conveyor speed and operating pressure reach their desired values (
509
). For purposes of illustration, the desired values of conveyor speed and operating pressure are shown as the common line (
504
). Upon being given a deceleration command (
530
), the conveyor speed decreases (
532
) to a zero velocity (
534
). However, upon the dispensing gun closing, the pressure rises (
536
) until the pressure relief valve opens and stabilizes the pressure (
538
).
In other recirculation systems, a solenoid actuated pressure relief valve is in series with a restricted orifice; and upon the recirculation valve opening, the recirculation pressure (
510
) is held at a level lower than desired operating pressure. Upon the conveyor accelerating (
506
), the gun pressure initially drops to a still lower pressure (
512
) faster than the metering pump can increase the pressure. Therefore, for a short period of time after the conveyor line starts, an excessive amount of fluid is dispensed which results in the production of scrap product. As the conveyor line accelerates, at some point (
514
), for a current conveyor speed, the correct amount of fluid is being dispensed; but continued conveyor line acceleration (
516
) with lower pressure (
518
) results in less than the desired flowrate of fluid through the dispensing gun. Thus, scrap product continues to be produced until the conveyor speed and operating pressure both reach their desired values (
504
). Upon the conveyor starting a deceleration, the recirculation valve is opened and the pressure decreases until it is stabilized at a value (
542
) determined by the restricted orifice.
As can be seen in
FIG. 5A
, with the lower recirculation pressure just described, the conveyor accelerates to its desired speed well before the dispensing gun pressure reaches its desired operating pressure. A significant contributing factor to this extended pressure recovery time is the use of flexible hoses connecting the pump with the dispensing gun. At the desired operating pressure, the hoses expand slightly; and the quantity of fluid being dispensed is small relative to the volume of the hoses. In fact, many times, the quantity of fluid dispensed is no more, and often less, than the expansion, or increased volume, of the hose at the desired operating pressure. Therefore, it takes longer for the pump to restore the desired gun pressure because the pumped fluid has to again expand the hose with fluid in order to achieve the desired operating pressure. As will be appreciated, the graphical representations of the pressure and line speed in
FIG. 5
are only exemplary. The acceleration and deceleration of the conveyor often varies nonlinearly and normally is not linear as shown. Further, the acceleration and deceleration of the conveyor may differ from day to day and may be different with different systems. Further, the the exact profile of pressure with respect to time often varies substantially on an instantaneous basis and is not in any respect related to the conveyor speed.
Therefore, there is a need for a fluid dispensing system which maintains a desired flowrate of fluid through the dispensing gun while the speed of the conveyor carrying the substrate is changing, for example, when the conveyor is accelerating from rest to its desired conveying speed.
SUMMARY OF THE INVENTION
The fluid dispensing system of the present invention addresses the above and other problems associated with known systems in providing a system for pumping a fluid to a dispensing gun. The fluid dispensing system of the present invention minimizes the production of scrap product during periods of changing conveyor speed. The fluid dispensing system of the present invention is especially useful at the beginning of a production run when the conveyor is accelerating from rest to a desired full production speed. In addition, the fluid dispensing system provides the same benefits at the end of a production run when the conveyor is decelerating from its full production speed to rest. Thus, by reducing scrap production, the fluid dispensing system of the present invention reduces scrap product, maintenance, and the product unit cost.
In accordance with the principles of the present invention and the described embodiments, the invention in one embodiment provides an apparatus for controlling a speed of a motor of a metering pump providing pressurized fluid at a dispensing gun. The dispensing gun is opened and closed to dispense fluid onto a substrate being carried by a conveyor past the dispensing gun. The apparatus has a pressure control producing first motor speed signals as a function of changing speeds of the conveyor and changing pressures of the fluid in the dispensing gun when the dispensing gun is open. A flow control produces second motor speed signals as a function of the changing speeds of the conveyor. A motor control responds automatically to the first and second motor speed signals to produce speed command signals for the motor. The speed command signals operate the motor at speeds causing the pump to provide fluid to the dispensing gun at pressures changing at a rate tracking a rate of change of the speed of the conveyor.
The first motor speed signal from the pressure control operates the pump motor in response to both conveyor speed and fluid pressure at the dispensing gun during an acceleration or deceleration of the conveyor. Thus, the pressure at the dispensing gun changes at a rate that follows the acceleration and deceleration of the conveyor, and the flow of fluid from the dispenser also follows the acceleration and deceleration of the conveyor to dispense the proper amount of fluid on the substrate. When the conveyor reaches a constant full speed, the motor control provides the second motor speed signal to the pump motor, thereby controlling flow of the fluid in accordance with the constant full conveyor speed.
In another embodiment, the invention includes a method of providing fluid under pressure to a dispensing gun with a metering pump connected to a motor. The dispensing gun opened and closed to dispense fluid onto a substrate being carried by a conveyor past the dispensing gun. First, a speed of the conveyor is changed. Then, fluid pressures at the dispensing gun are detected while the speed of the conveyor is changing and the dispensing gun is dispensing fluid. In addition, speeds of the conveyor are detected while the speed of the conveyor is changing. In response to detecting the pressures and the speeds, the fluid pressures at the dispensing gun are changed at a rate substantially tracking a rate of change of the speed of the conveyor. Thereafter, the flow of the fluid is automatically controlled as a function of detecting a full speed of the conveyor.
In one aspect of the invention, first motor speed signals are generated in response to the detected fluid pressures and conveyor speeds, and a second motor speed signal is generated in response to detecting a full conveyor speeds. The control of motor speed is automatically switched from the first motor speed signals to the second motor speed signal in response to conveyor having the full conveyor speed.
In a further aspect of the invention, control of the motor speed is gradually switched from the first motor speed signals to the second motor speed signal utilizing differing proportions of the first and second motor speed signals.
The above and other objects and advantages of the present invention shall be made apparent from the accompanying drawings and the description thereof.
BRIEF DESCRIPTION OF THE DRAWINGS
The accompanying drawing, which is incorporated in and constitutes a part of this specification, illustrates embodiments of the invention and, together with a general description of the invention given above, and the detailed description of the embodiments given below, serves to explain the principles of the invention.
FIG. 1
is an overall schematic block diagram of a fluid dispensing system in accordance with the principles of the invention.
FIGS. 2A-2B
are flowcharts illustrating one embodiment of a process for controlling pump motor speed for the fluid dispensing system of FIG.
1
.
FIGS. 3A
,
3
B and
3
C are flowcharts illustrating another embodiment of a process for controlling pump motor speed for the fluid dispensing system of FIG.
1
.
FIG. 4
is a flowchart illustrating a cycle for capturing values of parameters used in the processes of controlling pump motor speed for the fluid dispensing system of FIG.
1
.
FIG. 5A
is a graphical illustration of known relationships of conveyor speed and fluid dispenser pressure with respect to time.
FIG. 5B
is a graphical illustration of a new relationship of fluid dispenser pressure with respect to time when using the fluid dispensing system of FIG.
1
.
DETAILED DESCRIPTION OF THE INVENTION
Referring to
FIG. 1
, a fluid dispensing system is comprised of a fluid dispensing gun
22
having a nozzle
24
for dispensing a fluid
26
, for example, an adhesive, onto a substrate
28
. The substrate
28
is carried by a conveyor
30
past the dispensing gun
22
. The conveyor
30
is mechanically coupled to a conveyor drive having a conveyor motor
32
. The speed of the conveyor is detected by a conveyor feedback device
34
, for example, an encoder, mechanically coupled to the conveyor
30
. The feedback device
34
has an output
36
connected to a dispensing gun controller
38
, and the feedback device
34
provides a feedback signal that changes as a function of changes in the conveyor speed.
A system control
42
generally functions to coordinate the operation of the overall fluid dispensing system. For example, the system control
42
normally provides a user interface for the system and controls the operation of the conveyor motor
32
via signal line
43
. Further, within the system control
42
is a pattern controller
44
that controls the operation of the fluid dispensing gun
22
as a function of the particular application being run. The pattern controller
44
receives, on input
40
, a part present or trigger signal that provides a synchronization with motion of the substrate
28
on the moving conveyor
30
. In response to the trigger signal on an input
40
of a system control
42
, the system control provides a first signal to the gun controller
38
via an input
45
requesting the gun controller to close a recirculation valve
56
. The recirculation valve
56
is used to shunt fluid from the metering pump
52
around the dispensing valve
50
and back to the reservoir
54
during idle periods, for example, between parts. Further, in response to the trigger signal, the pattern controller
44
provides a sequence of gun ON/OFF signals normally in the form of pulses to the gun controller
38
via an input
47
.
The gun controller
38
provides output signals to operate the dispensing gun
22
as a function of the timing and duration of the gun ON/OFF signals from the pattern controller
44
. In response to the leading edge of the gun ON/OFF pulse, the gun controller
38
provides a gun command on an output
46
that operates a solenoid
48
within the dispensing gun
22
. The solenoid
48
is mechanically coupled to a dispensing valve
50
that is fluidly connected to a metering pump
52
that, in turn, receives fluid from a fluid reservoir
54
. Upon receiving a signal on output
46
from the gun controller
38
, the solenoid
48
opens the dispensing valve
50
. The pressurized adhesive in the dispensing gun passes through the nozzle
24
and is deposited onto the substrate
28
. The dispensing valve remains open for the duration of the gun ON/OFF pulse; and in response to the trailing edge of a gun ON/OFF pulse, the gun controller changes the state of the solenoid
48
to close the dispensing valve
50
. In most applications, as the substrate
28
is moved past the dispensing gun
22
, a plurality of gun ON/OFF pulses cause the gun controller to rapidly open and close the dispensing valve to deposit the fluid at different locations on the substrate.
The pump
52
is a positive displacement pump; and therefore, over a dispensing time period, the volume of fluid supplied to the dispensing valve
50
and dispensed through the nozzle
24
is directly proportional to the speed of the pump motor
58
. A motor speed controller
57
within the gun controller
38
is responsive to the conveyor feedback device
34
and a pressure feedback device
62
for providing motor speed command signals on an output
61
to the pump motor
58
. A flow control
60
within the motor speed controller
57
is responsive to the feedback signal from the feedback device
34
to provide a motor-speed-dependent-on-line-speed (“MS
LS
”) motor speed signal. The MS
LS
signal is provided by the motor speed control
68
over a signal line
61
to the pump motor
58
. The MS
LS
signal changes as a function of the line speed of the conveyor
30
; and thus, the pump motor
58
is controlled to have a speed that is related to the speed of the conveyor
30
. Consequently, the flow of fluid through the dispensing valve
50
changes as a function of changes in the conveyor speed.
As previously described, such a line speed control system has certain disadvantages during periods of acceleration and deceleration of the conveyor. Therefore, the present invention utilizes a pressure transducer
62
that detects pressure at a point immediately upstream of the dispensing nozzle
24
. A pressure control
66
provides a motor-speed-dependent-on-pressure (“MS
p
”) motor speed signal in response to the feedback signal from the feedback device
34
and a pressure feedback signal on an output
64
. The motor speed control
68
switches control of the pump motor
58
between the MS
LS
signal on an input
70
and the MS
p
signal on an input
72
. Essentially, at the beginning of an acceleration or deceleration period, the motor speed selector
68
controls the pump motor
58
as a function of dispensing gun fluid pressure, that is, the MS
p
signal from the pressure control
66
. When the dispensing gun pressure is equal to the desired operating pressure with the conveyor at full line speed, the motor speed selector
68
switches control of the pump motor
58
from a pressure control to a flow control using the MS
LS
signal from the control
60
.
One embodiment of such an operation of the gun controller
38
is illustrated by the flowchart of
FIGS. 2A and 2B
. Upon initially starting a fluid dispensing system as illustrated in
FIG. 1
, the pump motor
58
is started before the conveyor motor
32
in order to initially stabilize and pressurize the fluid system comprised of the pump
52
, recirculation valve
56
and fluid reservoir
54
. The motor
58
is operated at a constant recirculation speed such that a known pressure is provided at the output of the pump
52
. The pressure may be created by the recirculation valve
56
being a pressure relief valve. Alternatively, the recirculation valve
56
may be a solenoid valve having a serially connected restricted orifice that provides the desired pressure drop. The pressure at the output of the pump
52
may be higher or lower than the normal operating pressure detected by the transducer
62
immediately upstream of the nozzle
24
.
In providing a better control of the speed of the pump motor
58
, the gun controller
38
first, at
202
of
FIG. 2A
, determines whether a conveyor start command has been given by the system control
42
to the conveyor motor
32
. A signal representing the start of the conveyor line is also provided to the gun controller
38
by the system control
42
. The gun controller
38
, at
204
, switches to pressure control of the pump motor
58
and ends the recirculation control. To end recirculation control, the controller
38
provides a signal over an output
59
causing the recirculation valve
56
to close, thereby terminating the recirculation mode. This step is necessary if the recirculation path includes a solenoid valve. If the recirculation valve is provided by a pressure relief valve, the recirculation mode is terminated by a lesser pressure differential across the relief valve caused by the dispensing valve opening. Thereafter, at
206
, the gun controller
38
samples the feedback signal from the conveyor encoder
34
representing the conveyor speed. The controller
38
, at
208
, then multiplies the recently sampled conveyor speed times a stored pressure scaling constant to determine a target pressure value or setpoint. The stored pressure scaling constant is a fraction having a numerator equal to the desired dispensing pressure and a denominator equal to the full line speed. Thereafter, at
210
, the controller
38
determines whether the target pressure value is greater than a maximum pressure limit, for example, 1500 pounds per square inch (psi); and if it is, the target pressure, at
212
, is set equal to the maximum pressure limit. The controller
38
then determines whether the target pressure value is less than a minimum pressure limit, for example, 25 psi; and if so, at
216
, the target pressure is set to a value equal to the minimum pressure limit.
The controller then, at
218
, samples a pressure feedback signal provided from output
64
of the pressure transducer
62
. The pressure control
66
within the controller
38
, at
220
, determines a value for MS
p
using the target pressure and the sampled gun operating pressure in a known PID process with acceleration PID constants. With the PID process, depending on the application and desired response, proportional and/or integral and/or derivative terms are determined from the pressure values, and each of the terms has a gain or multiplier that is in the range of from zero to a value that is empirically determined to provide the desired response and stability to the operation of the motor
58
of the pump
52
. At the initiation of a conveyor acceleration cycle, the motor speed selector
68
applies the MS
p
signal to the pump motor
58
.
The results of utilizing pressure as a pump motor control signal is illustrated in FIG.
5
B. As can be seen with this embodiment, the recirculation pressure (
550
) is less than with prior systems. Further, when the line speed provides a target pressure value equal to the recirculation pressure (
552
), the controller
38
provides a signal over output
59
to close the recirculation valve
56
. Simultaneously, the controller
38
provides a signal over output
46
to cause the solenoid
48
to open the dispensing valve
50
. The pressure control
66
provides an MS
p
signal to the pump motor
58
, so that changes in the dispensing gun pressure (
554
) follow changes in the conveyor speed (
516
) with respect to time. To provide a desired response, the PID constants are set such that the pressure (
558
) slightly overshoots the full line speed (
504
). It should be noted that the desired response will differ with different applications and designers. The pressure curve in
FIG. 5B
at
558
is shown as being slightly underdamped; however, as will be appreciated, the PID process can be adjusted to provide a more critically damped pressure function or even an overdamped pressure function.
The controller
38
then, at
222
(FIG.
2
B), determines whether the operating gun pressure is equal to the target pressure at full line speed. The point at which the pressure intersects the constant line speed at
555
is theoretically the ideal pressure to be detected. However, for many reasons, for example, the target pressure is determined from a scaling constant based on noncurrent values, the detection of the pressure at
555
is very difficult. Thus, applicants have chosen to detect when the operating gun pressure has stabilized and thus, has a substantially zero slope for some period of time. As will be appreciated, other methods of detecting pressure at full line speed may be employed. Upon detecting the target pressure at full line speed (
562
of FIG.
5
B), motor speed controller
57
at
224
switches to flow control the pump motor
58
. Thus, the motor speed control
68
within the motor speed controller
57
switches control of the pump motor
58
from the MS
p
motor speed signal to the MS
LS
motor speed signal. At this point, the control of the pressure within the dispensing gun
22
transitions (
564
) from the switch point (
562
) to a flow control (
566
) determined by the full line speed of the conveyor.
During the time that the conveyor is operating at full line speed, the speed of the pump motor
58
is controlled by the gun controller
38
as a function of the conveyor feedback signal in a known manner. The flow control continues until the controller
38
, at
226
(FIG.
2
B), determines whether a conveyor stop command has been issued by the system control
42
. As with the acceleration mode, controlling the speed of the pump motor
58
with the conveyor feedback signal does not take into account the variations in pressure arising from the fluid dispensing process in a deceleration mode. Therefore, the motor speed selector
68
within the gun controller
38
switches control of the pump motor
58
from the flow control
60
to the pressure control
66
. Once again, a conveyor speed is sampled at
228
, and a target pressure determined, at
230
, in a the same manner as previously described. Also, as previously described, the target pressure is checked against maximum and minimum limits at
232
-
238
. The gun pressure is again sampled at
240
. A motor speed value (MS
p
) is determined, at
242
, by the controller
38
using the target pressure and the sampled pressure in a PID loop with deceleration PID constants; and the MS
p
value is applied to the pump motor
58
. The gun controller
38
then at
244
detects from the pressure feedback signal on line
64
when the dispensing gun pressure is equal to the desired recirculation pressure. When the recirculation pressure is achieved, the gun controller
38
, at
246
, switches to recirculation control of the pump motor
58
. The controller
38
provides a first signal over line
61
commanding the pump motor
58
to operate at a recirculation speed and a second signal over line
59
commanding the recirculation valve to open. Thereafter, the system control
42
stops the operation of the conveyor motor at the end of the deceleration cycle.
Again, referring to
FIG. 5B
, upon starting a deceleration (
574
), the pressure (
576
) results from control of the pump motor
58
being switched to the pressure control
66
. Changes in the dispensing gun pressure (
580
) generally follow changes in the slowing conveyor line speed (
532
) so that the proper amount of fluid is supplied by the pump
52
to the dispensing gun
22
and dispensed on the substrate
28
. Upon reaching the recirculation pressure, the recirculation valve
56
is opened; and the pump motor is operated at the recirculation speed, thereby stabilizing the recirculation pressure. The conveyor comes to rest at a zero velocity (
534
).
The above system provides a substantially improved relationship of dispensing gun pressure with respect to conveyor line speed during periods of acceleration and deceleration of the conveyor
30
. With the above system, when the conveyor is accelerating or decelerating, a pressure control system is active in which the motor pump speed is under the control of a pressure loop that causes a rate of change in fluid pressure at the gun to follow or track a rate of change in the conveyor speed. However, when the conveyor reaches a full speed condition, control of the pump motor is switched from a pressure control system to a flow control system in which the pump motor speed is controlled exclusively as a function of the conveyor line speed. Such a system is effective in different applications and on different systems where the acceleration and deceleration of the conveyor will vary. Further, with the dispensing system of the present invention, the dispensing of fluid onto the substrate
28
during periods of acceleration and deceleration is within specification; and scrap product is eliminated.
However, there is a disadvantage to the operating process described with respect to
FIGS. 2A and 2B
. Referring to
FIG. 5B
, control of the pump motor
58
is switched from the pressure control
66
to the flow control
60
at a point in time (
562
). However, at the switching point (
562
), the motor speed resulting from operation of the pressure control
66
is different from the motor speed resulting from the operation of the flow control
60
. Therefore, the system attempts to provide an instantaneous motor speed change equal to that difference. Such an abrupt switch in motor speed can result in an erratic or jerky operation of the pump motor
58
which creates mechanical stresses on the motor and pump as well as pressure irregularities and inconsistent fluid dispensing within the dispensing gun
22
.
FIGS. 3A-3C
illustrate an alternative embodiment of the invention in which the transition between pressure control of the pump motor
58
and line speed control of the pump motor
58
is gradual and controlled. In this embodiment, the operation of process steps
302
-
320
are identical to the operation of process steps
202
-
220
previously described with respect to
FIGS. 2A-2B
. Referring to
FIG. 3B
, the controller
38
, at
321
, also determines a target line speed value or setpoint by multiplying the current value of the conveyor speed times a motor speed scaling constant. The motor speed scaling constant is a fraction having a numerator equal to the full speed of the pump motor
58
and a denominator equal to the full line speed of a conveyor
30
. The product of the most recently sampled conveyor line speed times the motor speed scaling constant is stored by the controller
38
as an MS
LS
value.
Again, as previously described with respect to
FIG. 2
, the motor speed selector
68
within the motor speed controller
57
determines, at
322
, whether the current dispensing gun pressure is equal to the target pressure at full scale line speed. When that switching point is detected, the motor speed selector
68
then gradually shifts control of the speed of the pump motor
58
from the pressure control
66
to the flow control
60
. That shift in control can be performed linearly or nonlinearly with time. Further, the incremental resolution of each step in the transition is selectable in accordance with a particular the application, user preferences, etc. The motor speed selector
68
first, at
324
, sets a transition constant F equal to 1. Thereafter, at
326
, the mode speed selector
68
determines a first increment of the transition in accordance with the following:
MS=F×MS
p
+(1
−F
)×
MS
LS
,
and that value of MS is applied to the pump motor
58
. Thereafter, at
328
, the motor speed selector decreases the value of F and, at
330
, determines whether the value of F equals zero. The process of steps
324
-
330
is iterated until the value of F equals zero. With each iteration through steps
324
-
330
, F may be fractionally decreased in equal or nonequal increments. Further any number of increments may be used. When F equals zero, the full value of the MS
LS
motor speed signal is being applied to the pump motor
58
, and, at
331
, the motor speed control
57
switches to the flow control of the motor
58
. Thus, the control of the pump motor
58
is gradually shifted from the pressure control
66
to the flow control
60
. Such gradual shifting of control helps to minimize any sudden changes in the motor speed command to the pump motor
58
that may result in abrupt changes in the pressure within the dispensing gun
22
, thereby causing sudden changes in the fluid being dispensed.
Thereafter, at
332
, the gun controller
38
is provided with an input from the system control
42
indicating that the conveyor
30
has been commanded to stop. In an identical manner as previously described with respect to steps
306
-
321
, the conveyor speed is sampled at
334
, a target pressure determined and checked against maximum and minimum limits at
336
-
344
. The gun pressure is then sampled at
346
, and a MS
p
value determined at
348
and applied to the pump motor. The recirculation pressure is detected at
250
; and if the pressure is above the recirculation pressure, the process of steps
334
-
350
is iterated. The command of the pump motor
58
remains under the control of the pressure control
66
until the recirculation pressure is reached. Thereafter, in a manner as previously described, and the gun controller
38
switches the system back to recirculation control at
352
.
In the embodiments illustrated in
FIGS. 2 and 3
, various scaling constants are utilized which are based on full dispensing pressure, full line speed and full motor speed. Those values may be determined in advance and manually entered into the system control
42
and passed to the gun controller
38
for storage. Alternatively, those values may be continuously determined and stored by the gun controller
38
. For example, referring to
FIG. 4
, at
402
, the controller
38
first determines when the conveyor has reached its full line speed. Upon detecting full line speed, the gun controller
38
at
404
, samples the pressure feedback signal, determines the average dispensing pressure and stores that value. Thereafter, at
406
, the controller
38
samples the conveyor feedback signal, determines the average full line speed value and stores that value. At
408
, the controller
38
samples a pump motor feedback signal on line
63
, determines an average motor speed value and stores that value. The process of
FIG. 4
may be executed continuously while the conveyor is running at full line speed so that the stored values always represent the most recent full scale values of dispensing gun pressure, conveyor line speed and pump motor speed. Alternatively, the process of
FIG. 4
may be run at selected times during the operation of the conveyor, for example, immediately prior to the conveyor being commanded to stop.
The fluid dispensing system described above permits an accurate deposition of fluid onto the substrate during periods of conveyor acceleration and conveyor deceleration, thereby permitting the production of good product during the full time of conveyor operation. Thus, the fluid dispensing system described above is effective to reduce scrap as well as maintenance and product unit cost.
While the present invention has been illustrated by a description of various embodiments and while these embodiments have been described in considerable detail, it is not the intention of the applicants to restrict or in any way limit the scope of the appended claims to such detail. Additional advantages and modifications will readily appear to those skilled in the art. For example, in the described embodiments, during periods of changing conveyor speed, a pressure feedback signal is used with a target pressure in a PID process to provide motor speed signals operating the motor at speeds causing fluid pressure changes at the dispensing gun to follow changes in conveyor speed over time. As will be appreciated, fuzzy logic, neural nets, model based systems or other processes and systems may be used to provide a motor speed signal as a function of fluid pressure at the dispensing gun.
The invention in its broader aspects is therefore not limited to the specific details, representative apparatus and method, and illustrative example shown and described. Accordingly, departures may be made from such details without departing from the spirit or scope of applicant's general inventive concept.
Claims
- 1. A method of providing fluid under pressure to a dispensing gun with a metering pump connected to a motor, the dispensing gun being opened and closed to dispense fluid onto a substrate being carried by a conveyor past the dispensing gun, the method comprising:changing a conveyor speed at a rate of change; detecting pressures of the fluid at the dispensing gun while the conveyor speed is changing and the dispensing gun is dispensing fluid; detecting conveyor speeds; changing a pressure of the fluid at the dispensing gun in response to detecting the pressures and the conveyor speeds, so that the pressure of the fluid at the dispensing gun changes at a rate tracking a rate of change of the conveyor speed; detecting a full conveyor speed; and thereafter automatically controlling a flow of the fluid at the dispensing gun as a function of only the full conveyor speed.
- 2. The method of claim 1 wherein the step of automatically controlling a flow of the fluid at the dispensing gun further comprises:detecting a desired operating pressure of the fluid at the dispensing gun at the full speed of the conveyor.
- 3. A method of providing fluid under pressure to a dispensing gun with a motor connected to a metering pump, the dispensing gun being opened and closed to dispense fluid onto a substrate being carried by a conveyor past the dispensing gun, the method comprising:changing a conveyor speed at a rate of change; determining pressures of the fluid at the dispensing gun while the speed of the conveyor is changing and the dispensing gun is dispensing fluid; determining conveyor speeds; generating first motor speed signals in response to the pressures and the speeds; changing a pressure of the fluid at the dispensing gun by controlling the speed of the motor as a function of the first motor speed signals, so that the pressure of the fluid at the dispensing gun changes at a rate tracking a rate of change of the conveyor speed; detecting a full conveyor speed; and then automatically switching control of the speed of the motor from the first motor speed signals to second motor speed signals representing only the full conveyor speed.
- 4. The method of claim 3 further comprising:providing a sampled speed of the conveyor; generating a target pressure as a function of the sampled speed; providing a sampled pressure of the fluid at the dispensing gun; and determining the first motor speed signal as a function of the target pressure and the sampled pressure.
- 5. The method of claim 4, wherein generating the target pressure further comprises multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a pressure at the dispensing gun and a denominator representing a conveyor speed.
- 6. The method of claim 4 wherein generating the target pressure further comprises multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a desired dispensing pressure at the dispensing gun during a dispensing operation and a denominator representing a full speed of the conveyor.
- 7. The method of claim 4 wherein generating the target pressure further comprises multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a full pressure at the dispensing gun at full conveyor speed of the during an immediately prior dispensing operation and a denominator representing a full conveyor speed during the immediately prior dispensing operation.
- 8. The method of claim 4 further comprising determining the first motor speed signal by utilizing the target pressure and the sampled pressure in a proportional, derivative, integral process loop.
- 9. A method of providing fluid under pressure to a dispensing gun with a motor connected to a metering pump, the dispensing gun being opened and closed to dispense fluid onto a substrate being carried by a conveyor past the dispensing gun, the method comprising:increasing a conveyor speed from rest to a full conveyor speed at a rate of change; detecting a sampled pressure of the fluid at the dispensing gun while the speed of the conveyor is increasing and the dispensing gun is dispensing fluid; detecting a sampled conveyor speed; generating a first motor speed signal in response to the sampled pressure and the sampled conveyor speed; changing a pressure of the fluid at the dispensing gun by controlling the speed of the motor in response to the first motor speed signal, so that the pressure of the fluid at the dispensing gun changes at a rate tracking the rate of change of the conveyor speed; detecting a full conveyor speed; and then automatically switching control of the speed of the motor from the first motor speed signal to a second motor speed signal representing only the full conveyor speed.
- 10. The method of claim 9 wherein the step of switching control of the speed of the motor further comprises:detecting a target pressure of the fluid at the gun at a full conveyor speed; and generating the second motor speed signal in response to detecting the target pressure of the fluid at the gun at the full conveyor speed.
- 11. The method of claim 10 further comprising generating a plurality of motor speed command signals as a function of a combination of the first and second motor speed signals, each successive motor speed command signal being generated with successively smaller portions of the first motor speed signal and successively larger portions of the second motor speed signal.
- 12. The method of claim 11 further comprising:generating initial motor speed command signals as a function of principally the first motor speed signal; generating successive motor speed command signals as a function of successively smaller portions of the first motor speed signal and successively larger portions of the second motor speed signal; and generating final motor speed command signals as a function of principally the second motor speed signal.
- 13. The method of claim 11 further comprising generating motor speed command signals in accordance withMS=F×MSp+(1−F)×MSLS, where:MS=a motor speed command, MSp=the first motor speed signal, MSLS=the second motor speed signal, and F=a factor that varies incrementally between 0 and 1 with time.
- 14. The method of claim 9 further comprising:generating a target pressure by multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a pressure at the dispensing gun and a denominator representing a conveyor speed; and determining the first motor speed signal as a function of the target pressure and the sampled pressure.
- 15. The method of claim 14 wherein generating the second motor speed signal further comprises multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a motor speed and a denominator representing a conveyor speed.
- 16. The method of claim 9 further comprising:generating a target pressure by multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a desired dispensing pressure at the dispensing gun during a dispensing operation and a denominator representing a full speed of the conveyor; and determining the first motor speed signal as a function of the target pressure and the sampled pressure.
- 17. The method of claim 16 wherein generating the second motor speed signal further comprises multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a full motor speed during a fluid dispensing operation and a denominator representing a full speed of the conveyor.
- 18. The method of claim 9 further comprising:generating a target pressure by multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a full pressure at the dispensing gun at full conveyor speed of the during an immediately prior dispensing operation and a denominator representing a full conveyor speed during the immediately prior dispensing operation; and determining the first motor speed signal as a function of the target pressure and the sampled pressure.
- 19. The method of claim 18 wherein generating the second motor speed signal further comprises multiplying the sampled speed times a stored constant, the stored constant representing a fraction having a numerator representing a full motor speed at full conveyor speed during an immediately prior dispensing operation and a denominator representing a full conveyor speed during the immediately prior dispensing operation.
- 20. The method of claim 19 further comprising generating motor speed command signals in accordance withMS=F×MSp+(1−F)×MSLS, where:MS=a motor speed command, MSp=the first motor speed signal, MSLS=the second motor speed signal, and F=a factor that varies incrementally between 0 and 1 with time.
- 21. The method of claim 9 further comprising:decreasing the speed of the conveyor from a full conveyor speed to rest at a rate of change; generating the first motor speed signal in response to the sampled pressure and the sampled conveyor speed; changing the speed of the motor in response to the first motor speed signal while the conveyor speed is decreasing and changing the pressure of the fluid at the dispensing gun at a rate tracking the rate of change of the speed of the conveyor; detecting a pressure being equal to a recirculation pressure; and then automatically switching control of the speed of the motor from the first motor speed signal to a motor speed signal representing a recirculation mode.
US Referenced Citations (5)