CA2066581C - Computer controlled metering pump - Google Patents

Computer controlled metering pump Download PDF

Info

Publication number
CA2066581C
CA2066581C CA002066581A CA2066581A CA2066581C CA 2066581 C CA2066581 C CA 2066581C CA 002066581 A CA002066581 A CA 002066581A CA 2066581 A CA2066581 A CA 2066581A CA 2066581 C CA2066581 C CA 2066581C
Authority
CA
Canada
Prior art keywords
media
pumping
computer
diaphragm
piston
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CA002066581A
Other languages
French (fr)
Other versions
CA2066581A1 (en
Inventor
Eric C. Van Bork
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Pulsafeeder Inc
Original Assignee
Pulsafeeder Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Pulsafeeder Inc filed Critical Pulsafeeder Inc
Publication of CA2066581A1 publication Critical patent/CA2066581A1/en
Application granted granted Critical
Publication of CA2066581C publication Critical patent/CA2066581C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D7/00Control of flow
    • G05D7/06Control of flow characterised by the use of electric means
    • G05D7/0617Control of flow characterised by the use of electric means specially adapted for fluid materials
    • G05D7/0629Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means
    • G05D7/0676Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on flow sources
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/06Control using electricity
    • F04B49/065Control using electricity and making use of computers
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F11/00Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it
    • G01F11/02Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement
    • G01F11/021Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement of the piston type
    • G01F11/023Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement of the piston type with provision for varying the stroke of the piston
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F11/00Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it
    • G01F11/02Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement
    • G01F11/021Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement of the piston type
    • G01F11/029Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement of the piston type provided with electric controlling means
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01FMEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F11/00Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it
    • G01F11/02Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement
    • G01F11/08Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement of the diaphragm or bellows type
    • G01F11/086Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers which expand or contract during measurement of the diaphragm or bellows type using an auxiliary pressure to cooperate with the diaphragm or bellows
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D7/00Control of flow
    • G05D7/005Control of flow characterised by the use of auxiliary non-electric power combined with the use of electric means

Abstract

A computer (28) controlled metering pump. The displacement of a metering pump (10) is accurately monitored using a position sensor (13) connected to a piston. A control computer (28) receives the sensor signal as well as a desired pumping volume rate (119). The pumped volume is continuously monitored by the computer as a function of the piston displacement, and compared with the desired rate (119). The metering pump (10) is controlled to bring the pumped volume rate into agreement with the desired volumetric pumping rate.

Description

V1~'' 91/06062 ,..
COMPUTER CONTROLLED METERING PUMP
Background of the Invention The present application relates to metering pumps.
Specifically, a computerized control system is described for accurately monitoring and controlling the amount of pumped media in a chemical process application.
Metering pumps are used ~in a variety of chemical processes to control the quantities of chemicals which are used in the process. For instance, in chemical processing plants, and to water treatment plants, it is necessary to accurately add precise quantities of difficult-to-handle fluids with other constituent products during the chemical process. Metering pumps manufactured by the assignee of the present application, Pulsafeeder, Inc., are capable of providing precise quantities of pumped media within 1% of a nominal media volume.
Large chemical process plants typically are computer-controlled from a central processor. The amounts and rate of individual constituent chemicals used in a process are controlled by metering pumps which may be distributed at various points within a chemical process plant. The flow rate produced by these pumps must be monitored and precisely regulated if the overall chemical process is to be accurately controlled.
The present application is directed to providing for the distributed control over these various metering pumps such that the central control processor for the chemical plant may be operated in confidence that each of the metering pumps throughout the plant are being accurately controlled by a localized control system.
2 PCT/US90/060~4 ...~

Summary of the Invention It is a primary object of this invention to provide for a localized control system for a metering pump.
It is a specific object of .this invention to provide computerized control over a metering pump to accurately control the quantity of fluid pumped in a chemical process system.
These and other objects of the invention are provided by a computer control system. The computer control system will accurately monitor the displacement in a metering pump, and based on the displacement, determine whether ar not the-desired quantity of fluid has been dispensed within a given stroke of the metering pump. When the pumped quantity of fluid as determined by the pumping stroke displacement is determined not to be in accordance with the desired quantity of fluid displaced during a pump cycle, control~is effected over the metering pump to reduce or increase the amount of pumped fluid in a given stroke cycle.
In carrying' out the invention in accordance with a first embodiment, a position sensor accurately monitors the position of a piston during a pumping cycle. The monitored position is used to calculate a volumetric displacement for the pump.
When the calculated volumetric displacement for the pump exceeds or is less than the desired amount, control over the pump may be effected in a variety of ways. In a first embodiment, control is effected over the amount of pumped media discharged by the pump during the exhaust portion of the pumg stroke.
In a further embodiment of the invention, the metering pump is a diaphragm metering pump in which the amount of pumped i~' ' 91/06062 PC.'T/US90/06054 ~~~~~~~ . ,::
media is controlled by controlling the fluid media within the pressurizing chamber. During a pumpincf stroke, when the diaphragm has been displaced a distance which produces the precise quantity of fluid into the pump, the pressurizing chamber is vented, inhibiting any further pumping of media.
In yet another embodiment of the invention, accurate diaphragm positioning is provided by a set of diaphragm position sensors which measures the displacement of the diaphragan. It is thus possible to accurately position the l0 diaphragm prior to an exhaust cycle of the metering pump to thereby discharge the precise volume of pumped media.
Brief Descriution of the Figures Figure 1A illustrates a schematic drawing of a computerized metering pump in accordance with a first embodiment of the invention.
Figure 1B illustrates a second embodiment of the invention wherein a diaphragm metering pump is computer controlled.
Figure 2 illustrates the operation of the computerized metering pumps of Figures 1A and 1B.
Figure 3 is a third embodiment of a camputerized metering pump having a provision to recirculate vented pumping fluid.
Figure 4A illustrates the programming carried out by the computer of the embodiments of Figures 1-3.
Figure .4B demonstrates a diagnostic routine implemented with the computer, verifying the operation of the pump.
Figure 5 illustrates control over the metering pump in accordance with a fourth embodiment of the invention wherein pumping pressure is controlled to accurately meter the WO 91/06062 PC1'/US90/OS054 .., quantity of pumped fluid.
Figure 6 schematically illustrates additional control over a diaphragm metering pump wherein the starting position for the diaphragm is accurately monitored.
Figures 7A and 7B illustrate the programming routine for the embodiment of Figure 6 wherein a metering pump includes a hydraulically balanced diaphragm.
Figure 8 illustrates the computer program routine for diagnosing diaphragm failures.
Description of the Preferred Embodiments Referring now to Figure.lA, there is spawn a metering pump 9 which is controlled by a computer 28 to provide a precise measured quantity of pumped fluid for each stroke of a piston 11. The pump 9 includes a pumping chamber 15, as well as a piston chamber 12. A reciprocating piston 11 is shown connected to a slider/crank mechanism and motor 30 to reciprocate on a periodic basis as a rate 1/T. The piston ll will move forward and backward in the piston chamber 12, drawing pumped media from reservoir 25 through valve 21 into the inlet 16. During the forward discharge portion of the piston stroke, the material will be forced through outlet 17, spring loaded check valve 19 and then to outlet pipe 20.
The amount of fluid displaced by the piston 11 can be defined as follows:
~f_Irdz x L

This volume displacement is, of course, proportional to the area of the piston 'll, expressed in terms of its diameter as 1/4 ~T( d2 times the stroke length L of the piston. The flow rate far the pump 9 is determined by dividing this volumetric displacement by the stroke period, T, where 1/T - f, the W~ 91106062 PCT/US90/06054 frequency of piston reciprocation.
From the foregoing, it is clear that the volume displaced is a function of the stroke length of the piston 11. By providing a means to effectively shorten this stroke length 5 L, it is possible to establish a fractional amornt of the maximum pumping capacity in any given stroke cycle.
The embodiment shown in Figures lA and 1B vary the effective stroke length L of the piston 11 from a maximum Lmax~
representing the full piston amplitude hydraulically such as to provide a fractional volumetric output, or a fractional flow rate, as desired. This fractional flow rate is achieved by controlling the inlet valve 21 which supplies pumped media from a reservoir 25 via conduit 24. The piston position is monitored by a sensor 13 connected through the A/D converter 29 to computer 28. The computer 28 makes an accurate calculation of the flow rate for the pump based on the piston displacement L, the stroke period T which is the reciprocal of the stroke frequency f, and the piston diameter d which is constant for a given pump.
Q = f d2L
Control over the effective stroke length L is accomplished in the embodiments of Figures 1A and 1B by opening previously closed valve 21 as soon as the piston 11 has moved the required stroke lew-.gth L. The computer 28 receives a desired flow rate Q as an input from an operator, and from the foregoing equation, calculates for the desired flow rate Q a stroke length L.
L =
3 0 ~i'f d The operation of the embodiments of Figures lA and 1B is illustrated in Figure 2. The diagram of Figure 2 begins at the portion of the stroke cycle wherein piston 11. is fully retracted. The piston begins to advance, discharging pumping WO 91/Ob062 PLT/US90I06054 ..~
s Q ~, w media from the pumping chamber 15 'through valve 19. Once the piston 11 has travelled the required distance L as indicated by sensor 13, valve 21 is opened by cantrol 22, permitting any remaining pumping media in pumping chamber 15 to be vented through valve 21, back to reservoir 25. Once the piston 11 has advanced its full stroke length, Lmax it will begin to retract, drawing pumping fluid from the reservoir 25 into the chamber 15.
Thus, the effective volume displacement from the pump 9 is controlled by detecting when the piston 11 has travelled the required length L to discharge the desired quantity Q of pumping media. It is clear that as the effecive stroke length L is increased for an increased flow rate, valve 22 will be closed for a greater duration of the total stroke cycle, until the discharge portion of the stroke cycle equals the intake portion of the stroke cycle.
As can be seen comparing Figures lA and 1B, the principles involved in controlling the effective stroke length L, arid hence the pumped flow rate, are the same. The presence of the diaphragm 14 in a diaphragm metering pump separates the pumping chamber 15 from a hydraulic chamber 18 having an intermediate fluid.
Figure 3 illustrates an improvement over the embodiment of Figure 1A, wherein a separate path for venting pumped media into reservoir 25 is provided. This path is shown as outlet 33 connected to a valve 30 which is connected to reservoir 25. Valves 30 and 21 are operated so that pumping media is supplied through valve 21 and inlet 16 to the pumping chamber 15. When the computer 28 has determined that the piston 11 has travelled the appropriate length L to discharge the required quantity of pumped media, valve 30 will be opened and valve 21 will remain closed. During the intake portion ., of the piston stroke, wherein pumping media fills chamber 15, W°' 91/06062 PCT/US90/06054 valve 21 is open and valve 30 is closed.
The embodiment of Figure 3 will provide for recirculation of pumped media which will assist when the pumping media has large quantities of solids in suspension ass there is only one directional flow in each pipe. This will promote positive media recirculation.
Figure 5 shows another embodiment of the invention which provides for venting the intermediate chamber 18 in a diaphragm pump arrangement. When the piston 11 has moved the 1o appropriate distance, as determined by the signal produced by sensor 13, indicating that the required quantity of pumping media has been forced from the pumping chamber 15, valve 38 may be opened to vent the intermediate chambex 18 back to the intermediate reservoir 44. In this way, once the venting begins, diaphragm 14 will not advance any further as the hydraulic pressure imparted by the piston 11~ is relieved through the valve 38 into the intermediate reservoir 44.
Once the piston 11 has extended its full stroke length, the valve 38 may be closed and valve 39 opened to permit piston 11 to draw intermediate media through valve 39 into the intermediate chamber 18 during its intake cycle in which it is being retracted, thus expanding the volume in intermediate chamber 18.
With the embodiment of Figure 5, it is possible to reduce the effective stroke length for the piston 11 by appropriately venting the intermediate chamber 18. The inlet 16 is connected through a check valve 3? to a pumping media supply reservoir 25.
Another embodiment is shown in Figure 6 in which a diaphragm metering.pump is employed to control the precise discharge of pumped media. The diaphragm 14 is shown positioned between two sensor elements 43 and 4s. The sensor elements 43 and.46 iW0 91/06062 PCT/US90/06054 ..., x,06 8 are connected to computer 28. Computer 28 thus monitors the position of the diaphragm 14 between a maximum displacement adjacent transducer 46 to a minimum displacement adjacent transducer 43. Control over pump stroke is implemented using the valve 38 and valve control 40, operated by .the computer 28. When the piston 11 has reached a value indicating the required quantity of pumped media has been discharged through outlet 17, valve 38 will be opened in order to vent the intermediate chamber 18 to the intermediate media reservoir 44. Thus, the remaining piston displaced intermediate media will be transferred to the reservoir.
Sensing of the diaphragm l4 position .is useful to accurately position the diaphragm 14 prior to beginning of a discharge cycle of the piston 11. Thus, by closing valve 38 while the piston withdraws, the diaphragm 14 will retract. In this manner, diaphragm 14 can be reliably returned to a beginning position. The proximity sensors 43 and 46 will. also detect when the diaphragm is being over or under inflated, a dangerous condition in which diaphragm rupture may be imminent.
The foregoing principles which make use of measuring stroke length of a reciprocating piston, and then hydraulically controling the effective stroke length L may also be implemented by sensing diaphragm position. It is possible, using a diaphragm position sensor, to measure the diaphragm deflection, and use this measurement to determine when a desired quantity of media has been pumped. if the volume of the deflected shape of the diaphragm can be mathematically approximated, the computer can calculate the displaced volume accordingly. Hydraulic control over a venting valve may be effected using this measured deflection, venting the pumping chamber back to the reservoir, thereby controlling the pumped volume and volume rate.

V"°~ 91/06062 PCT/US90/06054 ,, Figure 4A shows a particular instruction sequence for controlling the metering pump of Figures 1A, 1B and 3 to deliver the determined flow rate. At the beginning of the program, the desired volumetric flow rate ~? is read into the computer 28 in step 102. The desired flow rate is based on a stroke cycle time and volumetric discharge which occurs within the stroke cycle time. Assuming that the stroke cycle time is known and constant, using the earlier formula, the required effective stroke length L may be calculated in step 103. The calculation of the stroke length also depends upon having input certain information about the metering pump, such as piston diameter d, piston cycle rate T per the aforesaid equation.
Having thus calculated the desired stroke length for the piston, the intake valve is opened in step 104. This intake valve permits the pumped media to enter the pumping chamber 15 of the embodiments of Figures 1A and 18.~ The piston reciprocation begins in step 105 by energizing the motor drive to the piston.
The piston position is continually read and recorded in step 107 by monitoring the output of sensor 13. A diagnostics routine 108 is shown which is an optional subroutine to effectively diagnose any failure which might be indicated by the position sensor. This diagnostic routine 108 will be more specifically described with respect to Figure 4B.
:fin decision block 109, the piston position is determined to be fully retracted at which point the beginning of the pumping of media from the pumping chamber 15 begins. The intake valve 21 is closed in step 110 to prohibit venting of the pumped media from pumping chamber 15 to the pumping media reservoir 25. The piston position during the subsequent advance of the piston is continuously monitored and recorded in step 111. A further diagnostic routine is shown in 112 W~ 91/06062 ~~ PCT/US90/06054 to which is optional, but described more particularly in Figure 4B. The diagnostic routine will assist in determining any failure which may occur such that position measurements in step 111 are not within a predicted range.
Once the piston reaches the calculated stroke length L, decision block 113 will indicate it is time to end effective pumping from the chamber 1.5. In the event a single intake valve such as shown in Figures lA and 1B is employed, as determined by block 114, the inlet valve 21 is opened in step 118, thus effectively ending the pumping stroke for the piston 11. The remaining piston volume is displaced to the media reservoir 25.
In step 119, the desired flow rate is again read into the computer, and a new stroke length is calculated in step 120, identical to the calculation of step 103. In this way, in the event the operator at any point changes the desired flow rate Q, a new stroke length may be correspondingly calculated.
The flow chart of Figure 4A may also be applied to the system.
shown in Figure 3. As will be recalled, this system employs separate valves 2l~and 30 to accomplish the intake and vent functions. When two such valves are used, step 121 will follow decision block 114. In block 121, the auxiliary valve is opened in order to vent the pumping chamber back to the 25 reservoir 25. The position of the piston is continuously monitored in step 122 and another. diagnostic routine 123 is entered in the event the position of the piston is determined not to be in accordance with a predicted position.
Once the piston reaches its maximum stroke length L, 30 determined by block 124, the intake valve 21 is opened again in step 126 as the piston is fully advanced. At the same time, in step 12~ the auxiliary valve 30 is closed, _ P~.TlUS90106054 W~ 9110062 permitting additional pumped media to enter the pumping chamber 15 while the piston 11 retracts to its initial position.
A similar flow chart can be developed for the embodiment of Figure 5. As will be recalled, the embodiment of Figure 5 includes an inlet valve 38 and a vent valve 39. Control over these valves by the computer is accomplished with similar instruction sets which will be obvious in light of the previous flow chart (Figure 4A).
The flow chart outlined in Figure 4A could utilize diaphragm displacement to determine and/or verify volumetric discharge.
As stated previously, the volume of the deflected shape of the diaphragm can be mathematically approximated. Therefore, given a desired volumetric displacement, a value for diaphragm deflection can be calculated. This is analogous to the calculation of L effective fox the piston. The diaphragm position can then be monitored during pump discharge ° in a manner similar to the way the piston is monitored - until it reaches the proper level of deflection. At this point, the appropriate volume of media will have been discharged.
Referring now to Figure 4B, the diagnostic routine which is entered at various stages of vthe programming shown in Figure 4A. The routine begins with block 201. The first check made is whether or not the piston has changed position as evidenced by the output from the sensor 13. if the piston has changed position, the piston flag is set FALSE in step 202 and the drive flag is also set FALSE in step 203. The two false designations for the drive and piston flags indicate that these components are both operating properly. The current piston position is recorded in step 205 to be used in the next re-entrance to the diagnostics routine. The diagnostic program than exits to the main program in Figure 4A.

WO 91/0662 . PCT/US9U/06054 .~
., .

In the event there is no indication of a change in piston position, step 207 will be used to determine whether or not the motor is active. It is contemplated that a motor enable line will be provided by the computer 28. If this enable line is not active, step 208 will determine whether or not the drive flag has been set true. If not, the drive flag will be set true in step 209, and an atteTnpt made to start the motor in step 210. The ENABLE signal will be raised by the computer to try to restart the motor drive.
If the drive flag is set true, and the motor is determined not to be active in step 207, the operator is notified of a failed motor drive in step 222.
Continuing in the diagnostic program, the position sensor output is checked in decision block 212. The normal voltage potential is a non-zero value. If the output is.equal to 0, the piston flag is checked to see whether it is true or false. In the event it is not true, the piston flag is set true before exiting via step 205 to the main program. Tn the event the piston flag has been set true, the operator is notified in step 220 of a failed piston position sensor.
If the piston sensor output is not equal to 0 in block 212, and the drive flag has previously been set true in block 213, the operator is notified in block 221 of a failed drive mechanism. If the drive flag has been set false in block 213P the flag is set true in 214 before exiting via step 205.
If the piston flag has been set true in block 216, or the drive flag has been set 'true in 208 or 223, a failure condition has been determined and the pump is shut down in step 223. The operator is notified in steps 220-222 of the particular sensed failure.

~'~ 91/Ob062 PCT/U590/0605d ~~665~~ , .

Thus, the foregoing diagnostics will be used to determine whether there has been any piston motion. In 'the event there has not been, the fault condition is analyzed to determine whether a piston position sensor failure has occurred, there is a drive mechanism failure, or a motor failure.
Referring now to Figures 7A and 7B, there is shown a program routine for controlling the metering pump of Figure 6. The flow chart shown in Figures 7A and 7B describe the programming steps executed by computer 28 for controlling the hydraulically balanced diaphragm metering pump.
There are shown programming steps for the compii~ter 28 in the embodiments shown in Figure 6. This. embodiment is a hydraulically balanced diaphragm metering pump which accurately positions the diaphragm prior to beginning a pumping discharge stroke. In the embodiment shown in Figure 6, two proximity sensors are shown, 43 and 46, ~wha.ah detect whether or not the diaphragm is properly positioned to begin a discharge portion of the pump cycle.
The programming steps shown in Figure 7 include two branches, I and II. Each of these branches is used to position the diaphragm at pump start-up. The branch that is taken depends on whether it has been determined that the diaphragm is forward or rearward of its start position. As is clear from Figure 7A., two decision blocks 306 and 320 will make the determination as to whether or not the diaphragm is in its correct position. If not, the program will exit to the prepositioning appropriate subroutine shown in I and II.
The beginning of the computer--executed sequence starts with a reading of the desired flow rate Q in step 301. From this signal, i.e., inputted data by the operator, a pump stroke L
is determined which will generate the appropriate flow rate in accordance with the previous equations. The hydraulic WO 91/0606 ~~~~~'~y, PCT/US90/06054 ', V »

intake valve is opened in step 303, corresponding to the valve 38 shown in Figure 6. At this time, the piston reciprocation is started in step 304, while simultaneously reading the diaphragm position in step 3t)5. The diaphragm position is determined from signals produced by proximity sensors 43 and 46.
If the diaphragm has been determined to be in the proper starting position, decision blocks 306 and 320 will transfer control to programming step 331. At this time, the piston position is read from the position sensor 13. Piston drive diagnostics are included in step 332 which were described previously with regard to Figure 4~. It should be noted that this is optional and the program can be configured to operate without the diagnostics subroutine of 332.
Decision block 333 will determine whether or not the piston has been fully retracted. When the piston is in its fully retracted position, as noted from the position sensor 13, valve 38 is closed to begin the start of the discharge portion of the stroke cycle step 334. The positions of the piston and diaphragm are continually read and diagnosed in steps 335-338, and when the piston reaches the calculated distance L for discharging the appropriate amount of pumped media as determined by decision block 339 within the required time interval, decision block 340 will transfer control to steps 341 or 349, depending on whether two or a single valve is provided in the intermediate fluid circuit.
Assuming that only a single valve is included in the intermediate reservoiz~ supply, step 341 will open the intake valve, thus venting the intermediate pressure chamber 18 into the reservoir 44. The piston position is continually read in step 342, and when the piston has been fully extended, decision block 344 will transfer control to step 345 which closes the hydraulic intake valve 38.

W''' 91/06062 P(°f/US90/Ofi054 ~Q~~Sgl Sehen two valves are employed in venting and supplying fluid to the intermediate chamber, such as is shown in Figure 5, it being appreciated that the embodiment of .Figure 5 could also include two proximity sensors 43, and 46, the decision block 5 340 will transfer control to step 349. The second valve is opened to permit venting of the intermediate chamber through the second such valve 38 of Figure 5. The position of the piston is monitored in step 350 and when a fully extended position is obtained, decision block 352 will close the 10 previously opened valve 38 by executing step 353.
Diagnostics are included in step 351, similar to step 343, and are totally optional.
Once the required stroke length has been achieved in either a single or two valve configuration, the diaphragm and piston 15 positions are noted in steps 354 and 356, respectively, and when the diaphragm has been returned to its START position as determined in step 358, the intake valve is opened in step 359. The current desired flow rate Q is again read in step 360 and the pump parameters calculated in step 361 each time the program passes through a completed stroke.
The subroutine designated by I will position the diaphragm to a starting position when it has been found to be forward of its predetermined starting position. Step 3~D8 and decision block 310 will continuously read the position of the piston and when it has reached its maximum extension, will close the hydraulic iwtake valve in step 311. step 312 and decision block 314 will monitor the diaphragm position as it retracts with the piston. Once the position of the diaphragm has been determined to be correct in decision block 314, due to the retraction of the piston which will exert a pressure on the diaphragm, pulling it towards its starting position, control will switch to step 317. Tn step 317, the hydraulic intake valve will be opened to stop movement of the diaphragm.

WO 91/06062 PCT/US90/060j4 ..~
6~~1. . ~ ; .

Control will proceed with step 331. If the diaphragm is not at its starting position as determined in block 314, block 315 will evaluate the piston position. If the piston is fully retracted, the hydraulic intake valve will be opened in step 316, permitting fluid to enter the intermediate chamber while the piston is extended to its furthest position. The program then recycles to step 308 until the diaphragm is properly positioned.
Subroutine II similarly operates to position the diaphragm to ZO its correct star'eing position when it is found to be in back of its correct position. This requires continuously reading the position of the piston in step 321 and determining whether or not the piston is fully retracted in step 323.
When it has become fully retracted, the intake valve is closed in step 324. Measurements of the diaphragm ,position are made in step 325. Once the diaphragm is determined to be at its correct starting position, as determined by block 327, the hydraulic intake valve is opened in step 330 and control can switch to step 331. When the piston becomes fully extended, and the diaphragm has not reached starting position, as determined by block 328, the intake valve is opened in step 329 and the process recycles to 321 until the diaphragm has been correctly positioned.
Thus, there is shown one programming scheme which will permit the implementation of the embodiment shown in Figure 6, using a single valve, as well as a double valve configuration shown in Figure 5, when accompanied by a proximity sensor for positioning the diaphragm. The computer control over the start position for the diaphragm will make the accurate discharge. of a predetermined quantity of pumped fluid more consistent over time. Additionally, the various diagnostic routines will aid in determining when the diaphragm pump has suffered a failure, and permits warning of the operator that the: failure has occurred.

6~''' 9il06062 PCT/US90/06054 1?
The diagnostic routines are piston drive diagnostic routines and diaphragm diagnostic routines. The piston drive diagnostic routine is shown in Figure 4B and is incorporated throughout the execution of the program of Figures 7A and ?B.
The diaphragm diagnostic routine of Figure 8 begins by detecting whether or not the diaphragm ha~a changed position in step 401. If it has, there is a diaphragm flag which is set FALSE in step 403. The routine then exits through step 411.
20 When the .diaphragm has not been determined to have changed position, the sensor output signal from sensors 43 and 46 is checked in step 404. In the event the sensor output is determined not to be 0, and the drive flag has not been set true as determined in step 405, the operator is warned of a diaphragm malfunction in step 406. Should the drive flag be set true in 405, the routine exits through.block 411. The drive flag is set during the piston diagnostic routine, as previously explained regarding Figure 4B.
In the event decision block 404 indicates that the output from. sensors 43 and 46 ~is 0, and the diaphragm flag has been set to true in step 408, failure in the diaphrac~n position sensor is noted in step 412. This could be a failure of the sensor or the diaphragm itself. The pump is shut down in step 413 upon notification of the operator in step 412 of the failed component. Should the diaphragm flag be set false in block 408, it is subsequently set true in block 409. The routine then exits through 411.
Assuming the diaphragm diagnostics indicate no problem, the old diaphragm position value is set in step 411 to the new value and the program continues as though no failure had occurred. The routine subsequently exits to the calling dV0 91/06062 ~CT/iJS90/06054 -.
,.
is program.
The foregoing computer implementations are exemplary only of .
schemes Which may be implemented to include diagnostic routines or to admit diagnostic routines. These embodiments will provide for distributed localized control over metering pumps which may be updated by an operator as convenient, and which will warn of malfunctions as they occur.

Claims (16)

What is claimed is:
1. A computer controlled pumping system comprising:
a metering pump having a pumping piston which moves a predetermined stroke distance, forcing a predetermined quantity of pumped fluid from an inlet to an outlet:
a first electrically operated solenoid valve connected between said inlet and a supply reservoir;
a displacement sensor connected to monitor the position of said pumping piston within said stroke distance: and, a computer connected through an interface to said displacement sensor and said electrically operated solenoid valve, said computer receiving an operator-supplied value of volume flow for said metering pump, and calculating a volume displacement of media from a signal from said sensor, said computer comparing said calculated volume flow rate with said operator-supplied volume flow rate, and operating said solenoid valve when said volumes are equal, whereby a flow of fluids from said metering pump equals said operator-supplied volume of flow.
2. The computer controlled system of claim 1 comprising a second electrically operated solenoid valve connecting a recirculation port of said pump to said reservoir, and operated by said computer.
3. A computer controlled pump comprising:
a diaphragm pump having a pumping piston displacing an intermediate fluid in an intermediate chamber against a movable diaphragm in fluid communication with a pumping chamber;

a media reservoir connected to said pumping chamber;
a media outlet connected to said pumping chamber;
a displacement sensor connected to measure said pumping piston displacement;
an intermediate media reservoir connected by electrically controlled valve means to said intermediate chamber for supplying said intermediate fluid to said intermediate chamber, and venting said intermediate chamber from said intermediate media reservoir; and, a computer connected to receive a signal from said displacement sensor, said computer determining from said sensor signal a related volumetric displacement of said pumping media, and comparing said related volumetric displacement with a desired displacement, and for supplying an actuation signal to said electrically controllable valve means for terminating pumping by said diaphragm pump when said related volumetric displacement equals said desired volumetric displacement.
4. A computer controlled pump according to claim 3 comprising a second electrically controlled valve means connecting said intermediate media reservoir to said intermediate chamber for recirculating fluid through said intermediate chamber.
5. The computer controlled pump according to claim 3 further comprising a position sensor for detecting the relative position of said diaphragm.
6. The computer controlled pump according to claim 5 wherein said diaphragm position sensor is connected to said computer, and said computer monitors said diaphragm position.
7. The computer controlled pump according to claim 6 wherein said computer determines a starting position for said diaphragm from a diaphragm position sensor signal.
8. The computer controlled pump of claim 7 wherein said computer is programmed to return said diaphragm to a starting position before commencing pumping of said pumping media by controlling said electrically controlled valve means.
9. The computer controlled pump of claim 7 further including a diagnostic programming routine for detecting when a failure has occurred in said computer controlled pump.
10. A computer controlled metering pump comprising:
(a) a metering pump having a reciprocating piston which pumps a quantity of pumping media based upon a stroke length of the piston;
(b) a stroke position sensor connected to measure a stroke length of said piston;
(c) means connected to said metering pump for inhibiting pumping of pumped media, by changing the effective piston stroke length; and, (d) a computer connected to said stroke position sensor and said means for controlling the effective volume of pumped media, said computer determining from said position sensor a volume of pumping media being pumped, and comparing said computed volume of media with a desired volume of media, said computer connected to provide a signal to said means for controlling when said pumped media volume equals said desired volume inhibiting further pumping of said pumping media.
11. The computer controlled metering pump of claim 10 wherein said means for controlling inhibition of pumped media is an electrically operated solenoid valve means connected between a pumped media reservoir and a metering pump for venting said metering pump when said volume of pumped media equals said desired volume of media.
12. The computer controlled metering pump of claim 10 wherein said means for controlling inhibition of pumped media comprises:
an intermediate pressurizing means for transferring a hydraulic force from said piston to a pumping chamber of said metering pump; and, electrically operated valve means connected to said intermediate pressurizing means for controlling the effective hydraulic force.
13. The computer controlled metering pump of claim 11 wherein said valve means is connected to a reservoir of intermediate hydraulic media.
14. A computer controlled pump comprising:
a diaphragm pump having a pumping piston displacing an intermediate fluid in an intermediate chamber against a movable diaphragm in fluid communication with a pumping chamber;
a media reservoir connected to said pumping chamber;

a media outlet connected to said pumping chamber;
a diaphragm position sensor means connected to measure said diaphragm displacement;
an intermediate media reservoir connected by electrically controlled valve means to said intermediate chamber for supplying said intermediate fluid to said intermediate chamber, and venting said intermediate chamber from said intermediate media reservoir; and, a computer connected to receive a signal from said diaphragm sensor, said computer determining from said sensor signal a related volumetric displacement of said pumping media, and comparing said related volumetric displacement with a desired displacement, and for supplying an actuation signal to said electrically controllable valve means for terminating pumping by said diaphragm pump when said related volumetric displacement equals said desired volumetric displacement.
15. A computer controlled pump according to claim 14 comprising a second electrically connected valve means connecting said intermediate media reservoir to said intermediate chamber for recirculating fluid through said intermediate chamber.
16. The computer controlled pump according to claim 14 further comprising a position sensor for detecting the position of said pumping piston.
CA002066581A 1989-10-20 1990-10-22 Computer controlled metering pump Expired - Fee Related CA2066581C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US07/424,443 US5056036A (en) 1989-10-20 1989-10-20 Computer controlled metering pump
US424,443 1989-10-20
PCT/US1990/006054 WO1991006062A1 (en) 1989-10-20 1990-10-22 Computer controlled metering pump

Publications (2)

Publication Number Publication Date
CA2066581A1 CA2066581A1 (en) 1991-04-21
CA2066581C true CA2066581C (en) 2000-10-10

Family

ID=23682652

Family Applications (1)

Application Number Title Priority Date Filing Date
CA002066581A Expired - Fee Related CA2066581C (en) 1989-10-20 1990-10-22 Computer controlled metering pump

Country Status (7)

Country Link
US (1) US5056036A (en)
EP (1) EP0496803B1 (en)
JP (1) JPH05508700A (en)
AT (1) ATE154152T1 (en)
CA (1) CA2066581C (en)
DE (1) DE69030881T2 (en)
WO (1) WO1991006062A1 (en)

Families Citing this family (89)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5249932A (en) * 1991-10-07 1993-10-05 Erik Van Bork Apparatus for controlling diaphragm extension in a diaphragm metering pump
US5378122A (en) 1993-02-16 1995-01-03 Wilden Pump & Engineering Co. Air driven diaphragm pump
FR2706857B1 (en) * 1993-06-25 1995-10-27 Dussau Distribution Sarl
US5526685A (en) * 1995-01-17 1996-06-18 Graseby Andersen Inc. Fluid flow rate measuring and controlling apparatus and method for using same
JP3371687B2 (en) * 1996-06-11 2003-01-27 株式会社スリーボンド Dispensing method
US5751599A (en) * 1996-07-10 1998-05-12 Bortnik; Michael Probeless microprocessor based controller for open recirculating evaporative cooling systems
US5975854A (en) * 1997-05-09 1999-11-02 Copeland Corporation Compressor with protection module
US6017200A (en) * 1997-08-12 2000-01-25 Science Applications International Corporation Integrated pumping and/or energy recovery system
DE19742632A1 (en) * 1997-09-26 1999-04-08 Fresenius Medical Care De Gmbh Pumping and dosing device
US6109881A (en) * 1998-01-09 2000-08-29 Snodgrass; Ocie T. Gas driven pump for the dispensing and filtering of process fluid
DE19826610A1 (en) 1998-06-16 1999-12-23 Bran & Luebbe Diaphragm pump and device for controlling the same
US6585933B1 (en) 1999-05-03 2003-07-01 Betzdearborn, Inc. Method and composition for inhibiting corrosion in aqueous systems
US6280147B1 (en) 1998-10-13 2001-08-28 Liquid Metronics Incorporated Apparatus for adjusting the stroke length of a pump element
US6174136B1 (en) 1998-10-13 2001-01-16 Liquid Metronics Incorporated Pump control and method of operating same
US6505475B1 (en) 1999-08-20 2003-01-14 Hudson Technologies Inc. Method and apparatus for measuring and improving efficiency in refrigeration systems
US6264432B1 (en) * 1999-09-01 2001-07-24 Liquid Metronics Incorporated Method and apparatus for controlling a pump
US6302654B1 (en) * 2000-02-29 2001-10-16 Copeland Corporation Compressor with control and protection system
US7047753B2 (en) * 2000-03-14 2006-05-23 Hussmann Corporation Refrigeration system and method of operating the same
US6973794B2 (en) 2000-03-14 2005-12-13 Hussmann Corporation Refrigeration system and method of operating the same
US6647735B2 (en) 2000-03-14 2003-11-18 Hussmann Corporation Distributed intelligence control for commercial refrigeration
US7000422B2 (en) 2000-03-14 2006-02-21 Hussmann Corporation Refrigeration system and method of configuring the same
US6332327B1 (en) 2000-03-14 2001-12-25 Hussmann Corporation Distributed intelligence control for commercial refrigeration
US6999996B2 (en) * 2000-03-14 2006-02-14 Hussmann Corporation Communication network and method of communicating data on the same
US6393338B1 (en) * 2000-03-17 2002-05-21 Tadeusz Kemnitz Apparatus and control method for accurate rotary peristaltic pump filling
US6350110B1 (en) * 2000-03-31 2002-02-26 B&G International Multiport metering pump
US6668240B2 (en) 2001-05-03 2003-12-23 Emerson Retail Services Inc. Food quality and safety model for refrigerated food
US6892546B2 (en) 2001-05-03 2005-05-17 Emerson Retail Services, Inc. System for remote refrigeration monitoring and diagnostics
US6640556B2 (en) 2001-09-19 2003-11-04 Westport Research Inc. Method and apparatus for pumping a cryogenic fluid from a storage tank
US6625519B2 (en) 2001-10-01 2003-09-23 Veeder-Root Company Inc. Pump controller for submersible turbine pumps
US7204679B2 (en) * 2002-09-30 2007-04-17 Emerson Electric Co. Flow control system
JP4187500B2 (en) * 2002-10-25 2008-11-26 アルパイン株式会社 Message processing apparatus and system
US6889173B2 (en) 2002-10-31 2005-05-03 Emerson Retail Services Inc. System for monitoring optimal equipment operating parameters
US7094353B2 (en) * 2002-11-04 2006-08-22 Arch Chemicals, Inc. Method of water treatment
US8463441B2 (en) 2002-12-09 2013-06-11 Hudson Technologies, Inc. Method and apparatus for optimizing refrigeration systems
WO2005022049A2 (en) 2003-08-25 2005-03-10 Computer Process Controls, Inc. Refrigeration control system
US6946968B1 (en) 2003-09-24 2005-09-20 Johnson Clifford C Hydraulic stroke measuring system
CN100368199C (en) * 2004-02-12 2008-02-13 佳能株式会社 Liquid applying apparatus and ink jet printing apparatus
US7412842B2 (en) 2004-04-27 2008-08-19 Emerson Climate Technologies, Inc. Compressor diagnostic and protection system
US7275377B2 (en) 2004-08-11 2007-10-02 Lawrence Kates Method and apparatus for monitoring refrigerant-cycle systems
WO2006091521A2 (en) 2005-02-21 2006-08-31 Computer Process Controls, Inc. Enterprise control and monitoring system
DE202005013090U1 (en) * 2005-08-19 2007-01-04 Prominent Dosiertechnik Gmbh Motor e.g. asynchronous motor, dosing pump for dosing e.g. oil, has position sensor providing motion sequence of displacement organ so that electronic controlling of pump responds to operating conditions of dosing circle and dosing pump
DE102005039237A1 (en) * 2005-08-19 2007-02-22 Prominent Dosiertechnik Gmbh motor-driven metering
US7594407B2 (en) 2005-10-21 2009-09-29 Emerson Climate Technologies, Inc. Monitoring refrigerant in a refrigeration system
US7596959B2 (en) 2005-10-21 2009-10-06 Emerson Retail Services, Inc. Monitoring compressor performance in a refrigeration system
US7752854B2 (en) 2005-10-21 2010-07-13 Emerson Retail Services, Inc. Monitoring a condenser in a refrigeration system
US7752853B2 (en) 2005-10-21 2010-07-13 Emerson Retail Services, Inc. Monitoring refrigerant in a refrigeration system
US7665315B2 (en) 2005-10-21 2010-02-23 Emerson Retail Services, Inc. Proofing a refrigeration system operating state
SE529328C2 (en) 2005-11-15 2007-07-10 Johan Stenberg Control system and method for controlling electromagnetically driven pumps
US8590325B2 (en) 2006-07-19 2013-11-26 Emerson Climate Technologies, Inc. Protection and diagnostic module for a refrigeration system
US20080216494A1 (en) 2006-09-07 2008-09-11 Pham Hung M Compressor data module
CN101245770B (en) * 2007-02-17 2012-05-30 卓越剂量技术有限公司 Electromotor driven metering pump
US20090037142A1 (en) 2007-07-30 2009-02-05 Lawrence Kates Portable method and apparatus for monitoring refrigerant-cycle systems
US20090041588A1 (en) * 2007-08-08 2009-02-12 Halliburton Energy Services, Inc. Active valve system for positive displacement pump
US8152476B2 (en) * 2007-08-24 2012-04-10 Toyo Pumps North America Corp. Positive displacement pump with a working fluid and linear motor control
US8393169B2 (en) 2007-09-19 2013-03-12 Emerson Climate Technologies, Inc. Refrigeration monitoring system and method
US9140728B2 (en) 2007-11-02 2015-09-22 Emerson Climate Technologies, Inc. Compressor sensor module
US8160827B2 (en) 2007-11-02 2012-04-17 Emerson Climate Technologies, Inc. Compressor sensor module
US8185237B2 (en) * 2007-12-28 2012-05-22 Malema Engineering Corporation Dispense verification meters
NO330021B1 (en) * 2009-02-11 2011-02-07 Statoil Asa Installations for storage and supply of compressed gas
BRPI1014993A8 (en) 2009-05-29 2016-10-18 Emerson Retail Services Inc system and method for monitoring and evaluating equipment operating parameter modifications
US8565925B2 (en) * 2009-09-29 2013-10-22 Virid Services Llc System and method for injecting a fluid additive into a fluid dispensation system
NL1037427C2 (en) * 2009-10-30 2011-05-03 Lely Patent Nv MILK PUMP DEVICE AND METHOD FOR MOVING A QUANTITY OF MILK.
US9850889B2 (en) * 2010-02-02 2017-12-26 Dajustco Ip Holdings Inc. Hydraulic fluid control system for a diaphragm pump
EP2362100B2 (en) * 2010-02-18 2020-07-08 Grundfos Management A/S Metering pump aggregate and method for controlling same
FR2965864B1 (en) * 2010-10-08 2012-12-14 Dosatron International LIQUID DOSING PUMP, AND DEVICE FOR DETECTING PRESSURE VARIATION FOR SUCH A PUMP.
EP2661412A4 (en) * 2011-01-05 2014-10-08 Noam Levine A fluid flow meter
CA2934860C (en) 2011-02-28 2018-07-31 Emerson Electric Co. Residential solutions hvac monitoring and diagnosis
US8459195B2 (en) 2011-04-28 2013-06-11 Michael H. IRVING Self load sensing circuit board controller diaphragm pump
US8434697B1 (en) * 2011-05-12 2013-05-07 Peter Olt Autonomous system for injecting additives into irrigation water
ITCO20110071A1 (en) * 2011-12-22 2013-06-23 Nuovo Pignone Spa ALTERNATIVE COMPRESSORS HAVING TIMED VALVES AND RELATED METHODS
US8964338B2 (en) 2012-01-11 2015-02-24 Emerson Climate Technologies, Inc. System and method for compressor motor protection
CN102661766B (en) * 2012-05-16 2013-06-12 长沙伟诺机电有限公司 Asphalts small flow metering device
US8687180B2 (en) * 2012-06-07 2014-04-01 Molecular Devices, Llc System, method, and device for determining a focal position of an objective in a microscopy imaging system
US9480177B2 (en) 2012-07-27 2016-10-25 Emerson Climate Technologies, Inc. Compressor protection module
US9310439B2 (en) 2012-09-25 2016-04-12 Emerson Climate Technologies, Inc. Compressor having a control and diagnostic module
CA2904734C (en) 2013-03-15 2018-01-02 Emerson Electric Co. Hvac system remote monitoring and diagnosis
US9803902B2 (en) 2013-03-15 2017-10-31 Emerson Climate Technologies, Inc. System for refrigerant charge verification using two condenser coil temperatures
US9551504B2 (en) 2013-03-15 2017-01-24 Emerson Electric Co. HVAC system remote monitoring and diagnosis
US9765979B2 (en) 2013-04-05 2017-09-19 Emerson Climate Technologies, Inc. Heat-pump system with refrigerant charge diagnostics
FR3005647B1 (en) * 2013-05-17 2015-09-04 Cirmeca DEVICE AND METHOD FOR DETERMINING PRODUCTS AND FILLING CONTAINERS WITH SAID PRODUCTS
CN103244390B (en) * 2013-05-20 2015-06-24 贝恩医疗设备(广州)有限公司 Metering pump
US9605664B2 (en) * 2014-01-07 2017-03-28 Ingersoll-Rand Company Pneumatic piston pump metering and dispense control
US10954931B2 (en) * 2014-12-12 2021-03-23 Dh Technologies Development Pte. Ltd. Linear displacement pump with position sensing and related systems and methods
ITUB20160404A1 (en) 2016-01-26 2017-07-26 Global Service Design Ltd Uk Company Number 07411425 APPARATUS FOR THE CONTROLLED DISTRIBUTION OF A FLUID FROM A CONTAINER AND ITS RELATION METHOD
DE102016117357A1 (en) * 2016-09-15 2018-03-15 Prominent Gmbh Method for operating metering devices
WO2018093385A1 (en) * 2016-11-21 2018-05-24 Halliburton Energy Services, Inc. Cylinder pump systems and methods for pumping and measuring fluids
US20180372083A1 (en) * 2017-06-22 2018-12-27 Wanner Engineering, Inc. Hydraulic diaphragm control
AU2018204487B1 (en) * 2017-11-10 2019-05-30 Quantum Servo Pumping Technologies Pty Ltd Pumping systems
CA3200839A1 (en) * 2020-11-09 2022-05-12 Pdc Machines Inc. Active oil injection system for a diaphragm compressor

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1084486B (en) * 1954-04-15 1960-06-30 Kontak Mfg Company Ltd Liquid metering pump
US3227314A (en) * 1964-03-03 1966-01-04 Porter Lancastrian Ltd Delivering of measured quantities of pressurised liquids
US3756456A (en) * 1972-05-22 1973-09-04 Graco Inc Apparatus and method for a metering system
US3913314A (en) * 1972-06-09 1975-10-21 Westinghouse Electric Corp System and method for operating a gas turbine electric power plant with bypass flow fueling operation to provide improved reliability and extended apparatus life
US4241602A (en) * 1979-04-20 1980-12-30 Seismograph Service Corporation Rheometer
DE2933327A1 (en) * 1979-08-17 1981-03-26 Bayer Ag, 51373 Leverkusen METHOD AND DEVICE FOR PRODUCING A FLOWABLE REACTION MIXTURE MAKING SOLID OR FOAM
US4315523A (en) * 1980-03-06 1982-02-16 American Flow Systems, Inc. Electronically controlled flow meter and flow control system
US4474309A (en) * 1981-10-22 1984-10-02 Oximetrix, Inc. Stepping motor control procedure for achieving variable rate, quasi-continuous fluid infusion
DE3203087A1 (en) * 1982-01-30 1983-08-04 Gebrüder Sucker, 4050 Mönchengladbach METHOD AND DEVICE FOR COATING OR IMRAEGNING A SUBSTRATE GUIDED IN A TRAIN
DE3204050C1 (en) * 1982-02-06 1983-07-21 Chemie Und Filter Gmbh, Verfahrenstechnik Kg, 6900 Heidelberg Electromagnetically operated axial piston pump, especially diaphragm pump
US4715786A (en) * 1984-12-14 1987-12-29 Cole-Parmer Instrument Company Control method and apparatus for peristaltic fluid pump
US4796782A (en) * 1985-10-30 1989-01-10 Automation, Inc. Ink monitor system
US4723976A (en) * 1986-07-30 1988-02-09 Owens-Illinois Television Products Inc. Method and apparatus for pressing glass cathode ray tube faceplates
DE3706338A1 (en) * 1987-02-27 1988-09-08 Wagner Gmbh J DIAPHRAGM PUMP DEVICE
US4897797A (en) * 1988-04-25 1990-01-30 Betz Laboratories, Inc. Proportional chemical feeding system

Also Published As

Publication number Publication date
EP0496803B1 (en) 1997-06-04
EP0496803A4 (en) 1993-08-04
DE69030881D1 (en) 1997-07-10
ATE154152T1 (en) 1997-06-15
CA2066581A1 (en) 1991-04-21
DE69030881T2 (en) 1997-09-18
WO1991006062A1 (en) 1991-05-02
JPH05508700A (en) 1993-12-02
US5056036A (en) 1991-10-08
EP0496803A1 (en) 1992-08-05

Similar Documents

Publication Publication Date Title
CA2066581C (en) Computer controlled metering pump
RU2086806C1 (en) System and method for control of liquid diaphragm pump
JP5586958B2 (en) System and method for pump operation
RU2106561C1 (en) Method and device for check of medium-actuated fittings
EP1092131B1 (en) Determining when fluid has stopped flowing within an element
EP2795266B1 (en) Method for dosing a fluid
EP3187735B1 (en) Pump system as well as a method for determining the flow in a pump system
CN102211390B (en) Hydraulic drive unit for injection moulding machine and injection moulding machine
CN103619480A (en) Process for detecting anomalies during the filling of a liquid metering device and liquid metering device
KR101998395B1 (en) High speed high capacity flow measuring device for repeated pressurized testing of ultra high pressure container
US4649734A (en) Apparatus and method for calibrating a flow meter
NL1004028C2 (en) Method for determining the amount of undissolved gas in a hydraulic system.
JP3317778B2 (en) Automatic measuring method of gas pressure of accumulator
CN113950340A (en) Pressure detection device and blood purification device using same
JP2004212128A (en) Abnormality monitoring method of hydraulic device
EP0451752A2 (en) Method and apparatus for testing gas dispersed in a liquid
EP3579994B1 (en) Die-casting machine with a valve diagnosis system
CN110778487B (en) Method for determining the volume delivered by means of a piston pump and dual-acting pneumatically drivable piston pump for carrying out the method
US9926925B2 (en) Sludge flow measuring system
DE60307446T2 (en) Apparatus and method for dosing a predetermined amount of compressible air containing liquid
RU1779781C (en) Method for measuring delivery of positive displacement pump with valve distributor
CA2118144C (en) Improved method and apparatus for calculating flow rates through a pumping station
JP2023146911A (en) hydraulic unit
WO2019119412A1 (en) Device for measuring filling time of balancing chamber system, device for detecting abnormity in balancing chamber system, balancing chamber module, dialysis system and corresponding method
CN114704524A (en) Equipment state monitoring system and monitoring method

Legal Events

Date Code Title Description
EEER Examination request
MKLA Lapsed