EP2969893B1 - Procédé de lavage de contenants - Google Patents

Procédé de lavage de contenants Download PDF

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Publication number
EP2969893B1
EP2969893B1 EP14704750.0A EP14704750A EP2969893B1 EP 2969893 B1 EP2969893 B1 EP 2969893B1 EP 14704750 A EP14704750 A EP 14704750A EP 2969893 B1 EP2969893 B1 EP 2969893B1
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EP
European Patent Office
Prior art keywords
pressure
purge gas
container
gas
filling
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Active
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EP14704750.0A
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German (de)
English (en)
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EP2969893A1 (fr
Inventor
Ludwig Clüsserath
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KHS GmbH
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KHS GmbH
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Priority to SI201430688T priority Critical patent/SI2969893T1/en
Publication of EP2969893A1 publication Critical patent/EP2969893A1/fr
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/002—Automated filling apparatus
    • F17C5/007—Automated filling apparatus for individual gas tanks or containers, e.g. in vehicles
    • 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
    • B67C3/10—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 preliminary filling with inert gases, e.g. carbon dioxide
    • 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
    • B67C3/12—Pressure-control devices
    • 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
    • B67C3/2614—Filling-heads; Means for engaging filling-heads with bottle necks specially adapted for counter-pressure filling
    • B67C3/2617—Filling-heads; Means for engaging filling-heads with bottle necks specially adapted for counter-pressure filling the liquid valve being opened by mechanical or electrical actuation

Definitions

  • the invention relates to a method according to the preamble of claim 1 for rinsing containers with a purge gas.
  • Methods for filling, even pressure filling of containers are known in different designs. It is also known in this case to evacuate the respective container or its interior before filling and then to rinse with a purge gas formed by an inert gas (eg CO2 gas or serine air) to existing ambient air or another gas and / or vapor Remove medium from the container interior.
  • an inert gas eg CO2 gas or serine air
  • a generic method has been exemplified by the DE 199 39 521 A1
  • the proposed method is to evacuate PET bottles in a very short time, whereby the resulting negative pressure in the bottle should be above a pressure at which the PET bottles would implode.
  • a disadvantage of this method is that it comes due to the high pressure in the PET bottle to a high consumption of purge gas.
  • the object of the invention is to provide a method which allows a particularly effective rinsing of the respective container interior with low consumption of purge gas. To solve this problem, a method according to claim 1 is formed.
  • a special feature of the invention is that when purging in a first process step, the container interior is evacuated by connecting to a vacuum source and then takes place in a second process step, the actual rinsing of the container by blowing the purge gas, wherein the container interior is further connected to the vacuum source, so that the blowing of the purge gas takes place in a vacuum or high vacuum in the container interior.
  • the evacuation of the container in the first step of rinsing is carried out so that in the container, a pressure of about 0.05 - 0.4 bar, preferably a pressure of about 0.05 to 0.25 bar sets, ie, a negative pressure of about 0th , 6 bar - 0.95 bar, preferably 0.75 to 0.95 bar relative to the ambient pressure.
  • the introduction or injection the flushing gas is then carried out with such a pressure and / or with such a flow that at most a pressure increase in the container interior at most 0.1 bar to 0.2 bar results.
  • the advantage of the method according to the invention consists inter alia in an effective rinsing of the bottle interior and in a significant reduction in the consumption of purge gas.
  • the above-described method is compared with rinsing processes that are carried out under atmospheric or ambient pressure or at a pressure above atmospheric or ambient pressure, with up to 10 times lower purge gas or Spülgasmenge.
  • the lower consumption of purge gas or inert gas further represents a significant cost savings.
  • an oxygen uptake during the subsequent filling can be considerably reduced.
  • containers are those made of glass, including glass bottles or similarly stable containers made of metal or plastic, such as kegs, party kegs, reusable plastic bottles, etc. It is essential that the containers used in the method according to the invention have sufficient stability so that they are not deformed or even destroyed to an undesirable degree during evacuation.
  • container In sealing position with the treatment head or filling element befindaji container means in the context of the invention that the respective container in the manner known to those skilled with its container mouth tightly pressed against the treatment head or to the filling element or to a local seal.
  • the expression “essentially” or “approximately” in the sense of the invention means deviations from the exact value by +/- 10%, preferably by +/- 5% and / or deviations in the form of changes that are insignificant for the function.
  • the generally designated 1 in the figures filling element is provided together with a plurality of similar filling elements on the circumference of a vertical machine axis MA rotatably driven rotor 2 and forms together with a container carrier 3 a filling for filling, for example pressure filling of containers 4 in the form of bottles 4. These are made of glass, metal or plastic with sufficient strength.
  • a common Gregutkessel 5 is provided in the form of a ring boiler for all filling elements 1 of the filling system or filling machine, which is partially filled during the filling operation with the liquid product, to form a lower liquid space 5.1 and an upper gas space 5.2, which is filled with an inert gas (eg CO2 gas or nitrogen) under filling pressure.
  • an inert gas eg CO2 gas or nitrogen
  • the liquid space 5.1 is connected to a formed in the housing 6 of the filling element 1 liquid channel 7, which forms a vertical Gearelementachse FA concentrically enclosing annular discharge opening 8 on the underside of the filling element.
  • a liquid valve 9 is further provided, which is formed on a valve stem 10 formed valve body 11 is axially movable by an actuator, for opening and closing of the liquid valve 9.
  • the valve stem 10 is formed by a piece of pipe which is coaxially with the Artelementachse FA disposed at its upper and at its lower, over the discharge opening 8 downwardly projecting end is open and forms a first gas channel 12 which opens at the upper end of the valve stem 10 in a housing 6 formed in the first gas chamber 13.
  • a return gas pipe 14 is further arranged, which serves as the filling level in the bottle 4 determining element and a second open at the bottom and at the upper end of the return gas pipe 14 when filling.
  • the gas channel 15 opens at the upper end of the return gas pipe 14 in a second formed in the housing 6 gas space 16.
  • the gas chambers 13 and 16 are part of different, the control valves 17.1 - 17.4 of the filling element 1 contained gas paths through which the gas channels 12 and 15 controlled by the Gas chamber 5.2 and can be connected to two annular channels 18 and 19, which are provided for all filling elements 1 of the filling machine or the filling system together.
  • the annular channel 18 serves, for example, to relieve the filled bottles 2 at the end of the respective filling process.
  • the annular channel 19 is acted upon during the filling operation with a vacuum or negative pressure, for example at a pressure of 0.05 bar - 0.25 bar or deviating therefrom.
  • the gas chamber 5.2 is charged during filling with the inert gas under pressure.
  • a Zentriertulpe shown sealed by means of a seal against the underside of the housing 6 and abuts against the respective bottle 4 with the Pressed edge of its bottle opening in sealing position, so that the discharge opening 8 and the lower opening of the first gas channel 12 open into the upper region of the bottle interior.
  • the return gas pipe 14 projects beyond the lower end of the valve tappet 10 into the interior of the bottle 4.
  • the peculiarity of the filling element or of the method carried out with this filling element consists in the special type and embodiment of purging the interior of the respective bottle 4 arranged in sealing position on the filling element 1 for displacing ambient air entrained in the bottle from the interior of the bottle.
  • the subsequent process steps of the filling process such as biasing the interior of the bottle with inert gas from the gas chamber 5.2 to the filling pressure, the pressure filling of the bottle 2 and the unloading of the filled bottle 2 to atmospheric pressure, for example in the annular channel 18 in accordance with e.g. usual, known methods.
  • the aim is an effective flushing of the bottle interior with low consumption of purge gas or inert gas.
  • the purge includes at least two steps.
  • a first method step is evacuated with closed liquid valve 9 and closed control valves 17.1, 17.2 and 17.4 via the open control valve 17.3, the gas space 13 and the gas channel 12, the interior of the bottle 2, for example, to a 95% vacuum or on a pressure in the range of 0.05 - 0.25 bar.
  • control valve 17.1 is then opened while the control valve 17.3 is still open, so that inert gas from the gas chamber 5.2 via the open control valve 17.1 and via a throttle 21 (fine throttle) in the gas chamber 16 and from this via the gas channel 15 centrally, ie in the direction of the filler element axis FA down as flushing gas into the interior of the bottle 4 and in the local high vacuum is blown. Since the return gas pipe 14 extends far into the interior of the bottle 4 down, the purge gas exiting the return gas pipe 14 also reaches the bottom of the bottle 4, for example and the displaced by this from the interior of the bottle 4 air discharged into the annular channel 19.
  • the purge gas flow or the flow rate of the purge gas are throttled so far that the negative pressure, the set at the end of the first process step when flushing in the bottle 4, only slightly increases, by about 0.1 bar - 0.2 bar. So that in the second process step, an internal pressure or scavenging pressure results in the bottle, which is still significantly below the ambient pressure, and for example about 0.15 bar - 0.45 bar.
  • the supply of purge gas in the second step can be timed and without interruptions. Alternatively, the supply of purge gas but also at intervals, so take place in several sub-steps.
  • a filling element 1a which differs from the filling element 1 only in that the control valve 17.1 on the input side is not connected to the gas chamber 5.2, but with a source 22, which provides the purge gas at least with a certain overpressure.
  • the pressure of the purge gas can be selected independently of the filling pressure, in such a way that the desired low purge pressure is easily achieved.
  • the regulation or control of the scavenging pressure then takes place, for example, by a control valve which is arranged in the corresponding gas path for the purge gas and which has at least two operating states, namely an operating state of low throttling and an operating state of higher throttling, but preferably also a third blocking state ,
  • a control valve 24 is in the Fig. 5 shown very schematically.
  • the control valve 24 has a valve body 25 with a throttle-like narrowing flow channel 26 and an axially movable valve element 27, which releases the flow channel 26 depending on its position or additionally narrows or completely closes.
  • the rinsing of the bottles 2 or other containers takes place in a rinsing phase of a filling process with the filling elements 1 or 1a.
  • the rinsing of the containers can also be effected via other treatment heads which are not filling elements, for example in a machine or component of a system preceding a filling machine.
  • the rinsing process in a 0.5 l bottle should preferably be carried out for about 150 to 300 ms, correspondingly longer for larger container volumes.
  • only insignificant gas exchange processes were observed, or longer rinsing appear economically not useful.
  • the optimum purging duration, at which flushing gas is injected is interrupted one or more times by pause phases (no flushing of flushing gas) and the total duration of such pause times totals approximately 0.5 to 1.2 times the ( active) rinsing time is.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Claims (13)

  1. Procédé de lavage de contenants (2) en verre, métal ou plastique par exemple des bouteilles en verre, des fûts, des tonnelets, des bouteilles en plastique réutilisables avec un gaz de lavage avant leur remplissage en utilisant une tête de traitement (1, 1a), au niveau de laquelle le contenant concerné (2) est agencé en position d'étanchéité lors du lavage et par le biais de laquelle le gaz de lavage est introduit dans le contenant et le gaz de lavage ainsi qu'un milieu sous forme de gaz et/ou de vapeur refoulé par celui-ci, par exemple de l'air est évacué du contenant, et dans lequel le contenant est évacué avant l'introduction du gaz de lavage respectivement est soumis au vide d'une source de vide (19),
    dans lequel pendant l'introduction du gaz de lavage dans le contenant (2), celui-ci continue d'être relié à la source de vide (19), et que la pression et/ou le débit volumique du gaz de lavage introduit dans le contenant (4) ainsi que la dépression de la source de vide (19) sont réglés de telle sorte que
    - dans une première étape de procédé, le contenant est réglé sur une pression dans la plage entre 0,05 bar à 0,4 bar, de préférence une pression d'environ 0,05 à 0,25 bar,
    caractérisé en ce que
    - dans une deuxième étape de procédé successive dans le temps, l'introduction ou l'insufflation du gaz de lavage dans le contenant a lieu et ce de telle sorte que la pression dans le contenant n'augmente pas ou seulement de 0,1 bar à 0,2 bar par l'introduction ou l'insufflation du gaz de lavage.
  2. Procédé selon la revendication 1, caractérisé en ce que la pression et/ou le débit volumique du gaz de lavage ainsi que la pression de la source de vide (19) sont réglés de sorte à obtenir dans la deuxième étape de procédé, une pression interne ou pression de lavage dans le contenant entre 0,15 bar et 0,45 bar.
  3. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que la liaison du contenant (2) à la source de vide (19) a lieu par le biais d'un premier canal de gaz (14) réalisé dans la tête de traitement (1, 1a) et l'introduction du gaz de lavage a lieu par le biais d'un deuxième canal de gaz (15) réalisé dans la tête de traitement (1, 1a).
  4. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que l'introduction du gaz de lavage dans le contenant (4) a lieu de manière centrée.
  5. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que l'introduction du gaz de lavage dans le contenant (4) a lieu par le biais d'un tube de gaz ou de gaz de retour (14) pénétrant dans l'espace intérieur de contenant.
  6. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que du gaz CO2 ou de l'azote est utilisé en tant que gaz de lavage, de préférence à partir d'un espace de gaz présentant le gaz de lavage sous pression et étranglé par un étrangleur (21).
  7. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que la pression de lavage dans le contenant est surveillée et/ou commandée à l'aide d'un capteur de pression (23).
  8. Procédé selon la revendication 7, caractérisé en ce que dans le cas d'un système de traitement avec plusieurs têtes de traitement (1, 1a), la pression de lavage est surveillée et/ou commandée pour chaque tête de traitement (1, 1a) avec un capteur de pression autonome (23).
  9. Procédé selon la revendication 8, caractérisé en ce que dans le cas d'un système de traitement avec plusieurs têtes de traitement (1, 1a), la pression de lavage est surveillée et/ou commandée pour toutes les têtes de traitement (1, 1a) avec un seul capteur de pression (23) prévu au niveau d'une tête de traitement (1, 1a).
  10. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que la tête de traitement est un élément de remplissage (1, 1a) d'un système de remplissage pour le remplissage des contenants (2) avec un produit de remplissage liquide.
  11. Procédé selon la revendication 10, caractérisé en ce que dans le cas d'un système de remplissage pour le remplissage sous pression des contenants (2) à partir d'un réservoir de produit de remplissage (5) sous une pression de remplissage, le gaz de lavage est mis à disposition par une source (22) indépendante du réservoir de produit de remplissage (5).
  12. Procédé selon l'une quelconque des revendications 1 à 11, caractérisé en ce que dans la phase ou l'étape de procédé, dans laquelle du gaz de lavage est insufflé, des phases de pause sont prévues en plus par une ou plusieurs interruptions du gaz de lavage.
  13. Procédé selon la revendication 12, caractérisé en ce que la durée totale de tels temps de pause est au total 0,5 à 1,2 fois la durée de lavage ; pour laquelle du gaz de lavage est insufflé.
EP14704750.0A 2013-03-14 2014-02-13 Procédé de lavage de contenants Active EP2969893B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SI201430688T SI2969893T1 (en) 2013-03-14 2014-02-13 Procedure for washing the containers

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102013102611.7A DE102013102611A1 (de) 2013-03-14 2013-03-14 Verfahren zum Spülen von Behältern
PCT/EP2014/000394 WO2014139624A1 (fr) 2013-03-14 2014-02-13 Procédé de lavage de contenants

Publications (2)

Publication Number Publication Date
EP2969893A1 EP2969893A1 (fr) 2016-01-20
EP2969893B1 true EP2969893B1 (fr) 2018-04-04

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Application Number Title Priority Date Filing Date
EP14704750.0A Active EP2969893B1 (fr) 2013-03-14 2014-02-13 Procédé de lavage de contenants

Country Status (5)

Country Link
US (1) US10088107B2 (fr)
EP (1) EP2969893B1 (fr)
DE (1) DE102013102611A1 (fr)
SI (1) SI2969893T1 (fr)
WO (1) WO2014139624A1 (fr)

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DE102011111483A1 (de) * 2011-08-30 2013-02-28 Khs Gmbh Behälterbehandlungsmaschine
ITTO20130302A1 (it) * 2013-04-15 2014-10-16 Gai Macchine Imbottigliatrici S P A Dispositivo di riempimento per macchine riempitrici per il riempimento a livello di bottiglie con liquidi alimentari e macchina riempitrice comprendente un tale dispositivo
PT2903929T (pt) * 2012-10-05 2017-05-03 Gai Macch Imbottigliatrici S P A Dispositivo de enchimento para máquinas de enchimento isobárico para enchimento de garrafas com líquidos alimentares
DE102013102616A1 (de) * 2013-03-14 2014-09-18 Khs Gmbh Verfahren sowie Füllsystem zum Füllen von Behältern
DE102013108638A1 (de) 2013-08-09 2015-03-05 Khs Gmbh Verfahren sowie System zum Spülen von Behältern
ITUA20164306A1 (it) * 2016-06-13 2017-12-13 Dr Tech S R L Dispositivo e metodo per il riempimento di contenitori con un liquido, in particolare per l’imbottigliamento
DE102017120745A1 (de) * 2017-09-08 2019-03-14 Krones Ag Verfahren zum Befüllen eines Behälters mit einem Füllprodukt sowie Füllorgan zum Befüllen eines Behälters mit einem Füllprodukt
CN109467038B (zh) * 2018-09-28 2020-11-17 温州澳鼎建材有限公司 利用静电整流防止气流吹散输出流体的藤茶饮料灌注机
DE102018127592B4 (de) * 2018-11-06 2020-07-16 Khs Gmbh Füllelement, Füllsystem und Verfahren zum Füllen von Behältern
US11203520B2 (en) * 2018-11-29 2021-12-21 Green Co2 Ip Llc Pressurized liquid fill gun apparatus and method of use
DE102019108829A1 (de) * 2019-04-04 2020-10-08 Khs Gmbh Verfahren zum Füllen von Behältern mit einem flüssigen Füllgut
DE102019135072A1 (de) * 2019-12-19 2021-06-24 Krones Aktiengesellschaft Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllprodukt
CN111943114A (zh) * 2020-07-31 2020-11-17 江苏新美星包装机械股份有限公司 一种含气液体灌装阀
DE102022103697A1 (de) * 2022-02-17 2023-08-17 Khs Gmbh Fülleinrichtung für eine Getränkeabfüllmaschine, Getränkeabfüllmaschine und Verfahren
US11718427B1 (en) * 2022-05-01 2023-08-08 Vital Manufacturing Inc. Volumetric isobaric filling system
CN114920194B (zh) * 2022-05-23 2024-07-02 杭州中亚机械股份有限公司 流量可调式灌装装置

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DE4207829A1 (de) * 1992-03-12 1993-09-16 Magdeburg Getraenkemasch Verfahren und vorrichtung zum sterilen abfuellen von getraenken
DE29807610U1 (de) * 1998-04-27 1999-05-12 KHS Maschinen- und Anlagenbau AG, 44143 Dortmund Einkammer-Füllsystem
DE19939521B4 (de) * 1999-03-04 2005-10-20 Khs Masch & Anlagenbau Ag Verfahren zur sauerstoffarmen Abfüllung von Getränken
US6457495B1 (en) * 2001-03-31 2002-10-01 Dave Meheen Filling apparatus and methods
DE102010006028A1 (de) * 2010-01-27 2011-07-28 KHS GmbH, 44143 Verfahren sowie Füllsystem zum Druckfüllen von Behältern

Also Published As

Publication number Publication date
US20160025267A1 (en) 2016-01-28
US10088107B2 (en) 2018-10-02
EP2969893A1 (fr) 2016-01-20
DE102013102611A1 (de) 2014-09-18
SI2969893T1 (en) 2018-05-31
WO2014139624A1 (fr) 2014-09-18

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