EP3013733B1 - Procédé et système de remplissage permettant de remplir des contenants - Google Patents

Procédé et système de remplissage permettant de remplir des contenants Download PDF

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Publication number
EP3013733B1
EP3013733B1 EP14733113.6A EP14733113A EP3013733B1 EP 3013733 B1 EP3013733 B1 EP 3013733B1 EP 14733113 A EP14733113 A EP 14733113A EP 3013733 B1 EP3013733 B1 EP 3013733B1
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EP
European Patent Office
Prior art keywords
filling
volumetric flow
phase
container
flow rate
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Application number
EP14733113.6A
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German (de)
English (en)
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EP3013733A1 (fr
Inventor
Hilmar FICKERT
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KHS GmbH
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KHS GmbH
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/22—Details
    • B67C3/28—Flow-control devices, e.g. using valves
    • B67C3/287—Flow-control devices, e.g. using valves related to flow control using predetermined or real-time calculated parameters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/06—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus using counterpressure, i.e. filling while the container is under pressure
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/22—Details
    • B67C3/225—Means for filling simultaneously, e.g. in a rotary filling apparatus or multiple rows of containers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/22—Details
    • B67C3/26—Filling-heads; Means for engaging filling-heads with bottle necks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/22—Details
    • B67C3/28—Flow-control devices, e.g. using valves
    • B67C3/286—Flow-control devices, e.g. using valves related to flow rate control, i.e. controlling slow and fast filling phases

Definitions

  • the invention relates to a method according to the preamble of claim 1 and to a filling system according to the preamble of claim 10.
  • a generic method and filling system are known from EP 0 406 092 A1 known.
  • the object of the invention is to provide a method by which at least two containers, but preferably more than two containers, for example, four containers with the required filling accuracy can be filled simultaneously with only a single Greinsky-effector with a liquid product, namely taking into account a target -Füllkurve.
  • a method according to claim 1 is formed.
  • a filling system is the subject of patent claim 10.
  • a special feature of the method according to the invention is that with only a single Greetrachinsky the simultaneous or temporally parallel filling of at least two containers, preferably more than two containers via filling heads, each of which is associated with each container. Since absolutely the same conditions can not be achieved in practice with regard to the product volume flow which flows to the individual containers or the filling heads during the filling phase, the invention provides that the control of a total product volume flow and thus of the product volume flows to the filling heads is generally general is performed by the single Golfgutstromregler, each of a container inflowing Golfgutvolumenstrom but monitored with a stand-alone flow meter and the measurement result of these flow meters, the control of Gregutvolumenstromreglers is corrected (correction control).
  • the general control of the Gregutvolumenstromreglers takes place according to a desired filling curve, which is either a standardized filling curve or a filling material and / or container-specific filling curve.
  • the inventive method results in a considerable structural and control engineering simplification of the filling system, by reducing the number of required functional elements.
  • only a single Greinsky-Natta and, for example, only a single product pump for the provision of the contents are required, despite the ability to fill at least two containers, but preferably more than two containers with the required filling accuracy at the same time.
  • the containers are preferably those with a container or filling volume in the range between three and ten liters.
  • the correction control takes place, for example, by shifting the time of the transition between individual partial phases. In any case, however, due to the measured values of the flow meter, a final termination of the filling or the filling phase for each container takes place when the required total filling quantity has reached it.
  • the method is designed, for example, such that a temporal displacement of the transition between at least two partial phases of the desired filling curve takes place by the control computer on the basis of the measured values fed to it by the flow meters, for example between the filling phase and the reduced product volume flow (Q1).
  • pressure filling is to be understood as meaning a filling process in which the container to be filled in each case rests in a sealing position against the filling element and, as a rule, before the actual filling phase, i. before opening the liquid valve, is biased by at least one controlled gas path formed in the filler element in a tempering phase with a pressurized gas (e.g. inert gas or CO2 gas, for example). This is then displaced during filling of the, the container inflowing contents increasingly as return gas from the container interior, and also via at least one controlled, formed in the filling element gas path in a return gas channel.
  • a pressurized gas e.g. inert gas or CO2 gas, for example
  • the preadjustment phase may be preceded by further treatment phases, for example evacuation and / or purging of the container interior with an inert gas, e.g. CO2 gas, etc., also via the gas paths formed in the filling element.
  • an inert gas e.g. CO2 gas, etc.
  • the term “essentially” or “approximately” or “approx.” means for the purposes of the invention deviations from the respective exact value by +/- 10%, preferably by +/- 5% and / or deviations in the form of insignificant for the function changes.
  • Fig. 1 generally designated 1 filling system is part of a filling machine and is used for simultaneous or parallel pressure filling of four containers 2 with a medium, for example with a CO2-containing filling material, eg beer.
  • the containers 2 are preferably cans, for example, party cans, having a volume of three to ten liters (eg, 3.1 liters, 5 liters or 10 liters).
  • the filling system forms four filling points 3.1 - 3.4, where the container 2 for filling each with their container opening lying above and oriented with its container axis in the vertical direction and are arranged with its container bottom upright on a container carrier 4.
  • the containers 2 are provided via seals 5.1 in a sealing position on a respective filling element or filling head 5.
  • Each filling head 5 comprises, inter alia, a controllable liquid valve 6 which can be controlled between an open state in which the filling material can flow into the relevant container 2 and a closed state in which the inflow of the filling material into the container 2 is interrupted by the liquid valve 6 is a Clamping gas valve 7 and a return gas valve 8. Furthermore, each filling head 5 has a long filling tube 9, which reaches far into the container interior during filling through the container opening and via which the filling of the respective container 2 with the liquid product takes place. The upper end of the filling tube 9 is connected to a liquid channel formed in the product 5, in which the liquid valve 6 is arranged and in the further the tensioning gas valve 7 opens on the output side.
  • the return gas valve 8 is connected on the input side to the headspace of the container interior not occupied by the contents, for example via an opening (not shown) provided laterally by the filling tube 9 within the seal 5.1.
  • the drive motor with a frequency converter in speed and / or torque can be regulated or controlled (FU-controlled pump).
  • the product pump 10 On the input side, the product pump 10 is connected to a source, not shown, the product (eg Sportsgutkessel) and the output side to a product line 11, which continues at one of a Zweifachderteiler formed first branch 12 in two product lines 13, which in turn to each a second continue branch formed by a dual manifold 14 in product lines 15, each of which leads to a filling head 5 and to the local liquid valve 6.
  • a source not shown
  • the product eg Golfkessel
  • the output side to a product line 11
  • the stepped effective flow cross section of the product lines 13 and 15 is realized, for example, in that the Inner cross-sections of these product lines forming pipes are graded accordingly, and / or but in that in the product lines 13 and 15 corresponding, the Gregutvolumenstrom throttling throttles are provided.
  • the branches 12 and 14 or these branches forming two-way distributor are preferably designed particularly streamlined as Y-shaped pipes, as shown in the Fig. 4 is shown very schematically.
  • a pressure sensor 16 is provided in the flow direction of the filling material on the Greinpumpe 10, which constantly monitors the pressure of the filling material within the product line 11 and the sensor signal via a control computer 17 u.a. the product pump 10 controls so that a constant or substantially constant Greguttik in the product line 11 at the output of Golfgutpumpe 10, regardless of fluctuations in Gugutvolumenstromes when filling the container 2.
  • a pneumatically controlled Golfgutvolumenstromregler 18 (DFC controller) is provided in front of the branch 12, during the filling of the container 2, ie during the filling phase the Geargut mechanicallass or the total Golfgutvolumenstrom and thus the Gregutvolumenströme to the filling heads 5 in Dependence on a stored in a memory of the control computer 17, for example, product and / or container-specific program, that is, depending on an example, product and / or container-specific time-dependent desired filling curve FK controls.
  • the Artgutvolumenstromregler 18 is for example designed so that a local Artgutkanal or passage limiting membrane, which is acted upon by a pneumatic control pressure, in response to this control pressure changes an opening cross section for the flow of the filling.
  • the Artgutvolumenstromregler 18 is controlled by the control computer 17 via an I / P converter 19 which converts the electrical control signal of the control computer 17 in the, the Ballgutvolumenstromregler 18 controlling control pressure.
  • an independent flow meter 20 which supplies an electrical measurement signal as a function of the product volume flow and, for example, as a magneto-inductive flow meter, i. is designed as an IDM.
  • the measurement signals of the flow meters 20 are also supplied to the control computer 17 for control and correction (correction control) of the filling process in the manner described in more detail below.
  • the clamping gas valves 7 of all filling heads 5 are connected on the input side to a common span gas line 21 which contains the span gas, which is for example an inert gas, e.g. CO2 gas or nitrogen, or sterile air, is supplied under clamping gas pressure, via a tension gas pressure regulating this arrangement 22 of a source, not shown, the clamping gas under clamping gas pressure available source.
  • the span gas which is for example an inert gas, e.g. CO2 gas or nitrogen, or sterile air
  • the filling heads 5 can also be acted upon with a purge gas in the manner described above. Both purge gas from the clamping gas, and the pressure of the purge gas can differ from the pressure of the clamping gas.
  • the return gas valves 8 are connected on the output side to a common return gas line 23 in which a pressure sensor 24 is provided which continuously measures the return gas pressure in the return gas line during the filling process and whose output signal is fed to the control computer 17.
  • a pressure sensor 24 which continuously measures the return gas pressure in the return gas line during the filling process and whose output signal is fed to the control computer 17.
  • a pneumatic, ie by a pneumatic control pressure controlled return gas regulator 25 is provided, which is controlled by the control computer 17 in response to the measurement signals of the pressure sensor 24 via an I / P converter 26 such that during the filling operation of the return gas pressure in the return gas line 23 is constant.
  • the return gas After passing the return gas regulator 25, the return gas is fed to a sink, not shown, for collecting the return gas, via an open valve 31 a gas or vapor separator 29, for example formed as a cyclone. Any moisture components separated from the return gas can be removed via a discharge line 29.
  • the contents and the return gas leading areas of the filling system 1 is provided that the flow of a CIP cleaning and / or disinfection medium on the product pump 10 and the product lines 11, 13 and 15 led to the filling heads 5 and is passed for the return of this medium via the return gas line 23 to a not shown tank or collection system via valve 27.
  • the return gas regulator 25 is connected on the output side with a switching valve 31 to the gas separator 28.
  • the switching valves 30 and 27 are opened and the switching valve 31 is closed.
  • the filling of the container 2 is, for example, such that initially in a bias phase with closed liquid valves 6 and closed return gas valves 8, the interior of the arranged in sealing position on the filling head 5 container 2 acted upon by biasing the clamping gas valves 27 at the same time with the pressurized clamping gas or biased be, which is also introduced via the filling tube 9 in the respective container 2.
  • this initial phase is preceded by a phase in which the interior of the container 2, which is already arranged in sealing position on the respective product head 5, is rinsed with an inert gas at the same time.
  • the liquid valve 6 is closed, for example, the clamping gas valves 7 and the return gas valves 8 are opened, so that with the in the respective container interior via the filling tube. 9 introduced span gas in the container interior existing air on the return gas valves 8 and the return gas line 23 is displaced.
  • the pressure filling of the container 2 takes place with closed clamping gas valves 7 by opening the return gas valves 8 and the liquid valves 7.
  • the filling phase i. the feeding of the contents to the respective container 2 is completed by closing the liquid valve 6 in any case, when the respective container 2 measured by the flow meter 20, the required quantity of contents was supplied.
  • filling the displaced from the inflowing medium from the interior of the container inert gas is discharged as a return gas via the return gas line 23.
  • the return gas pressure in this line By keeping constant the return gas pressure in this line by means of the pressure sensor 24 and the return gas regulator 25, the same conditions are achieved during filling for all containers 2 with respect to the internal pressure of the container.
  • a relieving of the container 2 for example via a not shown relief valve and / or a discharge line.
  • the filling of the container 2 in the filling phase in dependence on the stored in the memory of the control computer 17, preferably product and / or container specific time-dependent desired filling curve FK, after the Gregutvolumenstromregler 18 is primarily controlled.
  • the Fig. 3 shows a typical example of this target filling material curve FK or the curve corresponding to this curve of the Gregutvolumenstroms Q, which is generated at the output of Medgutvolumenstromreglers 18 when no correction control, and ideally corresponds to the Gregutvolumenstrom that each container 2 during the Filling phase flows.
  • the desired filling material curve FK at the beginning of the filling phase, ie with the opening of the liquid valve 6 and the return gas valve 8 at the time t1 in a filling phase, a product volume flow initially increases and then remains at a constant value Q1 until the end of the filling phase.
  • the filling phase is completed at time t2, ie at a time at which theoretically each container 2 is partially filled with a volume V2.
  • a fast filling phase starting at time t2, an increase in the volume of product charge initially occurs a value Q2, which is then kept constant until the end of the rapid filling phase at time t3, wherein each container 2 is then ideally partially filled with a volume V3.
  • the product volume flow Q1 is for example 0.2 l / sec., So that at the end of the filling phase, i.
  • each container 2 about 0.15 - 0.5 liters of product was supplied.
  • the value Q2 in these containers is about 1.2 l / sec, so that at the end of the fast fill phase, i.
  • each container about 4.5 - 4.75 liters of product was supplied.
  • the correction is made at the end of the rapid fill phase such that when the first container 2, i. the Guided Pasteur V3 is supplied to the fastest filled container 2, the final filling phase for all containers 2 is initiated by controlling the Greinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinskyinsky, etc.
  • the correction control is performed such that at the first sync point, i. At the time t2, the liquid valves of those filling heads 5 are closed for a short time, the container 2 was supplied before the last container 2, the Gregutmenge V2, and then reopened when in the last container, the Gregutmenge V2 was introduced, so that at the same time for all containers the fast filling phase is initiated.
  • the correction control at the second sync point i. take place at time t3.
  • the filling system 1 described forms, for example, without the container carrier 4, a complete assembly 32 (FIG. FIG. 5 ), which is prefabricated as such mounted on the machine frame of a filling machine.

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  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Basic Packing Technique (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Claims (12)

  1. Procédé servant à remplir des contenants (2) d'un produit de remplissage liquide, avec un système de remplissage, à l'aide duquel le produit de remplissage est amené aux contenants (2) par l'intermédiaire d'un régulateur de débit volumique de produit de remplissage (18), qui commande ou régule le débit volumique de produit de remplissage en fonction d'une courbe de remplissage théorique (FK), qui est enregistrée dans un calculateur de commande (17) pilotant le régulateur de débit volumique de produit de remplissage (18), et ce avec une évolution du débit volumique de produit de remplissage variant lors de plusieurs phases partielles se suivant les unes les autres dans le temps, laquelle évolution présente au moins un débit volumique de produit de remplissage (Q1, Q3) réduit au début et à la fin d'une phase de remplissage et un débit volumique de produit de remplissage (Q2) élevé lors d'une phase de remplissage rapide intercalée,
    dans le cadre duquel le système de remplissage (1) forme pour chaque contenant une position de remplissage (3.1 - 3.4) afin de remplir de manière simultanée un groupe de contenants composé au moins de deux contenants (2),
    le produit de remplissage est amené par l'intermédiaire du régulateur de débit volumique de produit de remplissage (18) commun à toutes les positions de remplissage (3.1 - 3.4) aux positions de remplissage (3.1 - 3.4) au cours de la phase de remplissage, et chaque débit volumique amené à chaque contenant est détecté en permanence en tant que valeur réelle à l'aide d'un dispositif de mesure de flux de produit (20) propre, ce qui permet d'effectuer une correction du pilotage du régulateur de débit volumique du produit de remplissage (18) dans l'ordinateur de commande (17),
    caractérisé en ce
    que chaque débit volumique amené à chaque contenant est détecté en permanence en tant que valeur réelle à l'aide d'un dispositif de mesure de flux de produit (20) propre réalisé sous la forme d'un débitmètre,
    et en ce qu'une commutation de la phase de remplissage sur la phase de remplissage rapide est effectuée dans le temps par le calculateur de commande (17) du fait des valeurs de mesure fournies par les débitmètres (20) seulement quand la quantité de produit de remplissage minimale (V2) requise au début de la phase de remplissage rapide est introduite également dans le contenant (2), dont le remplissage précisément est le plus lent.
  2. Procédé selon la revendication 1, caractérisé en ce qu'un report dans le temps du passage entre au moins deux phases partielles de la courbe de remplissage théorique est effectué par l'ordinateur de commande (17) sur la base des valeurs de mesure qui lui sont amenées par les débitmètres (20), par exemple entre la phase de remplissage présentant le débit volumique de produit de remplissage (Q1) réduit et la phase de remplissage rapide présentant le débit volumique de produit de remplissage (Q2) élevé et/ou entre la phase de remplissage rapide et la phase de remplissage final.
  3. Procédé selon la revendication 1 ou 2, caractérisé en ce qu'un report dans le temps de l'achèvement de la phase de remplissage est effectué par l'ordinateur de commande (17) sur la base des valeurs de mesure qui lui sont amenées par les débitmètres (20).
  4. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que l'ordinateur de commande surveille en parallèle les diverses courbes de remplissage réelles et commande, en partant des résultats de la comparaison avec la courbe de remplissage théorique, le processus de remplissage ou le régulateur de débit volumique de produit de remplissage (18).
  5. Procédé selon la revendication 4, caractérisé en ce que la correction du pilotage du régulateur de débit volumique de produit de remplissage (18) est effectuée par le fait que des courbes de remplissage réelles détectées à l'aide des débitmètres (20) et correspondant au débit volumique de produit de remplissage réel amené aux contenants (2) sont comparées à la courbe de remplissage théorique (FK) enregistrée dans l'ordinateur de commande (17), et en ce que dans le cas d'un écart, la correction du pilotage du régulateur de débit volumique de produit de remplissage (18) est effectuée, par exemple par le report dans le temps du passage entre au moins deux phases partielles de la courbe de remplissage théorique.
  6. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que la commutation de la phase de remplissage rapide sur une phase située immédiatement après présentant un débit volumique de produit de remplissage (Q3) réduit ou se réduisant, par exemple sur une phase de remplissage final est effectuée dès lors que le contenant, vers lequel précisément le produit de remplissage s'écoule à la vitesse de remplissage la plus grande, est rempli de la quantité de produit de remplissage (V3) requise à la fin de la phase de remplissage rapide.
  7. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que lors d'un remplissage à une pression contraire des contenants (2) précontraints par un gaz de tension, le gaz de retour refoulé par le produit de remplissage liquide hors des contenants (2) est évacué par l'intermédiaire d'une conduite de gaz de retour (23) commune à tous les points de remplissage, dans laquelle un régulateur de gaz de retour (25) est prévu afin de maintenir une pression de gaz de retour constante.
  8. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que lors du remplissage sous pression d'un produit de remplissage contenant du CO2, la pression de gaz de tension et/ou la pression de gaz de retour est légèrement supérieure à la pression d'équilibre de CO2 du produit de remplissage, par exemple est de 1,5 bar.
  9. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce qu'une courbe de remplissage théorique spécifique au produit et/ou au contenant est utilisée afin de piloter le régulateur de débit volumique de produit de remplissage (18).
  10. Système de remplissage servant à remplir des contenants (2) d'un produit de remplissage liquide, avec un système de remplissage, à l'aide duquel le produit de remplissage est amené aux contenants (2) par l'intermédiaire d'un régulateur de débit volumique de produit de remplissage (18), qui commande ou régule le débit volumique de produit de remplissage en fonction d'une courbe de remplissage théorique (FK), qui est enregistrée dans un ordinateur de commande (17) pilotant le régulateur de débit volumique de produit de remplissage (18), à savoir avec une évolution du débit volumique de produit de remplissage variant lors de plusieurs phases partielles se suivant dans le temps, laquelle présente au moins un débit volumique de produit de remplissage (Q1, Q3) réduit au début et à la fin d'une phase de remplissage et un débit volumique de produit de remplissage (Q2) élevé dans une phase de remplissage rapide intercalée, dans lequel au moins deux positions de remplissage (3.1 - 3.4) avec une tête de remplissage (5) avec une soupape de liquide (6) propre, une soupape de gaz de tension (7) et une soupape de gaz de retour (8) sont prévues afin de remplir de manière simultanée un groupe de contenants composé au moins de deux contenants (2), et les têtes de remplissage (5) sont raccordées au régulateur de débit volumique de produit de remplissage (18) par l'intermédiaire de conduites de produit (15) ramifiées, et un dispositif de mesure de débit (20) autonome dans la conduite de produit (15) menant au niveau de ladite tête de remplissage (5) est associé à chaque tête de remplissage (5),
    caractérisé en ce
    que chaque dispositif de mesure de flux de produit (20) est réalisé sous la forme d'un débitmètre, qui est mis au point de telle manière qu'une commutation de la phase de remplissage sur la phase de remplissage rapide est effectuée dans le temps par l'ordinateur de commande (17) du fait des valeurs de mesure fournies par les débitmètres (20) seulement quand la quantité de produit de remplissage minimale (V2) requise au début de la phase de remplissage rapide est introduite également dans le contenant (2) dont le remplissage précisément est le plus lent.
  11. Système de remplissage selon la revendication 10, caractérisé en ce que les têtes de remplissage (5) sont réalisées avec un tuyau de remplissage (9).
  12. Système de remplissage selon la revendication 10 ou 11, caractérisé en ce que les têtes de remplissage (5) sont raccordées par leurs soupapes de gaz de tension (7) à une conduite de gaz de tension (21) commune et par leurs soupapes de gaz de retour (8) à une conduite de gaz de retour (23) commune, et en ce qu'un régulateur de gaz de retour (25) ainsi qu'au moins un capteur de pression (24) sont prévus dans la conduite de gaz de retour, dont le signal de capteur commande le régulateur de gaz de retour (25) afin de maintenir une pression de gaz de retour constante dans la conduite de gaz de retour (23).
EP14733113.6A 2013-06-27 2014-06-13 Procédé et système de remplissage permettant de remplir des contenants Active EP3013733B1 (fr)

Applications Claiming Priority (2)

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DE102013106756.5A DE102013106756A1 (de) 2013-06-27 2013-06-27 Verfahren sowie Füllsystem zum Füllen von Behältern
PCT/EP2014/062427 WO2014206774A1 (fr) 2013-06-27 2014-06-13 Procédé et système de remplissage permettant de remplir des contenants

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EP3013733B1 true EP3013733B1 (fr) 2017-03-29

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US (1) US10131527B2 (fr)
EP (1) EP3013733B1 (fr)
CN (1) CN105307972B (fr)
DE (1) DE102013106756A1 (fr)
PL (1) PL3013733T3 (fr)
WO (1) WO2014206774A1 (fr)

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CN107532074A (zh) 2015-05-14 2018-01-02 旭硝子株式会社 流体组合物、制冷剂组合物和空调机
DE102015111536A1 (de) * 2015-07-16 2017-01-19 Khs Gmbh Verfahren sowie Füllsystem zum Befüllen von Behältern
CN109808924A (zh) * 2017-11-22 2019-05-28 Khs有限责任公司 用于向容器内灌装液体的方法和相应的灌装设备
DE102018122062B4 (de) * 2018-09-11 2021-07-08 Khs Gmbh Vorrichtung und Verfahren zum Befüllen von Behältern mit einem flüssigen Füllgut
DE102019118096A1 (de) * 2019-07-04 2021-01-07 Krones Ag Füllmaschine zum Abfüllen eines flüssigen Produkts in Behälter und Verfahren zur Kontrolle von Füllvorgängen und/oder CIP-Prozessen an einer Füllmaschine
DE102019125329A1 (de) * 2019-09-20 2021-03-25 Krones Ag Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllprodukt
CN111908400B (zh) * 2020-08-24 2022-04-08 贵州张巅子食品生产有限公司 一种油辣椒的灌装方法
WO2022108867A1 (fr) * 2020-11-18 2022-05-27 Wild Goose Canning Technologies, LLC Station de remplissage de contenant
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DE102021134033B3 (de) * 2021-12-21 2023-05-17 Krohne Messtechnik Gmbh Verfahren zum Betreiben einer Abfüllanlage und Abfüllanlage

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Also Published As

Publication number Publication date
WO2014206774A1 (fr) 2014-12-31
CN105307972B (zh) 2017-08-04
EP3013733A1 (fr) 2016-05-04
US20160368751A1 (en) 2016-12-22
CN105307972A (zh) 2016-02-03
DE102013106756A1 (de) 2014-12-31
US10131527B2 (en) 2018-11-20
PL3013733T3 (pl) 2017-09-29

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