JP2017024760A - Method and device for vaporizing bactericide - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for vaporizing a bactericide, the method allowing for simplification of the construction of a supply system regarding a bactericide and compressed air.SOLUTION: The method for vaporizing a bactericide of the present comprises: a first step of sucking a liquid bactericide stored in a storage pot into a flow channel by generating a Venturi effect on an optional position of the flow channel through which the compressed air flows from an upstream side toward a downstream side, thereby converting the liquid bactericide into a mist by pressure of the compressed air; and a second step of vaporizing a mist-like bactericide conveyed by the compressed air, in the process of passing of the mist-like bactericide through the flow channel at a downstream side of the optional position.SELECTED DRAWING: Figure 1

Description

  The present invention relates to an apparatus for vaporizing a liquid sterilizing agent when a beverage container is sterilized with a sterilizing agent.

In an aseptic filling system that fills containers with beverages, the containers are sterilized using a disinfectant such as hydrogen peroxide (H ₂ O ₂ ), peracetic acid (C ₂ H ₄ O ₃ ) before filling the beverage. .
Patent Document 1 proposes to blow hot air mixed with vaporized hydrogen peroxide from a nozzle inserted into a PET (Polyethylene Terephthalate) bottle as this sterilization method. According to the sterilization method of Patent Document 1, the sterilization condition of introducing hydrogen peroxide mist into the inside of the PET bottle for a certain period of time at a constant temperature can be easily realized. Can be obtained.
In the sterilization method of Patent Document 1, in order to vaporize hydrogen peroxide, an aqueous solution of hydrogen peroxide and compressed air are passed through a two-fluid nozzle to form a mist of the aqueous solution of hydrogen peroxide, and this is heated with a heater. ing.

JP 2010-132358 A

In order to generate hydrogen peroxide mist using a two-fluid nozzle, a system for supplying an aqueous solution of hydrogen peroxide to the two-fluid nozzle and a system for supplying compressed air are required. The beverage filling system usually prepares a number of filling nozzles corresponding to a number of containers held in a rotary conveying device called a star wheel, and the beverage is filled through the filling nozzles. . The mechanism for vaporizing hydrogen peroxide including the two-fluid nozzle in Patent Document 1 is also required in a number corresponding to the filling nozzle. Therefore, the total number of systems for supplying an aqueous solution of hydrogen peroxide and systems for supplying compressed air increases, and the configuration becomes complicated.
Accordingly, an object of the present invention is to provide a bactericide vaporizing method and apparatus capable of simplifying the configuration of a supply system related to a bactericidal agent and compressed air in a system for vaporizing a bactericidal agent and supplying it to a sterilization target. To do.

The method for vaporizing a sterilizing agent according to the present invention causes a liquid sterilizing agent stored in a storage pot to flow through a flow path by causing a venturi effect at an arbitrary position in the flow channel where compressed air flows from the upstream side toward the downstream side. The first step of making the sterilizing agent mist-like by the pressure of compressed air and the mist-like sterilizing agent conveyed by the compressed air pass through the flow path downstream from an arbitrary position. And a second step of vaporizing in the process.
In the method for vaporizing a bactericidal agent according to the present invention, a venturi effect is produced, the bactericidal agent is sucked, and the bactericidal agent is made into a mist by compressed air flowing through the flow path. Therefore, according to the method for vaporizing a bactericidal agent according to the present invention, it is only necessary to store the bactericidal agent in a storage pot. For example, when a two-fluid nozzle is used, a mechanism for pumping the bactericidal agent is required. Compared to this, the system configuration can be simplified and reduced in cost. In addition, since the venturi tube for obtaining the venturi effect is usually cheaper than the two-fluid nozzle, the sterilization system to which the present invention is applied becomes low in cost.

In the first step of the bactericide vaporizing method of the present invention, the amount of the liquid bactericide sucked into the flow path can be controlled to be constant.
Thereby, in the 2nd step, since the density | concentration of the vaporized disinfectant contained in compressed air can be made constant, the desired disinfection performance can be obtained.

  Various means for controlling the amount of the liquid sterilizing agent sucked into the flow path to be constant can be adopted, but the present invention can adopt the following means. That is, in the first step, the liquid sterilizing agent is sucked through a suction tube having a suction port and a discharge port, and the suction tube is inserted into the liquid sterilizing agent stored in the storage pot, and discharged. The amount of the liquid sterilizing agent sucked can be controlled to be constant by adjusting the depth d inserted into the sterilizing agent by the outlet communicating with the flow path where the venturi effect has occurred.

In the method for vaporizing a bactericide according to the present invention, in the second step, a heater provided around the flow path heats the flow path, thereby vaporizing the mist-shaped bactericide.
Thus, if a heater is provided around the flow path, there is no need to provide a special place for the heater, which contributes to space saving of the sterilization system.

In the first step, the bactericide vaporizing method of the present invention can preheat the compressed air.
Thereby, vaporization of the disinfectant in the second step can be performed more reliably.

The present invention provides the following vaporization apparatus for realizing the above-described method for vaporizing a bactericide according to the present invention.
That is, the bactericide vaporizing apparatus of the present invention is provided with a supply pipe having a flow path through which compressed air flows from the upstream side toward the downstream side, and at any position of the flow path of the supply pipe. A venturi tube provided with a suction port at one end, a discharge port at the other end, a suction tube connected to the pressure outlet, and a liquid disinfectant are stored, and the suction port of the suction tube It is characterized by comprising a storage pot into which the side is inserted and a heater for heating the flow path downstream of the venturi tube.

  In the bactericide vaporizing apparatus of the present invention, it is preferable that the suction port side of the suction pipe can adjust the insertion depth d into the bactericide stored in the storage pot.

  In the bactericide vaporizing apparatus of the present invention, the insertion depth d is preferably controlled to be constant.

  In the disinfectant vaporizing apparatus of the present invention, it is preferable that the storage pot is provided so as to be movable up and down.

  According to the method for vaporizing a bactericidal agent according to the present invention, it is only necessary to store the bactericidal agent in a storage pot. For example, when a two-fluid nozzle is used, a mechanism for pumping the bactericidal agent is required. In comparison, the system configuration can be simplified and reduced in cost. In addition, since the venturi tube for obtaining the venturi effect is usually cheaper than the two-fluid nozzle, the sterilization system to which the present invention is applied becomes low in cost.

It is a figure which shows the procedure of the sterilization system which concerns on this embodiment. It is a figure which shows schematic structure of the vaporization apparatus which concerns on this embodiment. It is a figure showing a schematic structure of a venturi pipe concerning this embodiment. It is a figure which shows the raising / lowering procedure of the storage pot in the vaporization apparatus which concerns on this embodiment.

Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.
As shown in FIG. 1, the sterilization system 1 according to the present embodiment sterilizes the inner peripheral surface of a container 100 made of, for example, a PET bottle. The sterilization system 1 includes a washing step S1 for washing the inner peripheral surface with warm water, a drying step S3 for blowing hot air into the container 100 and drying, and a sterilizing agent vaporized inside the container 100 for blowing inside. A sterilization step S5 for sterilizing the peripheral surface and finally a rinsing step S7 for washing away the sterilizing agent attached to the inner peripheral surface of the container 100 are included. The present embodiment is characterized by a method for vaporizing a sterilizing agent in the sterilizing step.
FIG. 1 shows only the steps related to sterilization. However, the container 100 is continuously formed in the pre-process of the sterilization method including these steps, or the beverage is continuously provided in the container 100 in the post-process. Or filling.

In the sterilization system 1 of the present embodiment, first, the cleaning step S1 is performed.
The cleaning step S <b> 1 is performed for the purpose of washing away foreign substances adhering to the inner peripheral surface of the container 100. In the cleaning step S <b> 1, the nozzle 2 is inserted from the mouth portion 101 of the inverted container 100 and hot water is blown from the nozzle 2, thereby cleaning the inner peripheral surface of the container 100.
The sterilization system 1 includes a hot water source 5, a hot water pipe 6 that guides the hot water generated by the hot water source 5 to the nozzle 2, and a pump 7 provided in the hot water pipe 6 in order to perform the cleaning step S <b> 1. . The hot water source 5 is constituted by, for example, a water tank provided with a heater.
In addition, the warm water blown in should just be about 60-80 degreeC.

The container 100 cleaned in the cleaning step S1 is supplied to the drying step S3. The drying step S3 is performed for the purpose of removing warm water (water) remaining on the inner peripheral surface in the cleaning step S1. This is because if water remains on the inner peripheral surface, the efficiency of sterilization by hydrogen peroxide performed next is inferior. In the drying step S <b> 3, the nozzle 3 is inserted from the mouth portion 101 of the container 100 into the inside, and warm air is blown from the nozzle 3, thereby drying and removing moisture remaining on the inner peripheral surface of the container 100.
The sterilization system 1 includes an air supply source 9, an air supply pipe 10 that guides compressed air generated by the air supply source 9 to the nozzle 3, and a heater provided around the air supply pipe 10 in order to perform the drying step S <b> 3. 11.
In addition, the warm air blown should just be about 60-100 degreeC.

  The container 100 whose inner peripheral surface has been dried is then subjected to a sterilization step S5. In the sterilization step S5, the nozzle 12 is inserted into the container 100 from the mouth portion 101, and the hydrogen peroxide vaporized from the nozzle 12 is blown to sterilize the inner peripheral surface of the container 100. The sterilization step S5 includes a vaporizer 20 that vaporizes hydrogen peroxide. The vaporizer 20 is a characteristic part in the present embodiment, and a specific configuration will be described later.

  The container 100 that has been sterilized is then subjected to a rinsing step S7. In the rinsing step S <b> 7, the nozzle 13 is inserted into the inside from the mouth portion 101 of the container 100, and rinse water is blown from the nozzle 13, thereby washing away the sterilizing agent remaining on the inner peripheral surface of the container 100. In order to perform the rinsing step S7, the sterilization system 1 includes a rinsing water storage tank 14, a rinsing water pipe 15 for guiding the rinsing water stored in the rinsing water storage tank 14 to the nozzle 13, and a pump 16 provided in the rinsing water pipe 15. It is equipped with. The rinsed container 100 is transferred to a lower process, for example, a beverage filling process.

Next, the vaporizer 20 will be described.
The vaporizer 20 draws a liquid sterilizing agent into the flow path through which the compressed air flows by a venturi effect and forms a mist, and further heats the mist-shaped sterilizing agent as it flows through the flow path using the compressed air as a carrier. Vaporize the agent. The vaporizer 20 has the following configuration in order to vaporize the bactericide.

  As shown in FIGS. 2 and 3, the vaporizer 20 includes a supply pipe 30 in which a flow path 31 through which the compressed air CA flows from the upstream side toward the downstream side is formed, and a flow path 31 of the supply pipe 30. A venturi tube 40 provided at an arbitrary position; a suction port 51 provided at one end; a discharge port 52 provided at the other end; and the suction tube 50 connected to the pressure outlet 47 of the venturi tube 40; Prepare. The vaporizer 20 includes a storage pot 55 in which the liquid sterilizer S is stored, and a heater 58 that heats the flow path 31 on the downstream side of the venturi tube 40.

  The venturi tube 40 is a cylindrical venturi tube as shown in the middle stage of FIG. 3, and includes an inlet cylindrical portion 41 located on the most upstream side, an inlet conical portion 42 connected downstream of the inlet cylindrical portion 41, and an inlet The throat part 43 is connected to the downstream side of the conical part 42, the outlet conical part 44 is connected to the downstream side of the throat part 43, and the outlet cylindrical part 45 is connected to the outlet conical part 44 and located on the most downstream side. . The venturi tube 40 is formed with a flow path 46 penetrating from the inlet cylindrical portion 41 to the outlet cylindrical portion 45. In the throat portion 43 of the venturi tube 40, a pressure outlet 47 that communicates with the outside and the flow path 46 is formed.

  In the venturi tube 40, the inlet cylindrical portion 41 and the outlet cylindrical portion 45 are formed so that the opening diameter of the flow path 46 is equal from the upstream side toward the downstream side. In the inlet cone portion 42, the opening diameter of the flow path 46 continuously decreases from the upstream side to the downstream side, and the outlet cone section 44 has the opening diameter of the flow path 46 from the upstream side to the downstream side. It is increasing continuously. The throat portion 43 located between the inlet cone portion 42 and the outlet cone portion 44 is formed so that the opening diameter of the flow path 46 is equal from the upstream side toward the downstream side. Comparing the entrance cone portion 42 and the exit cone portion 44, the entrance cone portion 42 is steeper to the extent that the opening diameter decreases (changes) than the exit cone portion 44.

When the compressed air CA passes through the venturi 40, the following behavior occurs in the flow path 46. Please refer to the upper pressure diagram in FIG.
The flow rate of the compressed air CA that has entered from the inlet cylindrical portion 41 increases because the flow path 46 narrows in the course of flowing through the inlet cone portion 42 and the throat portion 43 in this order. For this reason, pressure energy is converted into velocity energy according to Bernoulli's theorem, so that the pressure in the throat portion 43 drops most. A pressure take-out port 47 is formed in the throat portion 43, and a suction pipe 50 is connected thereto, so that fluid can be sucked through the suction port 51 of the suction pipe 50. In the present embodiment, the sterilizing agent S stored in the storage pot 55 is sucked, and the sucked sterilizing agent S is discharged through the suction pipe 50 to the flow path 46 corresponding to the throat portion 43. Since the compressed air CA continuously flows in the flow path 46, the discharged sterilizing agent S is atomized by the force of the compressed air CA and becomes mist.
On the downstream side of the throat portion 43, the outlet cone portion 44 whose opening diameter increases toward the downstream side is provided, so that the pressure of the compressed air CA is recovered and the supply pipe 30 is further directed toward the downstream side. Flowing.

The storage pot 55 includes a storage tank 56 that stores the sterilizing agent S, and is arranged so that the storage tank 56 is positioned on the downward extension of the suction pipe 50 of the venturi pipe 40. The capacity of the storage tank 56 is set so that the sterilizing agent S is not insufficient while the sterilization system 1 is continuously operated.
The storage pot 55 is supported by an actuator 57 and can be moved up and down by driving the actuator 57. As shown in FIG. 4, the storage pot 55 includes a suction port 51 of the suction pipe 50 from the storage tank 56. It is possible to move up and down between an upper position (see FIG. 4C) where the suction port 51 side is inserted to the vicinity of the bottom of the storage tank 56 from a lower position (see FIG. 4D).
When the sterilization of the planned number is completed and the sterilizing agent S stored in the storage tank 56 is insufficient, the storage pot 55 is lowered to a lower position and the sterilizing agent S is replenished. When the sterilization is continuously performed, the storage pot 55 is disposed at a height at which the suction pipe 50 is inserted by a predetermined depth d from the liquid level SS of the sterilizing agent S stored in the storage tank 56. Thereafter, even if the sterilizing agent S is consumed and the liquid level SS is lowered, the actuator 57 is driven to raise the storage pot 55 so that the depth d at which the suction pipe 50 is inserted from the floating surface of the sterilizing agent S is maintained. Let Control for raising the storage pot 55 is arbitrary, control based on the passage of time since the start of sterilization, control based on a change in the height of the liquid level SS of the sterilizing agent S stored in the storage tank 56, storage Control based on a change in the weight of the bactericide S stored in the tank 56 can be employed.
Since the amount of the sterilizing agent S to be sucked is determined by the depth d, in the present embodiment, the depth d is controlled to be constant so that the amount of the sterilizing agent S to be sucked becomes constant. As described above, in the present embodiment, the insertion depth d can be adjusted.

The heater 58 heats the flow path 31 of the supply pipe 30 on the downstream side of the venturi pipe 40.
The heating of the flow path 31 by the heater 58 is for vaporizing the mist-like hydrogen peroxide flowing through the flow path 31 by the compressed air CA, so that it is in the range of 200 to 300 ° C., preferably in the range of 240 to 260 ° C. Heat to. If this heating condition is obtained, the form of the heater 58 is not limited. In the present embodiment, the heater 58 disposed on the outer periphery of the supply pipe 30 is shown, but the heater 58 can be disposed on the inner peripheral surface of the supply pipe 30.

Now, the operation of the sterilization system 1 will be described focusing on the vaporizer 20.
When the container 100 that has passed through the cleaning step S1 and the drying step S3 is transferred to a predetermined position in the sterilization step S5, the air supply source 53 is driven to blow the compressed air CA into the flow path 31 of the supply pipe 30. At this time, in addition to the suction port 51 of the suction pipe 50 being inserted from the liquid level SS of the disinfectant S stored in the storage tank 56 to a predetermined depth d, the heater 58 warms the flow path 46. ing. Then, the disinfectant S is sucked into the suction pipe 50 and further discharged to the flow path 46 through the pressure outlet 47 of the throat portion 43. The liquid sterilizing agent S discharged to the flow path 46 becomes a mist form under the force of the compressed air CA flowing through the flow path 46. This corresponds to the first step of the present invention.
The mist-like disinfectant S conveyed using the compressed air CA as a carrier is vaporized in the process of passing through the heating region of the flow path 46. This corresponds to the second step of the present invention. The vaporized disinfectant S is supplied to the inside of the container 100 together with the compressed air CA, so that the inner peripheral surface of the container 100 is sterilized.

Next, the effect of the sterilization system 1 according to the present embodiment will be described.
First, the vaporizer 20 in the sterilization system 1 causes the venturi effect in the flow path 46 of the venturi pipe 40 to suck the bactericidal agent S through the suction pipe 50, and mists the bactericidal agent S with the compressed air CA flowing through the flow path 46. Shape. Therefore, according to the sterilization system 1, it is only necessary to store the sterilizing agent S in the storage pot 55. For example, when a two-fluid nozzle is used, a mechanism for pumping the sterilizing agent S is required. In comparison, the system configuration can be simplified and reduced in cost. In addition, since the venturi tube 40 is usually cheaper than the two-fluid nozzle, the vaporizer 20 contributes to the cost reduction of the sterilization system 1.

  Here, in the present embodiment, only the single sterilization step S5 has been described. However, in an actual beverage filling system, each container 100 is vaporized while being transported by a rotary transport device. B. Disinfectant S is supplied. Therefore, since the number of mist generation means corresponding to the number of containers 100 to be processed is necessary, in order to reduce the cost of the sterilization system 1, it is important to make the system configuration simple and low cost.

  Next, since the vaporizer 20 maintains a constant depth d at which the suction port 51 of the suction pipe 50 is inserted from the liquid surface SS of the sterilizing agent S, the amount of the sterilizing agent S sucked by the suction pipe 50 is Regardless of the progress of the sterilization step S5, it can be made constant. Thereby, since the density | concentration of the disinfectant S supplied with the compressed air CA to the container 100 can be maintained, the bactericidal effect of the container 100 can be obtained stably. In addition, in the present embodiment, since it is sufficient to control the position of the storage pot 55 with respect to the suction pipe 50, the control is simple.

Further, the vaporizer 20 is vaporized by heating by the heater 58 in the course of passing the sterilized sterilizing agent S together with the compressed air CA through the flow path 31, so that the possibility of directly touching the heater member is extremely high. Low.
For example, the liquid bactericidal agent S can be vaporized by dropping it on a heated heater member, but the energy required for vaporization becomes larger than that of a mist.
Further, when the liquid sterilizing agent S is dropped on the heater member, a residue is generated on the heater member after vaporization depending on the type of the sterilizing agent S. For example, an aqueous peracetic acid solution as a bactericide contains a stabilizer in order to maintain chemical equilibrium, and this stabilizer becomes a residue. Then, the residue must be removed so that the necessary heating can be continued, which hinders continuous operation of the sterilization system.
On the other hand, since the vaporizer 20 is vaporized in the process in which the sterilized sterilizing agent S passes through the flow path 46 together with the compressed air CA, the vaporization energy may be small and a residue may be generated. Since the property is extremely small, the possibility that the continuous operation is hindered by the residue is very small.
Furthermore, since the vaporizer 20 only needs to provide the heater 58 around the supply pipe 30, it is not necessary to provide a special place for the heater 58, which contributes to space saving of the sterilization system 1.

  In addition to the above, as long as the gist of the present invention is not deviated, the configuration described in the above embodiment can be selected or changed to another configuration as appropriate.

In the present embodiment, the example in which the heater 58 is provided on the downstream side of the venturi tube 40 has been described. However, the heater may be provided on the upstream side of the venturi tube 40. This upstream heater can also be provided to preliminarily heat the compressed air CA flowing into the venturi tube 40.
Further, if the compressed air CA is preheated, the warm air used in the drying step S3, which is the previous process of the sterilization step S5, can be used as the compressed air CA. That is, since the air supply source 9 can be shared as the air supply source 53, the cost of the sterilization system 1 can be reduced.

  Moreover, in this embodiment, in order that the suction inlet 51 of the suction pipe 50 may maintain the insertion depth d from the liquid level SS of the disinfectant S, the storage pot 55 is raised, but the depth d can be maintained. If it is, the means is not asked. For example, the present invention allows for the addition of bactericidal agent S by the amount consumed. The depth d can vary depending on, for example, the type of the product liquid, and can be changed to dX for the product liquid X and dY for the product liquid Y.

  Moreover, in this embodiment, although the example which passes through the procedure of washing | cleaning step S1, drying step S3, sterilization step S5, and rinse step S7 was demonstrated, the summary of this invention exists in sterilization step S5, About the pre-process and a post process Is optional.

DESCRIPTION OF SYMBOLS 1 Sterilization system 2, 3 Nozzle 5 Hot water source 6 Hot water pipe 7 Pump 9 Air supply source 10 Air supply pipe 11 Heater 12, 13 Nozzle 20 Vaporizer 30 Supply pipe 31 Flow path 40 Venturi pipe 41 Inlet cylindrical part 42 Inlet cone part 43 Throat portion 44 Outlet conical portion 45 Outlet cylindrical portion 46 Channel 47 Pressure outlet 50 Suction tube 51 Suction port 52 Discharge port 53 Air supply source 55 Storage pot 56 Storage tank 57 Actuator 58 Heater 100 Container 101 Port

Claims (9)

By generating a venturi effect at an arbitrary position in the flow path where the compressed air flows from the upstream side toward the downstream side, the liquid sterilant stored in the storage pot is sucked into the flow path, and the pressure of the compressed air A first step to mist the disinfectant by:
A second step of vaporizing the mist-disinfecting disinfectant conveyed by the compressed air in the course of passing through the flow path downstream from the arbitrary position;
A method for vaporizing a disinfectant, comprising: In the first step,
The amount of the liquid sterilizing agent sucked into the flow path is controlled to be constant,
The method for vaporizing a bactericide according to claim 1. In the first step,
The liquid sterilizer is sucked through a suction pipe having a suction port and a discharge port,
The suction tube is
The suction port is inserted into the liquid disinfectant stored in the storage pot,
The discharge port communicates with the flow path in which the venturi effect has occurred,
The suction port controls the amount of the liquid sterilizing agent to be sucked constant by adjusting the depth d inserted into the sterilizing agent,
The method for vaporizing a bactericide according to claim 2. In the second step,
A heater provided around the flow path heats the flow path to vaporize the sterilized mist.
The method for vaporizing a bactericide according to any one of claims 1 to 3. In the first step,
The compressed air is preheated,
The method for vaporizing a bactericide according to any one of claims 1 to 4. A supply pipe having a flow path through which compressed air flows from the upstream side toward the downstream side;
A venturi pipe provided at an arbitrary position of the flow path of the supply pipe and having a pressure outlet in the throat portion;
A suction pipe having a suction port at one end and a discharge port at the other end, the discharge port being connected to the pressure outlet;
A storage pot in which a liquid disinfectant is stored and the suction port side of the suction pipe is inserted,
A heater for heating the flow path downstream of the venturi pipe;
A bactericide vaporizing apparatus comprising: The depth d into which the suction port side of the suction pipe is inserted into the disinfectant stored in the storage pot is adjustable.
The disinfectant vaporizer according to claim 6. The depth d is controlled to be constant,
The disinfectant vaporizer according to claim 7. The storage pot is provided to be movable up and down;
The vaporizer of the disinfectant according to any one of claims 6 to 8.

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