WO2019207843A1 - Filling device - Google Patents
Filling device Download PDFInfo
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- WO2019207843A1 WO2019207843A1 PCT/JP2019/000260 JP2019000260W WO2019207843A1 WO 2019207843 A1 WO2019207843 A1 WO 2019207843A1 JP 2019000260 W JP2019000260 W JP 2019000260W WO 2019207843 A1 WO2019207843 A1 WO 2019207843A1
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- Prior art keywords
- pressure
- filling
- container
- liquid
- gas
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- 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
Definitions
- the present invention relates to a filling device suitable for filling a flexible container with a carbonated beverage.
- Patent Document 1 As a method of filling a container with a carbonated beverage, for example, a counter pressure system disclosed in Patent Document 1 has been common. Since the counter pressure system takes a long time to fill, in recent years, as disclosed in Patent Documents 2 and 3, carbonic acid that has been pressurized in a storage tank in a container that has previously been negatively pressurized. There has been proposed a method of injecting a product liquid containing the solution at once. In this filling, the filling amount is controlled by monitoring the change over time of the pressure rise inside the container while ejecting the product liquid containing carbonate into the container.
- the product liquid is filled using the pressure difference between the container and the storage tank, so that the product liquid is filled at a very high speed compared to the counter pressure method. Can do.
- the filling according to Patent Documents 2 and 3 can fill the container with the product liquid containing carbonic acid in a short time, but there is a limit to the target container.
- the pre-evacuation method is applicable only to a container having rigidity such as a glass bottle because it is necessary to make the inside of the container have a negative pressure before filling with the product liquid.
- the pre-evacuation method according to Patent Documents 2 and 3 is applied to a plastic container having flexibility, the plastic container may be crushed without being able to withstand negative pressure.
- an object of the present invention is to provide a filling device capable of filling a product liquid containing carbonic acid at a high speed while maintaining the shape of a flexible container.
- a pressure difference corresponding to a pre-pressure P B3 between the pressure (counter) P F to be added to the internal pressure (vessel pressure) P B of the container reservoir is formed It shall be.
- vessel pressure P B is, for example atmospheric pressure
- counter pressure P F is the pressure higher than the atmospheric pressure required for the product fluid handling.
- FIG. 1 (a) it can be filled with an amount of only Q 11 when filling the product solution into the container until the container pressure P B becomes a predetermined set pressure P B1.
- the set pressure P B1 is a pressure lower than the pressure that is in equilibrium with the pressure P B3 .
- the filling amount Q 13 is filled with a single differential pressure respectively, that is the maximum amount that can be filled in a container by one-stage filling (Qmax).
- Qmax the maximum amount that can be filled in a container by one-stage filling
- the volume of the container depending on the conditions such as the vessel pressure P B and the counter pressure P F, at one stage filling, it may not be possible to fill the amount of product liquid to be targeted.
- the differential pressure formation and filling may be repeated a plurality of times.
- the product liquid is filled (second filling) by the difference (Q 22 ) from the target filling amount Q.
- the second differential pressure can be performed by lowering the container pressure P B to atmospheric pressure, or can be performed by lowering the pressure to exceed atmospheric pressure.
- a storage tank where the product solution is stored under a counter pressure P F is added environment
- a liquid supply path for filling the product solution into the container from the reservoir
- opening and closing And a filling nozzle having a liquid valve for controlling the supply of the product liquid from the liquid supply path.
- the pressure P B in the container a positive pressure above atmospheric pressure, and maintained at a pressure lower than the counter pressure P F in the reservoir, and the counter pressure P F of the reservoir
- the container and the filling nozzle With the pressure difference formed between the container and the filling nozzle, the container and the filling nozzle are engaged in a sealed state, and then the liquid valve is opened to fill the container with the product liquid.
- the vessel pressure P B is in equilibrium with the counter pressure P F, or until the state of a predetermined pressure below the counter pressure P F, the product solution is filled a liquid
- the valve is closed.
- the filling device of the present invention preferably includes a supplementary chamber that is in communication with the container to complement the volume of the container.
- the auxiliary room in the present invention can be divided into two.
- the first auxiliary chamber is composed of an auxiliary chamber tank provided on a gas lead-out path for deriving a gas component discharged from the container.
- the second auxiliary chamber is a first auxiliary chamber volume consisting of a gap inside the gas outlet path for leading the gas component discharged from the container, and a gap inside the liquid supply path between the liquid valve and the container. Consisting of one or both of the second auxiliary chamber volume.
- the filling device including the auxiliary chamber tank in the present invention preferably includes a first gas valve that opens and closes the gas outlet passage.
- This filling device fills the container with the product liquid while keeping the gas component inside the container sealed without discharging the gas component inside the container to the outside with the liquid valve opened.
- the first gas valve is opened, and a part of the gas component is led out to the auxiliary chamber tank through the gas lead-out path.
- Filling apparatus comprising the auxiliary chamber vessel of the present invention is preferably filled up vessel pressure P B is in equilibrium with the counter pressure P F, or the product liquid in the container until the container pressure P B reaches the set pressure . Then, the vessel pressure P B to a pressure P R of the auxiliary chamber tank is balanced, gas component is discharged to the auxiliary chamber tank. The filling apparatus, by the gas component is led to the auxiliary chamber tank, vessel pressure P B is less pressure difference from the counter pressure P F is formed. Next, with the liquid valve opened, the container is filled with an amount of product liquid corresponding to the difference from the target filling amount.
- the auxiliary chamber tank in the present invention preferably has a structure with a variable internal volume. Moreover, the auxiliary chamber tank in the present invention preferably has a volume corresponding to the difference from the target filling amount.
- the first auxiliary chamber volume or the second auxiliary chamber volume and the interior of the container are formed in communication with the liquid valve closed. that the pressure differential between the vessel pressure P B and the counter pressure P F in the space is formed.
- the first auxiliary chamber volume or the second auxiliary chamber volume in the present invention preferably has a volume sufficient to fill the product liquid that satisfies the target filling amount through the formation of a single pressure difference and the filling of the product liquid. After the pressure difference has been formed, until the vessel pressure P B is in equilibrium with the counter pressure P F, or the product liquid is filled into the container until the container pressure P B reaches a set pressure.
- the first auxiliary chamber volume or the second auxiliary chamber volume in the present invention preferably has a volume corresponding to the difference from the target filling amount.
- a filling device of the present invention in a state where the differential pressure between the vessel pressure P B and the counter pressure P F in differential pressure forming step (pressure P B ⁇ pressure P F) is formed, the product solution container Since it is filled, high-speed filling is realized. Moreover, since none of the vessel pressure P B and the counter pressure P F in the differential pressure forming step before filling of the product solution is a positive pressure above atmospheric pressure, without the container collapses through differential pressure forming step and the charging step The shape can be maintained.
- FIG. 3 shows the principle of this invention, (a) shows the example of the one-step filling which completes filling by one differential pressure formation step and a filling step, (b) shows two differential pressure formation steps and a filling step. Shows an example of two-stage filling in which filling is completed. It is a figure which shows the main structures of the filling apparatus which implements the filling apparatus which concerns on 1st Embodiment of this invention. It is a figure which shows the time of the start of the filling operation
- FIG. 4 shows the start of the second filling A, and (b) shows the end of the second filling A.
- the 2nd filling B which uses the auxiliary chamber which concerns on a modification is shown, (a) shows a mode that the volume of the auxiliary chamber was enlarged, (b) shows a mode that the volume of the auxiliary chamber was made small.
- It is a flowchart which shows the procedure of the filling method which concerns on 1st Embodiment. It is a figure which shows an example of the filling part of the filling apparatus which concerns on 1st Embodiment of this invention.
- FIG. 8 shows the operation of filling the product liquid using the filling device of FIG.
- FIG. 12 It is a figure which shows the main structures of the filling apparatus which implements the filling method which concerns on 2nd Embodiment of this invention.
- the operation of the filling device of FIG. 12 is shown, (a) is a differential pressure forming step, and (b) is a filling step.
- the filling device uses the pressure difference between the storage tank 3 in which the product liquid L is stored and the container 100 in which the product liquid L is filled, so that the container 100 is filled in two stages.
- the product liquid L is filled at a high speed by the target filling amount.
- a carbonated beverage is applied as an example of the present invention.
- the filling device of the first embodiment since the inside of the container 100 is set to a positive pressure that is equal to or higher than the atmospheric pressure when filling is started, the shape of the container 100 is maintained even if it is a plastic container 100.
- the filling of the product liquid L can be finished.
- This high-speed filling is hereinafter referred to as a first function.
- the filling device according to the first embodiment immediately attaches and seals the cap 103 without substantially changing the position of the container 100 filled with the product liquid L at high speed.
- the mounting of the cap 103 at this filling position is hereinafter referred to as a second function.
- FIG. 2 shows a minimum unit configuration related to the first function in the filling apparatus 1A.
- the filling device 1 ⁇ / b> A includes a storage tank 3 in which the product liquid L is stored, and a liquid supply path 7 that guides the product liquid L stored in the storage tank 3 to the container 100.
- Carbon dioxide gas CG is stored in the gas phase 3S, which is the space above the product liquid L in the storage tank 3.
- the pressure P F of carbon dioxide gas CG in the gas phase 3S is controlled to a constant pressure above atmospheric corresponding to the characteristics of the product liquid L filling.
- Second pressure sensor 17 is provided to control the pressure P F.
- the product liquid L is controlled so that the container 100 is filled with the liquid and the liquid level in the storage tank 3 is in a fixed position. It referred to as counter pressure below the pressure P F.
- One end side of the liquid supply path 7 is connected to the lower end portion of the storage tank 3, and the other end side of the liquid supply path 7 is provided to face the mouth portion 101 of the container 100.
- the liquid supply path 7 includes a liquid valve VL that opens and closes a flow path through which the product liquid L flows. When the product liquid L is filled, the other end side of the liquid supply path 7 is hermetically sealed from the mouth of the container 100. The same applies to the first gas discharge path 11. Further, FIG.
- the product liquid L is filled into one container 100 from one storage tank 3, but this merely shows the minimum unit of the filling device 1A.
- the product liquid L is filled into a plurality of containers 100 from one storage tank 3.
- the filling device 1 ⁇ / b> A includes the auxiliary chamber tank 5 in which the gas components inside the container 100 are discharged in the process of filling the container 100 with the product liquid L, the auxiliary chamber tank 5, and the container 100.
- the auxiliary chamber tank 5 complements the container of the container 100, and the internal gap forms the pressure adjusting chamber 6, and the carbon dioxide gas CG in the head space 105 of the container 100 is in the second filling A described later. It is discharged into the pressure adjustment chamber 6.
- the volume V R of the pressure adjusting chamber 6 is in a predetermined volume corresponding to the amount to be filled into the container 100 in a second filling A.
- the first gas discharge path 11 corresponds to the downstream flow path of the present invention.
- the pressure regulation chamber 6 can be replaced with one or both of the first gas discharge path 11 and the second gas discharge path 13 having the same volume. That is, the pressure regulation chamber in the present invention has a concept including a pipe having a predetermined volume, such as the first gas discharge path 11 and the second gas discharge path 13.
- the first gas discharge path 11 is provided so that one end side is connected to the auxiliary chamber tank 5 and the other end side faces the container 100.
- the first gas discharge path 11 includes a first gas valve VG1 that opens and closes a flow path through which the carbon dioxide gas CG flows from the container 100. Further, the first gas discharge path 11 may be provided with a throttle between the first gas valve VG1 and the auxiliary chamber tank 5.
- the filling apparatus 1A includes a second gas discharge path 13 that connects the auxiliary chamber tank 5 and the outside of the system.
- the second gas discharge channel 13 includes a second gas valve VG2 that opens and closes a channel through which the carbon dioxide gas CG flows from the auxiliary chamber 5 to the outside of the system.
- Filling device 1A includes a first pressure sensor 15 for detecting the interior of the container 100 of the pressure P B, a second pressure sensor 17 for detecting a counter pressure P F of the gas phase 3S of reservoir 3, the pressure adjusting chamber 6 comprising a third pressure sensor 19 for detecting the pressure P R, the.
- the pressure P B inside the container 100 is the entire pressure of the volume of the container 100 at the time of forming the differential pressure before the product liquid L is filled, and the liquid level of the product liquid L when the product liquid L is filled. This is the pressure of the head space 105 generated further upward. Note that when the product liquid L starts to be filled, the pressure P B increases.
- the first pressure sensor 15 is provided in the first gas discharge path 11 between the first gas valve VG 1 and the container 100.
- the second pressure sensor 17 is connected to the gas phase 3S of the storage tank 3.
- the third pressure sensor 19 is connected to the pressure adjustment chamber 6 of the auxiliary chamber 5.
- the pressure applied to the reservoir 3 and P F the pressure inside the container P B, the volume of the container and V B.
- pressure applied to the reservoir 3 and the counter pressure P F refers to the pressure inside the container and vessel pressure P B, it referred to the pressure of the pressure adjusting chamber 6 and chamber pressure P R.
- the filling device 1 ⁇ / b> A includes a supply / discharge mechanism 40 that controls the supply of product liquid and the supply / exhaust of gas accompanying the storage tank 3.
- the supply / discharge mechanism 40 includes a liquid supply path 41 in which a pump 42 and a liquid control valve 48 are provided.
- the liquid supply path 41 replenishes the storage tank 3 with the product liquid L from a supply source (not shown) by the operation of the pump 42 and the liquid control valve 48.
- the supply / discharge mechanism 40 includes a gas supply path 43 that supplies carbon dioxide CG to the gas phase 3S of the storage tank 3, and a gas discharge path 45 that discharges carbon dioxide CG from the gas phase 3S of the storage tank 3. .
- a gas valve 44 is provided in the gas supply path 43, and a gas valve 46 is provided in the gas discharge path 45.
- the filling device 1A includes a controller 2 that controls opening and closing operations of the liquid valve VL, the first gas valve VG1, and the second gas valve VG2.
- the controller 2 includes a first pressure sensor 15, the sensed vessel pressure P B in the second pressure sensor 17 and the third pressure sensor 19, the counter pressure P F, to obtain a chamber pressure P R, the liquid valve VL ⁇ No.
- the opening / closing operation of the two-gas valve VG2 is controlled. Further, the controller 2 controls the opening / closing operations of the liquid valve VL to the second gas valve VG2 based on the setting conditions necessary for the product liquid L produced by the filling device 1A.
- the controller 2 controls the operation of the pump 42 and the liquid control valve 48 in the liquid supply path 41 so that the liquid level of the product liquid L in the storage tank 3 is at a fixed position. Furthermore, the control unit 2, so that the counter pressure P F is constant, to control the opening and closing of the gas valve 46 of the gas valve 44 and the gas discharge passage 45 of the gas supply passage 43. 3 to 7 described below, the open liquid valve VL to the second gas valve VG2 are shown in white, and the closed liquid valve VL to the second gas valve VG2 are shown in black.
- the filling method according to the first embodiment includes a first filling and a second filling A.
- the product liquid L is filled by the pressure difference into the container 100 which is closed in a state where the inside of the container 100 is replaced with the atmospheric carbon dioxide gas CG, but the product liquid having a set amount smaller than the target filling amount.
- Fill L In the second filling A, the product liquid L is filled into the container 100 so as to compensate for the difference between the target filling amount and the set amount. As shown in FIG.
- the series of steps starts from an initial state in which all of the liquid valve VL, the first gas valve VG1 and the second gas valve VG2 are closed.
- P B , P R atmospheric pressure
- the product liquid L has been added is the counter pressure P F above atmospheric pressure from the gas phase 3S, pressure differential between the interior of the container 100 and the interior of the reservoir 3 Is formed (FIG. 7 First differential pressure forming step S101).
- the gas phase 3S is made of a gas component necessary for maintaining the characteristics of the product liquid L, for example, carbon dioxide.
- FIG. 4A First filling (FIGS. 4A, 4B, 7)]
- the liquid valve VL is opened, and the storage tank 3 and the container 100 are communicated.
- the storage tank 3 whereas a lower pressure environment counter pressure P F is applied above atmospheric, vessel pressure P B is the atmospheric pressure.
- the product liquid L starts to be filled at high speed in a container 100 from reservoir 3 at a flow rate and a flow rate corresponding to the pressure difference between the counter pressure P F and vessel pressure P B (atmospheric pressure) (Fig. 7 first filling step S103) .
- the container pressure P B rises. If a set pressure is provided for the container pressure P B , the container 100 is filled with the product liquid L by a set amount corresponding to the set pressure.
- the pressure of the first gas outlet passage 11 is continuously detected by the first pressure sensor 15.
- the pressure detected by the first pressure sensor 15 is the container pressure P B in the head space 105 of the container 100.
- the liquid valve VL is closed and the filling of the product liquid L is stopped as shown in FIG.
- the first filling is completed, and a set amount of product liquid is filled.
- the carbon dioxide gas CG contained in the container 100 is charged while being confined in the container 100, so that the container pressure P B increases.
- the maximum limit set pressure P1 is a pressure counter pressure P F and the container 100 that is added to the storage tank 3 is balanced.
- a maximum pressure set pressure P1 and the counter pressure P F it is possible to a maximum pressure set pressure P1 and the counter pressure P F.
- vessel pressure P B for to rise to a high counter pressure P F than atmospheric pressure chamber pressure P R of the pressure adjusting chamber 6 remains at atmospheric pressure.
- the liquid valve VL is closed based on the set pressure P1, but the first embodiment is not limited to this.
- a set time T1 related to the time to reach the set pressure P1 can be experimentally obtained in advance, and the liquid valve VL can be closed based on the set time T1 related to this time.
- the set time T1 does not need to completely match the experimentally obtained value.
- a set time T1 shorter than the experimental value can be set for the purpose of shortening the filling time, and a set time T1 longer than the experimental value can be set for the purpose of stabilizing the state of the product liquid L. The same applies to the second filling A.
- the first loading to Q 1 to the container 100 in the first filling is obtained by the following equation (1).
- the first charge Q 1 is assumes that the vessel pressure P B becomes in equilibrium with the counter pressure P F of the reservoir 3.
- the volume V H of the head space 105 of the container 100 after being filled with the product liquid L by the first filling amount Q 1 is obtained by the following equation (2).
- Pressure adjusting chamber 6 of the auxiliary chamber vessel 5 as an example is made as the target filling amount Q and the first loading to Q 1 difference and its volume V R match. Equations (1) and (2) are based on Boyle's law, and the same applies to equations (3) to (7) described later.
- the counter pressure P F 5 atmospheres in the gas phase 3S positive pressure
- the 1 atm vessel pressure P B atmospheric pressure
- the first filling amount Q 1 and the head space volume V H1 are as follows, and the product liquid L is filled by an amount corresponding to 4/5 of the volume V B of the container 100 in the first filling, so that the remaining An amount corresponding to Q-4 / 5 ⁇ V B of the second filling A needs to be filled.
- An amount corresponding to the remaining Q-4/5 ⁇ V B is, corresponds to the second charge Q 2 is a differential needed to target filling amount, which is scheduled to the container 100.
- the container pressure P B needs to be less than the pressure resistance of the container 100.
- the container pressure P B after the first filling with the product liquid L is to satisfy the following formula (3).
- Counter pressure P F is 5 atmospheres in the gas phase 3S (positive pressure)
- the initial vessel pressure P B of the container 100 is 1 atm (atmospheric pressure)
- the vessel pressure after completion of the first filling a container 100 P B is is a 5 atm as the counter pressure P F and equilibrium. Therefore, the pressure resistance P P of the container 100 required for this first filling is 5 atmospheres.
- P P > P B V B / (V B -Q 1 ) (3)
- the second filling A After the first filling, the second filling A is performed.
- the second filling A performs only the filling of the product liquid L amount of the difference between the desired charge amount Q and the first charge Q 1.
- the second filling A opens the first gas valve VG1.
- the first gas valve VG1 and the liquid valve VL may be opened simultaneously, or the first gas valve VG1 may be opened in advance.
- the pressure adjustment chamber 6 receives the discharge of the carbon dioxide gas CG filling the head space 105, and it can be considered that the volume of the container 100 is increased by the pressure adjustment chamber 6. That is, the pressure adjusting chamber 6 constitutes an auxiliary chamber that functions as a part of the container 100 from the viewpoint of forming the second differential pressure.
- the product liquid L is filled from the storage tank 3 into the container 100 at a flow rate and a flow rate corresponding to the pressure difference (FIG. 7, second filling step S107). .
- the amount filled at this time corresponds to the difference.
- the amount of the product liquid L filled after the second filling A that is, the target filling amount Q is obtained by the following equation (4).
- the head space volume V H2 of the head space 105 of the container 100 after being filled with the product liquid L satisfying the target filling amount Q is obtained by the following equation (5).
- Target filling amount Q (1 ⁇ P B / P F ) ⁇ (V B + V R ) (4)
- Head space volume V H2 P B / P F ⁇ (V B + V R ) ⁇ V R Formula (5)
- the pressure of the first gas discharge path 11 is continuously detected by the first pressure sensor 15.
- the liquid valve VL and the first gas valve VG1 are closed as shown in FIG. 5B. This completes the second filling A, and the container 100 is filled with the product liquid L that satisfies the target filling amount Q.
- the set pressure P1 is a pressure necessary to fill the difference.
- the first embodiment can arbitrarily change the volume of the auxiliary chamber tank 5.
- the volume of the auxiliary chamber tank 5 it is necessary to change the amount of the product liquid L filled with the second filling A according to the type of the container 100. Therefore, by making the internal volume of the auxiliary chamber tank 5 arbitrarily variable, the filling amount corresponding to the type of the container 100 can be realized.
- the auxiliary chamber tank 5 may be a piston-cylinder mechanism. That is, the auxiliary chamber tank 5 is composed of a piston 5A and a cylinder 5B in which the piston 5A advances and retreats.
- the second filling performed using the auxiliary chamber 5 is referred to as a second filling B.
- the second charge Q 2 is large in the second filling B, as shown in FIG. 6 (a), to increase the volume V A which is formed by the piston 5A and the cylinder 5B by retracting the piston 5A.
- a small filling amount Q 2 of the second filling B as shown in FIG. 6 (b)
- the volume of the auxiliary chamber tank 5 can be arbitrarily changed by changing the relative position of the piston 5A with respect to the cylinder 5B.
- auxiliary chamber tank 5 having a fixed volume Even when the auxiliary chamber tank 5 having a fixed volume is used, a plurality of types of auxiliary chamber tanks 5 having different volumes according to the type of the container 100 are prepared, and the auxiliary chamber used depending on the type of the container 100 is used. The tank 5 can also be replaced. However, the use of the auxiliary chamber tank 5 having a variable internal volume is much less burdensome than the replacement of the auxiliary chamber tank 5.
- the first embodiment, the first packing and second packing A product solution L when starting the B, the counter pressure P F of the storage tank 3 is set higher than the vessel pressure P B. Therefore, according to 1st Embodiment, since the product liquid L is sent out to the container 100 using this pressure difference, the product liquid L can be filled into the container 100 at high speed.
- the first embodiment performs the two-stage filling including the first filling and the second filling A and B, the product liquid L in an amount satisfying the target filling amount Q can be reliably filled into the container 100.
- the pressure is instantaneously released, so that the carbon dioxide gas CG appears as bubbles.
- the foam from the vessel pressure P B at the completion of filling, in addition to a fine is a counter pressure P F, the foam disappears then redissolved immediately in the product solution. Therefore, according to the first embodiment, after passing through the first filling and the second filling A and B, the operation of mounting the sealing material 103 on the container 100 can be started quickly. This is realized as a second function of the first embodiment.
- the interior of the container 100 is replaced with a predetermined concentration of carbon dioxide gas CG prior to the first filling.
- 1st Embodiment can keep the density
- the filling apparatus 1 ⁇ / b> A includes a sealed chamber 20 having a sealed chamber 21 that is kept airtight with respect to the outside.
- a gas supply source (not shown) and a gas supply path 28 are connected to the sealed chamber 20, and a gas discharge path 29 is connected to the sealed chamber 20.
- the gas component in the sealed chamber 20 is substantially equal to the container pressure P B. Pressurized and held at pressure. 8 and 9, the gas supply path 28 and the gas discharge path 29 are open if the valve is white, and are closed if the valve is black.
- liquid supply path 7 and the first gas discharge path 11 are connected to the sealed chamber 20 so as to be able to advance and retreat in synchronization.
- the liquid supply path 7 and the first gas outlet path 11 are incorporated in a double-pipe structure 22 in which the liquid supply path 7 is provided on the inner side and the first gas outlet path 11 is provided on the outer side.
- the double-pipe structure 22 reciprocates between a standby position shown in FIG. 9 (d) and an operating position shown in FIGS. 9 (a) to 9 (c).
- a nozzle 25 is provided at the tip of the double tube structure 22. When filling the product liquid L, the nozzle 25 is pressed against the mouth portion 101 of the container 100 as shown in FIGS.
- the pressed portion is brought into close contact with the mouth portion 101 to seal the inside and outside of the container 100.
- the nozzle 25 is provided so as to be movable up and down between a standby position indicated by a solid line and an operation position indicated by an imaginary line in FIG.
- the product liquid L in the storage tank 3 is drawn into the sealed chamber 20 through the liquid supply path 7 and filled in the container 100.
- the first gas valve VG 1 when the first gas valve VG 1 is opened, the carbon dioxide gas CG in the head space 105 of the container 100 goes to the auxiliary chamber 5 through the first gas discharge path 11.
- the sealed chamber 20 includes a container holding opening 27 into which the mouth portion 101 of the container 100 is inserted when the container 100 is filled with the product liquid L.
- the container holding opening 27 penetrates the sealed chamber 20 and communicates the sealed chamber 21 with the outside.
- the container holding opening 27 has an opening diameter larger than the outer diameter of the sealing material 103 attached to the mouth portion 101. Even when the sealing material 103 is attached to the mouth portion 101 of the container 100, the mouth portion 101 of the container 100 is held by the container holding opening 27.
- a sealing member (not shown) is provided around the container holding opening 27 in order to keep the sealed chamber 21 airtight with respect to the outside while the mouth portion 101 is held in the container holding opening 27.
- a sealing head 30 as a sealing machine is provided in the sealed chamber 20 so as to be movable up and down.
- the sealing head 330 moves up and down between the standby position (FIGS. 8 and 9A) and the operation position (FIG. 9D) while holding the sealing material 103 at the tip (lower end in the drawing).
- the sealing head 30 moves from the operating position to the standby position after a new sealing material 103 is replenished and held after the sealing material 103 is attached to the mouth portion 101.
- the pressure of the carbon dioxide gas in the sealed chamber replaced at this time is supplied so as to coincide with the counter pressure P F (container pressure P B ) added to the storage tank 3.
- the carbon dioxide gas as a gas component added from the gas supply path 28 may be supplied from a gas supply source other than the storage tank 3.
- the container 100 is supported by the mouth portion 101 by a gripper called a gripper, and by applying a load toward the sealed chamber 20 to the gripper, the mouth portion 101 is hermetically sealed to the sealed chamber 20. Can be pressed.
- the liquid valve VL is opened in accordance with the first filling procedure described above. Then, the product liquid L is filled into the container 100 by the filling amount Q 1 through the liquid supply path 7. Thereafter, when the first gas valve VG1 is opened, the carbon dioxide gas CG filling the head space 105 of the container 100 is discharged toward the auxiliary chamber tank 5 through the first gas discharge path 11.
- the second filling A is performed after the second differential pressure is formed by the above-described procedure. Also in the second filling A, the double pipe structure 22 remains in the first filling state, and the liquid valve VL and the first gas valve VG1 are opened according to the procedure of the second filling A described above.
- the product liquid L is filled into the container 100 through the liquid supply path 7, and the product liquid L in an amount that satisfies the target filling amount Q is filled into the container 100.
- the carbon dioxide gas CG that fills the head space 105 travels through the first gas outlet path 11 toward the auxiliary chamber tank 5.
- the sealing material 103 attached to the container 100 to be filled with the subsequent product liquid L is loaded into the container holding opening 27 and replenished to the waiting sealing head 30.
- the sealing head 30 supplemented with the sealing material 103 moves backward to the standby position for the next filling operation.
- the sealing head 30 is incorporated in the sealed chamber 20 filled with the product liquid L, and the sealing material 103 can be attached to the container 100 without the movement of the container 100 filled with the product liquid L. Therefore, since the sealing material 103 can be quickly attached to the container 100 filled with the product liquid L, the beverage product can be manufactured in a short time in combination with the filling performed at high speed.
- the first embodiment of the present invention has been described above, the configuration described in the first embodiment can be selected or replaced with another configuration without departing from the gist of the present invention.
- the first embodiment employs a volume control system in which the volume of the pressure regulation chamber 6 is matched to the differential filling amount in the second filling A, but the present invention is not limited to this, and the differential filling amount in the second filling A.
- Other methods that can be filled can be adopted.
- the second filling C and the second filling D both of which use the auxiliary chamber tank 5, but the volume of the pressure regulating chamber 6 is set in advance to the amount filled in the container 100 in the second filling. There is no need to specify.
- the second filling C and the second filling D will be described in this order with reference to FIGS. 10 and 11. It is to be noted that the first filling is carried out by the same procedure as the second filling A, also, the vessel pressure P B and the auxiliary chamber pressure P R before the gas replacement is started and the atmospheric pressure.
- the second filling C first opens the first gas valve VG1. Then, since the carbon dioxide gas CG filled in the head space 105 of the container 100 is led out to the auxiliary chamber tank 5, a pressure difference is generated between the head space 105 and the gas phase 3S.
- vessel pressure P B and chamber pressure P R is the mean pressure by the sum of the vessel head space and Hoshitsu capacity. As a result, the counter pressure P F and the pressure differential is formed.
- the third pressure sensor 19 is continuously detected a chamber pressure P R of the pressure adjusting chamber 6.
- the liquid valve VL is opened. Then, the product liquid L is filled into the container 100 from the storage tank 3, but the carbon dioxide gas CG that fills the head space 105 of the container 100 gradually increases as the filling amount increases and the entrance line rises. It leads to the tank 5. Thus, chamber pressure P R of the pressure adjusting chamber 6 is raised.
- the control unit 2 is compared to a predetermined set pressure P B 'together with the first pressure sensor 15 or the third pressure sensor 19 acquires the room pressure P R which has detected.
- the control unit 2 if chamber pressure P R is increased to the set pressure P B ', recognized as the filling of product liquid L deficient in the first filling has been finished, as shown in FIG. 10 (c),
- the first gas valve VG1 is closed first, and then the liquid valve VL is closed.
- the product liquid L corresponding to the pressure difference is filled up to the target filling amount, and the second filling is completed.
- Second filling amount Q 2 V H1 ⁇ (1 ⁇ P R / PB B ′) + V R ⁇ (1 ⁇ P R / PB B ′) Formula (6)
- Target filling amount Q Q 1 + Q 2 (7)
- the second gas valve VG2 is opened while the first gas valve VG1 is kept open. Then, since the carbon dioxide gas CG meet the auxiliary chamber tank 5 is derived out of the system through the second gas outlet passage 13, the chamber pressure P R decreases. Note that the second gas valve VG2 does not open all of the flow paths but partially opens so that a small amount of carbon dioxide gas CG is derived. After the carbon dioxide gas CG is derived at a constant flow rate through the restriction, the head space 105 of the container 100 and the indoor pressure Pr of the auxiliary chamber tank 5 are kept constant until the difference from the target amount is filled. The liquid valve VL and the second gas valve GV2 are closed.
- the control unit 2 is compared to a predetermined set pressure P B 'together with the third pressure sensor 19 acquires the room pressure P R which has detected.
- the control unit 2 if chamber pressure P R is reduced to the set pressure P B ', as shown in FIG. 11 (c), first, closing the second gas valve VG2.
- a pressure difference can be provided between the gas phase 3 ⁇ / b> S of the storage tank 3 and the head space 105 of the container 100.
- the liquid valve VL is opened.
- the product liquid L corresponding to the pressure difference is filled up to the target filling amount Q, and the second filling D is completed.
- the filling amount of the product liquid L in the second filling D can be calculated in the same manner as the second filling C except that the carbon dioxide gas CG discharged outside the system is taken into account.
- the second filling C and the second filling D make up for the difference filling amount based on the pressure detected in the pressure regulating chamber 6, so it is necessary to specify the volume of the pressure regulating chamber 6 in advance. Absent. However, the pressure regulation chamber 6 needs to have a volume exceeding the difference filling amount.
- the second embodiment relates to one-stage filling in which filling is performed in an amount that satisfies the target filling amount Q by a single filling cycle.
- the container 100 is filled with the target filling amount of the product liquid L by forming the pressure difference once and filling the product liquid L.
- the second embodiment will be described with reference to FIGS. In the following, description will be made centering on differences from the first embodiment.
- the filling apparatus 1B of the second embodiment is configured to discharge a third gas as an alternative to the first gas discharge path 11 to the second gas discharge path 13 provided in the filling apparatus 1A of the first embodiment.
- a path 14 is provided.
- the third gas discharge path 14 is hermetically connected to the container 100.
- the third gas discharge path 14 is provided with a third gas valve VG3, which has a configuration in which the auxiliary chamber tank 5 (pressure adjustment chamber 6) is removed from the first gas discharge path 11 in the first embodiment. Can be considered.
- a cleaning liquid return piping circuit in a CIP (Cleaning In Place) apparatus included in the beverage filling apparatus can be used.
- one-stage filling can also be performed by the filling device 1A including the first gas discharge path 11 to the second gas valve VG2.
- the functions of the first gas discharge path 11 to the second gas valve VG2 are not used, but the filling device 1A is a device for both single-stage filling and multiple-stage filling.
- the filling device 1 ⁇ / b> B positively gives a function as a part of the volume of the container 100 to the void inside the third gas discharge path 14 connecting the container 100 and the third gas valve VG ⁇ b> 3. That is, in FIG. 12, closing the third gas valve VG3, than the container 100 of the third gas valve VG3 side, i.e. the interior of the third gas discharge passage 14 on the downstream side of the container 100 an auxiliary chamber volume V B3 It becomes a void having. As will be described below, this gap corresponds to the first auxiliary chamber volume in the present invention.
- the auxiliary chamber volume V B3 of the third gas discharge passage 14 between the container 100 and the third gas valve VG3 is set so that the filling amount Q1 matches the target filling amount Q.
- the product liquid L can be filled into the container 100 by the target filling amount Q only by one-stage filling.
- the auxiliary chamber volume V B3 is set so that the filling amount Q1 exceeds the target filling amount Q, and the opening and closing of the liquid valve VL is controlled.
- the container 100 can be filled with the product liquid L that satisfies the target filling amount Q.
- vessel pressure P B in the head space 105 of the container 100 to the counter pressure P F which is added to the storage tank 3 is continued filling until the equilibrium.
- the counter pressure P F and vessel pressure P B respectively 5 atm similarly to the first embodiment (positive pressure), and 1 atm (atmospheric pressure).
- the volume V B1 of the container 100 is set to 520 ml, and the target filling amount Q is set to 500 ml.
- the target filling amount Q is set to 500 ml.
- V B2 (500-416)
- ⁇ 4/5 105 (ml)
- case 2 in which two-stage filling is required is shown with respect to the above-described case 1 which is an example in which the target filling amount can be filled in one stage filling.
- the auxiliary chamber volume V B3 is the same as that in case 1 (105 ml).
- the pressure and filling amount in the container after filling with the product liquid L was determined based on the differential pressure.
- the results are as follows. If Case 1 has a small volume of 500 ml, the target filling amount Q can be satisfied by one-stage filling. On the other hand, in case 2 where the capacity of the container is as large as 1000 ml, the target filling amount Q cannot be satisfied by one-stage filling. Furthermore, assuming that the filling so as to satisfy the target filling amount Q in one stage filling, vessel pressure P B after filling may exceed the pressure resistance P P of the container 100. Therefore, for the case 2, it is necessary to adopt multi-stage filling, for example, two-stage filling.
- a dedicated filling device that performs single-stage filling and a dedicated filling device that performs multiple-stage filling can also be prepared.
- the filling device dedicated to single-stage filling may become empty. Therefore, it is preferable for a beverage manufacturer to have a filling device that can perform both single-stage filling and multiple-stage filling. If a necessary configuration is added to the filling device 1A shown in the first embodiment, single-stage filling and multi-stage filling can be realized individually.
- the controller 2 (FIG. 2) mainly has a configuration that needs to be added.
- the controller 2 specifies the type of container to be produced. This type has the concept of including volume.
- the controller 2 prompts the operator of the filling apparatus 1A to input the container type.
- the controller 2 specifies the type of container by receiving input from the operator to the controller 2.
- a production plan for a predetermined period, for example, one week is input to the controller 2. If this production plan includes the type of container, the controller 2 can specify the type of container for one week.
- the controller 2 determines whether to perform one-stage filling or two-stage filling according to the type (size) of the container.
- the controller 2 preferably includes container-filling stage number information in which the type of container and the number of filling stages are associated with each other.
- the controller 2 selects either one-stage filling or two-stage filling with reference to this container-filling stage number information. Although only two-stage filling will be described here, filling with a larger number of stages such as three or four stages may be selected.
- the controller 2 controls the operation of the first gas valve VG1, the second gas valve VG2, and the liquid valve VL so that the single-stage filling or the two-stage filling can be realized when the single-stage filling or the two-stage filling is selected.
- the operation of one-stage filling is as described in the second embodiment, and the operation of two-stage filling is as described in the first embodiment.
- the present invention has been described above, but various modifications can be made without departing from the spirit of the present invention.
- the present invention can also be applied to beverages that do not contain carbonic acid and other product liquids.
- the gas replacement described above is intended for a carbonated beverage, carbon dioxide is used.
- the gas replacement gas in the present invention is not limited to the carbon dioxide gas, and can be replaced with a gas component necessary for maintaining the characteristics of the product liquid filled in the container, for example, an inert gas such as nitrogen gas.
- the container 100 described in the present embodiment is made of resin, but in the present invention, the object of filling is not limited to the resin container, but is applicable to other flexible containers, for example, metal can containers. it can. In addition, the present invention does not exclude, for example, glass bottles that are not flexible from being filled.
- the one-stage filling is not limited to the method of the second embodiment.
- the condition that the pressure difference between the inside of the container 100 and the gas phase 3S of the storage tank 3 is sufficiently large and the head space 105 of the container 100 when the product liquid L reaches the target filling amount is satisfied.
- one-stage filling may be realized.
- One-stage filling can also be realized by positively providing the liquid supply path 7 connecting the storage tank 3 and the container 100 as a part of the volume of the container 100. That is, in FIG. 12, when the liquid valve VL is closed, the product liquid L is filled between the storage tank 3 and the liquid valve VL, but the inside of the container 100 side of the liquid valve VL has a volume V B2. Make.
- This gap corresponds to the second auxiliary chamber volume of the present invention provided between the liquid valve VL and the container 100.
- the auxiliary chamber volume V B2 is assumed to be zero, that is, the second auxiliary chamber volume does not exist.
Landscapes
- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
Abstract
The present invention provides a filling device that can quickly fill even a flexible container with a carbonated product liquid, while maintaining the shape of the container. This filling device 1A is provided with a storage tank 3 in which a product liquid L is stored in a high-pressure atmosphere that has been brought to a pressure PF and a liquid supply path 7 through which the product liquid L is supplied to a container 100 from the storage tank. The interior of the filling device 1A is at or above atmospheric pressure, and the product liquid L is supplied via the liquid supply path 7 to the container 100, which has been brought to a pressure PB that is lower than that of the pressurized atmosphere in the storage tank, which has been brought to the pressure PF. The container 100 is filled with the product liquid L via the liquid supply path 7 until the pressure PB reaches an equilibrium with the pressure PF or reaches a prescribed pressure below the equilibrium pressure.
Description
本発明は、可撓性の容器に炭酸入りの飲料を充填するのに好適な充填装置に関する。
The present invention relates to a filling device suitable for filling a flexible container with a carbonated beverage.
従来、炭酸入りの飲料を容器に充填する方法として、例えば特許文献1に開示されるカウンタープレッシャー方式が一般的であった。
カウンタープレッシャー方式は充填に要する時間が長くかかることから、近年、特許文献2、特許文献3に開示されるように、あらかじめ内部を負圧にしている容器に、貯留槽において加圧されている炭酸入りの製品液を一気に注入させる方法が提案されている。この充填は、炭酸入りの製品液を容器に噴出させながら、容器の内部の圧力上昇の継時変化を監視することで充填量を制御する。
Conventionally, as a method of filling a container with a carbonated beverage, for example, a counter pressure system disclosed in Patent Document 1 has been common.
Since the counter pressure system takes a long time to fill, in recent years, as disclosed in
特許文献2,3によるプリエバキュエーション方式による充填は、容器と貯液槽の間の圧力差を利用して製品液を充填するので、カウンタープレッシャー方式に比べて極めて高速で製品液を充填することができる。
In the pre-evacuation method according to
以上のように、特許文献2,3による充填は、炭酸入りの製品液を短時間で容器に充填することができるが、対象となる容器に制限がある。つまり、プリエバキュエーション方式は、製品液の充填に先立って容器の内部を負圧にすることが必要であることから、ガラスびんのように剛性を有する容器にしか適用できない。例えば、可撓性を有するプラスチック製容器に特許文献2,3によるプリエバキュエーション方式を適用すると、プラスチック製容器は負圧に耐えられずに潰れてしまう。
As described above, the filling according to
そこで本発明は、可撓性の容器であってもその形状を維持したままで炭酸入りの製品液を高速で充填できる充填装置を提供することを目的とする。
Accordingly, an object of the present invention is to provide a filling device capable of filling a product liquid containing carbonic acid at a high speed while maintaining the shape of a flexible container.
はじめに、図1を参照して、本発明の充填装置における基本的な原理を説明する。
図1(a)に示すように、容器の内部の圧力(容器圧力)PBと貯留槽に付加される圧力(カウンタ)PFとの間に予め圧力PB3に相当する圧力差が形成されているものとする。当初の容器圧力PBは例えば大気圧であり、カウンタ圧力PFは取り扱う製品液に必要な大気圧より高い圧力である。
図1(a)において、容器圧力PBが所定の設定圧力PB1になるまで製品液を充填するとQ11だけの量を容器に充填できる。この設定圧力PB1は圧力PB3と平衡になる圧力未満の圧力である。同様に、容器圧力PBが貯留槽と平衡になる圧力PB3になるまで製品液を充填するとQ13だけの量を容器に充填できる。この充填量Q13は、それぞれ一回の差圧形成と充填、つまり一段充填により容器に充填できる最大の量(Qmax)である。
一方で、容器が可撓性を有していても、容器圧力PBが大気圧以上の正圧であれば、容器がつぶれることはない。
First, the basic principle of the filling apparatus of the present invention will be described with reference to FIG.
As shown in FIG. 1 (a), a pressure difference corresponding to a pre-pressure P B3 between the pressure (counter) P F to be added to the internal pressure (vessel pressure) P B of the container reservoir is formed It shall be. Originally vessel pressure P B is, for example atmospheric pressure, counter pressure P F is the pressure higher than the atmospheric pressure required for the product fluid handling.
In FIG. 1 (a), it can be filled with an amount of only Q 11 when filling the product solution into the container until the container pressure P B becomes a predetermined set pressure P B1. The set pressure P B1 is a pressure lower than the pressure that is in equilibrium with the pressure P B3 . Similarly, it can be filled with an amount of only Q 13 when filling the product solution in the container to a pressure P B3 the vessel pressure P B becomes in equilibrium with the reservoir. The filling amount Q 13 is filled with a single differential pressure respectively, that is the maximum amount that can be filled in a container by one-stage filling (Qmax).
On the other hand, even if the container has flexibility, if the container pressure P B is a positive pressure equal to or higher than atmospheric pressure, the container will not be crushed.
以上が本発明の原理であるが、容器の容積、容器圧力PBおよびカウンタ圧力PFなどの条件によっては、一段充填で、目標とする量の製品液を充填できないことがある。このような場合には、差圧形成と充填を複数回繰り返せばよい。図1(b)は、差圧形成、充填を二回繰り返す二段充填の例を示している。
予め圧力差が形成されている状態(第一差圧形成)から、容器圧力PBがカウンタ圧力PFと平衡になるまで製品液の充填(第一充填)を行うとQ21の量だけ充填される。しかし、これでは目標充填量Q(=Q21+Q22)には達しない。そこで、また容器と貯留槽の間に圧力差(第二差圧形成)を設けてから、目標充填量Qとの差分(Q22)だけ製品液の充填(第二充填)を行う。
第二差圧は、容器圧力PBを大気圧まで下げて行うことができるし、大気圧を超える圧力まで下げて行うこともできる。
Above it is the principle of the present invention, the volume of the container, depending on the conditions such as the vessel pressure P B and the counter pressure P F, at one stage filling, it may not be possible to fill the amount of product liquid to be targeted. In such a case, the differential pressure formation and filling may be repeated a plurality of times. FIG. 1B shows an example of two-stage filling in which differential pressure formation and filling are repeated twice.
From the state advance pressure differential is formed (first differential pressure forming), an amount of the case of filling with the product solution to vessel pressure P B is in equilibrium with the counter pressure P F (first filling) Q 21 Filling Is done. However, this does not reach the target filling amount Q (= Q 21 + Q 22 ). Therefore, after providing a pressure difference (second differential pressure formation) between the container and the storage tank, the product liquid is filled (second filling) by the difference (Q 22 ) from the target filling amount Q.
The second differential pressure can be performed by lowering the container pressure P B to atmospheric pressure, or can be performed by lowering the pressure to exceed atmospheric pressure.
以上の原理に基づく本発明の充填装置は、カウンタ圧力PFが付加された環境下で製品液が貯えられる貯留槽と、貯留槽から製品液を容器に充填する液供給路と、開閉することにより、液供給路からの製品液の供給を制御する液弁を有する充填ノズルと、を備える。
本発明の充填装置において、容器内の圧力PBが、大気圧以上の正圧であって、かつ、貯留槽におけるカウンタ圧力PFより低い圧力に保たれ、貯留槽の前記カウンタ圧力PFとの間に圧力差が形成された状態で、容器と前記充填ノズルとを密封状態に係合させ、次いで、液弁を開き、製品液が前記容器に充填される。
Filling device of the present invention based on the principle described above, a storage tank where the product solution is stored under a counter pressure P F is added environment, a liquid supply path for filling the product solution into the container from the reservoir, opening and closing And a filling nozzle having a liquid valve for controlling the supply of the product liquid from the liquid supply path.
In the filling apparatus of the present invention, the pressure P B in the container, a positive pressure above atmospheric pressure, and maintained at a pressure lower than the counter pressure P F in the reservoir, and the counter pressure P F of the reservoir With the pressure difference formed between the container and the filling nozzle, the container and the filling nozzle are engaged in a sealed state, and then the liquid valve is opened to fill the container with the product liquid.
本発明の充填装置において、好ましくは、容器圧力PBがカウンタ圧力PFと平衡になるまで、または、カウンタ圧力PF未満の所定の圧力の状態になるまで、製品液が充填されると液弁が閉じられる。
In the filling apparatus of the present invention, preferably, until the vessel pressure P B is in equilibrium with the counter pressure P F, or until the state of a predetermined pressure below the counter pressure P F, the product solution is filled a liquid The valve is closed.
本発明の充填装置は、好ましくは、容器に連通することで、容器の容積の補完する補室を備える。
本発明における補室は、二つに区分できる。一つ目の補室は、容器から排出されるガス成分を導出させるガス導出路上に設けられる補室槽からなる。二つ目の補室は、容器から排出されるガス成分を導出するガス導出路の内部の空隙からなる第一補室容積か、および、液弁と容器の間における液供給路の内部の空隙からなる第二補室容積の一方または双方からなる。
The filling device of the present invention preferably includes a supplementary chamber that is in communication with the container to complement the volume of the container.
The auxiliary room in the present invention can be divided into two. The first auxiliary chamber is composed of an auxiliary chamber tank provided on a gas lead-out path for deriving a gas component discharged from the container. The second auxiliary chamber is a first auxiliary chamber volume consisting of a gap inside the gas outlet path for leading the gas component discharged from the container, and a gap inside the liquid supply path between the liquid valve and the container. Consisting of one or both of the second auxiliary chamber volume.
本発明における補室槽を備える充填装置は、好ましくは、ガス導出路を開閉する第一ガス弁を備える。
この充填装置は、液弁が開いた状態において、容器の内部のガス成分を外部に排出することなく、容器の内部のガス成分を密閉したままで、製品液が容器に充填される。
また、設定量の製品液が充填されると、第一ガス弁を開いて、ガス成分の一部がガス導出路を通って補室槽に導出される。
The filling device including the auxiliary chamber tank in the present invention preferably includes a first gas valve that opens and closes the gas outlet passage.
This filling device fills the container with the product liquid while keeping the gas component inside the container sealed without discharging the gas component inside the container to the outside with the liquid valve opened.
When the set amount of product liquid is filled, the first gas valve is opened, and a part of the gas component is led out to the auxiliary chamber tank through the gas lead-out path.
本発明における補室槽を備える充填装置は、好ましくは、容器圧力PBがカウンタ圧力PFと平衡になるまで、または、容器圧力PBが設定圧力に達するまで製品液が容器に充填される。
次いで、容器圧力PBと補室槽の圧力PRが平衡になるまで、ガス成分が補室槽に排出される。
この充填装置は、ガス成分が補室槽に導出されることで、容器圧力PBはカウンタ圧力PFより低い圧力差が形成される。次いで、液弁を開いた状態で、目標充填量との差分に対応する量の製品液が容器に充填される。
Filling apparatus comprising the auxiliary chamber vessel of the present invention is preferably filled up vessel pressure P B is in equilibrium with the counter pressure P F, or the product liquid in the container until the container pressure P B reaches the set pressure .
Then, the vessel pressure P B to a pressure P R of the auxiliary chamber tank is balanced, gas component is discharged to the auxiliary chamber tank.
The filling apparatus, by the gas component is led to the auxiliary chamber tank, vessel pressure P B is less pressure difference from the counter pressure P F is formed. Next, with the liquid valve opened, the container is filled with an amount of product liquid corresponding to the difference from the target filling amount.
本発明における補室槽は、好ましくは、内容積が可変の構造を有している。
また、本発明における補室槽は、好ましくは、目標充填量との差分に対応する容積を有する。
The auxiliary chamber tank in the present invention preferably has a structure with a variable internal volume.
Moreover, the auxiliary chamber tank in the present invention preferably has a volume corresponding to the difference from the target filling amount.
本発明における第一補室容積または第二補室容積を備える充填装置において、液弁が閉じた状態で、第一補室容積または第二補室容積と容器の内部とが連通して形成される空間における容器圧力PBとカウンタ圧力PFとの間に圧力差が形成される。
In the filling apparatus having the first auxiliary chamber volume or the second auxiliary chamber volume in the present invention, the first auxiliary chamber volume or the second auxiliary chamber volume and the interior of the container are formed in communication with the liquid valve closed. that the pressure differential between the vessel pressure P B and the counter pressure P F in the space is formed.
本発明における第一補室容積または第二補室容積は、好ましくは、一度の圧力差の形成および製品液の充填を通じて、目標充填量を満たす製品液の充填をするのに足りる容積を有する。
圧力差が形成された後には、容器圧力PBがカウンタ圧力PFと平衡になるまで、または、容器圧力PBが設定圧力に達するまで製品液が容器に充填される。
本発明における第一補室容積または第二補室容積は、好ましくは、目標充填量との差分に対応する容積を有する。
The first auxiliary chamber volume or the second auxiliary chamber volume in the present invention preferably has a volume sufficient to fill the product liquid that satisfies the target filling amount through the formation of a single pressure difference and the filling of the product liquid.
After the pressure difference has been formed, until the vessel pressure P B is in equilibrium with the counter pressure P F, or the product liquid is filled into the container until the container pressure P B reaches a set pressure.
The first auxiliary chamber volume or the second auxiliary chamber volume in the present invention preferably has a volume corresponding to the difference from the target filling amount.
本発明の充填装置によれば、差圧形成ステップで容器圧力PBとカウンタ圧力PFの間に差圧(圧力PB<圧力PF)が形成されている状態で、容器に製品液が充填されるので、高速な充填が実現される。しかも、製品液の充填前における差圧形成ステップにおける容器圧力PBおよびカウンタ圧力PFのいずれもが大気圧以上の正圧であるから、差圧形成ステップおよび充填ステップを通じて容器が潰れることがなくその形状を維持できる。
According to a filling device of the present invention, in a state where the differential pressure between the vessel pressure P B and the counter pressure P F in differential pressure forming step (pressure P B <pressure P F) is formed, the product solution container Since it is filled, high-speed filling is realized. Moreover, since none of the vessel pressure P B and the counter pressure P F in the differential pressure forming step before filling of the product solution is a positive pressure above atmospheric pressure, without the container collapses through differential pressure forming step and the charging step The shape can be maintained.
[第1実施形態]
以下、図2~図11を参照して本発明の第1実施形態に係る充填装置を説明する。
第1実施形態に係る充填装置は、製品液Lが貯えられている貯留槽3と製品液Lが充填される容器100との間の圧力差を利用することで、二段充填により容器100に目標充填量だけ製品液Lを高速で充填する。この製品液Lは本発明の一例として炭酸飲料が適用される。第1実施形態の充填装置は、充填を開始する時点で、容器100の内部は大気圧以上の正圧とされているために、プラスチック製の容器100であってもその形状を維持したままで製品液Lの充填を終えることができる。この高速充填のことを、以下では第一機能という。
また、第1実施形態に係る充填装置は、高速で製品液Lが充填された容器100の位置を実質的に変えることなく、即座にキャップ103を装着して封緘する。この充填位置におけるキャップ103の装着のことを、以下では第二機能という。
[First Embodiment]
Hereinafter, the filling apparatus according to the first embodiment of the present invention will be described with reference to FIGS.
The filling device according to the first embodiment uses the pressure difference between the
The filling device according to the first embodiment immediately attaches and seals the
[第一機能の構成要素]
図2~図6を参照して、第1実施形態に係る第一機能を説明する。
図2は充填装置1Aの中で第一機能に関る最小単位の構成を示している。
充填装置1Aは、図2に示すように、製品液Lが貯えられている貯留槽3と、貯留槽3に貯えられている製品液Lを容器100に導く液供給路7と、を備える。貯留槽3の製品液Lよりも上方の空間であるガス相3Sには炭酸ガスCGが貯えられている。ガス相3Sにおける炭酸ガスCGの圧力PFは充填する製品液Lの特性に対応した大気圧を超える一定の圧力になるように制御されている。この圧力PFを制御するために第二圧力センサ17が設けられている。また、製品液Lは、容器100に充填される分が補充され、貯留槽3における液面が定位置になるように制御される。圧力PFを以下ではカウンタ圧力と称する。
液供給路7の一端側は貯留槽3の下端部に接続され、液供給路7の他端側は容器100の口部101に対峙するように設けられている。液供給路7は、製品液Lが流れる流路を開閉する液弁VLを備える。
なお、製品液Lを充填する際には、液供給路7の他端側は容器100の口部とは気密に封止される。第一ガス排出路11も同様である。また、図2は、一つの貯留槽3から一つの容器100に製品液Lが充填される例を示しているが、これはあくまで充填装置1Aの最小単位を示しているにすぎない。実際の生産に用いる充填装置においては、一つの貯留槽3から複数の容器100に製品液Lが充填される。
[Components of the first function]
The first function according to the first embodiment will be described with reference to FIGS.
FIG. 2 shows a minimum unit configuration related to the first function in the
As shown in FIG. 2, the filling device 1 </ b> A includes a
One end side of the
When the product liquid L is filled, the other end side of the
充填装置1Aは、図2に示すように、製品液Lを容器100に充填している過程で容器100の内部のガス成分が排出される補室槽5と、補室槽5と容器100を接続する第一ガス排出路11と、を備える。補室槽5は、容器100の容器を補完するものであって、内部の空隙が圧力調整室6をなしており、後述する第二充填Aにおいて容器100のヘッドスペース105の炭酸ガスCGがこの圧力調整室6に排出される。この圧力調整室6の容積VRは、第二充填Aにおいて容器100に充填される量に対応した所定容積にされている。なお、第一ガス排出路11が本発明の下流流路に該当する。
As shown in FIG. 2, the filling device 1 </ b> A includes the
圧力調整室6は、同等の容積を有する第一ガス排出路11および第二ガス排出路13の一方または双方で代替できる。つまり、本発明における圧力調整室は、第一ガス排出路11および第二ガス排出路13のように所定の容積を有する配管を包含する概念を有している。
The
第一ガス排出路11は、一端側が補室槽5に接続されるとともに、他端側が容器100に対峙するように設けられている。第一ガス排出路11は、容器100から炭酸ガスCGが流れる流路を開閉する第一ガス弁VG1を備える。また、第一ガス排出路11には、第一ガス弁VG1と補室槽5の間に絞りを設けてもよい。
充填装置1Aは、補室槽5と系外を繋ぐ第二ガス排出路13を備える。第二ガス排出路13は、補室槽5から炭酸ガスCGが系外に流れる流路を開閉する第二ガス弁VG2を備える。
The first
The filling
充填装置1Aは、容器100の内部の圧力PBを検知する第一圧力センサ15と、貯留槽3のガス相3Sのカウンタ圧力PFを検知する第二圧力センサ17と、圧力調整室6の圧力PRを検知する第三圧力センサ19と、を備える。容器100の内部の圧力PBは、製品液Lが充填される前の差圧形成時点においては容器100の容積の全体の圧力であり、製品液Lが充填されると製品液Lの液面より上方に生じるヘッドスペース105の圧力である。なお、製品液Lが充填されだすと、圧力PBは上昇する。
第一圧力センサ15は、第一ガス弁VG1と容器100の間の第一ガス排出路11に設けられる。第二圧力センサ17は貯留槽3のガス相3Sに接続される。また、第三圧力センサ19は補室槽5の圧力調整室6に接続される。
Filling
The
充填装置1Aにおいて、図2に示すように、貯留槽3に付加される圧力をPFとし、容器内部の圧力をPB、容器の容積をVBとする。また、圧力調整室6の内部の圧力(室内圧力)PR、容積をVRとする。なお、以下では、貯留槽3に付加される圧力をカウンタ圧力PFと称し、容器の内部の圧力を容器圧力PBと称し、圧力調整室6の圧力を室内圧力PRと称する。
In the
充填装置1Aは、貯留槽3に付随して製品液の給液並びにガスの給排気を制御する給排機構40を備える。
給排機構40は、ポンプ42および液制御弁48が設けられている液供給路41を備える。液供給路41は、ポンプ42および液制御弁48の動作により図示を省略する供給源から製品液Lを、貯留槽3に補充する。
また、給排機構40は、貯留槽3のガス相3Sに炭酸ガスCGを供給するガス供給路43と、貯留槽3のガス相3Sから炭酸ガスCGを排出するガス排出路45と、を備える。ガス供給路43にはガス弁44が、また、ガス排出路45にはガス弁46が設けられている。
The filling device 1 </ b> A includes a supply /
The supply /
The supply /
充填装置1Aは、液弁VL、第一ガス弁VG1および第二ガス弁VG2の開閉動作を制御する制御器2を備える。
制御器2は、第一圧力センサ15、第二圧力センサ17および第三圧力センサ19で検知された容器圧力PB,カウンタ圧力PF,室内圧力PRを取得して、液弁VL~第二ガス弁VG2の開閉動作を制御する。また、制御器2は、充填装置1Aが製造する製品液Lに必要な設定条件に基づき、液弁VL~第二ガス弁VG2の開閉動作を制御する。さらに、制御器2は、貯留槽3における製品液Lの液面が定位置になるように、液供給路41のポンプ42および液制御弁48の動作を制御する。さらにまた、制御器2は、カウンタ圧力PFが一定になるように、ガス供給路43のガス弁44とガス排出路45のガス弁46の開閉を制御する。
なお、以下で説明する図3~図7において、開いている液弁VL~第二ガス弁VG2は白抜きで示し、閉じている液弁VL~第二ガス弁VG2は黒塗りで示す。
The
The
3 to 7 described below, the open liquid valve VL to the second gas valve VG2 are shown in white, and the closed liquid valve VL to the second gas valve VG2 are shown in black.
[飲料充填の手順]
次に、充填装置1Aを用いて容器100に製品液Lを充填する方法を説明する。
第1実施形態による充填方法は、第一充填および第二充填Aからなる。第一充填は、大気圧の炭酸ガスCGで容器100内が置換された状態で閉塞されている容器100へ圧力差により製品液Lを充填するが、目標充填量よりも少ない設定量の製品液Lを充填する。第二充填Aは目標充填量と設定量との差分を補うように製品液Lを容器100に充填する。一連の工程は、図3に示すように、液弁VL、第一ガス弁VG1および第二ガス弁VG2の全ての弁が閉じられている初期状態からはじまる。初期状態において、容器100および圧力調整室6は、一例として炭酸ガスCGで満たされた大気圧(PB,PR=大気圧)の雰囲気とされている。
一方で、貯留槽3の内部において、製品液Lにはガス相3Sから大気圧を超えるカウンタ圧力PFが加えられており、容器100の内部と貯留槽3の内部との間には圧力差が形成されている(図7 第一差圧形成ステップ S101)。
以下、各工程を順に説明する。ガス相3Sは、製品液Lの特性を維持するために必要なガス成分、例えば炭酸ガスからなる。
[Beverage filling procedure]
Next, a method for filling the
The filling method according to the first embodiment includes a first filling and a second filling A. In the first filling, the product liquid L is filled by the pressure difference into the
Meanwhile, inside the
Hereinafter, each process is demonstrated in order. The
[第一充填(図4(a)、(b)、図7)]
第一充填は、図4(a)に示すように、はじめに液弁VLを開いて、貯留槽3と容器100を連通させる。貯留槽3は大気圧を超えるカウンタ圧力PFが印加された加圧環境下であるのに対して、容器圧力PBは大気圧とされる。したがって、カウンタ圧力PFと容器圧力PB(大気圧)の圧力差に対応する流量および流速で製品液Lが貯留槽3から容器100に高速で充填され始める(図7 第一充填ステップ S103)。充填が進むのにつれて容器圧力PBは上昇し、容器圧力PBに設定圧力を設けておけばこの設定圧力に対応する設定量だけ製品液Lが容器100に充填される。
[First filling (FIGS. 4A, 4B, 7)]
In the first filling, as shown in FIG. 4A, first, the liquid valve VL is opened, and the
ここで、第一充填の間には、第一圧力センサ15により第一ガス導出路11の圧力が継続的に検知される。第一圧力センサ15により検知される圧力は、容器100のヘッドスペース105における容器圧力PBである。第一圧力センサ15が検知する圧力が設定圧力P1に達したならば、図4(b)に示すように、液弁VLを閉じて製品液Lの充填を停止する。これで第一充填が終了し、設定量の製品液が充填される。この第一充填の間、容器100に収容されていた炭酸ガスCGは、容器100に閉じ込められたままで充填が進行するので、容器圧力PBが上昇する。この場合、設定圧力P1の最大限度は貯留槽3に付加されたカウンタ圧力PFと容器100が平衡になる圧力である。従って設定圧力P1の最大圧力をカウンタ圧力PFとすることができる。ここで、第一充填の終了時には、容器圧力PBは大気圧よりも高いカウンタ圧力PFまで上昇するのに対して、圧力調整室6の室内圧力PRは大気圧のままである。
なお、ここでは圧力の設定圧力P1に基づいて液弁VLを閉じるが、第1実施形態はこれに限らない。例えば、設定圧力P1に達する時間に関する設定時間T1を予め実験的に求めておき、この時間に関する設定時間T1に基づいて液弁VLを閉じることもできる。ただし、設定時間T1は、実験的に求めた値と完全に一致する必要はない。充填時間を短縮することを目的として実験値より短い設定時間T1を設定できるし、製品液Lの状態を安定させることを目的として実験値より長い設定時間T1を設定できる。第二充填Aにおいても同様である。
Here, during the first filling, the pressure of the first
Here, the liquid valve VL is closed based on the set pressure P1, but the first embodiment is not limited to this. For example, a set time T1 related to the time to reach the set pressure P1 can be experimentally obtained in advance, and the liquid valve VL can be closed based on the set time T1 related to this time. However, the set time T1 does not need to completely match the experimentally obtained value. A set time T1 shorter than the experimental value can be set for the purpose of shortening the filling time, and a set time T1 longer than the experimental value can be set for the purpose of stabilizing the state of the product liquid L. The same applies to the second filling A.
ここで、第一充填における容器100への第一充填量Q1は以下の式(1)により求められる。なお、この第一充填量Q1は容器圧力PBが貯留槽3のカウンタ圧力PFと平衡になることを前提としている。また、第一充填量Q1だけ製品液Lが充填された後の容器100のヘッドスペース105の容積VHは以下の式(2)により求められる。一例として補室槽5の圧力調整室6は、目標充填量Qと第一充填量Q1の差分とその容積VRとが一致するように作製されている。なお、式(1)および式(2)は、ボイルの法則に基づいており、後述する式(3)~式(7)も同様である。また、目標充填量Qと第一充填量Q1の差分は、第二充填ステップにおける第二充填量Q2と一致する。
第一充填量Q1=(1-PB/PF)×VB … 式(1)
ヘッドスペース容積VH1=PB/PF×VB … 式(2)
PB:容器100の圧力
VB:容器100の容積
VH1:第一充填後のヘッドスペース105の容積
PF:ガス相3Sの圧力(一定)
Here, the first loading to Q 1 to the
First filling amount Q 1 = (1−P B / P F ) × V B Formula (1)
Head space volume V H1 = P B / P F × V B Formula (2)
P B : Pressure of
V B : Volume of the
V H1 : Volume of the
P F :
例えば、ガス相3Sのカウンタ圧力PFを5気圧(正圧)、容器圧力PBを1気圧(大気圧)とする。そうすると、第一充填量Q1およびヘッドスペース容積VH1は以下の通りであり、製品液Lは第一充填において容器100の容積VBの4/5に相当する量だけ充填されるので、残りのQ-4/5×VBに相当する量を第二充填Aにおいて充填する必要がある。この残りのQ-4/5×VBに相当する量が、容器100に予定されている目標充填量にするために必要な差分である第二充填量Q2に該当する。
第一充填量Q1=4/5・VB
ヘッドスペース容積VH1=1/5・VB
ここで、第一充填の過程において、容器圧力PBは容器100の耐圧力未満であることが必要である。これは、第二充填A~第二充填Dおよび第2実施形態の一段充填においても同様である。
容器100の耐圧力をPPとし、製品液Lの第一充填後の容器圧力PBとすると、以下の式(3)を満たす必要がある。ガス相3Sのカウンタ圧力PFが5気圧(正圧)、容器100の当初の容器圧力PBが1気圧(大気圧)とすると、容器100の第一充填の終了後の容器圧力PBはカウンタ圧力PFと平衡となる5気圧である。したがって、この第一充填に対して要求される容器100の耐圧力PPは5気圧である。
PP>PB=VB/(VB-Q1) … 式(3)
For example, the
First filling amount Q 1 = 4/5 · V B
Head space volume V H1 = 1/5 · V B
Here, in the first filling process, the container pressure P B needs to be less than the pressure resistance of the
When the pressure resistance of the
P P > P B = V B / (V B -Q 1 ) (3)
[第二充填A(図5(a)、(b)、図7)]
第一充填の後には第二充填Aが行われる。第二充填Aは目標充填量Qと第一充填量Q1の差分の量だけ製品液Lの充填を行う。
第二充填Aは、図5(a)に示すように、第一ガス弁VG1を開く。なお、第一ガス弁VG1および液弁VLを同時に開いてもよいし、第一ガス弁VG1を先行して開いてもよい。
[Second filling A (FIGS. 5A, 5B, 7)]
After the first filling, the second filling A is performed. The second filling A performs only the filling of the product liquid L amount of the difference between the desired charge amount Q and the first charge Q 1.
As shown in FIG. 5A, the second filling A opens the first gas valve VG1. The first gas valve VG1 and the liquid valve VL may be opened simultaneously, or the first gas valve VG1 may be opened in advance.
第一ガス弁VG1を開くと、容器100のヘッドスペース105と補室槽5の圧力調整室6が連通するが、ヘッドスペース105における容器圧力PBが圧力調整室6の室内圧力PRより高い。したがって、ヘッドスペース105を満たしている炭酸ガスCGの一部は補室槽5の圧力調整室6に排出される。これにより、容器圧力PBは貯留槽3のガス相3Sのカウンタ圧力PFよりも低くなり、容器圧力PBとカウンタ圧力PFには圧力差(第二差圧)が生じる(図7 第二差圧形成ステップ S105)。
圧力調整室6は、ヘッドスペース105を満たしている炭酸ガスCGの排出を受けるが、これにより容器100の容積が圧力調整室6の分だけ増えたものとみなすことができる。つまり、圧力調整室6は、第二差圧を形成するという観点からすると、容器100の一部として機能する補室を構成している。
When opening the first gas valve VG1, the
The
この圧力差が生じている状態で液弁VLが開いていれば、貯留槽3から容器100に圧力差に対応する流量および流速で製品液Lが充填される(図7 第二充填ステップ S107)。このときに充填される量が差分に該当する。第二充填Aを終えて充填された製品液Lの量、つまり目標充填量Qは、下記の式(4)により求められる。また、目標充填量Qを満たす製品液Lが充填された後の容器100のヘッドスペース105のヘッドスペース容積VH2は以下の式(5)により求められる。
目標充填量Q=(1-PB/PF)×(VB+VR) … 式(4)
ヘッドスペース容積VH2=PB/PF×(VB+VR)-VR … 式(5)
If the liquid valve VL is opened in a state where this pressure difference is generated, the product liquid L is filled from the
Target filling amount Q = (1−P B / P F ) × (V B + V R ) (4)
Head space volume V H2 = P B / P F × (V B + V R ) −V R Formula (5)
式(4)と式(1)の比較、式(5)と式(2)の比較より、第二充填Aにおいて、圧力調整室6の容積VRの分だけ貯留槽3から容器100に製品液Lが充填されることがわかる。換言すれば、第二充填Aにおいて充填したい量、つまり目標充填量Qと第一充填量Q1の差分である第二充填量Q2に一致するように補室槽5の容積VRが定められる。
Comparison of formula (4) and equation (1), equation (5) and from the comparison of equations (2), in a second filling A, products from an
第二充填Aにおいても、第一圧力センサ15により第一ガス排出路11の圧力を継続的に検知する。第一圧力センサ15が検知する圧力が設定圧力P1に達したならば、図5(b)に示すように、液弁VLおよび第一ガス弁VG1を閉じる。これで第二充填Aが終了し、容器100に目標充填量Qを満たす製品液Lが充填される。設定圧力P1は、差分を充填するのに必要な圧力となる。
Also in the second filling A, the pressure of the first
以上では、圧力調整室6の容積が固定された例を示したが、第1実施形態は補室槽5の容積を任意に変えることもできる。例えば容積が異なる複数種類の容器100を充填の対象とするときには、容器100の種類に応じて第二充填Aで充填する製品液Lの量を変える必要がある。そこで、補室槽5の内容積を任意に可変とすることにより、容器100の種類に応じた充填量を実現できる。
Although the example in which the volume of the
例えば図6(a),(b)に示すように、ピストン-シリンダ機構からなる補室槽5とすればよい。つまり、この補室槽5は、ピストン5Aとピストン5Aが進退するシリンダ5Bとから構成される。この補室槽5を用いて行う第二充填を第二充填Bと称する。
第二充填Bにおける第二充填量Q2が多いときは図6(a)に示すように、ピストン5Aを後退させることでピストン5Aとシリンダ5Bで形成される容積VAを大きくする。第二充填Bにおける充填量Q2が少ないときには図6(b)に示すように、ピストン5Aを前進させることでピストン5Aとシリンダ5Bで形成される容積VAを小さくする。このように、シリンダ5Bに対するピストン5Aの相対的な位置を変えることにより補室槽5の容積を任意に変更できる。
For example, as shown in FIGS. 6A and 6B, the
When the second charge Q 2 is large in the second filling B, as shown in FIG. 6 (a), to increase the volume V A which is formed by the
なお、容積が固定された補室槽5を用いる場合でも、容器100の種類に応じた容積の異なる複数種類の補室槽5を用意しておき、容器100の種類に応じて使用する補室槽5を交換することもできる。ただし、内容積が可変の補室槽5を用いる方が、補室槽5を交換するのに比べて格段に作業負担が小さい。
Even when the
[第一機能の効果]
以上説明した第1実施形態の第一機能に関する奏する効果を説明する。
第1実施形態は、製品液Lの第一充填および第二充填Aを開始するときに、容器圧力PBが大気圧である。よって、第1実施形態によれば、樹脂製で可撓性を有する容器100を充填の対象としたとしても、容器100が潰れることなくその形状を維持できる。
[Effect of the first function]
The effect which concerns regarding the 1st function of 1st Embodiment demonstrated above is demonstrated.
In the first embodiment, when the first filling and the second filling A of the product liquid L are started, the container pressure P B is atmospheric pressure. Therefore, according to the first embodiment, even if a
しかも、第1実施形態は、製品液Lの第一充填および第二充填A,Bを開始するときに、貯留槽3のカウンタ圧力PFが容器圧力PBよりも高く設定されている。よって、第1実施形態によれば、この圧力差を利用して製品液Lが容器100に送出されるので、製品液Lを高速で容器100に充填することができる。
Moreover, the first embodiment, the first packing and second packing A product solution L, when starting the B, the counter pressure P F of the
さらに、第1実施形態は、第一充填と第二充填A,Bからなる二段充填を行うので、目標充填量Qを満たす量の製品液Lを容器100に確実に充填できる。
Furthermore, since the first embodiment performs the two-stage filling including the first filling and the second filling A and B, the product liquid L in an amount satisfying the target filling amount Q can be reliably filled into the
さらに、第1実施形態の第一充填および第二充填A,Bにおいて容器100に充填された直後には瞬間的に圧力が開放されるために炭酸ガスCGが泡となって現れる。ところが、この泡は微細であるのに加えて充填終了時に容器圧力PBはカウンタ圧力PFであるから、泡はすぐに製品液に再溶解して消失する。よって、第1実施形態によれば、第一充填および第二充填A,Bを経た後に、封緘材103を容器100に装着する作業を迅速に始めることができる。これは、第1実施形態の第二機能として実現される。
Furthermore, immediately after the
第1実施形態において、第一充填に先立って容器100の内部が所定濃度の炭酸ガスCGで置換されている。これにより、第1実施形態は、製品液Lに酸素が混入するのを避けつつ製品液Lに含まれる炭酸ガスの濃度を所定の値に保つことができる。
In the first embodiment, the interior of the
[第二機能]
以下、第1実施形態に係る第二機能を図8および図9を参照して説明する。
充填装置1Aは、図8に示すように、外部に対して気密に保持される密閉室21を有する密閉チャンバ20を備える。
密閉チャンバ20には、図示しないガス供給源とガス供給路28が接続されるとともに、ガス排出路29が接続されている。ガス供給路28からのガス成分の供給およびガス排出路29からのガス成分の排出を制御することにより、充填ステップの最中に、密閉チャンバ20の内部が容器圧力PBにほぼ等しいガス成分と圧力に加圧、保持される。
図8および図9において、ガス供給路28とガス排出路29は、弁が白抜きであれば開いており、弁が黒塗りであれば閉じられている。
[Second function]
Hereinafter, the second function according to the first embodiment will be described with reference to FIGS. 8 and 9.
As shown in FIG. 8, the filling apparatus 1 </ b> A includes a sealed
A gas supply source (not shown) and a
8 and 9, the
また、密閉チャンバ20には、液供給路7と第一ガス排出路11が同期して進退可能に接続されている。液供給路7と第一ガス導出路11は、内側に液供給路7が設けられ、外側に第一ガス導出路11が設けられる、二重管構造22に組み込まれている。二重管構造22は、図9(d)に示す待機位置と図9(a)~(c)に示す動作位置との間を往復移動する。また、二重管構造22の先端にはノズル25が設けられている。ノズル25は、製品液Lの充填の際に、図9(b),(c)に示すように、容器100の口部101に押し付けられる。押し付けられた部分は口部101に密着されて、容器100の内外を封止する。ノズル25は、図8に実線で示す待機位置と仮想線で示す動作位置の間で昇降可能に設けられている。
Further, the
第一充填、第二充填において、液弁VLを開くと、貯留槽3の製品液Lが液供給路7を通って密閉チャンパ20まで引き込まれ、容器100に充填される。
また、第二充填において、第一ガス弁VG1を開くと、容器100のヘッドスペース105の炭酸ガスCGが第一ガス排出路11を通って補室槽5に向かう。
In the first filling and the second filling, when the liquid valve VL is opened, the product liquid L in the
Further, in the second filling, when the first gas valve VG 1 is opened, the carbon dioxide gas CG in the
また、密閉チャンバ20は、図8に示すように、容器100に製品液Lを充填するときに、容器100の口部101が挿入される容器保持開口27を備える。容器保持開口27は、密閉チャンバ20を貫通し、密閉室21と外部を連通する。
容器保持開口27は、口部101に取り付けられる封緘材103の外径よりも大きな開口径を有する。容器100の口部101に封緘材103を取り付けるときにも、容器100の口部101は容器保持開口27に保持されている。
口部101が容器保持開口27に保持されている間に、密閉室21が外部に対して気密な状態を保つために、容器保持開口27の周りに図示を省略するシール部材が設けられる。
Further, as shown in FIG. 8, the sealed
The
A sealing member (not shown) is provided around the
次に、密閉チャンバ20には、図8に示すように、封緘機としての封緘ヘッド30が昇降可能に設けられている。
封緘ヘッド330は、先端(図中の下端)で封緘材103を保持しながら、待機位置(図8、図9(a))と動作位置(図9(d))の間を昇降する。封緘ヘッド30は、口部101に封緘材103を装着した後には、新たな封緘材103が補充、保持されてから、動作位置から待機位置に移動する。
Next, as shown in FIG. 8, a sealing
The sealing head 330 moves up and down between the standby position (FIGS. 8 and 9A) and the operation position (FIG. 9D) while holding the sealing
次に、密閉チャンバ20、封緘ヘッド30の動作を説明する。
[充填前準備]
はじめに、図9(a)に示すように、容器100が容器保持開口27の下方で位置合わせされる。二重管構造22は動作位置まで移動するが、ノズル25は待機位置に留まっている。
その後、図9(b)に示すように、容器100の口部101が容器保持開口27に挿入されかつ容器保持開口27の内側に保持される。また、ノズル25は前進しかつ容器100の口部101まで下降する。そうすると、密閉室21及び容器100が外部に対して気密に封止される。この後、ガス供給路28からガス成分としての炭酸ガスを密閉室21へ供給しつつ排気して密閉室のガス成分を炭酸ガスに置換する。この時置換された密閉室の炭酸ガスの圧力は、貯留槽3に付加されるカウンタ圧力PF(容器圧力PB)と一致するように供給される。
なお、ガス供給路28から加えられるガス成分としての炭酸ガスは、貯留槽3以外のガス供給源から供給されるものであってもよい。
図示を省略するが、容器100はグリッパと称される把持具により口部101で支持されており、グリッパに密閉チャンバ20に向けて負荷を加えることにより、口部101を密閉チャンパ20に気密に押し付けることができる。
Next, operations of the sealed
[Preparation before filling]
First, as shown in FIG. 9A, the
Thereafter, as shown in FIG. 9B, the
The carbon dioxide gas as a gas component added from the
Although not shown, the
[第一充填および第二充填A]
第一充填および第二充填Aは、図9(c)に示すように、容器100の口部101が容器保持開口27に保持されるのを維持したままで、かつ、ノズル25が動作位置に移動して行われる。封緘ヘッド30は待機位置に置かれている。
[First filling and second filling A]
As shown in FIG. 9C, in the first filling and the second filling A, the
前述した第一充填の手順に従って液弁VLを開く。そうすると、液供給路7を通って充填量Q1だけ製品液Lが容器100の内部に充填される。その後、第一ガス弁VG1を開くと、容器100のヘッドスペース105を満たす炭酸ガスCGは第一ガス排出路11を通って補室槽5に向けて排出される。
第一充填を終えると、前述した手順で第二差圧形成を行った後に、第二充填Aが行われる。
また、第二充填Aにおいても、二重管構造22は第一充填のままの状態として、前述した第二充填Aの手順に従って液弁VLおよび第一ガス弁VG1を開く。そうすると、液供給路7を通って製品液Lが容器100の内部に充填され、目標充填量Qを満たす量の製品液Lが100に充填される。このとき、ヘッドスペース105を満たす炭酸ガスCGは第一ガス導出路11を通って補室槽5に向かう。
The liquid valve VL is opened in accordance with the first filling procedure described above. Then, the product liquid L is filled into the
When the first filling is finished, the second filling A is performed after the second differential pressure is formed by the above-described procedure.
Also in the second filling A, the
[封緘]
第二充填Aを終えると、図9(d)に示すように、二重管構造22およびノズル25が待機位置に後退した後に、封緘ヘッド30が動作位置まで前進する。封緘ヘッド30を動作させることにより、キャップ103を口部101に装着する(図7 キャッピングステップ S109)。封緘材103を装着するまで、容器100の口部101が容器保持開口27に保持されている。これにより、容器圧力PBを維持したままで、封緘材103を装着できる。
封緘材103の装着後には、封緘ヘッド30が待機位置まで後退する。また、封緘材103が装着された容器100は容器保持開口27から離脱するとともに、さらに下流の工程に向けて搬送される。さらに、後続の製品液Lの充填対象となる容器100に装着される封緘材103が容器保持開口27に装填され、待ち受けている封緘ヘッド30に補充される。封緘材103が補充された封緘ヘッド30は、次の充填作業のために、待機位置まで後退する。
[Enclosure]
When the second filling A is finished, as shown in FIG. 9D, after the
After the sealing
[第二機能の効果]
以上説明した第1実施形態の第二機能に関する奏する効果を説明する。
第1実施形態は、製品液Lを充填する密閉チャンバ20に封緘ヘッド30が組み込まれており、製品液Lが充填された容器100の移動を伴うことなく封緘材103を容器100に装着できる。したがって、製品液Lが充填された容器100に迅速に封緘材103を装着できるので、高速で行われる充填と相まって、飲料製品を短時間で製造することができる。
[Effect of the second function]
The effect which concerns regarding the 2nd function of 1st Embodiment demonstrated above is demonstrated.
In the first embodiment, the sealing
[第1実施形態の変形例]
以上、本発明の第1実施形態を説明したが、本発明の主旨を逸脱しない限り、第1実施形態で挙げた構成を取捨選択したり、他の構成に置き換えたりすることができる。
はじめに、第1実施形態は圧力調整室6の容積を第二充填Aで差分の充填量に整合させる容積制御方式を採用しているが、これに限らず、第二充填Aで差分の充填量を充填できる他の方式を採用できる。その一例として、圧力の変動に基づいて充填を制御する圧力制御方式がある。圧力制御方式は、第二充填Cと第二充填Dの二形態があり、いずれも補室槽5を用いるものの、圧力調整室6の容積を第二充填において容器100に充填される量に予め特定する必要がない。
以下、図10及び図11を参照して第二充填C、第二充填Dの順に説明する。なお、第一充填は、第二充填Aと同じ手順で行われ、また、ガス置換が始まる前の容器圧力PBおよび補室内圧力PRは大気圧とする。
[Modification of First Embodiment]
Although the first embodiment of the present invention has been described above, the configuration described in the first embodiment can be selected or replaced with another configuration without departing from the gist of the present invention.
First, the first embodiment employs a volume control system in which the volume of the
Hereinafter, the second filling C and the second filling D will be described in this order with reference to FIGS. 10 and 11. It is to be noted that the first filling is carried out by the same procedure as the second filling A, also, the vessel pressure P B and the auxiliary chamber pressure P R before the gas replacement is started and the atmospheric pressure.
[第二充填C]
第二充填Cは、図10(a)に示すように、はじめに第一ガス弁VG1を開く。そうすると、容器100のヘッドスペース105に充填されている炭酸ガスCGが補室槽5に導出されるので、ヘッドスペース105とガス相3Sとの間に圧力差が生じる。第一ガス弁VG1を開くと、容器圧力PBと室内圧力PRは容器ヘッドスペースと補室容量の合計による平均圧力になる。その結果、カウンタ圧力PFと圧力差が形成される。なお、第三圧力センサ19は圧力調整室6の室内圧力PRを継続して検知している。
[Second filling C]
As shown in FIG. 10A, the second filling C first opens the first gas valve VG1. Then, since the carbon dioxide gas CG filled in the
その後、図10(b)に示すように、液弁VLを開く。そうすると、貯留槽3から容器100に製品液Lが充填されるが、充填量が増えて入身線が上昇するのに伴って容器100のヘッドスペース105を満たしていた炭酸ガスCGが次第に補室槽5に導出される。これにより、圧力調整室6の室内圧力PRが上昇する。
Thereafter, as shown in FIG. 10B, the liquid valve VL is opened. Then, the product liquid L is filled into the
制御器2は、第一圧力センサ15または第三圧力センサ19が検知した室内圧力PRを取得するとともに予め定められた設定圧力PB’と比較する。制御器2は、室内圧力PRが設定圧力PB’まで上昇したならば、第一充填で不足した製品液Lの充填が終了したものと認定し、図10(c)に示すように、先に第一ガス弁VG1を閉じてからその後に液弁VLを閉じる。これで圧力差に対応する製品液Lが目標充填量まで充填され、第二充填が終了する。
The
第二充填Cで充填される製品液Lの量は以下の式(6)および式(7)で特定される。
第二充填量Q2=VH1×(1-PR/PBB’)+VR×(1-PR/PBB’) … 式(6)
目標充填量Q=Q1+Q2 … 式(7)
The amount of the product liquid L filled in the second filling C is specified by the following formulas (6) and (7).
Second filling amount Q 2 = V H1 × (1−P R / PB B ′) + V R × (1−P R / PB B ′) Formula (6)
Target filling amount Q = Q 1 + Q 2 (7)
[第二充填D]
第二充填Dは、図11(a)に示すように、はじめに第一ガス弁VG1を開く。そうすると、容器100のヘッドスペース105に充填されている炭酸ガスCGが補室槽5に導出される。第三圧力センサ19は、圧力調整室6の室内圧力PRを継続して検知している。なお、ここまでは第二充填Cと同じである。
[Second filling D]
In the second filling D, first, the first gas valve VG1 is opened as shown in FIG. Then, the carbon dioxide gas CG filled in the
その後、図11(b)に示すように、第一ガス弁VG1を開いたままで第二ガス弁VG2を開く。そうすると、補室槽5を満たしている炭酸ガスCGが第二ガス導出路13を通って系外に導出されるので、室内圧力PRが低下する。なお、第二ガス弁VG2は、流路を全て開くのではなく部分的に開くことで、微量の炭酸ガスCGが導出されるようにする。絞りを介し一定流量で炭酸ガスCGを導出することで、容器100のヘッドスペース105、補室槽5の室内圧力Prを一定に保持しながら目標量との差分が充填される時間まで継続した後に、液弁VLと第2ガス弁GV2を閉止する。
Thereafter, as shown in FIG. 11B, the second gas valve VG2 is opened while the first gas valve VG1 is kept open. Then, since the carbon dioxide gas CG meet the
第二ガス弁VG2を開いたままで、制御器2は、第三圧力センサ19が検知した室内圧力PRを取得するとともに予め定められた設定圧力PB’と比較する。制御器2は、室内圧力PRが設定圧力PB’まで低下したならば、図11(c)に示すように、まず、第二ガス弁VG2を閉じる。これで、貯留槽3のガス相3Sと容器100のヘッドスペース105の間に圧力差を設けることができる。
次いで、図11(c)に示すように、液弁VLを開く。これで圧力差に対応する製品液Lが目標充填量Qまで充填され、第二充填Dが終了する。第二充填Dにおける製品液Lの充填量は、系外へ排出される炭酸ガスCGを加味することを除けば、第二充填Cと同様に算出できる。
It remains open and the second gas valve VG2, the
Next, as shown in FIG. 11C, the liquid valve VL is opened. Thus, the product liquid L corresponding to the pressure difference is filled up to the target filling amount Q, and the second filling D is completed. The filling amount of the product liquid L in the second filling D can be calculated in the same manner as the second filling C except that the carbon dioxide gas CG discharged outside the system is taken into account.
以上の通りであり、第二充填Cおよび第二充填Dは、圧力調整室6で検知される圧力に基づいて、差分の充填量を補うので、圧力調整室6の容積を予め特定する必要がない。ただし、圧力調整室6は差分の充填量を超える容積を有している必要はある。
As described above, the second filling C and the second filling D make up for the difference filling amount based on the pressure detected in the
[第2実施形態]
次に、本発明の第2実施形態を説明する。
第2実施形態は、一回の充填サイクルにより目標充填量Qを満たす量の充填をする一段充填に関する。一段充填は、一度の圧力差の形成および製品液Lの充填により、容器100に目標充填量の製品液Lを満たす。以下、図12~図13を参照して、第2実施形態を説明する。なお、以下では第1実施形態と相違する部分を中心に説明する。
[Second Embodiment]
Next, a second embodiment of the present invention will be described.
The second embodiment relates to one-stage filling in which filling is performed in an amount that satisfies the target filling amount Q by a single filling cycle. In the first-stage filling, the
第2実施形態の充填装置1Bは、図12に示すように、第1実施形態の充填装置1Aが備えていた第一ガス排出路11~第二ガス排出路13の代替として、第三ガス排出路14を備えている。第三ガス排出路14は、容器100に対して気密に接続されている。第三ガス排出路14には第三ガス弁VG3が設けられており、第1実施形態における第一ガス排出路11から補室槽5(圧力調整室6)を除いた構成を有しているとみなすことができる。第三ガス排出路14として、例えば飲料充填装置が備えるCIP(Cleaning In Place:定置洗浄)装置における洗浄液の戻り配管回路を用いることができる。
ただし、第一ガス排出路11~第二ガス弁VG2を備える充填装置1Aで一段充填を実施することもできる。この場合、第一ガス排出路11~第二ガス弁VG2の機能を使用しないことになるが、この充填装置1Aは一段充填と複数段充填の兼用の装置である。
As shown in FIG. 12, the filling
However, one-stage filling can also be performed by the
充填装置1Bは、容器100と第三ガス弁VG3を繋ぐ第三ガス排出路14の内部の空隙を容器100の容積の一部としての機能を積極的に持たせる。つまり、図12において、第三ガス弁VG3を閉じると、容器100よりも第三ガス弁VG3の側、つまり容器100よりも下流側の第三ガス排出路14の内部は補室容積VB3を有する空隙となる。この空隙が、以下説明するように、本発明における第一補室容積に該当する。
The filling device 1 </ b> B positively gives a function as a part of the volume of the container 100 to the void inside the third gas discharge path 14 connecting the container 100 and the third gas valve VG <b> 3. That is, in FIG. 12, closing the third gas valve VG3, than the container 100 of the third gas valve VG3 side, i.e. the interior of the third gas discharge passage 14 on the downstream side of the container 100 an auxiliary chamber volume V B3 It becomes a void having. As will be described below, this gap corresponds to the first auxiliary chamber volume in the present invention.
ここで容器100の容積をVB1とおくと、連通したときの両者の合計の容積はVB1+VB3(=VB)となり、容器100の容積が見掛け上は増えることになる。したがって、下記の式(1a),(1b)に示すように、補室容積VB3を備える場合(式(1b))と補室容積VB3を備えない場合(式(1a))を比較すれば、前者による製品液Lの充填量が補室容積VB3の分だけ増える。
充填量Q1=(1-PB/PF)×VB1 … 式(1a)
充填量Q1=(1-PB/PF)×(VB1+VB3) … 式(1b) Here, if the volume of thecontainer 100 is set to V B1 , the total volume of both when communicating is V B1 + V B3 (= V B ), and the volume of the container 100 is apparently increased. Accordingly, the following formula (1a), by comparing, as shown in (1b), if not provided with the Hoshitsu volume V B3 to the case (equation (1b)) comprising an auxiliary chamber volume V B3 (formula (1a)) In this case, the filling amount of the product liquid L by the former increases by the auxiliary chamber volume V B3 .
Filling amount Q1 = (1−P B / P F ) × V B1 Formula (1a)
Filling amount Q1 = (1−P B / P F ) × (V B1 + V B3 ) (1b)
充填量Q1=(1-PB/PF)×VB1 … 式(1a)
充填量Q1=(1-PB/PF)×(VB1+VB3) … 式(1b) Here, if the volume of the
Filling amount Q1 = (1−P B / P F ) × V B1 Formula (1a)
Filling amount Q1 = (1−P B / P F ) × (V B1 + V B3 ) (1b)
下記式(1c)に示すように、充填量Q1が目標充填量Qに一致するように容器100と第三ガス弁VG3との間の第三ガス排出路14の補室容積VB3を設定すれば、一段充填だけで製品液Lを容器100に目標充填量Qだけ充填できることになる。さらに、下記式(1c)に示すように、充填量Q1が目標充填量Qを超えるように補室容積VB3を設定して、液弁VLの開閉を制御することによっても、一段充填だけで容器100に目標充填量Qを満たす製品液Lを充填できる。
目標充填量Q=充填量Q1=(1-PB/PF)×(VB1+VB3) … 式(1c) As shown in the following formula (1c), the auxiliary chamber volume V B3 of the thirdgas discharge passage 14 between the container 100 and the third gas valve VG3 is set so that the filling amount Q1 matches the target filling amount Q. In this case, the product liquid L can be filled into the container 100 by the target filling amount Q only by one-stage filling. Furthermore, as shown in the following formula (1c), the auxiliary chamber volume V B3 is set so that the filling amount Q1 exceeds the target filling amount Q, and the opening and closing of the liquid valve VL is controlled. The container 100 can be filled with the product liquid L that satisfies the target filling amount Q.
Target filling amount Q = filling amount Q1 = (1−P B / P F ) × (V B1 + V B3 ) (1c)
目標充填量Q=充填量Q1=(1-PB/PF)×(VB1+VB3) … 式(1c) As shown in the following formula (1c), the auxiliary chamber volume V B3 of the third
Target filling amount Q = filling amount Q1 = (1−P B / P F ) × (V B1 + V B3 ) (1c)
[差圧形成ステップ]
第2実施形態においても、図13(a)に示すように、液弁VLを閉じることで、充填装置1Bは貯留槽3と容器100の間にカウンタ圧力PFが容器圧力PBよりも大きい圧力差を形成する。カウンタ圧力PFおよび容器圧力PBがともに大気圧以上の正圧であることは第1実施形態と同じである。容器100の内部には例えば大気圧の炭酸ガスCGが充填されている。この差圧形成ステップおよび次の充填ステップを通じて、第三ガス弁VG3は閉じられている。 [Differential pressure forming step]
In the second embodiment, as shown in FIG. 13 (a), by closing the liquid valve VL, the fillingdevice 1B is greater than the counter pressure P F is vessel pressure P B during the storage tank 3 and the container 100 Create a pressure differential. It counter pressure P F and vessel pressure P B is a positive pressure above both atmospheric pressure is the same as the first embodiment. The inside of the container 100 is filled with, for example, carbon dioxide gas CG at atmospheric pressure. Through this differential pressure forming step and the next filling step, the third gas valve VG3 is closed.
第2実施形態においても、図13(a)に示すように、液弁VLを閉じることで、充填装置1Bは貯留槽3と容器100の間にカウンタ圧力PFが容器圧力PBよりも大きい圧力差を形成する。カウンタ圧力PFおよび容器圧力PBがともに大気圧以上の正圧であることは第1実施形態と同じである。容器100の内部には例えば大気圧の炭酸ガスCGが充填されている。この差圧形成ステップおよび次の充填ステップを通じて、第三ガス弁VG3は閉じられている。 [Differential pressure forming step]
In the second embodiment, as shown in FIG. 13 (a), by closing the liquid valve VL, the filling
[充填ステップ]
次に、図13(b)に示すように、液弁VLを開くと、貯留槽3に貯えられている製品液Lは液供給路7を通って容器100に充填される。この充填は、容器100液供給路7との接続部分を除く部分は密閉して、炭酸ガスCGを容器100の外部に逃がすことなく閉じ込めたままで圧力差により製品液Lを充填する。 [Filling step]
Next, as shown in FIG. 13 (b), when the liquid valve VL is opened, the product liquid L stored in thestorage tank 3 is filled into the container 100 through the liquid supply path 7. In this filling, the product liquid L is filled by a pressure difference while the portion other than the connection portion with the container 100 liquid supply path 7 is sealed and the carbon dioxide gas CG is confined without escaping outside the container 100.
次に、図13(b)に示すように、液弁VLを開くと、貯留槽3に貯えられている製品液Lは液供給路7を通って容器100に充填される。この充填は、容器100液供給路7との接続部分を除く部分は密閉して、炭酸ガスCGを容器100の外部に逃がすことなく閉じ込めたままで圧力差により製品液Lを充填する。 [Filling step]
Next, as shown in FIG. 13 (b), when the liquid valve VL is opened, the product liquid L stored in the
この充填ステップにおいて、貯留槽3に付加されているカウンタ圧力PFに容器100のヘッドスペース105における容器圧力PBが平衡になるまで充填が継続される。
In the filling step, vessel pressure P B in the head space 105 of the container 100 to the counter pressure P F which is added to the storage tank 3 is continued filling until the equilibrium.
ここで、容器100への充填量Q1は、以下に再掲する式(1c)により求められる。
目標充填量Q=充填量Q1=(1-PB/PF)×(VB1+VB3) … 式(1c) Here, the filling amount Q1 into thecontainer 100 is obtained by the following formula (1c).
Target filling amount Q = filling amount Q1 = (1−P B / P F ) × (V B1 + V B3 ) (1c)
目標充填量Q=充填量Q1=(1-PB/PF)×(VB1+VB3) … 式(1c) Here, the filling amount Q1 into the
Target filling amount Q = filling amount Q1 = (1−P B / P F ) × (V B1 + V B3 ) (1c)
カウンタ圧力PFおよび容器圧力PBを、第1実施形態と同様にそれぞれ5気圧(正圧)、1気圧(大気圧)とする。また、容器100の容積VB1を520mlとし、目標充填量Qを500mlとする。
これらを式(1c)に代入して、VB3について解くと以下の通りである。つまり、105(ml)以上の補室容積VB3が確保されれば、容積VB1が520mlの容器100に対して、500mlの目標充填量Qを充填できる。これをケース1とする。
目標充填量Q=500=(1-1/5)×(520+VB3)
VB2=(500-416)×4/5=105(ml) The counter pressure P F and vessel pressure P B, respectively 5 atm similarly to the first embodiment (positive pressure), and 1 atm (atmospheric pressure). Further, the volume V B1 of the container 100 is set to 520 ml, and the target filling amount Q is set to 500 ml.
Substituting these into equation (1c) and solving for V B3 is as follows. That is, if the auxiliary chamber volume V B3 of 105 (ml) or more is secured, the target filling amount Q of 500 ml can be filled into thecontainer 100 having the volume V B1 of 520 ml. This is case 1.
Target filling amount Q = 500 = (1-1 / 5) × (520 + V B3 )
V B2 = (500-416) × 4/5 = 105 (ml)
これらを式(1c)に代入して、VB3について解くと以下の通りである。つまり、105(ml)以上の補室容積VB3が確保されれば、容積VB1が520mlの容器100に対して、500mlの目標充填量Qを充填できる。これをケース1とする。
目標充填量Q=500=(1-1/5)×(520+VB3)
VB2=(500-416)×4/5=105(ml) The counter pressure P F and vessel pressure P B, respectively 5 atm similarly to the first embodiment (positive pressure), and 1 atm (atmospheric pressure). Further, the volume V B1 of the container 100 is set to 520 ml, and the target filling amount Q is set to 500 ml.
Substituting these into equation (1c) and solving for V B3 is as follows. That is, if the auxiliary chamber volume V B3 of 105 (ml) or more is secured, the target filling amount Q of 500 ml can be filled into the
Target filling amount Q = 500 = (1-1 / 5) × (520 + V B3 )
V B2 = (500-416) × 4/5 = 105 (ml)
[第2実施形態の変形例]
また、第1実施形態は二段充填行う充填装置1Aを説明し、第2実施形態は一段充填を行う充填装置1Bを説明した。ところが、充填装置1Aは、一段充填と二段充填の兼用の充填装置として用いることができる。 [Modification of Second Embodiment]
Moreover, 1st Embodiment demonstrated 1 A of filling apparatuses which perform two-stage filling, and 2nd Embodiment demonstrated fillingapparatus 1B which performs one-stage filling. However, the filling device 1A can be used as a filling device for both single-stage filling and two-stage filling.
また、第1実施形態は二段充填行う充填装置1Aを説明し、第2実施形態は一段充填を行う充填装置1Bを説明した。ところが、充填装置1Aは、一段充填と二段充填の兼用の充填装置として用いることができる。 [Modification of Second Embodiment]
Moreover, 1st Embodiment demonstrated 1 A of filling apparatuses which perform two-stage filling, and 2nd Embodiment demonstrated filling
ここで、一段充填で目標充填量を充填できるか否かは、容器100の容積および目標充填流量によるところが大きい。そこで、一段充填で目標充填量を充填できる例である前述のケース1に対して二段充填が必要となるケース2を示す。なお、ケース2においても、補室容積VB3はケース1と同じ(105ml)ものとする。
Here, whether or not the target filling amount can be filled by one-stage filling largely depends on the volume of the container 100 and the target filling flow rate. Therefore, a case 2 in which two-stage filling is required is shown with respect to the above-described case 1 which is an example in which the target filling amount can be filled in one stage filling. In case 2, the auxiliary chamber volume V B3 is the same as that in case 1 (105 ml).
ケース1、ケース2について、差圧に基づいて製品液Lを充填した後の容器内の圧力と充填量を求めた。結果は以下の通りであり、容器の容積が500mlと小さいケース1であれば一段充填で目標充填量Qを満たすことができる。これに対して、容器の容量が1000mlと大きいケース2においては一段充填では目標充填量Qを満たすことができない。また、仮に一段充填で目標充填量Qを満たすように充填すると、充填後の容器圧力PBが容器100の耐圧力PPを超えてしまう。したがって、ケース2については、複数段充填、例えば二段充填を採用することが必要である。
For Case 1 and Case 2, the pressure and filling amount in the container after filling with the product liquid L was determined based on the differential pressure. The results are as follows. If Case 1 has a small volume of 500 ml, the target filling amount Q can be satisfied by one-stage filling. On the other hand, in case 2 where the capacity of the container is as large as 1000 ml, the target filling amount Q cannot be satisfied by one-stage filling. Furthermore, assuming that the filling so as to satisfy the target filling amount Q in one stage filling, vessel pressure P B after filling may exceed the pressure resistance P P of the container 100. Therefore, for the case 2, it is necessary to adopt multi-stage filling, for example, two-stage filling.
ケース1:
容器の容積VB1:520ml 補室容積VB3:105ml 目標充填量Q:500ml
カウンタ圧力PF=5気圧
充填前の容器の圧力PB=1気圧
容器の耐圧力PP=7気圧
充填後の容器の圧力PB=(VB1+VB3)/(VB1+VB3-Q)
=625/(625-500)=5気圧
充填量Q1=(1-PB/PF)×(VB1+VB3)=4/5×625=500ml Case 1:
Container volume V B1 : 520 ml Auxiliary chamber volume V B3 : 105 ml Target filling amount Q: 500 ml
Counter pressure P F = Pressure of container before filling at 5 atmospheres P B = 1 atmosphere Pressure resistance of container P P = Pressure of container after filling at 7 atmospheres P B = (V B1 + V B3 ) / (V B1 + V B3 −Q )
= 625 / (625-500) = 5 atm Filling amount Q1 = (1-P B / P F ) × (V B1 + V B3 ) = 4/5 × 625 = 500 ml
容器の容積VB1:520ml 補室容積VB3:105ml 目標充填量Q:500ml
カウンタ圧力PF=5気圧
充填前の容器の圧力PB=1気圧
容器の耐圧力PP=7気圧
充填後の容器の圧力PB=(VB1+VB3)/(VB1+VB3-Q)
=625/(625-500)=5気圧
充填量Q1=(1-PB/PF)×(VB1+VB3)=4/5×625=500ml Case 1:
Container volume V B1 : 520 ml Auxiliary chamber volume V B3 : 105 ml Target filling amount Q: 500 ml
Counter pressure P F = Pressure of container before filling at 5 atmospheres P B = 1 atmosphere Pressure resistance of container P P = Pressure of container after filling at 7 atmospheres P B = (V B1 + V B3 ) / (V B1 + V B3 −Q )
= 625 / (625-500) = 5 atm Filling amount Q1 = (1-P B / P F ) × (V B1 + V B3 ) = 4/5 × 625 = 500 ml
ケース2:
容器の容積VB1:1040ml 補室容積VB3:105ml 目標充填量Q:1000ml
カウンタ圧力PF=5気圧
充填前の容器の圧力PB=1気圧
容器の耐圧力PP=7気圧
充填後の容器の圧力PB=(VB1+VB3)/(VB1+VB3-Q)
=1145/(1145-1000)=7.9気圧
充填量Q1=(1-PB/PF)×(VB1+VB3)=4/5×1145=916ml Case 2:
Container volume V B1 : 1040 ml Auxiliary chamber volume V B3 : 105 ml Target filling amount Q: 1000 ml
Counter pressure P F = Pressure of container before filling at 5 atmospheres P B = 1 atmosphere Pressure resistance of container P P = Pressure of container after filling at 7 atmospheres P B = (V B1 + V B3 ) / (V B1 + V B3 −Q )
= 1145 / (1145-1000) = 7.9 atmospheres Filling amount Q1 = (1-P B / P F ) × (V B1 + V B3 ) = 4/5 × 1145 = 916 ml
容器の容積VB1:1040ml 補室容積VB3:105ml 目標充填量Q:1000ml
カウンタ圧力PF=5気圧
充填前の容器の圧力PB=1気圧
容器の耐圧力PP=7気圧
充填後の容器の圧力PB=(VB1+VB3)/(VB1+VB3-Q)
=1145/(1145-1000)=7.9気圧
充填量Q1=(1-PB/PF)×(VB1+VB3)=4/5×1145=916ml Case 2:
Container volume V B1 : 1040 ml Auxiliary chamber volume V B3 : 105 ml Target filling amount Q: 1000 ml
Counter pressure P F = Pressure of container before filling at 5 atmospheres P B = 1 atmosphere Pressure resistance of container P P = Pressure of container after filling at 7 atmospheres P B = (V B1 + V B3 ) / (V B1 + V B3 −Q )
= 1145 / (1145-1000) = 7.9 atmospheres Filling amount Q1 = (1-P B / P F ) × (V B1 + V B3 ) = 4/5 × 1145 = 916 ml
一段充填を行う専用の充填装置と複数段充填を行う専用の充填装置を揃えることもできる。しかしこれでは、一段充填専用の充填装置を使用しているときに複数段充填専用の充填装置が空いてしまうこともあり得る。したがって、飲料製造者にとって、一段充填と複数段充填を兼用できる充填装置が存在することが好ましい。第1実施形態で示した充填装置1Aに必要な構成を加えれば、一段充填と複数段充填を個別に実現できる。
専 用 A dedicated filling device that performs single-stage filling and a dedicated filling device that performs multiple-stage filling can also be prepared. However, in this case, when a filling device dedicated to single-stage filling is used, the filling device dedicated to multiple-stage filling may become empty. Therefore, it is preferable for a beverage manufacturer to have a filling device that can perform both single-stage filling and multiple-stage filling. If a necessary configuration is added to the filling device 1A shown in the first embodiment, single-stage filling and multi-stage filling can be realized individually.
主に制御器2(図2)が加えることが必要な構成を備える。
制御器2は、生産の対象となる容器の種類を特定する。この種類は、容積を含む概念を有している。
一例として、容器を切り替えて生産する度に、制御器2が充填装置1Aのオペレータに容器の種類を入力するように促す。制御器2は、オペレータの制御器2への入力を受けることで容器の種類を特定する。また他の例として、制御器2に所定の期間、例えば一週間の生産計画が入力される。この生産計画に容器の種類が含まれていれば、制御器2は一週間分の容器の種類を特定できる。 The controller 2 (FIG. 2) mainly has a configuration that needs to be added.
Thecontroller 2 specifies the type of container to be produced. This type has the concept of including volume.
As an example, every time the container is switched for production, thecontroller 2 prompts the operator of the filling apparatus 1A to input the container type. The controller 2 specifies the type of container by receiving input from the operator to the controller 2. As another example, a production plan for a predetermined period, for example, one week is input to the controller 2. If this production plan includes the type of container, the controller 2 can specify the type of container for one week.
制御器2は、生産の対象となる容器の種類を特定する。この種類は、容積を含む概念を有している。
一例として、容器を切り替えて生産する度に、制御器2が充填装置1Aのオペレータに容器の種類を入力するように促す。制御器2は、オペレータの制御器2への入力を受けることで容器の種類を特定する。また他の例として、制御器2に所定の期間、例えば一週間の生産計画が入力される。この生産計画に容器の種類が含まれていれば、制御器2は一週間分の容器の種類を特定できる。 The controller 2 (FIG. 2) mainly has a configuration that needs to be added.
The
As an example, every time the container is switched for production, the
また、制御器2は、容器の種類(大きさ)に応じて一段充填と二段充填のいずれを行うかを判断する。そのためには、制御器2は、容器の種類と充填の段数とが対応付けられた容器-充填段数情報を備えることが好ましい。制御器2は、生産の開始にあたって容器の種類を特定すると、この容器-充填段数情報を参照して、一段充填か二段充填のいずれかを選択する。ここでは二段充填までしか説明しないが、三段、四段などのより多い段数の充填を選択できるようにしてもよい。
Further, the controller 2 determines whether to perform one-stage filling or two-stage filling according to the type (size) of the container. For this purpose, the controller 2 preferably includes container-filling stage number information in which the type of container and the number of filling stages are associated with each other. When the controller 2 specifies the type of container at the start of production, the controller 2 selects either one-stage filling or two-stage filling with reference to this container-filling stage number information. Although only two-stage filling will be described here, filling with a larger number of stages such as three or four stages may be selected.
制御器2は、一段充填か二段充填が選択されると、一段充填または二段充填が実現できるように、第一ガス弁VG1、第二ガス弁VG2および液弁VLの動作を制御する。一段充填の動作は第2実施形態で説明した通りであり、二段充填の動作は第1実施形態で説明した通りである。
The controller 2 controls the operation of the first gas valve VG1, the second gas valve VG2, and the liquid valve VL so that the single-stage filling or the two-stage filling can be realized when the single-stage filling or the two-stage filling is selected. The operation of one-stage filling is as described in the second embodiment, and the operation of two-stage filling is as described in the first embodiment.
以上、本発明の好ましい実施形態を説明したが、本発明の主旨を逸脱しない限り、種々の変更を加えることができる。
例えば、第1実施形態および第2実施形態においては、製品液として炭酸入りの飲料の例を説明したが、本発明は炭酸が含まれていない飲料、その他の製品液にも適用できる。
また、以上で説明したガス置換は、炭酸入りの飲料を対象としているために、炭酸ガス用いる。ところが、本発明におけるガス置換ガスは炭酸ガスに限らず、容器に充填される製品液の特性維持に必要なガス成分、例えば窒素ガスなどの不活性ガスによりガス置換することができる。
また、本実施形態で説明した容器100は樹脂製であるが、本発明において充填の対象は樹脂製の容器に限らず、可撓性を有する他の容器、例えば金属製の缶容器にも適用できる。また、本発明は可撓性を有しない例えばガラス製のびんを充填の対象から排除するものではない。 The preferred embodiments of the present invention have been described above, but various modifications can be made without departing from the spirit of the present invention.
For example, in the first embodiment and the second embodiment, an example of a carbonated beverage has been described as the product liquid. However, the present invention can also be applied to beverages that do not contain carbonic acid and other product liquids.
Further, since the gas replacement described above is intended for a carbonated beverage, carbon dioxide is used. However, the gas replacement gas in the present invention is not limited to the carbon dioxide gas, and can be replaced with a gas component necessary for maintaining the characteristics of the product liquid filled in the container, for example, an inert gas such as nitrogen gas.
Further, thecontainer 100 described in the present embodiment is made of resin, but in the present invention, the object of filling is not limited to the resin container, but is applicable to other flexible containers, for example, metal can containers. it can. In addition, the present invention does not exclude, for example, glass bottles that are not flexible from being filled.
例えば、第1実施形態および第2実施形態においては、製品液として炭酸入りの飲料の例を説明したが、本発明は炭酸が含まれていない飲料、その他の製品液にも適用できる。
また、以上で説明したガス置換は、炭酸入りの飲料を対象としているために、炭酸ガス用いる。ところが、本発明におけるガス置換ガスは炭酸ガスに限らず、容器に充填される製品液の特性維持に必要なガス成分、例えば窒素ガスなどの不活性ガスによりガス置換することができる。
また、本実施形態で説明した容器100は樹脂製であるが、本発明において充填の対象は樹脂製の容器に限らず、可撓性を有する他の容器、例えば金属製の缶容器にも適用できる。また、本発明は可撓性を有しない例えばガラス製のびんを充填の対象から排除するものではない。 The preferred embodiments of the present invention have been described above, but various modifications can be made without departing from the spirit of the present invention.
For example, in the first embodiment and the second embodiment, an example of a carbonated beverage has been described as the product liquid. However, the present invention can also be applied to beverages that do not contain carbonic acid and other product liquids.
Further, since the gas replacement described above is intended for a carbonated beverage, carbon dioxide is used. However, the gas replacement gas in the present invention is not limited to the carbon dioxide gas, and can be replaced with a gas component necessary for maintaining the characteristics of the product liquid filled in the container, for example, an inert gas such as nitrogen gas.
Further, the
さらに、一段充填は第2実施形態の手法に限るものではない。例えば、容器100の内部と貯留槽3のガス相3Sとの差圧が十分に大きく、かつ、製品液Lが目標充填量に達したときの容器100のヘッドスペース105が大きいという条件を満足すれば、一段充填を実現できる場合がある。
また、貯留槽3と容器100を繋ぐ液供給路7に容器100の容積の一部としての機能を積極的に持たせることによっても一段充填は実現される。つまり、図12において、液弁VLを閉じると、貯留槽3と液弁VLとの間は製品液Lが満たされるが、液弁VLよりも容器100の側の内部は容積VB2を有する空隙をなす。この空隙は液弁VLと容器100の間に設けられる、本発明の第二補室容積に該当する。なお、上述した第1実施形態および第2実施形態においては、補室容積VB2をゼロ、つまり第二補室容積は存在しないものとみなしている。 Furthermore, the one-stage filling is not limited to the method of the second embodiment. For example, the condition that the pressure difference between the inside of thecontainer 100 and the gas phase 3S of the storage tank 3 is sufficiently large and the head space 105 of the container 100 when the product liquid L reaches the target filling amount is satisfied. In this case, one-stage filling may be realized.
One-stage filling can also be realized by positively providing theliquid supply path 7 connecting the storage tank 3 and the container 100 as a part of the volume of the container 100. That is, in FIG. 12, when the liquid valve VL is closed, the product liquid L is filled between the storage tank 3 and the liquid valve VL, but the inside of the container 100 side of the liquid valve VL has a volume V B2. Make. This gap corresponds to the second auxiliary chamber volume of the present invention provided between the liquid valve VL and the container 100. In the first and second embodiments described above, the auxiliary chamber volume V B2 is assumed to be zero, that is, the second auxiliary chamber volume does not exist.
また、貯留槽3と容器100を繋ぐ液供給路7に容器100の容積の一部としての機能を積極的に持たせることによっても一段充填は実現される。つまり、図12において、液弁VLを閉じると、貯留槽3と液弁VLとの間は製品液Lが満たされるが、液弁VLよりも容器100の側の内部は容積VB2を有する空隙をなす。この空隙は液弁VLと容器100の間に設けられる、本発明の第二補室容積に該当する。なお、上述した第1実施形態および第2実施形態においては、補室容積VB2をゼロ、つまり第二補室容積は存在しないものとみなしている。 Furthermore, the one-stage filling is not limited to the method of the second embodiment. For example, the condition that the pressure difference between the inside of the
One-stage filling can also be realized by positively providing the
1A,1B 充填装置
2 制御器
3 貯留槽
3S ガス相
5 補室槽
6 圧力調整室
5A ピストン
5B シリンダ
7 液供給路
11 第一ガス導出路
13 第二ガス導出路
14 第三ガス排出路
15 第一圧力センサ
17 第二圧力センサ
19 第三圧力センサ
20 密閉チャンバ
21 密閉室
22 二重管構造
23 内管
24 外管
25 ノズル
27 容器保持開口
28 ガス供給路
29 ガス排出路
30 封緘材ヘッド
40 給排機構
41 液供給路
43 ガス供給路
44,46 ガス弁
45 ガス排出路
100 容器
101 口部
103 封緘材
105 ヘッドスペース
VG1 第一ガス弁
VG2 第二ガス弁
VG3 第三ガス弁
VL 液弁 1A,1B Filling device 2 Controller 3 Storage tank 3S Gas phase 5 Auxiliary chamber tank 6 Pressure adjusting chamber 5A Piston 5B Cylinder 7 Liquid supply path 11 First gas outlet path 13 Second gas outlet path 14 Third gas outlet path 15 One pressure sensor 17 Second pressure sensor 19 Third pressure sensor 20 Sealed chamber 21 Sealed chamber 22 Double tube structure 23 Inner tube 24 Outer tube 25 Nozzle 27 Container holding opening 28 Gas supply passage 29 Gas discharge passage 30 Sealing material head 40 Supply Exhaust mechanism 41 Liquid supply path 43 Gas supply path 44, 46 Gas valve 45 Gas discharge path 100 Container 101 Mouth 103 Sealing material 105 Head space VG1 First gas valve VG2 Second gas valve VG3 Third gas valve VL Liquid valve
2 制御器
3 貯留槽
3S ガス相
5 補室槽
6 圧力調整室
5A ピストン
5B シリンダ
7 液供給路
11 第一ガス導出路
13 第二ガス導出路
14 第三ガス排出路
15 第一圧力センサ
17 第二圧力センサ
19 第三圧力センサ
20 密閉チャンバ
21 密閉室
22 二重管構造
23 内管
24 外管
25 ノズル
27 容器保持開口
28 ガス供給路
29 ガス排出路
30 封緘材ヘッド
40 給排機構
41 液供給路
43 ガス供給路
44,46 ガス弁
45 ガス排出路
100 容器
101 口部
103 封緘材
105 ヘッドスペース
VG1 第一ガス弁
VG2 第二ガス弁
VG3 第三ガス弁
VL 液弁 1A,
Claims (14)
-
カウンタ圧力PFが付加された環境下で製品液が貯えられる貯留槽と、
前記貯留槽から前記製品液を容器に充填する液供給路と、
開閉することにより、前記液供給路からの前記製品液の供給を制御する液弁を有する充填ノズルと、を備え、
前記容器内の容器圧力PBが、大気圧以上の正圧であって、かつ、前記貯留槽における前記カウンタ圧力PFより低い圧力に保たれ、前記貯留槽の前記カウンタ圧力PFとの間に圧力差が形成された状態で、前記容器と前記充填ノズルとを密封状態に係合させ、
次いで、前記液弁を開き、前記製品液が前記容器に充填される、
ことを特徴とする充填装置。
A reservoir where the product solution is stored under a counter pressure P F is added environment,
A liquid supply path for filling the product liquid into the container from the storage tank;
A filling nozzle having a liquid valve for controlling the supply of the product liquid from the liquid supply path by opening and closing;
Vessel pressure P B of the vessel, a positive pressure above atmospheric pressure, and maintained at said counter pressure P F lower pressures in the reservoir, between the counter pressure P F of the reservoir In a state where a pressure difference is formed, the container and the filling nozzle are engaged in a sealed state,
Next, the liquid valve is opened, and the product liquid is filled in the container.
A filling device characterized by that.
-
前記容器圧力PBが前記カウンタ圧力PFと平衡になるまで、または、前記カウンタ圧力PF未満の所定の圧力の状態になるまで、前記製品液が充填されると前記液弁が閉じられる、
請求項1に記載の充填装置。
Until said vessel pressure P B is in equilibrium with the counter pressure P F, or the counter until a predetermined condition of a pressure below the pressure P F, the liquid valve is closed and the product liquid is filled,
The filling device according to claim 1.
-
前記容器に連通する、前記容器の容積を補完する補室を備える、
請求項1に記載の充填装置。
An auxiliary chamber that communicates with the container and supplements the volume of the container;
The filling device according to claim 1.
-
前記補室は、
前記容器から前記製品液の充填によって置換されるガス成分を導出させるガス導出路上に設けられる補室槽からなる、請求項3に記載の充填装置。
The auxiliary room is
The filling device according to claim 3, comprising a supplementary chamber tank provided on a gas lead-out path for leading a gas component to be replaced by filling the product liquid from the container.
-
前記容器と前記補室槽の間の前記ガス導出路を開閉する第一ガス弁を備え、
前記液弁が開いた状態において、前記容器の内部の前記ガス成分を外部に排出することなく、前記容器の内部の前記ガス成分を密閉したままで、前記製品液が前記容器に充填され、
設定量の前記製品液が充填されると、前記第一ガス弁を開いて、前記ガス成分の一部が前記ガス導出路を通って前記補室槽に導出される、
請求項4に記載の充填装置。
A first gas valve for opening and closing the gas outlet path between the container and the auxiliary chamber tank;
In a state where the liquid valve is opened, the product liquid is filled in the container while the gas component inside the container is sealed without discharging the gas component inside the container to the outside.
When the set amount of the product liquid is filled, the first gas valve is opened, and a part of the gas component is led out to the auxiliary chamber tank through the gas lead-out path.
The filling device according to claim 4.
-
前記容器圧力PBが前記カウンタ圧力PFと平衡になるまで、または、前記容器圧力PBが設定圧力に達するまで前記製品液が前記容器に充填され、
次いで、前記容器圧力PBと前記補室槽の圧力PRが平衡になるまで、前記ガス成分が前記補室槽に導出される、
請求項4または請求項5に記載の充填装置。
Until said vessel pressure P B is in equilibrium with the counter pressure P F, or the product fluid to said vessel pressure P B reaches a set pressure is filled into the container,
Then, the pressure P R of the auxiliary chamber vessel and the vessel pressure P B is until equilibrium, the gas component is led to the auxiliary chamber tank,
The filling device according to claim 4 or 5.
-
前記ガス成分が前記補室槽に導出されることで、前記容器圧力PBは前記カウンタ圧力PFより低い前記圧力差が形成され、
次いで、前記液弁を開いた状態で、目標充填量との差分に対応する量の前記製品液が前記容器に充填される、
請求項6に記載の充填装置。
Said that the gas components are guided to the auxiliary chamber vessel, the vessel pressure P B is the pressure differential lower than the counter pressure P F is formed,
Next, in a state where the liquid valve is opened, the container is filled with an amount of the product liquid corresponding to a difference from a target filling amount.
The filling device according to claim 6.
-
前記補室槽は、前記差分に対応する容積を有する、
請求項7のいずれか一項に記載の充填装置。
The auxiliary chamber tank has a volume corresponding to the difference,
The filling device according to claim 7.
-
前記補室槽は、その内容積が可変の構造を有する、
請求項4~請求項8のいずれか一項に記載の充填装置。
The auxiliary chamber tank has a structure whose internal volume is variable,
The filling device according to any one of claims 4 to 8.
-
前記補室は、
前記容器から排出されるガス成分を導出するガス導出路の内部の空隙からなる第一補室容積、および、前記液弁と前記容器の間における前記液供給路の内部の空隙からなる第二補室容積の一方または双方である、
請求項3に記載の充填装置。
The auxiliary room is
A first auxiliary chamber volume consisting of a gap inside the gas outlet path for leading the gas component discharged from the container, and a second auxiliary chamber consisting of a gap inside the liquid supply path between the liquid valve and the container. One or both of the chamber volumes,
The filling device according to claim 3.
-
前記液弁が閉じた状態で、前記第一補室容積または前記第二補室容積と前記容器の内部とが連通して形成される空間における前記容器圧力PBと前記カウンタ圧力PFとの間に前記圧力差が形成される、
請求項10に記載の充填装置。
In a state where the liquid valve is closed, and the first auxiliary chamber volume or the second auxiliary chamber volume and the interior of the container and the vessel pressure P B in a space is formed in communication with the counter pressure P F The pressure difference is formed between,
The filling device according to claim 10.
-
前記第一補室容積または前記第二補室容積は、一度の前記圧力差の形成および前記製品液の充填を通じて、目標充填量を満たす前記製品液の充填をするのに足りる容積を有する、
請求項11に記載の充填装置。
The first auxiliary chamber volume or the second auxiliary chamber volume has a volume sufficient to fill the product liquid that satisfies a target filling amount through the formation of the pressure difference once and the filling of the product liquid.
The filling device according to claim 11.
-
前記容器圧力PBが前記カウンタ圧力PFと平衡になるまで、または、前記容器圧力PBが設定圧力に達するまで前記製品液が前記容器に充填される、
請求項10~請求項12のいずれか一項に記載の充填装置。
Until said vessel pressure P B is in equilibrium with the counter pressure P F, or the product fluid to said vessel pressure P B reaches the set pressure is filled into the container,
The filling device according to any one of claims 10 to 12.
-
前記第一補室容積または前記第二補室容積は、目標充填量との差分に対応する容積を有する、
請求項10~請求項13のいずれか一項に記載の充填装置。
The first auxiliary chamber volume or the second auxiliary chamber volume has a volume corresponding to a difference from a target filling amount,
The filling device according to any one of claims 10 to 13.
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2019
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- 2019-01-08 WO PCT/JP2019/000260 patent/WO2019207843A1/en active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS59199492A (en) * | 1983-07-27 | 1984-11-12 | 三菱重工業株式会社 | Liquid filler |
JPH03176398A (en) * | 1989-11-30 | 1991-07-31 | Mitsubishi Heavy Ind Ltd | Filling method for liquid |
JPH07300196A (en) * | 1994-05-10 | 1995-11-14 | Mitsubishi Heavy Ind Ltd | Charging method and device with charging valve |
JP2001139095A (en) * | 1999-11-16 | 2001-05-22 | Shibuya Kogyo Co Ltd | Gas flush filling machine |
JP2014221644A (en) * | 2013-05-13 | 2014-11-27 | 三菱重工食品包装機械株式会社 | Liquid filling device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4450452A1 (en) * | 2023-04-17 | 2024-10-23 | Krones Ag | Device and method for filling containers with a filling product |
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JP7163371B2 (en) | 2022-10-31 |
JPWO2019207843A1 (en) | 2021-03-18 |
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