Method and device for producing a container filled with a liquid filling material
10597175 · 2020-03-24
Assignee
Inventors
- Dieter Klatt (Hamburg, DE)
- Frank Haesendonckx (Hamburg, DE)
- Ludwig Clüsserath (Bad Kreuznach, DE)
- Manfred Härtel (Weilerbach, DE)
- Wilfried Ehmer (Dortmund, DE)
Cpc classification
B65B3/022
PERFORMING OPERATIONS; TRANSPORTING
B29C49/1212
PERFORMING OPERATIONS; TRANSPORTING
B29C49/46
PERFORMING OPERATIONS; TRANSPORTING
B29C49/42802
PERFORMING OPERATIONS; TRANSPORTING
B29C49/4205
PERFORMING OPERATIONS; TRANSPORTING
B29C2049/7832
PERFORMING OPERATIONS; TRANSPORTING
B29C2049/5855
PERFORMING OPERATIONS; TRANSPORTING
B29C2049/4664
PERFORMING OPERATIONS; TRANSPORTING
B29C49/66
PERFORMING OPERATIONS; TRANSPORTING
International classification
B65B3/02
PERFORMING OPERATIONS; TRANSPORTING
B29C49/46
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method and a device for producing a container filled with a liquid filling material from preforms made of a thermoplastic material, wherein each preform is thermally conditioned and subsequently, during a molding and filling phase, remolded into the container in a mold having at least one liquid filling material as a pressure medium. The filling material or parts of the filling material are supplied at at least two points in time and/or in at least two process phases with different contents of carbon dioxide and/or at different temperatures. In the second process phase, dry ice, particularly in form of pellets, is supplied.
Claims
1. A method for producing containers filled with a liquid filling material from preforms made of a thermoplastic material, the method comprising the steps of: thermally conditioning a respective preform and subsequently transforming the preform during a forming and filling phase in a mold with at least one liquid filling material as pressure medium so as to simultaneously form and fill the container; supplying the filling material or portions of the filling material in at least two process phases with different carbon dioxide contents; and in a second of the process phases providing the liquid filling material with a desired carbon dioxide concentration by introducing dry ice formed as pellets while the container is being formed.
2. The method of claim 1, wherein degassed filling material is conveyed in a first of the process phases.
3. The method of claim 1, wherein in the second process phase chronologically following a first of the process phases the filling material or the portion of filling material with a higher concentration of carbon dioxide is supplied.
4. The method of claim 1, wherein the preform is guided during transformation into the container at least temporarily via a stretching rod and is stretched in axial direction.
5. The method of claim 4, wherein the dry ice is inserted into the filling material or shot into the filling material.
6. The method of claim 4, wherein the filling material or the portion of filling material with the higher concentration of carbon dioxide is cooled before introduction, and/or in the second process phase the filling material or the portion of filling material with the higher concentration of carbon dioxide has a lower temperature than the filling material or the portion of filling material of the first process phase.
7. The method of claim 1, wherein the carbon dioxide content of the filling material or of the portion of filling material in the second process phase is at least 30% in weight greater than the carbon dioxide content of the filling material or of the portion of filling material of the first process phase.
8. The method of claim 7, wherein the carbon dioxide content of the filling material or of the portion of the filling material in the second process phase is 50 to 100% in weight greater than the carbon dioxide content of the filling material or of the portion of filling material of the first process phase.
9. The method of claim 1, wherein the temperature of filling material or of the portion of filling material of the second process phase is lower than 10 C.
10. The method of claim 9, wherein the temperature is between 4 and 8 C.
11. The method of claim 6, wherein a pressure of the filling material or of the portion of filling material with the higher carbon dioxide concentration and/or the lower temperature, is at least temporarily higher than a pressure of at least one other portion or of a residual portion of filling material by at least 1 bar.
12. The method of claim 11, wherein a pressure on a section of a conducting path is higher than the pressure of the filling material or of the portion of the filling material which has the higher carbon dioxide concentration and/or the lower temperature, and during the forming and filling phase or during the shaping process is at least temporarily higher by 2 bars to 5 bars than a pressure of at least one other portion or a residual portion of the filling material.
13. The method of claim 11, including providing a throttle element or a narrowing cross-section in a flow path of the filling material or of the portion of the filling material flowing inside the stretching rod, whereas the throttle element is arranged before at least one filling material discharge.
14. The method of claim 4, including guiding a portion of the filling material past the stretching rod and guiding a portion of the filling material through the stretching rod.
15. The method of claim 4, including cooling the filling material with a higher concentration of carbon dioxide-containing or the portion of said filling material, and/or guiding at least the filling material with the higher concentration of carbon dioxide or the portion of said filling material through the stretching rod.
16. The method of claim 4, wherein the stretching rod is thermally insulated at least in certain sections with respect to the filling material.
17. The method of claim 1, wherein the filling material or the portion of the filling material without carbon dioxide or with a reduced concentration of carbon dioxide is introduced into the preform into the container in formation in a first of the process phases through at least two filling material outlets at different height levels, and in the chronologically following second process phase of the forming and filling phase at least said filling material or the portion of filling material with a higher concentration of carbon dioxide is introduced into the preform or into the forming container at a lower height level, whereas the filling material or the portion of filling material Without carbon dioxide or with the reduced concentration of carbon dioxide is introduced in the second process phase or a greater height level above the lower height level.
18. The method of claim 17, wherein in a third process phase between the first and second process phase a liquid connection is pre-cooled by cooled filling material or a cooled portion of filling material without carbon dioxide or with the reduced concentration of carbon dioxide, the liquid connection through which in the second process phase the filling material or the portion of filling material with the higher concentration of carbon dioxide is guided for introduction into the preform or into the container in formation.
19. The method of claim 1, wherein the process phases are partial phases of the forming and filling phase.
Description
BRIEF DESCRIPTION OF THE DRAWING
(1) The invention is described more in detail below in the light of the figures illustrating exemplary embodiments. The figures are as follows:
(2)
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DETAILED DESCRIPTION OF THE INVENTION
(12) The general configuration of a combined forming and filling device or machine is represented in
(13) After sufficient tempering (also thermal conditioning), the preforms 2 are transferred by a transfer wheel 8 to a rotor or process wheel 9, which can be driven to rotate around a vertical machine axis, or to forming and filling stations 10 arranged rotatably, i.e. on the rotor or process wheel 9. The process wheel 9 is fitted with a plurality of such forming stations 19, in the region of which the preforms 2 are transformed into the diagrammatically represented containers 11, as well as the containers 11 are filled with the filling material provided. Every container 11 is formed at the same time as it is the filled whereby the filling material serves as a pressure medium during the forming process.
(14) After forming and filling, the containers 11 are transported away from the process wheel 9 by an extraction wheel 12 and conveyed to an output line 13.
(15) According to the embodiment of
(16) Preferably, various thermoplastic materials can be used as a material for the preforms 1. By way of example, we may quote polyethylene terephthalate (PET), polyethylene (PE), polyethylene naphthalate (PEN) or polypropylene (PP). The dimensioning as well as the weight of the preforms 2 can be adapted to the size, the weight and/or the design of the containers 11 to be manufactured.
(17) A plurality of electrical and electronic components is arranged typically in the region of the heating device 4. Moreover, the heating elements 6 are fitted with moisture-sensitive reflectors. As the containers are filled and formed in the region of the process wheel 9 by using the liquid filling material, it must be ensured that any unintentional ingress of moisture into the region of the heating device 4 is prevented. This can for instance be in the form of a partitioning 16 which at least provides a splashguard. Moreover, it is also possible to temper the transport elements for the preforms as appropriate in the region of the transfer wheel 8 or to act upon them with thrusts of compressed gas in such a way that any adhering moisture cannot reach into the region of the heating device 4.
(18) The preforms 2 and/or the containers 11 can be manipulated preferably using claws and/or clamping or plug-in elements acting upon the mouth section 5 at least in certain areas from the inside or from the outside.
(19)
(20) The filling material 21 is metered by using a multi-way metering valve 22. In the exemplary embodiment represented, the stretching rod 17 is at least in certain areas hollow or has a duct and the filling material 21 is conveyed to a cavity 23 of the stretching rod 17. The region of a wall of the stretching rod 17 includes outlet openings 24 which can be shut off by a return valve 25 with respect to the multi-way metering valve 22. This enables to avoid or to minimize unintentional dripping of the filling material 21 from the stretching rod 17.
(21) The preform 2 can be vented by using a venting valve 26. The venting valve 26 is connected to an outlet opening 27 which is arranged in the region of a connecting element 28 acting upon the preform 1. The stretching rod 17 can be positioned through the connecting element 28. The preform 2 is sealed by a gasket 29 with respect to the connecting element 28, which can be in the form of an O-ring for instance. A cavity 30 of the preform 2 can be connected to the outlet opening 27 via an annular slit 31. To do so, the annular slit 31 surrounds the stretching rod 17.
(22)
(23) In accordance with the invention, there is furthermore diagrammatically shown a device for supplying dry ice 70, with which in the second process phase dry ice, in the present example in the form of pellets, can be shot from an insulated storage tank 71 into the developing or the already formed container. The foaming of the filling medium after relieving the container can thereby be delayed until the container is closed. At the same time, it is possible to fill a filling medium having a high CO.sub.2 content in the containers.
(24) According to the embodiment of
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(29) Certain process-typical parameters are for example described more in detail below. The filling material 21 is supplied to the connecting element 28 preferably with a temperature of the surrounding room, for example in the range of 20 C. to 30 C. The filling material 21 thereby cools the material of the container 11 and supports a rapid form stability of the formed container 11. This provides a very short cycle time. Likewise, it is also possible to supply the filling material 21 once it has been cooled or heated up more strongly.
(30) During the forming of the container 11, the filling material 21 can be introduced at least temporarily with a constant volume flow rate into the preform 2 or into the container 11.
(31) But it is also possible to provide for the volume flow rate an appropriate temporal profile in such a way that different volume flow rates are generated at different points in time.
(32) Before introducing the filling material 21 it is possible to suck away the air situated inside the preform 1 and/or to replace it with an inert gas. This is particularly recommended with oxidation-sensitive filling media 21.
(33) As filling material 21, either pure liquids or liquids provided with additives, can be used. The supply of carbonized filling media is considered in particular. Since the filling material 21 is supplied to the preform 1 or to the container 2 under pressure, for instance with a pressure of 10 bars, it appears appropriate to design all the flow paths for the filling material 21 in such a way that local decompressions are prevented by the flow processes. Otherwise, a local or temporary decompression could lead to outgassing of the carbon dioxide.
(34) Alternatively to the heating represented in
(35) Corrosion-resistant substances are preferably used as materials for the components of the process wheel 9, in particular stainless steels as well as plastics. In particular, the moulds 37 can be made totally or partially out of an appropriate plastic.
(36) In order to minimize the necessary stretching forces, it is possible to support the stretching cycle by the supply of the filling material 21. When supporting the stretching cycle in this way, it must however be assured that the preform 2 is guided by the stretching rod 17. The operation may for instance consist in measuring the acting stretching force and in controlling the volume flow rate of the filing material 21 in such a way that a minimum stretching force is always maintained. The magnitude of the stretching force can be determined in particular quite easily with electrically driven stretching systems by measuring the drive current or with pneumatic stretching systems by measuring the pressure.
(37) When filling containers 11 with the filling material 21 it is often desirable to provide a gas-filled headroom after closing the container hermetically 11. Said free headroom can be generated by the volume reduction which results from the retraction of the stretching rod 17.
(38) The selection of materials already mentioned above takes given hygiene requirements into account. Degermination or sterilization can thus be guaranteed. The construction design shall be carried out in such a way that the requirements in good cleanability are fulfilled.
(39) One or several of the transfer wheels can be fitted with servo drives.
(40) This supports in particular a complete separation of the heating device 4 from the process wheel 9 during cleaning cycles. Likewise, in the region of at least one of the transfer wheels, retractable manipulation elements may be arranged. The use of a dry air tunnel can provide a further protection against moisture.
(41) By way of example, a concrete process flow is described below. Before or after inserting the preform 2 into the mould 37, there is first of all a gas exchange in the cavity of the preform, in order to repel oxygen in particular or to reduce the portion of oxygen. The flushing and/or exhaust cycle lasts typically at most 0.1 second. The stretching of the preform 2 by using the stretching rod 17 lasts typically approx. 0.2 second. Likewise, a time span of approx. 0.2 second is provided for the filling and the resulting transformation of the preform 2 into the container 11. A maximum time span of 0.2 second is typically required for the subsequent creation of a headroom. The container filled with still beverages can be calmed down and relieved from tension extremely fast, whereas with carbonated beverages, this cycle can take a time span of up to 5 seconds.
(42) The headroom can be treated subsequently for example by using a high-pressure foaming or by feeding oxygen. The subsequent supply of a closing cap can take a time span of up to 1.5 seconds with carbonated beverages. Likewise, the closing or screwing cycle takes for instance a time span of 1.5 seconds.
(43) Once the container 11 has been closed hermetically, the mould 37 opens and the filled container 11 is removed and transported away.
(44) When inserting the filling material into the preform 2 to be transformed or into the container 11 still in the forming process there is usually a typical pressure gradient in the filling system or in the preform 2 or more precisely the container 11 still in the forming process. Due to the expansion of the container 11, there is first of all a relatively low pressure which increases till the end of the forming cycle. The corresponding pressure rise or the height of the pressure rise in the filling system, in particular in the filling conduit, can be used as a control parameter for a following process step and if applicable determine the moment of introduction of said next process step. Alternately or in addition thereto, the characteristic of the pressure gradient and/or of the volume flow rate of the filling material can be used as control parameters.
(45) As regards the temperature of the filling material, the filling material may be conveyed with a surrounding temperature. Depending on the respective conditions of application, instead of filling at surrounding temperature, a temperature increase or a temperature decrease can be contemplated.
(46) According to a further variation, the filling process may be implemented in two stages, whereas during the first process step the filling material is conveyed at a temperature which is higher than the temperature during the second process step. The first process step can for example be carried out when the longitudinal stretching of the preform 2 is performed over the stretching rod 11. The second process step follows the performance of the stretching cycle and corresponds to the transversal expansion of the container 11.
(47) During the aforementioned appeasement in the headroom after pressure relief, it may also be carried out an aspiration of developing gases and/or foam, if applicable.
(48) As regards the closing of the finished formed and filled containers 11, different variations can also be realized. In a variation, it is possible to fit a portion of the manipulation or forming and filling stations 10 on the rotor or process wheel 9 with a revolver head. The revolver head includes on the one hand a blowing or forming and filling head and on the other hand a closing head. This corresponds to the diagrammatical representation of
(49) According to a further variation, the forming and filling head as well as the closing head are designed as separate components, but arranged to pivot at every forming and filing station 10. According to a third variation, only the forming and filling head is provided on the rotor or process wheel 9 and the container still open is transferred to a separate closing system, for example to a transport wheel, which is fitted with a closing head.
(50) The application of the closing elements 15, for instance of the closing caps, can take place immediately after opening the respective mould 37 and the gripping of the container 11 via a holding and gripping element. An advantageous variation consists in maintaining the mould 37 closed and hence to fix the container 11 in correct position, whereas only the mouth is released for a closing element. Said release takes place in moving the mould 37 either for an angular distance on a radially different position or in pivoting and/or moving the forming and filling head so that the container mouth is free for a closing element.
(51) To do so, the closing caps would be placed on the rotor or the process wheel 9. In particular, an inert gas may be applied to the mouth space of the filled container 11 before positioning the closing elements 15.
(52) In the above description it was considered for simplifying purposes that only one supply device 20 is provided for the filling material 21. In fact, the forming and filling system or machine includes a further supply device 20.1 for an additional portion or a further component of the filling material, which exhibit a higher CO.sub.2 content than the filling material 21 and is designated below with 21.1.
(53) It has proved particularly advantageous to achieve stratification with the aforementioned methods and in particular with respect to the introduction of the portion or of the component of the filling material 21.1 with a CO.sub.2 content or with the higher CO.sub.2 content. It has namely appeared problematic in the case of a full or partial carbonization of the filling material, to obtain the rapid pressure relief after removal from the mould and filling of the containers 11, from the high forming and filling pressure up to the closing of the respective container for instance at ambient pressure without product loss. A massive foaming occurring here with product loss has prevented the use of this hydraulic transformation technique for CO.sub.2 containing products so far.
(54) According to a cognition underlying the invention, it is particularly advantageous to avoid such product losses if the filling material 21 or 21.1 or the portions of the filling material 21 or 21.1 are supplied at least at two points in time or in at least two process phases with different carbon dioxide contents and/or with different temperatures. To do so, it is appropriate in a second or subsequent process phase, to feed the filling material or the filling material component 21.1 with the higher concentration of carbon dioxide. This has the advantage that the filling material 21 and 21.1 in the generated container 11 commonly constitute the hydraulic pressure medium to form the container 11, but the filling material 21 already introduced in the developing container 11 has calmed down and when introducing the filling material 21.1 or the portion of filling material 21.1 with the higher CO.sub.2 concentration, first of all further solution processes take place in the liquid volume. The second or subsequent process phase is thereby for instance a process phase completing the forming and filling phase. The introduction of the filling material 21.1 or of the portion of filling material 21.1 with the higher CO.sub.2 concentration is preferably stratified into the already present liquid volume, i.e. for instance in the region of the bottom of the developing container 11. The introduction of the filling material components or of the filling material 21 and 21.1 takes place in a controlled manner through the multi-way metering valve 22.
(55) There is a variation which consists in cooling the filling material 21.1 or the portion of filling material 21.1 with the higher concentration of carbon dioxide before introduction, and in that in the aforementioned second process phase introducing said filling material 21.1 or the corresponding portion with the higher concentration of carbon dioxide with a lower temperature than the filling material 21 or the portion of filling material 21 of the first process phase into the developing container 11. The result is a lower layer with a filling material rich in CO.sub.2, whereas a foaming, also a foaming during the relieving process is decreased to the extent that disadvantageous product losses do not occur.
(56) Therefore, the carbon dioxide content in the second process phase should be 30% in weight above the carbon dioxide content during the first process phase, in particular 50% in weight to 100% in weight above the carbon dioxide content in the first phase. Ideally, during the first or initial process phase, a quiet, i.e. a filling material component free from CO.sub.2, such as the filling material 21 and during the second process phase a filling material component rich in CO.sub.2, i.e. the filling material 21.1, are introduced into the developing container 11.
(57) There is an alternative in which the temperature of the filling material 21.1 or of the portion of filling material 21 of the second process phase is cooled, in which it is at least 10 C. below the temperature of the first or a previous process phase, and in particular is lower than 10 C. and ideally ranges between 4 C. and 8 C.
(58) It has appeared advantageous that the pressure of the filling material 21.1 or of the portion of filling material 21.1, which exhibits the higher carbon dioxide concentration and/or the lower temperature, at least during the transformation process or during the forming and filling phase is partially higher than the pressure of at least another portion or of the residual portion of the filing material 21, and preferably by at least 1 bar.
(59) Moreover, the pressure on a conduit section 42 or a portion of the conduit section, via which the filling material 21.1 or the portion of the filling material 21.1 with the higher carbon dioxide concentration and/or the lower temperature is conveyed, is higher than the pressure of the residual filling material 21 or of the residual portion of the filling material 21, and during the shaping process at least temporarily higher by 2 bars to 5 bars.
(60) An embodiment provides that a throttle element or a narrowing cross-section is provided in the flow path of the filling material 21 and 21.1 flowing inside the stretching bar 17, whereas the throttle element is arranged in the flow direction of the filling material 21 and 21.1 for instance shortly before at least one output 24 of the stretching rod 17. Consequently, the advantageous high pressure is maintained up to shortly before the first relaxation. This pressure can be raised further when a portion of the filling material 11 is guided past the horizontal rod 17 and a portion of the filling material 11 is guided through the horizontal rod. To do so, the stronger carbon dioxide-containing filling material 21.1 should be conveyed more appropriately through the stretching rod 17. It is also advantageous if the stretching rod 17 is thermally insulated at in a section with respect to the filling material 21 and 21.1.
(61) The forming and filling system or machine thereby encompasses for producing filled containers 11 made of a thermoplastic material among others the at least one heating section or heating system 4 arranged along a transport path of a preform 2 and at least one forming and filling station 10 fitted with a mould.
(62) Moreover, the forming and filling system or machine encompasses among other things a feeding device 1 for the filling material 21 and 21.1 to be filled into the container 11 as well a carbonization unit 43, which for example is provided in the conduit section 42 and with which carbon dioxide can be dissolved at least in the partial flow of the filling material 21.1, whereas the forming and filling station 10 has a guiding device in the form of a stretching rod 17 acting at least temporarily upon the preform 2 during its transformation into the container 11 and at least one portion of the filling material 21 can be conveyed through the duct or the cavity 23 of the stretching rod 17. At least one outlet opening 24 of the conduit or cavity 23 is provided at the lower end of the stretching rod 17.
(63) Advantageously, a cooling unit 44 is provided at least along the conduit section 42 for the filling material 21.1, in which downstream carbon dioxide is dissolved or which flows from the carbonation unit 43.
(64) At least the conduit section 42, in which the filling material 21.1 rich in carbon dioxide or a portion thereof is guided, at least thermally insulated on a partial length, for example with a Teflon insulation or made of a Teflon-containing material, and/or is cladded with a thermal insulation, for instance with Teflon or a Teflon-containing material.
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(67) Different operating modes are possible with the stretching rod 17a, namely for example the simultaneous introduction of the filling material, for example of the filling material 21 without CO.sub.2 content or with reduced CO.sub.2 content on the lower level N1 via the outlet openings 47 and on the higher level N2 via the outlet openings 49 into the preform 2 or into the developing container 11. Therefore, the control valve 50 is opened by suitable control from the control unit 53 for a connection of both ducts 46 and 48 and moreover the multi-way metering valve 22 is controlled through the control unit 53 in such a way that this metering valve only provides a connection with the liquid connection 55. Said operating condition is represented in
(68) With a closed control valve 50, it is moreover possible to establish a connection to both ducts 46 and 48 by a suitable control of the multi-way metering valve 22 via said valve for the filling material 21 so that the filling material 21 is again inserted according to the arrows via the outlet openings 47 and 49 at the different levels of height N1 and N2 into the preform 2 or into the developing container 11. In the operating condition represented in
(69) Moreover, there is the possibility, by suitable control of the multi-way metering valve 22, to supply the filling material 21.1 via the liquid connection 54 in the internal duct 46 for the exit exclusively at the lower outlet openings 47 or on the high level N1 and to supply the filling material 21 for the exit exclusively at the upper outlet openings 49 or on the higher level N2, whereas the supply of the filling material 21 and 21.1 is either simultaneous, time-delayed or with a time overlap, and namely with an evacuation which is time-delayed or with a time overlap preferably in such a form that first of all the filling material 21 is supplied via the upper outlet openings 47 and then the filling material 21.1 is supplied via the lower outlet openings 49. Said operating condition, in which again the filling material 21.1 is cooled in the cooling unit 44, is represented in
(70) It is for example possible during the respective forming and filling phase in a first partial or process phase according to
(71) A calmed intermediate zone is formed in each of the cases between the height levels N1 and N2, a zone which delineates the portions of filling material from each other. An advantageous influence lies in the aforementioned electromagnetically driven control valve 50, because it enables a low-impulse and low-blending changeover. A further advantage consists with said electromagnetically driven control valve 50 that it is quite robust and can be cleaned very easily in corresponding cleaning cycles using quick, and, if necessary, multiple switching.
(72)
(73) The stretching rods 17a or 17b represented in
(74) As shown in
(75) The outlet openings 47 or 49 have in particular rounded edges or radii so that local turbulences and cavitation are avoided and result in a stable stratification. More advantageously, the rounded edges of the outlet openings 47 and 49 are provided at the stretching rod radially and inwardly as well as radially and outwardly.
LIST OF REFERENCE SIGNS
(76) 1 Feeding device 2 Preform 3 Transfer wheel 4 Heating device 5 Mouth section 6 Heating element 7 Transport device 8 Transfer wheel 9 Process wheel 10 Forming and filling station 11 Container 12 Extraction wheel 13 Output distance 14 Input device 15 Closing member 16 Mould partitioning 17 Stretching bar or stretching rod 17.1 Narrowing portion 18 Tip of the stretching rod 19 Bottom of the preform 20 Supply device 21 Filling material 22 Multi-way metering valve 23 Cavity of the stretching rod 24 Outlet opening 25 Return valve 26 Venting valve 27 Outlet opening 28 Connecting element 29 Seal 30 Cavity of the preform 31 Annular slit 32 Longitudinal axis of the bottle or 33 Sealing element 34 Counter element 35 Bearing 36 Supply opening 37 Mould 38 Closing device 39 Gripper 40 Tool carrier 41 Rotational axis 42 Conduit or conduit section 43 Carbonation unit 44 Cooling unit 45 Stretching rod body 45.1 Stretching rod end 46 Duct 47 Outlet opening 48 Duct 49 Outlet opening 50 Control valve 51 Lock ring 52 Magnet coil 53 Control electronics 54,55 Liquid connections 56 Duct 57 Outlet opening 58 Control valve 59 Headroom 60 Control valve 70 Feeding device for dry ice pellets 71 Storage tank for dry ice pellets