EP2763930B1 - Procédé de commande d'une installation d'embouteillage et installation d'embouteillage - Google Patents

Procédé de commande d'une installation d'embouteillage et installation d'embouteillage Download PDF

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Publication number
EP2763930B1
EP2763930B1 EP12769328.1A EP12769328A EP2763930B1 EP 2763930 B1 EP2763930 B1 EP 2763930B1 EP 12769328 A EP12769328 A EP 12769328A EP 2763930 B1 EP2763930 B1 EP 2763930B1
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EP
European Patent Office
Prior art keywords
filling
bypass
pump
volume flow
container
Prior art date
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EP12769328.1A
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German (de)
English (en)
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EP2763930A1 (fr
Inventor
Olaf Muszinski
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KHS GmbH
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KHS GmbH
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Publication date
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Priority to SI201230512A priority Critical patent/SI2763930T1/sl
Publication of EP2763930A1 publication Critical patent/EP2763930A1/fr
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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
    • 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
    • B67C3/007—Applications of control, warning or safety devices in filling machinery
    • 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
    • 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

Definitions

  • the invention relates to a method for controlling a filling plant for filling containers with a filling material, preferably with a filling material which contains solid constituents or solids, for example fibers and / or product pieces, in at least one liquid component, according to the preamble of patent claim 1. Furthermore, the invention relates to a filling system, in particular for filling containers with a filling material, preferably with a solid ingredients containing filling material according to the preamble of claim. 7
  • the JP 2002 337 988 A discloses a generic method and a generic filling.
  • liquid component for example fruit juice and solid components, for example product pieces, cells, fibers, etc.
  • solid components for example product pieces, cells, fibers, etc.
  • Damage to the solid components may be caused i.a. thermal type, for example, by too long heating of the filling material, or else of a mechanical nature, in particular due to shear forces, which are provided by product damaging internals in the filling material leading flow paths of a filling system.
  • Product damaging internals are in particular control and control valves, overflow valves, but also to promote the filling serving pumps, also positive displacement pumps, if they must be operated with high pump speed, but displacement pumps are much gentle on the product than flow pumps, such as centrifugal pumps. For this reason, it is generally common and known in the beverage industry to promote products containing solid components with displacement pumps, such as piston pumps, rotary piston pumps or with membrane pumps.
  • filling systems are known, in which the hot product or product is provided by a process plant and the Gregutkessel a container filling machine is supplied, with a volume flow which is greater than the current filling or bulk capacity of the container filling machine.
  • a subset of the supplied filling material is passed through the Be Daveer Schollmaschine and their filling elements and returned via a bypass line as a "bypass flow rate" to the process plant.
  • This bypass flow rate is preferably controlled using at least one bypass pump so that the Be fiscaler spallmaschine is held alone by the bypass flow rate of the contents at the required temperature.
  • the control or regulation of the bypass pump or its delivery rate is dependent on at least one temperature sensor provided on the container filling machine, wherein high delivery rates or high pump speeds can not be avoided.
  • bypass flow rates are required. This applies in particular to the heating of the container filling machine during a production preparation, but also during operation of the container filling machine or during a machine standstill due to a production interruption.
  • These different bypass volumes or bypass volume flows can be given, for example, in volume percent of the rated bulk capacity of the container filling machine and, for example, during startup and heating of the filling machine up to 10% of the rated bulk capacity, during normal, trouble-free operation about 5 to 10% of Nominal bulk capacity and during a product interruption between 5% and 10% of the rated bulk capacity, which is achieved in particular by the above-mentioned control and / or regulation of the bypass pump.
  • volume flow of the product provided by the process plant due to the thermal inertia of the process plant can be considered substantially constant.
  • the filling machine depending on the current operating state of the filling machine to redirect a certain amount of the provided by the process plant contents, for example at an emergency stop of the filling machine 100% of the provided by the process plant volume flow.
  • a disadvantage of the known filling systems u.a. the high load of solids contained in the contents by product damaging internals, in particular by the required in the primary line control or control valve, provided by the overflow in the overflow valve and also by the relatively high flow rate driven bypass pump.
  • a disadvantage of known filling systems continues to be high energy consumption, since considerable volume flows undergo a considerable pressure difference.
  • the object of the invention is to provide a method by which a particularly gentle product filling of containers is achieved even with a solid constituents having contents with high reliability.
  • a method according to claim 1 is formed.
  • a filling system is the subject of claim 7.
  • the bypass pump in the bypass line is, for example, regulated so that the volume flow recirculated via the bypass line and the bypass pump during normal normal operation is only about 5% of a basic value, for example, the rated bulk capacity of the container filling machine, so that alone by the Reduced flow of this pump a product gentle recycling of the contents is reached.
  • the bypass pump is therefore operated in this embodiment during normal operation at a constant speed and thus with a constant flow rate.
  • the control of the bypass pump and / or arranged in an overflow line overflow pump is preferably carried out in the filling system according to the invention via frequency converters, which allow infinite control or regulation of the pump delivery rate and thus the corresponding volume flows.
  • Influencing variables or parameters for the control and / or regulation are, for example, the actual bulk capacity of the container filling machine, the rated bulk capacity of the container filling machine, also depending on the type, size and shape of the containers, the current product performance of the process plant or the current from the process plant provided volume flow of the filling material.
  • the control and / or regulation can also take into account a forecast of the future, expected performance or bulk output of the container filling machine and / or the performance of a container blowing machine upstream of the container filling machine.
  • the volume flow of the filling material provided by the process plant is constant, for example, during normal operation and set so that taking into account the current bulk capacity of the container filling machine via the bypass line, the volume flow of 5% of the base value, eg the nominal bulk power, and over the overflow or over the local Overflow pump, a volume flow between about 5% to 105% of the underlying value to be promoted.
  • product-sparing filling means filling of products or products containing solid constituents in such a way that these solid constituents are as intact as possible, i. get into the respective container as not mechanically damaged as possible.
  • the product-sparing filling also requires, in particular, that in product-carrying lines of the filling system, i. at least in the primary line, which connects the boiler of the filling machine with the process plant providing the filling material, the solid components in the filling harmful components are avoided as far as possible.
  • Such installations are u.a. Overflow valves and control or control valves.
  • “Bulk performance” in the sense of the invention means e.g. in liters measured filling capacity of the container filling machine per unit time, for example, per hour.
  • “rated bulk power” in the sense of the invention means e.g. Capacity of the container filling machine measured in liters / hour during normal operation. For example, this nominal bulk capacity may be 100,000 liters per hour when filling containers having a container volume of 0.5 liters.
  • Container are in the context of the invention in particular cans, flanges, tubes, Pourches, each made of metal, glass and / or plastic, but also other packaging, which are suitable for filling of liquid or viscous products.
  • free-jet filling is to be understood as meaning a process in which the liquid product flows into the container to be filled in a free filling jet, the container with its container mouth or opening not bearing against the filling element, but rather from the filling element or from a local one Drgutauslass is spaced.
  • pressure filling is generally to be understood as meaning a filling process in which the container to be filled rests in sealing position against the filling element and, as a rule, before the actual filling phase, ie before the liquid valve is opened via at least one controlled element in the filling element trained gas path with a pressurized gas span (inert gas or CO2 gas) is biased, which is then displaced during filling of the inflowing of the container contents increasingly as return gas from the container interior, and also via at least one controlled, formed in the filling element gas path.
  • This pretensioning phase can be preceded by further treatment phases, for example evacuation and / or flushing of the container interior with an inert gas, for example CO.sub.2 gas etc., also via the gas paths formed in the filling element.
  • pressureless filling is generally to be understood as meaning a filling process in which the container to be filled, preferably with its container mouth, also rests in sealing position against the respective filling element and the container interior is filled before the actual filling phase, ie. is pretreated before the opening of the liquid valve via controlled, formed in the filling element gas paths, for example, evacuated and / or purged with an inert gas such as CO2 gas, in which case during filling of the container flowing inflow increasingly displaced gas as the return gas over at least a controlled, formed in the filling element gas path is discharged from the container interior.
  • an inert gas such as CO2 gas
  • the filling system generally indicated at 1 in the figure serves to hot fill a liquid product with solid components into container 2, i. for filling the container 2 with the heated contents.
  • the filling system 1 includes u.a. a container filling machine 3 of rotating design, of which schematically two filling elements 4, which are provided with a plurality of similar filling elements 4 on the circumference of a vertical machine axis rotatably driven rotor and each forming a filling position for filling the container 2, and one for all filling elements. 4 or filling positions common Gregutkessel or ring boiler 5 is shown.
  • filling systems according to the invention can also have container filling machines in a linear design.
  • the product heated to a predetermined temperature is supplied to the ring vessel 5 via a primary line 6 from the outlet 7.1 of a generally designated 7 in the figure process plant (eg KZE), so in the manner described in more detail below the ring boiler 5 at least during the filling operation the liquid contents to form a lower liquid space is partially filled, while keeping constant the height or the level of Medgutapts in the ring bowl 5.
  • the filling elements 4 are each formed with a filling elements 4 in this and a liquid valve having Gregutkanal to the liquid space of the ring bowl 5 connected.
  • the filling elements 4 are in particular also designed for heating by the hot filling material so that they are flowed through in a production stop and closed liquid valves of the hot medium.
  • the filling elements 4 are each connected with a separate outlet to a bypass line 8, in which a bypass pump 9, preferably arranged in the form of a positive displacement pump and a Gregutrestmenge or a bypass flow from the Be Zeller Stahlmaschine third or the local filling elements 4 to the central processing unit 7, for example, to a local, the recirculated filling material collecting "Rework" container is returned.
  • the filling system 1 further comprises an overflow line 10, in which an overflow pump 11 is preferably provided, for example, in the form of a positive displacement pump and which connects the primary line 6 with the bypass line 8 in the flow direction of the filling material after the bypass pump 9, specifically for a controlled Gregutstrom directly between the outlet 7.1 and the inlet 7.2 of the process plant.
  • an overflow pump 11 is preferably provided, for example, in the form of a positive displacement pump and which connects the primary line 6 with the bypass line 8 in the flow direction of the filling material after the bypass pump 9, specifically for a controlled Gregutstrom directly between the outlet 7.1 and the inlet 7.2 of the process plant.
  • the filling system 1 is operated so that the process plant 7 at its outlet 7.1 a first volume flow VS1 (contents per unit time) provides that is constant or substantially constant and greater than the current bulk capacity of the Be Daveer Bergllmaschine 3.
  • the first volume flow VS1 is, for example, 110% of a base value, for example the rated bulk capacity of the container filling machine 3.
  • the bypass pump 9 or its delivery rate are controlled or regulated so that in normal operation, i. with trouble-free, uninterrupted operation on, by the bypass pump 9 to the process plant 7 returned volume flow VS2 of the contents, which is constant or substantially constant in the illustrated embodiment and, for example, 5% of the base value, e.g. the rated bulk capacity of the container filling machine 3 corresponds.
  • the process plant 7 can react to changes in the performance of the Be female spallmaschine 3 with respect to the change in the provided volume flow VS1 only with relatively long time delay, ie in particular short-term changes the bulk performance of the Be fiscaler spallmaschine 3, as for example in case of malfunction of Be partnerser spallmaschine 3 or a system having this machine occur in the filling system 1 outside the process plant 7 must be compensated.
  • the volume flow VS3 in the overflow line 10 is between a range of 5% - 105% of the base value, e.g. the rated bulk capacity of the container filling machine 3 is regulated, in the form that at least during normal operation of the container filling machine 3 and / or the filling system 1 via the overflow line 10 about 5% of the base value, e.g. the rated bulk power, and at an interruption of the filling operation, i. when the actual bulk capacity of the container filling machine 3 is zero, 105% of the base value, e.g. be returned to the nominal bulk power.
  • the base value e.g. the rated bulk capacity of the container filling machine 3 is regulated
  • the level of Medgutspiegels is kept constant or substantially constant in the partially filled ring bowl 5, because the filling of the container, and in particular the accuracy of each introduced into the container 2 capacity or the accuracy of the filling level is primarily determined by the geodetic height of the level of Medgutspiegels in the ring tank.
  • This level control takes place in the filling system 1 according to the invention not by a control or regulating valve provided in the primary line 6, but indirectly by changing the volume flow VS3 in the overflow line 10.
  • the main flow path of the filling material i. the primary line 6 free of product damaging internals.
  • the bypass pump 9 in the bypass line 8 and the overflow pump 11 in the overflow line 10 are preferably designed as positive displacement pumps, for example as piston or rotary piston pumps or diaphragm pumps.
  • positive displacement pumps for example as piston or rotary piston pumps or diaphragm pumps.
  • the pumps 9 and 11 cause damage to the solids in the contents only to an extremely small extent because, during normal, trouble-free filling operation, i. in the periods when the container filling machine 3 has its maximum bulk capacity or rated bulk capacity, the bypass line 8 as well as the overflow line 10 lead only small amounts of contents.
  • the advantages of the filling system 1 are thus u.a. in the prevention of damage to the solids in the product introduced into the container 2 and thus in the avoidance of customer complaints, in particular by the fact that the main flow path of the filling material, i. the primary line 6 is free of product damaging internals.
  • Another important advantage of the filling system 1 is also that by using the pumps 9 and 11 both in the bypass line and in the overflow line 10 both lines can still be brought together outside the process plant 7, ie before the inlet 7.2. This results in comparison to known filling plants and their process equipment not only a significant simplification of the process plant 7 itself, by avoiding additional flow paths within the process plant, but it is also necessary in known filling systems and product damaging overflow valve avoided.
  • the filling plant 1 is used for hot or hot aseptic filling of the contents into the containers 2.
  • the filling system 1 is also suitable for the aseptic filling of solids containing products or products at normal or ambient temperature or in the cooled state.
  • the filling system 1 is suitable for different filling methods, for example for jet filling, for pressure filling, for pressureless filling, etc.

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

Claims (10)

  1. Procédé servant à commander une installation de remplissage (1) comprenant une machine de remplissage de contenants (3) servant à remplir des contenants (2) d'un produit de remplissage liquide, de préférence d'un produit de remplissage liquide contenant des constituants solides, sachant que la machine de remplissage de contenants (3) présente au moins une cuve de produit de remplissage (5) servant à recevoir le produit de remplissage ainsi qu'au moins un élément de remplissage (4) servant à déverser de manière commandée dans le contenant (2) concerné le produit de remplissage provenant de la cuve de produit de remplissage (5) affluant en sa direction, comprenant une installation de traitement (7) servant à fournir le produit de remplissage amené à la cuve de produit de remplissage (5), comprenant au moins un conduit de dérivation (8) relié à au moins un élément de remplissage, (4) pourvu d'une pompe de dérivation (9) servant à ramener une quantité restante de produit de remplissage ou un flux volumique de dérivation (VS2) de l'élément de remplissage (4) au moins au nombre de un et/ou de la cuve de produit de remplissage (5) à l'installation de traitement (7), comprenant également un conduit de trop-plein (10) servant à ramener une quantité de produit de remplissage (VS3) non requise à l'installation de traitement (7), caractérisé en ce que la quantité restante de produit de remplissage et/ou le flux volumique de dérivation (VS2) sont extraits de manière active de l'élément de remplissage (4) au moins au nombre de un et/ou de la cuve de produit de remplissage (5) par la pompe de dérivation (9) réalisée sous la forme d'une pompe volumétrique, sachant que le niveau du produit de remplissage dans la cuve de produit de remplissage (5) est réglé et/ou commandé par la variation du flux volumique (VS3) dans le conduit de trop-plein, par la variation de la puissance de refoulement d'une pompe de trop-plein (11) dans le conduit de trop-plein (10).
  2. Procédé selon la revendication 1, caractérisé en ce que la pompe de dérivation (9) fonctionne au moins au cours de mode normal de remplissage pour un flux volumique (VS2) constant dans le conduit de dérivation (8), à une puissance de refoulement constante.
  3. Procédé selon l'une quelconque des revendications précédentes, caractérisé par un remplissage aseptique, par exemple aseptique à froid ou aseptique à chaud, des contenants (2) en produit de remplissage.
  4. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que le flux volumique (VS1), fourni par l'installation de traitement (7), du produit de remplissage est plus grand que la somme de la puissance de déchargement (SL) actuelle de la machine de remplissage de contenants (3) et du flux volumique (VS2) ramené par l'intermédiaire du conduit de dérivation (8).
  5. Procédé selon la revendication 4, caractérisé en ce que le flux volumique (VS3) ramené par l'intermédiaire du conduit de trop-plein (10) est égal à la différence entre le flux volumique (VS1) fourni par l'installation de traitement et la somme de la puissance de déchargement (SL) actuelle de la machine de remplissage de contenants (3) et du flux volumique de dérivation (VS2) ramené par l'intermédiaire du conduit de dérivation (8).
  6. Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce que le flux volumique fourni par l'installation de traitement (7) est d'environ 110 % d'une valeur de base, et en ce que le flux volumique (VS2) ramené par l'intermédiaire du conduit de dérivation (8) correspond à environ 5 % de la valeur de base, sachant que la valeur de base est par exemple une puissance de déchargement nominale de la machine de remplissage de contenants (3).
  7. Installation de remplissage comprenant une machine de remplissage de contenants (3), comprenant au moins un élément de remplissage (4), de préférence une pluralité d'éléments de remplissage (4) au niveau d'un élément de transport en circulation ou au niveau d'un rotor, ainsi qu'une cuve de produit de remplissage (5) réalisée sous la forme d'une cuve annulaire, laquelle est au moins partiellement remplie au cours du mode de remplissage d'un produit de remplissage liquide, de préférence d'un produit de remplissage présentant des constituants solides et à laquelle l'élément de remplissage (4) au moins au nombre de un est relié, comprenant une installation de traitement (7), qui est reliée à la cuve de produit de remplissage (5) par l'intermédiaire d'un conduit primaire (6) afin de fournir le produit de remplissage, comprenant au moins un conduit de dérivation (8) relié à l'élément de remplissage (4) au moins au nombre de un ou à la cuve de produit de remplissage (5), pourvue d'une pompe de dérivation (9) servant à ramener une quantité partielle de produit de remplissage ou un flux volumique de dérivation (VS2) à l'installation de traitement (7), comprenant également au moins un conduit de trop-plein (10) sevrant à ramener une quantité partielle de produit de remplissage (VS3) non requise pour le remplissage ou la recharge de la cuve de produit de remplissage (5) dans l'installation de traitement (7), caractérisée en ce la pompe de dérivation (9) est réalisée sous la forme d'une pompe volumétrique, et en ce que qu'est prévue dans le conduit de trop-plein (10) une pompe de trop-plein (11), et caractérisée par au moins un circuit de commande et/ou de réglage servant à commander ou à régler la puissance de refoulement de la pompe de trop-plein (11) dans le conduit de trop-plein (10) en fonction d'un niveau du produit de remplissage dans la cuve de produit de remplissage (5) partiellement remplie de la machine de remplissage de contenants (3) afin de maintenir ledit niveau constant.
  8. Installation de remplissage selon la revendication 7, caractérisée en ce que la pompe de trop-plein (11) est une pompe volumétrique.
  9. Installation de remplissage selon l'une quelconque des revendications 7 ou 8, caractérisée en ce que les pompes volumétriques sont par exemple des pompes à piston ou des pompes à piston tournant ou des pompes à membrane.
  10. Installation de remplissage selon l'une quelconque des revendications 7 à 9, caractérisée en ce que le circuit de commande et/ou de réglage au moins au nombre de un servant à commander ou à régler la puissance de refoulement de la pompe de trop-plein (11) afin de maintenir le niveau du produit de remplissage constant dans la cuve de produit de remplissage (5) partiellement remplie tient compte de la puissance de déchargement actuelle ou attendue de la machine de remplissage de contenants (3) et/ou du flux volumique actuel ou attendu de l'installation de traitement installée en amont de la machine de remplissage de contenants.
EP12769328.1A 2011-10-04 2012-09-28 Procédé de commande d'une installation d'embouteillage et installation d'embouteillage Active EP2763930B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SI201230512A SI2763930T1 (sl) 2011-10-04 2012-09-28 Postopek za krmiljenje polnilnega postrojenja in polnilno postrojenje

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DE102011114690A DE102011114690A1 (de) 2011-10-04 2011-10-04 Verfahren zum Steuern einer Füllanlage sowie Füllanlage
PCT/EP2012/004074 WO2013050124A1 (fr) 2011-10-04 2012-09-28 Procédé de commande d'une installation d'embouteillage et installation d'embouteillage

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EP2763930A1 EP2763930A1 (fr) 2014-08-13
EP2763930B1 true EP2763930B1 (fr) 2016-03-30

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US (1) US10059578B2 (fr)
EP (1) EP2763930B1 (fr)
DE (1) DE102011114690A1 (fr)
SI (1) SI2763930T1 (fr)
WO (1) WO2013050124A1 (fr)

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FR3104549A1 (fr) * 2019-12-16 2021-06-18 Serac Group Installation de conditionnement comprenant des becs de remplissage reliés à des canalisations de retour

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DE102007014702B4 (de) * 2007-03-23 2017-03-30 Khs Gmbh Füllsystem für Heißabfüllung
DE102007058047A1 (de) 2007-11-30 2009-06-10 Khs Ag Verfahren und Vorrichtung zur Abfüllung von Flüssigkeiten
DE102008031049A1 (de) * 2008-06-30 2009-12-31 Lewa Gmbh Vorrichtung zum Portionieren förderbarer Medien

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US20140238531A1 (en) 2014-08-28
DE102011114690A1 (de) 2013-04-04
WO2013050124A1 (fr) 2013-04-11
US10059578B2 (en) 2018-08-28
EP2763930A1 (fr) 2014-08-13
SI2763930T1 (sl) 2016-05-31

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