EP0776314B1 - Method of filling containers with liquid under pressure - Google Patents

Method of filling containers with liquid under pressure Download PDF

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Publication number
EP0776314B1
EP0776314B1 EP96916004A EP96916004A EP0776314B1 EP 0776314 B1 EP0776314 B1 EP 0776314B1 EP 96916004 A EP96916004 A EP 96916004A EP 96916004 A EP96916004 A EP 96916004A EP 0776314 B1 EP0776314 B1 EP 0776314B1
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EP
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Prior art keywords
filling
liquid
pressure
control device
measured
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EP96916004A
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German (de)
French (fr)
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EP0776314A1 (en
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Detlef Boertz
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Robert Bosch GmbH
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Robert Bosch GmbH
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67CCLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/20Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus with provision for metering the liquids to be introduced, e.g. when adding syrups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67CCLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/20Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus with provision for metering the liquids to be introduced, e.g. when adding syrups
    • B67C3/202Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus with provision for metering the liquids to be introduced, e.g. when adding syrups by weighing

Definitions

  • the invention is based on a method for filling Containers with a liquid under pressure the genus of claim 1. From JP 10 46 392 B4 Such a method has already become known. At This procedure uses the fluid pressure after opening of a filling valve measured once, whereupon a Control device based on the measured Liquid pressure a filling time or opening time for the Filling valve calculated for a certain filling quantity.
  • a disadvantage of the known method is that during the Filling process occurring pressure fluctuations that lead to a Do not change the flow rate at the filling valve be taken into account. The fill quantities also remain during the opening and closing process of the filling valve disregarded. The accuracy of the known Filling process is therefore limited.
  • the method according to the invention for filling containers with a pressurized liquid with the characteristic features of claim 1 has in contrast the advantage that it works very precisely. This will achieved according to the invention in that the liquid pressure is constantly measured during the filling process, so that occurring pressure fluctuations are taken into account.
  • the flow rates during the Opening and closing process of the filling valve is detected, and be taken into account when calculating the filling volumes.
  • the Conveying device 11 has a screw conveyor 12 for intermittent or continuous transport of the Packaging container 10 on.
  • the packaging container 10 stand and slide on rail sections 13 to 15. Between the rail sections 13 and 14 or 14 and 15 one controllable via a reject device 16 Weighing device 17, 18 for one packaging container each 10 arranged, one of which 17 the tare weight G1, and the other 18 the gross weight G2 the Packaging container 10 detected and a control device 19th as input variable.
  • control device 19 are, for example product-specific data, such as the viscosity curve of the Fluid over temperature as well as device data saved.
  • product-specific data such as the viscosity curve of the Fluid over temperature
  • device data saved With the control device 19 is an input / output unit 20 connected, in particular a Target filling quantity M or a target filling weight of Packaging container 10 to the control device 19th can be entered.
  • the Filling device 22 includes a cyclical transport the packaging container 10 one of the number of each conveying cycle to be filled packaging container 10 corresponding number of Filling heads 23, for example six, each one on and have removable hollow filling needle 24. Every filling head 23 is with a metering valve 25 for the liquid coupled, with all metering valves 25 of the Control device 19 can be controlled synchronously together.
  • the metering valves 25 are connected to a via short lines 26 common tubular manifold 30 connected in the one Liquid pressure P1 prevails.
  • the distributor 30 is in turn via a line 33 and a Quick release device 34 with a storage container 35 for the liquid connected.
  • the pressure drop between the with the liquid fully filled manifold 30 and individual metering valves 25 is, for example, by a Arrangement of the metering valves 25 in the same vertical Distance to the distributor 30 always the same size, and in the Control device 10 stored as a factor.
  • the reservoir 35 is a Pressure line 36 is pressurized with a gas pressure P2.
  • Pressure P2 generally increases the pressure Liquid at the metering valves 25, and thus a large one Outflow rate from the reservoir 35 enables which is especially the case with highly viscous liquids Flow behavior favors.
  • a temperature sensor 31 for detection is in the distributor 30 a liquid temperature T and a pressure sensor 32 for Detection of the liquid pressure P1 arranged.
  • the two Sensors 31, 32 are also connected to the control device 19 connected.
  • the liquid pressure P1 continuously at certain time intervals ⁇ t, for example every 150 ⁇ sec. until every 250 ⁇ sec. measured, and supplied to the control device 19 as an input variable becomes.
  • the duration of the time intervals ⁇ t between the individual Measurements of fluid pressure P1 should be chosen this way be that even during the opening and closing process of the metering valves 25 detects liquid pressures P1, and on the control device 19 are forwarded. From these For reasons there is a value for ⁇ t of 200 ⁇ sec. proven, the adequate resolution even during opening and Closing process of the filling valves 25 guaranteed.
  • the device described above works as follows:
  • the packaging container 10 are from the screw conveyor 21 fed to the filling device 22 in cycles.
  • the filling needles 24 of the Filling heads 23 lowered and into the packaging container 10 introduced.
  • a corresponding Control signal Z to the metering valves 25 through the Control device 19 the filling of the target filling quantity M in the Packaging container 10 initiated, i.e. the control signal Z, for example, energizes a coil in the Metering valve 25 so that its needle lifts off the valve seat.
  • the calculation of the filled filling quantity M (ist), and thus the duration of the control signal Z to the metering valves 25 takes place in that the control device 19th continuous partial volumes ⁇ M calculated and during the duration of the control signal Z are added up.
  • the partial volumes ⁇ M are calculated from the time intervals ⁇ t between the individual measurements of the liquid pressures P1, the respective the value supplied to the control device 19 Fluid pressure of P1, as well as one in the Control device 19 stored functional relationship k (p1) between the respective value of P1 and the resulting value in the Dosing valves 25 resulting flow rate per Time unit.
  • This limit value M (max) which causes the control signal Z to end, is in the simplest case the desired filling quantity M itself.
  • the limit value M (max) stored in the control device 19 can also be selected to be smaller in accordance with the closing characteristics of the filling valves 25, so that for example, the filling quantity or the partial volumes .DELTA.M are also taken into account that enter the containers 10 during the closing process (after the control signal Z has failed) of the metering valves 25. This means that in this case the limit value M (max) is smaller than the target filling quantity M.
  • Control device 19 The accuracy of the partial volume calculation ⁇ M Control device 19 is by taking into account the Temperature sensor 31 detected temperature T of the liquid elevated. This is achieved in that Control device 19 for the flow / viscosity characteristics the respective liquid are stored so that for Calculation of the individual partial volumes ⁇ M additionally on the corresponding temperature-corrected functional context k is accessed, i.e. the value of factor k is also depends on the temperature [k (P1, T)].
  • the filling needles 24 are introduced through the Filling heads 23 again from the packaging containers 10 lifted out. Then the packaging container 10 by the conveyor screw 12 cyclically another Processing station, for example a sealing station, promoted. At the same time repeats itself for new in the Filling machine conveyed packaging container 10 the process as described above.
  • the value is sufficient of the liquid pressure P1 only during the actual one Filling process. Usually and for Control purposes in the event of any malfunction of the Filling machine, however, the fluid pressure P1 becomes constant measured and fed to the control device 19.
  • the time intervals ⁇ t it is also conceivable for the time intervals ⁇ t to be so large to choose that the opening and closing of the Dosing valves 25 with respect to the partial volumes ⁇ M no longer is taken into account exactly, and in this case for opening and closing the metering valves 25 fixed partial volumes ⁇ M (fixed) (according to the metering valve characteristics) to assume. Even in this case, the accuracy improved compared to known filling methods because Pressure fluctuations during the actual filling be taken into account.

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  • Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
  • Basic Packing Technique (AREA)

Description

Stand der TechnikState of the art

Die Erfindung geht aus von einem Verfahren zum Befüllen von Behältern mit einer unter Druck stehenden Flüssigkeit nach der Gattung des Anspruchs 1. Aus der JP 10 46 392 B4 ist bereits ein derartiges Verfahren bekannt geworden. Bei diesem Verfahren wird der Flüssigkeitsdruck nach dem Öffnen eines Füllventils einmalig gemessen, worauf eine Steuereinrichtung aufgrund des gemessenen Flüssigkeitsdruckes eine Füllzeit bzw. Öffnungszeit für das Füllventil für eine bestimmte Füllmenge berechnet. Nachteilig bei dem bekannten Verfahren ist, daß während des Füllvorganges auftretende Druckschwankungen, die zu einer Änderung der Durchflußmenge an dem Füllventil führen, nicht berücksichtigt werden. Weiterhin bleiben auch die Füllmengen während des Öffnungs- und Schließvorganges des Füllventils unberücksichtigt. Die Genauigkeit des bekannten Füllverfahrens ist daher beschränkt.The invention is based on a method for filling Containers with a liquid under pressure the genus of claim 1. From JP 10 46 392 B4 Such a method has already become known. At This procedure uses the fluid pressure after opening of a filling valve measured once, whereupon a Control device based on the measured Liquid pressure a filling time or opening time for the Filling valve calculated for a certain filling quantity. A disadvantage of the known method is that during the Filling process occurring pressure fluctuations that lead to a Do not change the flow rate at the filling valve be taken into account. The fill quantities also remain during the opening and closing process of the filling valve disregarded. The accuracy of the known Filling process is therefore limited.

Vorteile der ErfindungAdvantages of the invention

Das erfindungsgemäße Verfahren zum Befüllen von Behältern mit einer unter Druck stehenden Flüssigkeit mit den kennzeichnenden Merkmalen des Anspruchs 1 hat demgegenüber den Vorteil, daß es sehr genau arbeitet. Dies wird erfindungsgemäß dadurch erreicht, daß der Flüssigkeitsdruck während des Abfüllvorganges ständig gemessen wird, so daß auftretende Druckschwankungen berücksichtigt werden.The method according to the invention for filling containers with a pressurized liquid with the characteristic features of claim 1 has in contrast the advantage that it works very precisely. this will achieved according to the invention in that the liquid pressure is constantly measured during the filling process, so that occurring pressure fluctuations are taken into account.

Weiterhin können auch die Durchflußmengen währned des Öffnungs- und Schließvorganges des Füllventils erfaßt, und bei der Berechnung der Füllvolumina berücksichtigt werden. Furthermore, the flow rates during the Opening and closing process of the filling valve is detected, and be taken into account when calculating the filling volumes.

Weitere Vorteile und vorteilhafte Weiterbildungen des erfindungsgemäßen Verfahrens zum Befüllen von Behältern mit einer unter Druck stehenden Flüssigkeit ergeben sich aus den Unteransprüchen und der Beschreibung.Further advantages and advantageous developments of the Method according to the invention for filling containers with a pressurized liquid result from the Subclaims and the description.

Zeichnungdrawing

Ein Ausführungsbeispiel der Erfindung ist in der Zeichnung dargestellt und wird in der nachfolgenden Beschreibung näher erläutert. Die einzige Figur 1 zeigt eine Füllmaschine in einer schematischen Darstellung.An embodiment of the invention is in the drawing shown and is described in more detail in the following description explained. The only Figure 1 shows a filling machine in a schematic representation.

Beschreibung des AusführungsbeispielsDescription of the embodiment

Die in der Figur 1 dargestellte Füllmaschine zum Dosieren und Abfüllen einer Flüssigkeit in Verpackungsbehälter 10 hat eine Fördereinrichtung 11, mit der Verpackungsbehälter 10, wie beispielsweise Ampullen oder Vials, hintereinander angeordneten Behandlungsstationen zugeführt werden. Die Fördereinrichtung 11 weist eine Transportschnecke 12 zum taktweisen oder kontinuierlichen Transport der Verpackungsbehälter 10 auf. Die Verpackungsbehälter 10 stehen und gleiten auf Schienenstücken 13 bis 15. Zwischen den Schienenstücken 13 und 14 beziehungsweise 14 und 15 ist jeweils eine über eine Ausschleußeinrichtung 16 ansteuerbare Wägeeinrichtung 17, 18 für jeweils einen Verpackungsbehälter 10 angeordnet, von denen die eine 17 das Tara-Gewicht G1, und die andere 18 das Brutto-Gewicht G2 der Verpackungsbehälter 10 erfaßt und einer Steuereinrichtung 19 als Eingangsgröße zuführt.The filling machine for dosing shown in Figure 1 and filling a liquid into packaging container 10 a conveyor 11 with the packaging container 10, such as ampoules or vials, one after the other arranged treatment stations are supplied. The Conveying device 11 has a screw conveyor 12 for intermittent or continuous transport of the Packaging container 10 on. The packaging container 10 stand and slide on rail sections 13 to 15. Between the rail sections 13 and 14 or 14 and 15 one controllable via a reject device 16 Weighing device 17, 18 for one packaging container each 10 arranged, one of which 17 the tare weight G1, and the other 18 the gross weight G2 the Packaging container 10 detected and a control device 19th as input variable.

In der Steuereinrichtung 19 sind beispielsweise produktspezifische Daten, wie der Viskositätsverlauf der Flüssigkeit über der Temperatur sowie Daten der Vorrichtung abgespeichert. Mit der Steuereinrichtung 19 ist eine Ein/Ausgabeeinheit 20 verbunden, über die insbesondere eine Sollfüllmenge M bzw. ein Sollfüllgewicht der Verpackungsbehälter 10 an die Steuereinrichtung 19 eingegeben werden kann.In the control device 19 are, for example product-specific data, such as the viscosity curve of the Fluid over temperature as well as device data saved. With the control device 19 is an input / output unit 20 connected, in particular a Target filling quantity M or a target filling weight of Packaging container 10 to the control device 19th can be entered.

Oberhalb der Fördereinrichtung 11 ist im Bereich des Schienenstücks 14 eine Abfülleinrichtung 22 angeordnet. Die Abfülleinrichtung 22 umfaßt bei einem taktweisen Transport der Verpackungsbehälter 10 eine der Zahl der pro Fördertakt zu füllenden Verpackungsbehälter 10 entsprechende Anzahl von Abfüllköpfen 23, beispielsweise sechs, die jeweils eine auf- und abbewegbare hohle Füllnadel 24 haben. Jeder Abfüllkopf 23 ist mit je einem Dosierventil 25 für die Flüssigkeit gekoppelt, wobei alle Dosierventile 25 von der Steuereinrichtung 19 gemeinsam synchron ansteuerbar sind. Die Dosierventile 25 sind über kurze Leitungen 26 mit einem gemeinsamen, rohrförmigen Verteiler 30 verbunden, in dem ein Flüssigkeitsdruck P1 herrscht. Der Verteiler 30 ist seinerseits über eine Leitung 33 und eine Schnellspanneinrichtung 34 mit einem Vorratsbehälter 35 für die Flüssigkeit verbunden. Das Druckgefälle zwischen dem mit der Flüssigkeit vollständig gefüllten Verteiler 30 und den einzelnen Dosierventilen 25 ist beispielsweise durch eine Anordnung der Dosierventile 25 in gleichem vertikalen Abstand zum Verteiler 30 stets gleich groß, und in der Steuereinrichtung 10 als Faktor abgespeichert.Above the conveyor 11 is in the area of Rail piece 14 a filling device 22 is arranged. The Filling device 22 includes a cyclical transport the packaging container 10 one of the number of each conveying cycle to be filled packaging container 10 corresponding number of Filling heads 23, for example six, each one on and have removable hollow filling needle 24. Every filling head 23 is with a metering valve 25 for the liquid coupled, with all metering valves 25 of the Control device 19 can be controlled synchronously together. The metering valves 25 are connected to a via short lines 26 common tubular manifold 30 connected in the one Liquid pressure P1 prevails. The distributor 30 is in turn via a line 33 and a Quick release device 34 with a storage container 35 for the liquid connected. The pressure drop between the with the liquid fully filled manifold 30 and individual metering valves 25 is, for example, by a Arrangement of the metering valves 25 in the same vertical Distance to the distributor 30 always the same size, and in the Control device 10 stored as a factor.

In dem Vorratsbehälter 35 befindet sich vorteilhafterweise die Menge an Flüssigkeit, die während einer Produktionsschicht zur Abfüllung der Verpackungsbehälter 10 benötigt wird. Dadurch ergibt sich, daß die Füllhöhe im Vorratsbehälter 35 bei jedem Abfüllzyklus nur in sehr geringem Maße abnimmt. Der Vorratsbehälter 35 ist über eine Druckleitung 36 mit einem Gasdruck P2 beaufschlagt.It is advantageously located in the storage container 35 the amount of fluid that flows during a Production layer for filling the packaging container 10 is needed. This means that the fill level in Storage container 35 in each filling cycle only in very decreases slightly. The reservoir 35 is a Pressure line 36 is pressurized with a gas pressure P2.

Vorteilhafterweise besteht dabei eine Beeinflussung zwischen den Drücken P1 und P2, so daß P2 beispielsweise von der Steuereinrichtung 19 so geregelt wird, daß sich stets ein Druck P1 einstellt, dessen Toleranz zum Beispiel +/- 0,05 bar beträgt. Somit können verschiedene Anordnungen des Vorratsbehälters 35 an der Füllmaschine sowie ein sinkender Flüssigkeitsspiegel in dem Vorratsbehälter 35 ausgeglichen werden.There is advantageously an influence between the pressures P1 and P2, so that P2, for example, from the Control device 19 is regulated so that there is always a Pressure P1 sets, its tolerance for example +/- 0.05 bar. Thus, various arrangements of the Storage container 35 on the filling machine and a sinking Liquid level in the reservoir 35 balanced become.

Durch den Druck P2 wird generell ein höherer Druck der Flüssigkeit an den Dosierventilen 25, und damit eine große Abflußgeschwindigkeit aus dem Vorratsbehälter 35 ermöglicht, was insbesondere bei hochviskosen Flüssigkeiten das Fließverhalten begünstigt.Pressure P2 generally increases the pressure Liquid at the metering valves 25, and thus a large one Outflow rate from the reservoir 35 enables which is especially the case with highly viscous liquids Flow behavior favors.

Im Verteiler 30 sind ein Temperatursensor 31 zur Erfassung einer Flüssigkeitstemperatur T und ein Drucksensor 32 zur Erfassung des Flüssigkeitsdruckes P1 angeordnet. Die beiden Sensoren 31, 32 sind ebenfalls mit der Steuereinrichtung 19 verbunden.A temperature sensor 31 for detection is in the distributor 30 a liquid temperature T and a pressure sensor 32 for Detection of the liquid pressure P1 arranged. The two Sensors 31, 32 are also connected to the control device 19 connected.

Wesentlich ist, daß insbesondere der Flüssigkeitsdruck P1 kontinuierlich in bestimmten Zeitabständen Δt, beispielsweise alle 150 µsec. bis alle 250 µsec. gemessen, und der Steuereinrichtung 19 als Eingangsgröße zugeführt wird. Die Dauer der Zeitabstände Δt zwischen den einzelnen Messungen des Flüssigkeitsdruckes P1 sollte so gewählt werden, daß auch während des Öffnungs- und Schließvorganges der Dosierventile 25 Flüssigkeitsdrücke P1 erfaßt, und an die Steuereinrichtung 19 weitergeleitet werden. Aus diesen Gründen hat sich ein Wert für Δt von 200 µsec. bewährt, der eine ausreichende Auflösung auch während des Öffnungs- und Schließvorganges der Füllventile 25 gewährleistet.It is essential that in particular the liquid pressure P1 continuously at certain time intervals Δt, for example every 150 µsec. until every 250 µsec. measured, and supplied to the control device 19 as an input variable becomes. The duration of the time intervals Δt between the individual Measurements of fluid pressure P1 should be chosen this way be that even during the opening and closing process of the metering valves 25 detects liquid pressures P1, and on the control device 19 are forwarded. From these For reasons there is a value for Δt of 200 µsec. proven, the adequate resolution even during opening and Closing process of the filling valves 25 guaranteed.

Die oben beschriebene Vorrichtung arbeitet wie folgt: Die Verpackungsbehälter 10 werden von der Transportschnecke 21 der Abfülleinrichtung 22 taktweise zugefördert. Sobald je ein Verpackungsbehälter 10 unter seinem zugeordneten Abfüllkopf 23 positioniert ist, werden die Füllnadeln 24 der Abfüllköpfe 23 abgesenkt und in die Verpackungsbehälter 10 eingeführt. Gleichzeitig wird durch ein entsprechendes Ansteuersignal Z an die Dosierventile 25 durch die Steuereinrichtung 19 das Abfüllen der Sollfüllmenge M in die Verpackungsbehälter 10 eingeleitet, d.h. das Ansteuersignal Z bewirkt beispielsweise eine Bestromung einer Spule im Dosierventil 25, so daß dessen Nadel vom Ventilsitz abhebt.The device described above works as follows: The packaging container 10 are from the screw conveyor 21 fed to the filling device 22 in cycles. As soon as ever a packaging container 10 under its associated Filling head 23 is positioned, the filling needles 24 of the Filling heads 23 lowered and into the packaging container 10 introduced. At the same time, a corresponding Control signal Z to the metering valves 25 through the Control device 19 the filling of the target filling quantity M in the Packaging container 10 initiated, i.e. the control signal Z, for example, energizes a coil in the Metering valve 25 so that its needle lifts off the valve seat.

Die Berechnung der abgefüllten Füllmenge M (ist), und somit die Dauer des Ansteuersignales Z an die Dosierventile 25 erfolgt dadurch, daß von der Steuereinrichtung 19 fortlaufend Teilvolumina ΔM berechnet und während der Dauer des Ansteuersignales Z aufsummiert werden. Die Teilvolumina ΔM berechnen sich aus den Zeitabständen Δt zwischen den einzelnen Messungen der Flüssigkeitsdrücke P1, dem jeweils der Steuereinrichtung 19 zugeführten Wert des Flüssigkeitsdruckes von P1, sowie einem in der Steuereinrichtung 19 abgelegten Funktionszusammenhang k (p1) zwischen dem jeweiligen Wert von P1 und der daraus in den Dosierventilen 25 resultierenden Durchflußmenge pro Zeiteinheit.The calculation of the filled filling quantity M (ist), and thus the duration of the control signal Z to the metering valves 25 takes place in that the control device 19th continuous partial volumes ΔM calculated and during the duration of the control signal Z are added up. The partial volumes ΔM are calculated from the time intervals Δt between the individual measurements of the liquid pressures P1, the respective the value supplied to the control device 19 Fluid pressure of P1, as well as one in the Control device 19 stored functional relationship k (p1) between the respective value of P1 and the resulting value in the Dosing valves 25 resulting flow rate per Time unit.

Die Steuereinrichtung 19 berechnet die in einen Behälter 10 abgefüllte Füllmenge M (ist) somit gemäß folgender Formel: M (ist) = Σ ΔM = Σ (P1 * Δt * k) Überschreitet M (ist), d.h. die Summe der Teilvolumina ΔM einen bestimmten Grenzwert M (max), so wird das Ansteuersignal Z für die Dosierventile 25 durch die Steuereinrichtung 19 gestoppt, und die Dosierventile 25 schließen. Dieser Grenzwert M (max), der das Beenden des Ansteuersignales Z bewirkt, ist im einfachsten Fall die Sollfüllmenge M selbst. Der in der Steuereinrichtung 19 abgelegte Grenzwert M (max) kann entsprechend der Schließcharakteristik der Füllventile 25 jedoch auch kleiner gewählt werden, so daß beispielsweise auch noch die Füllmenge bzw. die Teilvolumina ΔM berücksichtigt werden, die während des Schließvorganges (nach Ausbleiben des Ansteuersignales Z) der Dosierventile 25 in die Behälter 10 gelangt. Das bedeutet, daß in diesem Fall der Grenzwert M (max) kleiner als die Sollfüllmenge M ist.The control device 19 thus calculates the filling quantity M (actual) filled into a container 10 according to the following formula: M (is) = Σ ΔM = Σ (P1 * Δt * k) If M (ist), ie the sum of the partial volumes .DELTA.M exceeds a certain limit value M (max), the control signal Z for the metering valves 25 is stopped by the control device 19 and the metering valves 25 close. This limit value M (max), which causes the control signal Z to end, is in the simplest case the desired filling quantity M itself. However, the limit value M (max) stored in the control device 19 can also be selected to be smaller in accordance with the closing characteristics of the filling valves 25, so that for example, the filling quantity or the partial volumes .DELTA.M are also taken into account that enter the containers 10 during the closing process (after the control signal Z has failed) of the metering valves 25. This means that in this case the limit value M (max) is smaller than the target filling quantity M.

Die Genauigkeit der Teilvoluminaberechnung ΔM der Steuereinrichtung 19 wird durch die Berücksichtigung der vom Temperatursensor 31 erfaßten Temperatur T der Flüssigkeit erhöht. Dies wird dadurch erreicht, daß in der Steuereinrichtung 19 die Durchfluß/Viskositätskennlinien für die jeweilige Flüssigkeit abgespeichert sind, so daß zur Berechnung der einzelnen Teilvolumina ΔM zusätzlich auf den entsprechenden temperaturkorrigierten Funktionszusammenhang k zugegriffen wird, d.h., daß der Wert des Faktors k auch von der Temperatur abhängig ist [k(P1, T)].The accuracy of the partial volume calculation ΔM Control device 19 is by taking into account the Temperature sensor 31 detected temperature T of the liquid elevated. This is achieved in that Control device 19 for the flow / viscosity characteristics the respective liquid are stored so that for Calculation of the individual partial volumes ΔM additionally on the corresponding temperature-corrected functional context k is accessed, i.e. the value of factor k is also depends on the temperature [k (P1, T)].

Nachdem die Sollfüllmenge M in die Verpackungsbehälter 10 eingebracht ist werden die Füllnadeln 24 durch die Abfüllköpfe 23 wieder aus den Verpackungsbehältern 10 herausgehoben. Anschließend werden die Verpackungsbehälter 10 durch die Förderschnecke 12 taktweise einer anderen Bearbeitungsstation, beispielsweise einer Verschließstation, zugefördert. Gleichzeitig wiederholt sich für neu in die Füllmaschine geförderte Verpackungsbehälter 10 der Vorgang wie oben beschrieben.After the target filling quantity M into the packaging container 10 the filling needles 24 are introduced through the Filling heads 23 again from the packaging containers 10 lifted out. Then the packaging container 10 by the conveyor screw 12 cyclically another Processing station, for example a sealing station, promoted. At the same time repeats itself for new in the Filling machine conveyed packaging container 10 the process as described above.

Um die exakte Dosierung der Flüssigkeitsmenge und damit der Sollfüllmenge M durch die Füllmaschine zu kontrollieren bzw. zu regeln, werden stichprobenartig über die Ausschleußeinrichtungen 16 einzelne Verpackungsbehälter 10 entnommen und den Wägeeinrichtungen 17, 18 zugeführt. Die tatsächlich dosierte Flüssigkeitsmenge M (ist) wird von der Steuereinrichtung 19 als Differenz des Brutto-Gewichts G2 und des Tara-Gewichts G1 errechnet. Dabei ist es mit Hilfe der sogenannten statistischen Prozeßkontrolle (SPC) möglich, beim Unter- oder Überschreiten von definierten Eingriffsgrenzen, beispielsweise der Flüssigkeitsmenge M (ist), aber auch des Tara-Gewichts G1 der Verpackungsbehälter 10, von der Steuereinrichtung 19 ein entsprechend korrigiertes Ansteuersignal Z für die Dosierventile 25 zu ermitteln.To the exact dosage of the amount of liquid and thus the Check the set filling quantity M by the filling machine or to regulate, are sampled on the Reject devices 16 individual packaging containers 10 removed and fed to the weighing devices 17, 18. The actually metered amount of liquid M (is) is from the Control device 19 as the difference in gross weight G2 and the tare weight G1 is calculated. It is with help the so-called statistical process control (SPC) possible, when falling below or exceeding defined Control limits, for example the amount of liquid M (is), but also of the tare weight G1 Packaging container 10, from the control device 19 correspondingly corrected control signal Z for the Determine metering valves 25.

Ergänzend wird erwähnt, daß es prinzipiell genügt, den Wert des Flüssigkeitsdruckes P1 nur während des eigentlichen Füllvorganges zu erfassen. In der Regel und für Kontrollzwecke bei etwaigen Funktionsstörungen der Füllmaschine wird der Flüssigkeitsdruck P1 jedoch ständig gemessen und der Steuereinrichtung 19 zugeführt.In addition, it is mentioned that, in principle, the value is sufficient of the liquid pressure P1 only during the actual one Filling process. Usually and for Control purposes in the event of any malfunction of the Filling machine, however, the fluid pressure P1 becomes constant measured and fed to the control device 19.

Darüber hinaus ist es auch denkbar, die Zeitabstände Δt so groß zu wählen, daß der Öffnungs- und Schließvorgang der Dosierventile 25 in bezug auf die Teilvolumina ΔM nicht mehr exakt berücksichtigt wird, und in diesem Fall für das Öffnen und Schließen der Dosierventile 25 feste Teilvolumina ΔM (fest) (entsprechend der Dosierventilcharakteristik) anzunehmen. Selbst in diesem Fall ist die Genauigkeit gegenüber bekannten Füllverfahren verbessert, da Druckschwankungen während des eigentlichen Abfüllens berücksichtigt werden.In addition, it is also conceivable for the time intervals Δt to be so large to choose that the opening and closing of the Dosing valves 25 with respect to the partial volumes ΔM no longer is taken into account exactly, and in this case for opening and closing the metering valves 25 fixed partial volumes ΔM (fixed) (according to the metering valve characteristics) to assume. Even in this case, the accuracy improved compared to known filling methods because Pressure fluctuations during the actual filling be taken into account.

Claims (8)

  1. Method of filling containers (10) with a liquid under pressure (P1), in which the liquid is fed from a supply tank (35) to the respective container (10) in each case by means of a filling valve (25), the pressure (P1) of the liquid being measured and directed to a control device (19), which, from the measured pressure (P1) of the liquid and the desired filling quantity (M) to be filled, activates the filling valve (25) by means of an activating signal (Z), characterized in that the pressure (P1) of the liquid is measured continuously at certain time intervals (Δt) during the filling operation by the filling valve (25), in that the control device (19) calculates the filling quantity (M (actual)) actually filled from a summation of partial volumes (ΔM), which is obtained while taking into account the respectively measured pressure (P1) of the liquid, the time intervals (Δt) between the individual pressure measurements and a pressure/flow characteristic (k) of the filling valve (25), and in that the control device (19) stops the activating signal (Z) to the metering valve (25) when a limit filling quantity (M (max)) is exceeded.
  2. Method according to Claim 1, characterized in that the time intervals (Δt) between the individual measurements of the pressure (P1) of the liquid are constant.
  3. Method according to Claim 2, characterized in that the time intervals (Δt) are between 150 µsec and 250 µsec, preferably 200 µsec.
  4. Method according to one of Claims 1 to 3, characterized in that the pressure (P1) of the liquid is measured during the entire operating period of a filling machine.
  5. Method according to one of Claims 1 to 4, characterized in that the activating signal (Z) for the actuation of the filling valve (25) is stopped at a limit filling quantity (M (max)) which is smaller than the desired filling quantity (M).
  6. Method according to one of Claims 1 to 4, characterized in that the activating signal (Z) for the actuation of the filling valve (25) is stopped at a limit filling quantity (M (max)) which corresponds to the desired filling quantity (M).
  7. Method according to one of Claims 1 to 6, characterized in that volumes (ΔM fixed) preset for the opening and closing operations of the filling valve (25) are assumed, so that no partial volumes (ΔM) are calculated during the opening and closing of the filling valve.
  8. Method according to one of Claims 1 to 7, characterized in that the partial volumes (ΔM) are calculated while taking into account a temperature (T) measured in the liquid by means of a temperature sensor (31).
EP96916004A 1995-06-16 1996-06-13 Method of filling containers with liquid under pressure Revoked EP0776314B1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP7150670A JP2633820B2 (en) 1995-06-16 1995-06-16 Liquid pressure filling method
JP150670/95 1995-06-16
JP15067095 1995-06-16
PCT/DE1996/001037 WO1997000224A1 (en) 1995-06-16 1996-06-13 Method of filling containers with liquid under pressure

Publications (2)

Publication Number Publication Date
EP0776314A1 EP0776314A1 (en) 1997-06-04
EP0776314B1 true EP0776314B1 (en) 2000-05-03

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Application Number Title Priority Date Filing Date
EP96916004A Revoked EP0776314B1 (en) 1995-06-16 1996-06-13 Method of filling containers with liquid under pressure

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US (1) US5823234A (en)
EP (1) EP0776314B1 (en)
JP (1) JP2633820B2 (en)
DE (1) DE59605120D1 (en)
ES (1) ES2147378T3 (en)
TR (1) TR199700101T1 (en)
WO (1) WO1997000224A1 (en)

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CN101817493B (en) * 2010-03-16 2013-09-18 广州达意隆包装机械股份有限公司 Reverse control valve, reverse dosing filling machine and filling method thereof
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Also Published As

Publication number Publication date
DE59605120D1 (en) 2000-06-08
WO1997000224A1 (en) 1997-01-03
TR199700101T1 (en) 1997-04-22
ES2147378T3 (en) 2000-09-01
JPH092583A (en) 1997-01-07
EP0776314A1 (en) 1997-06-04
US5823234A (en) 1998-10-20
JP2633820B2 (en) 1997-07-23

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