WO2017065177A1 - Sterilization system - Google Patents

Sterilization system Download PDF

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Publication number
WO2017065177A1
WO2017065177A1 PCT/JP2016/080261 JP2016080261W WO2017065177A1 WO 2017065177 A1 WO2017065177 A1 WO 2017065177A1 JP 2016080261 W JP2016080261 W JP 2016080261W WO 2017065177 A1 WO2017065177 A1 WO 2017065177A1
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Prior art keywords
sterilization
plasma
sterilized
sterilizing
sterilization means
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PCT/JP2016/080261
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French (fr)
Japanese (ja)
Inventor
東山堅一
冨永健太
平山裕二
芳原和希
飯塚利昭
守家智士
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サントリーホールディングス株式会社
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Priority to JP2017545437A priority Critical patent/JP6843056B2/en
Publication of WO2017065177A1 publication Critical patent/WO2017065177A1/en

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/08Radiation
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/14Plasma, i.e. ionised gases
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/16Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances

Definitions

  • the present invention relates to a sterilization system for sterilizing an object to be sterilized such as a cap of a container.
  • Patent Document 1 describes a method of sterilizing a container by blowing a sterilizing agent containing hydrogen peroxide into the container or its cap.
  • the sterilization system is Plasma sterilization means for generating plasma and sterilizing the object to be sterilized with the obtained plasma,
  • the plasma sterilizing means is supplied with water vapor,
  • the plasma sterilizing means discharges a sterilizing agent containing the generated plasma, and active oxygen generated by the reaction between the supplied water vapor and the plasma,
  • another sterilization means for sterilizing the article to be sterilized by a method different from the plasma sterilization means is provided on a conveyance line for conveying the article to be sterilized.
  • the sterilization method using a sterilizing agent containing plasma and active oxygen is a novel sterilization method, there is a problem that a desired sterilization effect can be actually obtained when newly introduced into equipment. . Therefore, in the above configuration, in addition to the plasma sterilization means, for example, the sterilization efficiency and operation reliability (whether to operate without defects) that have already been introduced into the facility have been demonstrated by a method different from the plasma generation means. Even if the desired sterilization effect cannot be obtained by the plasma sterilization means, other sterilization means for sterilizing the sterilized material can be provided on the transport line for transporting the sterilized material. The object to be sterilized can be sterilized reliably.
  • the plasma sterilization means and the other sterilization means can be switched to sterilize the article to be sterilized.
  • the plasma sterilization means and the other sterilization means are provided in parallel on the transport line.
  • the sterilizing agent when the other sterilization means is sterilizing is the plasma sterilization means. It is possible to effectively suppress the situation that the gas flows back into the plasma sterilization means.
  • the plasma sterilization means and the other sterilization means are provided in series on the transfer line.
  • the object to be sterilized can only be sterilized by any one of the sterilization means, but according to this configuration, the plasma can be obtained by stopping one of the operations.
  • the plasma sterilization means and the other sterilization means are provided in the same aseptic chamber.
  • both sterilization means are provided in the same aseptic chamber, it is possible to save space compared to providing both sterilization means in separate aseptic chambers.
  • the plasma sterilizing means is provided with a control unit that ejects air for preventing backflow from the discharge port of the sterilizing agent.
  • both sterilization means are provided in the same aseptic chamber, other sterilization agents when other sterilization means are sterilizing may reach the plasma sterilization means and flow back into the plasma sterilization means.
  • this structure it can suppress effectively that other sterilizing agents flow backward in a plasma sterilization means with the air for backflow prevention.
  • the plasma sterilizing means is provided with a contracting means for contracting the article to be sterilized.
  • sterilization using active oxygen does not need to give heat to the object to be sterilized so as to cause heat shrinkage. Therefore, sterilization by plasma sterilization means hardly causes heat shrinkage to the object to be sterilized.
  • conventionally used sterilization means for example, sterilization using the above-described sterilizing agent containing hydrogen peroxide
  • the size of the object to be sterilized that has been sterilized only by the plasma sterilizing means and the object to be sterilized only by the other sterilizing means vary depending on the difference in shrinkage.
  • the object to be sterilized is contracted by the contraction means, so that variation in the size of the object to be sterilized can be effectively suppressed.
  • the contraction means is a heating means for heating the article to be sterilized.
  • the sterilization system 100A of this embodiment sterilizes a cap 80 of a container such as a PET bottle as an example of an object to be sterilized.
  • sterilization system 100A is provided with plasma sterilization means 120 which has a plurality of plasma sterilization devices which generate plasma and sterilize cap 80 with the obtained plasma.
  • the plasma sterilizer 1 is supplied with water vapor, and the supplied water vapor and the plasma react to generate active oxygen (Reactive Oxidizing Species (ROS), for example, OH radical or single oxygen).
  • ROS reactive Oxidizing Species
  • the plasma sterilization apparatus 1 then sterilizes the cap 80 by discharging a sterilizing agent containing the generated plasma and the generated active oxygen. Therefore, first, the apparatus configuration of the plasma sterilization apparatus 1 (hereinafter simply referred to as the sterilization apparatus 1) for performing sterilization using active oxygen will be described.
  • FIG. 1 shows a mechanism for generating active oxygen by the sterilizer 1.
  • the sterilizer 1 has a nozzle 10 that generates active oxygen and discharges (irradiates) a sterilizing agent 70 containing active oxygen to the cap 80.
  • the nozzle 10 includes a plasma generation unit 11 that generates plasma, a discharge port 12 that discharges a bactericide 70 containing plasma and active oxygen, and a relay unit 13 between the plasma generation unit 11 and the discharge port 12.
  • FIG. 1 shows a configuration in which the sterilizer 1 directly discharges the sterilizing agent 70 containing active oxygen to the cap 80.
  • the present invention is not limited to this.
  • the cap 80 may be sterilized indirectly, such as by discharging the sterilizing agent 70 into the chamber through which the cap 80 passes and sterilizing the cap 80 with the sterilizing agent 70 filled in the chamber.
  • This nozzle 10 generates so-called atmospheric pressure plasma as plasma in the apparatus.
  • atmospheric pressure plasma By using atmospheric pressure plasma, it is possible to reduce the cost of the apparatus without requiring a vacuum vessel or the like necessary for generating low-pressure plasma, and the work efficiency is high because continuous processing is possible. Moreover, since it can produce
  • generation of atmospheric pressure plasma hereinafter simply referred to as plasma
  • plasma generation of atmospheric pressure plasma (hereinafter simply referred to as plasma) by the nozzle 10 and generation of active oxygen using the plasma will be described.
  • the plasma generator 11 has a known structure and includes an internal electrode 11a and an external electrode 11b.
  • an electric field is generated in the plasma generation unit 11 by applying a high voltage (for example, an effective voltage of 20 kV at a frequency of 14 kHz) between the internal electrode 11 a and the external electrode 11 b by the AC power supply 20.
  • plasma is produced
  • the generated plasma is sent to the relay unit 13.
  • oxygen (O 2 , oxygen) is supplied as an example of gas into the plasma generation unit 11, and the plasma generation unit 11 generates oxygen plasma containing ozone as plasma. Specifically, oxygen radicals and ozone (O 3 ) are generated by the plasma, and these are sent to the relay unit 13.
  • the relay unit 13 is connected to an evaporator 40 (an example of a water vapor supply unit, which will be described in detail later), and further water vapor is sent to the relay unit 13.
  • the plasma oxygen radical and ozone
  • oxygen plasma oxygen radicals and ozone
  • water vapor hydroxy radicals (.OH) that are particularly reactive among active oxygens are mainly generated.
  • the hydrogen radical reacts with ozone to generate a hydroxy radical and oxygen (O 2 ) as shown in the following formula (2).
  • the reaction of the above formula (3) can be caused to generate hydroxy radicals (.OH) efficiently.
  • the generated active oxygen mainly contains hydroxy radicals.
  • a high bactericidal effect can be achieved by mainly including highly reactive hydroxy radicals.
  • the sterilizer 1 includes a generator 21 and a transformer 22 that constitute an AC power source 20 in addition to the nozzle 10, a gas supply device 30 that supplies various gases to the nozzle 10 and the evaporator 40, an evaporator 40 that sends water vapor to the relay unit 13, and an evaporator 40. And a chiller 60 for supplying cooling water to the nozzle 10.
  • Generator 21 generates an alternating current.
  • the frequency is 14 kHz
  • the effective voltage is 300 V
  • the effective current is 11 A.
  • the voltage of the alternating current supplied from the generator 21 is increased from 300 V to 20 kV by the transformer 22. Thereby, a high voltage of 20 kV is applied between the internal electrode 11a and the external electrode 11b in the plasma generation unit 11.
  • the gas supply machine 30 sends oxygen (O 2 ) to the nozzle 10 together with air. Further, the air for supplying the water vapor generated by the evaporator 40 to the relay unit 13 is supplied to the evaporator 40.
  • the gas supply machine 30 has a control panel 31. By operating the control panel 31, the supply amount of various gases to the target can be adjusted. In this embodiment, by operating the control panel 31, for example, air is sent to the nozzle 10 at 6 L / min and oxygen is sent at 3 L / min, and air is sent to the evaporator 40 at 3 L / min. is there.
  • the evaporator 40 heats a built-in heating wire (not shown) to 300 ° C., and heats water supplied from the pump 50 by the heating wire to generate water vapor. And water vapor is mixed with the air supplied from the gas supply machine 30, and water vapor is supplied to the relay part 13 with air.
  • the pump 50 supplies water to the evaporator 40 at 1.2 mL / min.
  • the chiller 60 cools the nozzle 10 that generates heat when high voltage is applied by supplying cooling water to the nozzle 10.
  • oxygen supplied together with air from the gas supply device 30 to the nozzle 10 is turned into plasma by the plasma generation unit 11 of the nozzle 10, and the generated oxygen plasma is generated in the relay unit 13. It reacts with water vapor supplied together with air from the evaporator 40 to continuously generate active oxygen mainly composed of hydroxyl radicals. Then, the active oxygen, water vapor, and unreacted plasma continuously generated in the relay unit 13 are continuously discharged from the discharge port 12 as the sterilizing agent 70, thereby enabling continuous processing of the cap 80. .
  • the bactericide 70 containing plasma and active oxygen is discharged from the discharge port at a temperature of 50 to 80 ° C. and a flow rate of 50000 mm / sec.
  • the following advantages are obtained by sterilization using active oxygen.
  • a sterilizing agent containing hydrogen peroxide When a sterilizing agent containing hydrogen peroxide is used, it is necessary to wash the sterilizing agent afterwards so that the sterilizing agent does not remain on the object to be sterilized. However, it is difficult to remove all the sterilizing agent by washing, and there is a risk that the sterilizing agent remains on the article to be sterilized.
  • the sterilizing agent spray and the subsequent cleaning are mainly performed at a high temperature, when the material to be sterilized is a material that causes heat shrinkage such as a resin material, various sterilization processes are performed in order to prevent excessive heat shrinkage and deformation. There will be constraints.
  • the configuration of the sterilization system 100A according to this embodiment will be described.
  • the sterilization system 100A according to the present embodiment in addition to the plasma sterilization means 120, another sterilization means 130 that sterilizes the cap 80 by a method different from the plasma sterilization means 120 conveys the cap 80.
  • the transfer line 110 On the transfer line 110.
  • the plasma sterilization unit 110 and the other sterilization unit 130 are provided in parallel on the transport line 110.
  • the conveyance line 110 is constituted by, for example, a conveyor. Then, the first branch line 112 and the second branch line 113 are branched at the first switching point 111. Plasma sterilizing means 120 is provided on the first branch line 112, and other sterilizing means 130 is provided on the second branch line 113.
  • the cap 80 conveyed from the upstream side can be switched between the first branch line 112 and the second branch line 113. Further, the first branch line 112 and the second branch line 113 merge at the second switching point 114, and the second switching point 114 is connected to either the first branch line 112 or the second branch line 113 downstream thereof. The connection to the line 115 on the side can be switched.
  • the sterilization system 100A it is possible to switch between the plasma sterilization means 120 and the other sterilization means 130 to sterilize the cap 80.
  • the downstream 112a of the plasma sterilization means 120 of the first branch line 112, the downstream 112a of the plasma sterilization means 120 of the first branch line 112, the second switching point 114, and the downstream of the second switching point 114 Since the sterilized cap 80 is conveyed with the line 115, it is aseptic environment.
  • the line switching between the first switching point 111 and the second switching point 114 may be a manual or automatic remote operation such as one performed by a switch operation at a control center or one automatically performed by a computer. It is also conceivable that a person switches directly on site. However, since the second switching point 114 needs to be an aseptic environment, switching by remote operation such as switch operation by a remote controller is preferable.
  • the plasma sterilization means 120 a plurality of plasma sterilization apparatuses 1 are arranged along the first switching line 112 (in FIG. 3, only the nozzle 10 is shown by omission).
  • the plasma sterilization means 120 includes the aseptic chamber 121, and the cap 80 is sterilized in the aseptic chamber 121.
  • the cap 80 is sterilized by a method different from that of the plasma sterilization means 120.
  • a method that has been conventionally used and that has already been generally used and has proven its sterilization efficiency and operation reliability (whether it operates without defects) is preferable. Examples include sterilization with hydrogen peroxide, sterilization with electron beam irradiation, and sterilization with a peracetic acid-based sterilizer.
  • the other sterilizing means 130 also has a sterile chamber 131, and the cap 80 is sterilized in the sterile chamber 131.
  • the plasma sterilization means 120 includes a hot air nozzle (heating means) as a contraction means for contracting the sterilized cap 80 on the first switching line 112 on the downstream side of the plasma sterilization apparatus 1. 122) is provided. That is, the sterilization using active oxygen by the plasma sterilization unit 120 does not need to apply heat to the cap 80 so as to cause thermal shrinkage. Therefore, the sterilization by the plasma sterilization unit 120 is unlikely to cause thermal contraction in the cap 80.
  • conventionally used sterilization means for example, sterilization using a hydrogen peroxide-containing sterilizing agent
  • the other sterilization means 130 is one in which the cap 80 contracts.
  • the size of the cap 80 may vary between the plasma sterilization means 120 and the other sterilization means 130. Therefore, by blowing the hot air 123 from the hot air nozzle 122 into the cap 80, the sterilized cap 80 can be heated, and the (heat) shrinkage of the cap 80 can be caused. Thereby, the variation in the size of the cap 80 after sterilization between the plasma sterilization means 120 and the other sterilization means 130 is effectively suppressed. Further, when dust or dust adheres to the cap 80, it can be removed.
  • the sterilization system 100A is effective in the following cases.
  • a new sterilization method using active oxygen which is a new sterilization method
  • operation is actually stopped due to an unexpected error. Or the risk that the equipment will malfunction. Therefore, in the sterilization system 100A, it is possible to switch between the plasma sterilization unit 120 that performs sterilization using active oxygen and the other sterilization unit 130 to perform the sterilization of the cap 80. Even if any trouble occurs in the plasma sterilization means 120 having the above risk during the sterilization by the above, if the sterilization of the cap 80 is switched from the plasma sterilization means 120 to another sterilization means 130, it will continue.
  • the cap 80 can be sterilized.
  • the first and second switching points 111 and 114 are set on the first branch line 112 side in order to perform sterilization using active oxygen. Then, the operation of the other sterilization means 130 is stopped, only the plasma sterilization means 120 is operated, and the plasma sterilization means 120 sterilizes the cap 80 using active oxygen. Thereafter, if no problem occurs, the operation is continued while maintaining this state. However, if any trouble occurs in the plasma sterilization means 120, the first and second switching points 111 and 114 are connected to the second branch line.
  • the operation is switched to the 113 side to stop the operation of the plasma sterilization means 120 and the operation of the other sterilization means 130 is started, and the cap 80 is sterilized by the other sterilization means 130.
  • the first and second switching points 111 and 114 are switched to the second branch line 113 side again, and the operation of the other sterilization means 130 is stopped,
  • the operation of the plasma sterilization means 120 is started, and the plasma sterilization means 120 again sterilizes the cap 80 using active oxygen.
  • the plasma sterilization means 110 that performs sterilization using active oxygen and the other sterilization means 130 that performs sterilization by other sterilization methods are arranged on separate lines 112 and 113. Therefore, when the other sterilizing means 130 is sterilizing, the sterilizing agent in the other sterilizing means 130 reaches the plasma sterilizing means 120 and flows back into the plasma sterilizing means 120. Is suppressed.
  • FIG. 1 A second embodiment of the sterilization system according to the present invention will be described with reference to FIG.
  • the arrangement of the plasma sterilizing means 120 and the other sterilizing means 130 on the transfer line 110 is different from that of the first embodiment.
  • differences between the sterilization system 100B according to the present embodiment and the first embodiment will be mainly described. Note that the points not particularly specified are the same as those in the first embodiment, and the same reference numerals are given and detailed description thereof is omitted.
  • the plasma sterilization means 120 and the other sterilization means 130 are provided in series on the transport line 110.
  • the plasma sterilization means 120 and the other sterilization means 130 have separate sterilization chambers 121 and 131, respectively, and perform sterilization in the chambers 121 and 131.
  • the plasma sterilization means 120 and the other sterilization means 130 are operated without switching the line as in the sterilization system 100A of the first embodiment, so that the plasma The cap 80 can be sterilized only by the sterilizing means 120, or the cap 80 can be sterilized only by the other sterilizing means 130.
  • the operation of the other sterilization means 130 is stopped, only the plasma sterilization means 120 is operated, and the cap only by the plasma sterilization means 120 is used. If any trouble occurs in the plasma sterilization means 120 while performing the sterilization of 80, the operation of the plasma sterilization means 120 is stopped and the operation of the other sterilization means 130 is started instead. An operation of sterilizing the cap 80 can be performed.
  • the cap 80 It is also possible to sterilize the cap 80 with the plasma sterilization means 120 and the other sterilization means 130 by operating both the plasma sterilization means 120 and the other sterilization means 130. Thereby, the bactericidal effect with respect to the cap 80 can also be improved. At this time, if any trouble occurs in the plasma sterilization means 120, the operation of the plasma sterilization means 120 may be stopped and only the other sterilization means 130 may be operated for sterilization.
  • the plasma sterilization means 120 is disposed upstream of the other sterilization means 130, and the other sterilization means 130 is also used as a preliminary and supplemental sterilization means for sterilization by the plasma sterilization means 120. it can.
  • a third embodiment of the sterilization system according to the present invention will be described with reference to FIG.
  • the sterilization system 100C of this embodiment is different from the second embodiment in that the plasma sterilization means 120 and other sterilization means 130 perform sterilization in the same aseptic chamber 140.
  • differences between the sterilization system according to the present embodiment and the second embodiment will be mainly described. Note that points not particularly specified are the same as those in the second embodiment, and the same reference numerals are given and detailed description thereof is omitted.
  • the sterilization system 100C of this embodiment performs sterilization in a sterilization chamber 140 in which a sterilization chamber 140a on the plasma sterilization means 120 side and a sterilization chamber 140b on the other sterilization means 130 side are integrated. It is configured. Thereby, space saving can be achieved compared with providing both sterilization means in a separate aseptic chamber.
  • the sterilization system 100B of the second embodiment by operating only one of the plasma sterilization means 120 and the other sterilization means 130, the cap 80 is sterilized only by the plasma sterilization means 120, or The cap 80 can be sterilized only by the other sterilization means 130. It is also possible to operate both the plasma sterilization means 120 and the other sterilization means 130 and sterilize the cap 80 with the plasma sterilization means 120 and the other sterilization means 130.
  • both sterilization means 120 and 130 are in the same sterilization chamber 140, when only the other sterilization means 130 is operating, the sterilizing agent used in the other sterilization means 130 is up to the plasma sterilization means 120. There is a possibility that the plasma sterilization means 120 may flow back into each plasma sterilization apparatus 1. Therefore, when only the other sterilization means 130 is sterilizing, the sterilization system 100C of this embodiment is used for preventing backflow from the discharge port 12 of the sterilizing agent 70 to each plasma sterilization apparatus 1 in the first plasma sterilization means 120. A control unit (not shown) for ejecting the air is provided. When only the other sterilizing means 130 is sterilizing, the plasma sterilizing means 120 is jetted with air for preventing backflow, and the sterilizing agent of the other sterilizing means 130 flows back into the plasma sterilizing apparatus 1. It is deterring.
  • FIG. 1 As a fourth embodiment of the sterilization system according to the present invention, a modified example of the plasma sterilization means will be described with reference to FIG.
  • the configuration in which the plasma sterilization means 120 is provided in the sterilization chambers 121 and 140a is shown.
  • the cap 80 may be sterilized indirectly by 70.
  • the configuration in which the plasma air sterilizing unit 120 is provided with the hot air nozzle 122 as a contracting unit that contracts the cap 80 after sterilization has been described as an example.
  • the embodiment of the present invention is not limited to this.
  • it is not limited to the hot air nozzle 122 but may be other heating means such as steam, and is not limited to sterilizing the cap 80 by heating, and other contraction means such as electron beam irradiation may be used.
  • the position where the contracting means is provided is not limited to the downstream side of the plasma sterilization apparatus 1 but may be disposed upstream of the plasma sterilization apparatus 1 so that the cap 80 before sterilization is contracted.
  • the contraction means is described as an example of the configuration provided in the plasma sterilization means 120 separately from the other sterilization means 130, but the present invention is not limited to this.
  • the plasma sterilization means 120 and the other sterilization means 130 are provided in series, and the other sterilization means 130 may be sterilized by heating or electron beam irradiation.
  • the sterilization system may be provided with a contraction means in addition to the plasma sterilization means 120. That is, the sterilization system includes plasma sterilization means for generating plasma and irradiating the obtained plasma to sterilize an object to be sterilized.
  • the plasma sterilization means is supplied with water vapor, and the plasma sterilization means Is for discharging a sterilizing agent containing the generated plasma and active oxygen generated by a reaction between the supplied water vapor and the plasma to the object to be sterilized.
  • a sterilization system provided with contraction means for contracting the article to be sterilized is also conceivable.
  • the contraction means may be provided at an arbitrary location on the transport line, for example, adjacent to the sterilization means or provided downstream or upstream thereof. Further, the contraction means may be intended only for contraction of the article to be sterilized.
  • the configuration in which the plasma sterilizing unit 120 is arranged on the upstream side of the other sterilizing unit 130 is shown.
  • the embodiment of the present invention is not limited to this, and the plasma sterilization means 120 may be arranged downstream of the other sterilization means 130.
  • the present invention can be used in a sterilization apparatus for sterilizing an object to be sterilized such as a cap.

Abstract

A sterilization system (100A) that comprises a plasma sterilization means (120) that generates plasma and uses the obtained plasma to sterilize an object to be sterilized (80). Water vapor is supplied to the plasma sterilization means (120), and the plasma sterilization means (120) discharges a sterilizer that includes the generated plasma and active oxygen that is generated as a result of the plasma reacting with the supplied water vapor. In addition to the plasma sterilization means (120), another sterilization means (130), which sterilizes the object to be sterilized (80) by means of a different method than the plasma sterilization means (120), is also provided on a transport line (110) that transports the object to be sterilized (80).

Description

殺菌システムSterilization system
 本発明は、容器のキャップ等の被殺菌物を殺菌するための殺菌システムに関する。 The present invention relates to a sterilization system for sterilizing an object to be sterilized such as a cap of a container.
 被殺菌物の一例としてのPETボトルなどの容器のキャップを殺菌する方法として、特開2013-28398号公報(特許文献1)に記載された殺菌方法が知られている。特許文献1では、過酸化水素の含む殺菌剤を容器やそのキャップ内に吹き込むことにより、容器内の殺菌を行う方法が記載されている。 As a method for sterilizing a cap of a container such as a PET bottle as an example of an object to be sterilized, a sterilization method described in JP2013-28398A (Patent Document 1) is known. Patent Document 1 describes a method of sterilizing a container by blowing a sterilizing agent containing hydrogen peroxide into the container or its cap.
 特許文献1の殺菌方法のように過酸化水素を含む殺菌剤を用いた場合、殺菌剤がキャップに残留しないようにその後洗浄する必要がある。しかし、洗浄によって全ての殺菌剤を除去することは困難であり、殺菌剤がキャップに残留するリスクがある。また、特許文献1の殺菌方法では、殺菌剤噴霧やその後の洗浄は主として高温下で行われるため、熱収縮が生じる樹脂素材で形成されているPETボトルのキャップにおいては、過剰な熱収縮や変形を防ぐためにその殺菌工程に種々の制約を抱えることになる。 When a sterilizing agent containing hydrogen peroxide is used as in the sterilizing method of Patent Document 1, it is necessary to subsequently clean the sterilizing agent so that it does not remain on the cap. However, it is difficult to remove all the disinfectant by washing, and there is a risk that the disinfectant remains in the cap. Further, in the sterilization method of Patent Document 1, since the sterilizing agent spray and the subsequent cleaning are mainly performed at a high temperature, excessive heat shrinkage or deformation is caused in a PET bottle cap formed of a resin material that causes heat shrinkage. In order to prevent this, the sterilization process has various restrictions.
特開2013-28398号公報JP 2013-28398 A
 ボトルに取付けるキャップ等の被殺菌物への殺菌剤の残留及び被殺菌物の過剰な熱収縮や変形のおそれのない、被殺菌物を殺菌するための殺菌システムの実現が望まれる。 It is desired to realize a sterilization system for sterilizing an object to be sterilized without causing a residue of the sterilizing agent on the object to be sterilized such as a cap attached to a bottle and excessive heat shrinkage or deformation of the object to be sterilized.
 本発明に係る殺菌システムは、
 プラズマを発生させて、得られた前記プラズマにより被殺菌物を殺菌するプラズマ殺菌手段を備え、
 前記プラズマ殺菌手段には、水蒸気が供給され、
 前記プラズマ殺菌手段は、発生させた前記プラズマと、供給される前記水蒸気と前記プラズマとが反応して生成される活性酸素と、を含む殺菌剤を吐出するものであり、
 前記プラズマ殺菌手段に加え、前記プラズマ殺菌手段とは異なる方法で前記被殺菌物の殺菌を行う他の殺菌手段が、前記被殺菌物を搬送する搬送ライン上に併設されている。
The sterilization system according to the present invention is
Plasma sterilization means for generating plasma and sterilizing the object to be sterilized with the obtained plasma,
The plasma sterilizing means is supplied with water vapor,
The plasma sterilizing means discharges a sterilizing agent containing the generated plasma, and active oxygen generated by the reaction between the supplied water vapor and the plasma,
In addition to the plasma sterilization means, another sterilization means for sterilizing the article to be sterilized by a method different from the plasma sterilization means is provided on a conveyance line for conveying the article to be sterilized.
 活性酸素は時間経過に伴い消滅するため残留することがなく、かつ、活性酸素を用いた殺菌は被殺菌物に対して熱収縮を生じさせるほどの熱を与える必要はない。したがって、このプラズマと活性酸素とを含む殺菌剤を吐出するプラズマ殺菌手段を用いることにより、上記した殺菌剤残留や被殺菌物の熱収縮・変形の問題を回避できる。 Since active oxygen disappears with time, it does not remain, and sterilization using active oxygen does not need to give heat to the object to be sterilized so as to cause heat shrinkage. Therefore, by using the plasma sterilizing means for discharging the sterilizing agent containing plasma and active oxygen, it is possible to avoid the above-described problems of the sterilizing agent residue and the thermal contraction / deformation of the sterilized object.
 ただし、プラズマと活性酸素とを含む殺菌剤を用いた殺菌方法は、新規な殺菌方法であるため、新たに設備に導入する際に、実際に所望の殺菌効果が得られるかなどの問題がある。そこで、上記構成では、プラズマ殺菌手段に加え、例えば、既に設備に導入済みでその殺菌効率や運転の確実性(不良なく運転するか)が実証されている、プラズマ発生手段とは異なる方法で被殺菌物の殺菌を行う他の殺菌手段を、被殺菌物を搬送する搬送ライン上に併設することにより、たとえ、プラズマ殺菌手段によって所望の殺菌効果を得られなかったとしても、他の殺菌手段により、被殺菌物を確実に殺菌することができる。 However, since the sterilization method using a sterilizing agent containing plasma and active oxygen is a novel sterilization method, there is a problem that a desired sterilization effect can be actually obtained when newly introduced into equipment. . Therefore, in the above configuration, in addition to the plasma sterilization means, for example, the sterilization efficiency and operation reliability (whether to operate without defects) that have already been introduced into the facility have been demonstrated by a method different from the plasma generation means. Even if the desired sterilization effect cannot be obtained by the plasma sterilization means, other sterilization means for sterilizing the sterilized material can be provided on the transport line for transporting the sterilized material. The object to be sterilized can be sterilized reliably.
 以下、本発明に係る殺菌システムの好適な態様について説明する。但し、以下に記載する好適な態様例によって、本発明の範囲が限定される訳ではない。 Hereinafter, preferred embodiments of the sterilization system according to the present invention will be described. However, the scope of the present invention is not limited by the preferred embodiments described below.
 1つの態様として、前記プラズマ殺菌手段と前記他の殺菌手段とのいずれにより前記被殺菌物の殺菌を行うかを切り替え可能にしてあると好適である。 As one aspect, it is preferable that the plasma sterilization means and the other sterilization means can be switched to sterilize the article to be sterilized.
 つまり、プラズマ殺菌手段により所望の殺菌効果が得られたとしても、新規な殺菌方法であるプラズマ殺菌手段を設備に導入する場合、導入実績が欠けているために、実際にその設備で運転を行うことについて、予期せぬエラーにより運転が停止したり、機器に不具合が生じるなどのリスクを包含したものとなる。そこで、この構成によれば、上記したリスクを抱えたプラズマ殺菌手段に何らかの不具合が生じたとしても、被殺菌物の殺菌をプラズマ殺菌手段から他の殺菌手段に切り替えれば、継続して被殺菌物の殺菌を行うことができる。 That is, even if a desired sterilization effect is obtained by the plasma sterilization means, when the plasma sterilization means, which is a new sterilization method, is introduced into the equipment, since the introduction record is lacking, the operation is actually performed with the equipment. This includes risks such as an operation that stops due to an unexpected error or a malfunction of the equipment. Therefore, according to this configuration, even if some trouble occurs in the plasma sterilization means having the above risk, if the sterilization of the sterilized object is switched from the plasma sterilization means to another sterilization means, the object to be sterilized continuously. Can be sterilized.
 一つの態様として、前記プラズマ殺菌手段と前記他の殺菌手段とは、前記搬送ライン上に並列に設けられていると好適である。 As one aspect, it is preferable that the plasma sterilization means and the other sterilization means are provided in parallel on the transport line.
 この構成によれば、前記プラズマ殺菌手段と前記他の殺菌手段とは別ライン上に配置されることになるから、他の殺菌手段が殺菌を行っている場合のその殺菌剤が、プラズマ殺菌手段まで及んでプラズマ殺菌手段中に逆流してしまうといった事態を効果的に抑制できる。 According to this configuration, since the plasma sterilization means and the other sterilization means are arranged on separate lines, the sterilizing agent when the other sterilization means is sterilizing is the plasma sterilization means. It is possible to effectively suppress the situation that the gas flows back into the plasma sterilization means.
 一つの態様として、前記プラズマ殺菌手段と前記他の殺菌手段とは、前記搬送ライン上に直列に設けられていると好適である。 As one aspect, it is preferable that the plasma sterilization means and the other sterilization means are provided in series on the transfer line.
 前記プラズマ殺菌手段と前記他の殺菌手段とを並列に設けた場合、被殺菌物はいずれか一方の殺菌手段でしか殺菌できないが、この構成によれば、一方の運転を停止させることにより前記プラズマ殺菌手段と前記他の殺菌手段とのいずれか一方のみで殺菌を行うことに加え、両方を運転させることにより両者で殺菌を行うことも可能であるなど、柔軟な形態で殺菌を行うことが可能となる。 When the plasma sterilization means and the other sterilization means are provided in parallel, the object to be sterilized can only be sterilized by any one of the sterilization means, but according to this configuration, the plasma can be obtained by stopping one of the operations. In addition to sterilizing only one of the sterilizing means and the other sterilizing means, it is also possible to perform sterilization in a flexible form, such as being able to sterilize both by operating both It becomes.
 一つの態様として、前記プラズマ殺菌手段と前記他の殺菌手段とは、同じ無菌チャンバー内に設けられていると好適である。 As one aspect, it is preferable that the plasma sterilization means and the other sterilization means are provided in the same aseptic chamber.
 この構成によれば、両方の殺菌手段を同じ無菌チャンバー内に設けるから、両方の殺菌手段を別々の無菌チャンバー内に設けるのに比べ、省スペース化を図ることができる。 According to this configuration, since both sterilization means are provided in the same aseptic chamber, it is possible to save space compared to providing both sterilization means in separate aseptic chambers.
 一つの態様として、前記他の殺菌手段のみが殺菌を行っているときは、前記プラズマ殺菌手段に前記殺菌剤の吐出口から逆流防止用のエアーを噴出させる制御部を設けてあると好適である。 As one aspect, when only the other sterilizing means is sterilizing, it is preferable that the plasma sterilizing means is provided with a control unit that ejects air for preventing backflow from the discharge port of the sterilizing agent. .
 両方の殺菌手段を同じ無菌チャンバー内に設けた場合、他の殺菌手段が殺菌を行っている場合の他の殺菌剤が、プラズマ殺菌手段まで及んでプラズマ殺菌手段中に逆流してしまう虞がある。これに対し、この構成によれば、逆流防止用のエアーにより、他の殺菌剤がプラズマ殺菌手段中に逆流してしまうことを効果的に抑制できる。 When both sterilization means are provided in the same aseptic chamber, other sterilization agents when other sterilization means are sterilizing may reach the plasma sterilization means and flow back into the plasma sterilization means. . On the other hand, according to this structure, it can suppress effectively that other sterilizing agents flow backward in a plasma sterilization means with the air for backflow prevention.
 一つの態様として、前記プラズマ殺菌手段には、前記被殺菌物を収縮させる収縮手段が設けてられていると好適である。 As one aspect, it is preferable that the plasma sterilizing means is provided with a contracting means for contracting the article to be sterilized.
 上記したように、活性酸素を用いた殺菌は被殺菌物に対して熱収縮を生じさせるほどの熱を与える必要はなく、そのためプラズマ殺菌手段による殺菌では被殺菌物に熱収縮は起こりにくい。一方、従来から用いられている殺菌手段(例えば上記した過酸化水素の含む殺菌剤による殺菌)は、被殺菌物に収縮が生じるものが主流である。そうすると、プラズマ殺菌手段による殺菌のみを行った被殺菌物と、他の殺菌手段による殺菌のみを行った被殺菌物とでは、収縮の差によりその大きさにばらつきが生じる。これに対し、この構成によれば、収縮手段により被殺菌物を収縮させるから、被殺菌物の大きさのばらつきを効果的に抑制できる。 As described above, sterilization using active oxygen does not need to give heat to the object to be sterilized so as to cause heat shrinkage. Therefore, sterilization by plasma sterilization means hardly causes heat shrinkage to the object to be sterilized. On the other hand, conventionally used sterilization means (for example, sterilization using the above-described sterilizing agent containing hydrogen peroxide) is one in which shrinkage occurs in an object to be sterilized. Then, the size of the object to be sterilized that has been sterilized only by the plasma sterilizing means and the object to be sterilized only by the other sterilizing means vary depending on the difference in shrinkage. On the other hand, according to this configuration, the object to be sterilized is contracted by the contraction means, so that variation in the size of the object to be sterilized can be effectively suppressed.
 一つの態様として、前記収縮手段は、前記被殺菌物を加熱する加熱手段であると好適である。 As one aspect, it is preferable that the contraction means is a heating means for heating the article to be sterilized.
 被殺菌物を収縮させる手段としては、被殺菌物を加熱すること、被殺菌物に電子線を照射することなどが考えられるが、被殺菌物に電子線を照射するのに比べ、被殺菌物を加熱する方が容易にそのための装置を準備でき、また装置コストも低減できる。 As means for shrinking the article to be sterilized, it is conceivable to heat the article to be sterilized and to irradiate the article to be sterilized with an electron beam. It is easier to prepare a device for heating the device, and the device cost can be reduced.
活性酸素を用いた殺菌を行うプラズマ殺菌装置の概略構成図Schematic configuration diagram of a plasma sterilizer that performs sterilization using active oxygen 活性酸素を用いた殺菌を行うプラズマ殺菌装置の装置構成ブロック図Device configuration block diagram of a plasma sterilizer that performs sterilization using active oxygen 第1実施形態における殺菌システムの概略図Schematic of the sterilization system in the first embodiment 第1実施形態におけるプラズマ殺菌手段の部分拡大図The elements on larger scale of the plasma sterilization means in 1st Embodiment 第2実施形態における殺菌システムの概略図Schematic of the sterilization system in the second embodiment 第3実施形態における殺菌システムの概略図Schematic of the sterilization system in the third embodiment 第4実施形態におけるプラズマ殺菌手段の部分拡大図Partial enlarged view of plasma sterilization means in the fourth embodiment
〔第1の実施形態〕
 本発明に係る殺菌システムの第1の実施形態について、図面を参照して説明する。本実施形態の殺菌システム100Aは、被殺菌物の一例としてのPETボトルなどの容器のキャップ80を殺菌するものである。そして、殺菌システム100Aは、プラズマを発生させて、得られたプラズマによりキャップ80を殺菌する複数のプラズマ殺菌装置を有するプラズマ殺菌手段120を備える。このプラズマ殺菌装置1には、水蒸気が供給され、供給される水蒸気とプラズマとが反応して活性酸素(Reactive Oxidizing Species(ROS)、例えばOH radicalやsingulet oxygenなど)が生成される。そして、プラズマ殺菌装置1は、発生させたプラズマと、生成された活性酸素と、を含む殺菌剤を吐出し、キャップ80の殺菌を行う。そこで、まず、活性酸素を用いた殺菌を行うためのプラズマ殺菌装置1(以下では、単に殺菌装置1と称することがある)の装置構成について説明する。
[First Embodiment]
A sterilization system according to a first embodiment of the present invention will be described with reference to the drawings. The sterilization system 100A of this embodiment sterilizes a cap 80 of a container such as a PET bottle as an example of an object to be sterilized. And sterilization system 100A is provided with plasma sterilization means 120 which has a plurality of plasma sterilization devices which generate plasma and sterilize cap 80 with the obtained plasma. The plasma sterilizer 1 is supplied with water vapor, and the supplied water vapor and the plasma react to generate active oxygen (Reactive Oxidizing Species (ROS), for example, OH radical or single oxygen). The plasma sterilization apparatus 1 then sterilizes the cap 80 by discharging a sterilizing agent containing the generated plasma and the generated active oxygen. Therefore, first, the apparatus configuration of the plasma sterilization apparatus 1 (hereinafter simply referred to as the sterilization apparatus 1) for performing sterilization using active oxygen will be described.
 図1は、殺菌装置1による活性酸素の生成機構を示す。殺菌装置1は、活性酸素を生成して、活性酸素を含む殺菌剤70をキャップ80に対して吐出(照射)するノズル10を有している。このノズル10は、プラズマを生成するプラズマ生成部11と、プラズマと活性酸素を含む殺菌剤70を吐出する吐出口12と、プラズマ生成部11と吐出口12との間の中継部13と、を備える。なお、図1では殺菌装置1が活性酸素を含む殺菌剤70をキャップ80に対して直接的に吐出する構成を示してあるが、これに限られず、キャップ80に殺菌剤を直接吐出させるのではなくキャップ80を通過させるチャンバー内に殺菌剤70を吐出して、チャンバー内に充満させた殺菌剤70によりキャップ80を殺菌する等、間接的にキャップ80を殺菌するようにしてもよい。 FIG. 1 shows a mechanism for generating active oxygen by the sterilizer 1. The sterilizer 1 has a nozzle 10 that generates active oxygen and discharges (irradiates) a sterilizing agent 70 containing active oxygen to the cap 80. The nozzle 10 includes a plasma generation unit 11 that generates plasma, a discharge port 12 that discharges a bactericide 70 containing plasma and active oxygen, and a relay unit 13 between the plasma generation unit 11 and the discharge port 12. Prepare. FIG. 1 shows a configuration in which the sterilizer 1 directly discharges the sterilizing agent 70 containing active oxygen to the cap 80. However, the present invention is not limited to this. Alternatively, the cap 80 may be sterilized indirectly, such as by discharging the sterilizing agent 70 into the chamber through which the cap 80 passes and sterilizing the cap 80 with the sterilizing agent 70 filled in the chamber.
 このノズル10は装置内でプラズマとしていわゆる大気圧プラズマを生成するものである。大気圧プラズマを用いることにより、低圧プラズマを生成する際に必要な真空容器などを要せず装置コストを低減でき、また連続処理が可能であるため作業効率が高い。また、低温下でも生成できるため、被処理物を高温にさらさずに済むという利点もある。以下に、ノズル10による大気圧プラズマ(以下、単にプラズマと称する)の生成と、プラズマを利用した活性酸素の生成について説明する。 This nozzle 10 generates so-called atmospheric pressure plasma as plasma in the apparatus. By using atmospheric pressure plasma, it is possible to reduce the cost of the apparatus without requiring a vacuum vessel or the like necessary for generating low-pressure plasma, and the work efficiency is high because continuous processing is possible. Moreover, since it can produce | generate also under low temperature, there also exists an advantage that it does not need to expose a to-be-processed object to high temperature. Hereinafter, generation of atmospheric pressure plasma (hereinafter simply referred to as plasma) by the nozzle 10 and generation of active oxygen using the plasma will be described.
 プラズマ生成部11は、周知の構造を有しており、内部電極11aと外部電極11bとを備える。プラズマ生成部11では、交流電源20により、内部電極11aと外部電極11bとの間に高電圧(例えば、周波数14kHzで実効電圧20kV)を印加することで、プラズマ生成部11内に電界を発生させる。そして、プラズマ生成部11内にエアー(air)とともにガスを供給し、発生電界にガスを通気させることにより、プラズマを生成する。生成されたプラズマは、中継部13へと送られる。本実施形態では、プラズマ生成部11内にガスの一例として酸素(O、ozygen)が供給され、プラズマ生成部11では、プラズマとして、オゾンを含む酸素プラズマが生成される。具体的にはプラズマ化により酸素ラジカルとオゾン(O)が発生し、これらが中継部13へと送られる。 The plasma generator 11 has a known structure and includes an internal electrode 11a and an external electrode 11b. In the plasma generation unit 11, an electric field is generated in the plasma generation unit 11 by applying a high voltage (for example, an effective voltage of 20 kV at a frequency of 14 kHz) between the internal electrode 11 a and the external electrode 11 b by the AC power supply 20. . And plasma is produced | generated by supplying gas with the air (air) in the plasma production | generation part 11, and making gas generate | occur | produce in the generated electric field. The generated plasma is sent to the relay unit 13. In the present embodiment, oxygen (O 2 , oxygen) is supplied as an example of gas into the plasma generation unit 11, and the plasma generation unit 11 generates oxygen plasma containing ozone as plasma. Specifically, oxygen radicals and ozone (O 3 ) are generated by the plasma, and these are sent to the relay unit 13.
 中継部13は、エバポレータ(水蒸気供給部の一例。詳しくは後述する)40と接続してあり、中継部13にはさらに水蒸気が送られる。これにより、中継部13において、プラズマ生成部11から送られるプラズマ(酸素ラジカルとオゾン)とエバポレータ40から送られる水蒸気(vapor)とが反応して、活性酸素が生成される。本実施形態では、酸素プラズマ(酸素ラジカルとオゾン)と水蒸気を反応させることにより、活性酸素の中でも特に反応性の高いヒドロキシラジカル(・OH)が主に生成されるようにしている。 The relay unit 13 is connected to an evaporator 40 (an example of a water vapor supply unit, which will be described in detail later), and further water vapor is sent to the relay unit 13. Thereby, in the relay part 13, the plasma (oxygen radical and ozone) sent from the plasma production | generation part 11 and the water vapor | steam (vapor) sent from the evaporator 40 react, and active oxygen is produced | generated. In this embodiment, by reacting oxygen plasma (oxygen radicals and ozone) with water vapor, hydroxy radicals (.OH) that are particularly reactive among active oxygens are mainly generated.
 具体的に説明すると、水蒸気とプラズマが反応することにより、以下の(1)式のようにHOから水素ラジカル(・H)とヒドロキシラジカルが生成される。 More specifically, when water vapor and plasma react, hydrogen radicals (.H) and hydroxy radicals are generated from H 2 O as shown in the following formula (1).
 HO → ・H+・OH・・・・・(1) H 2 O → H + OH (1)
 また、水素ラジカルはオゾンと反応して、以下の(2)式のようにヒドロキシラジカルと酸素(O)が生成される。 Further, the hydrogen radical reacts with ozone to generate a hydroxy radical and oxygen (O 2 ) as shown in the following formula (2).
 ・H+O → ・OH+O・・・・・(2) ・ H + O 3 → OH + O 2 (2)
 (1)式と(2)式は、次の(3)式にまとめることができる。 (1) and (2) can be combined into the following (3).
 HO+O → 2・OH+O・・・・・(3) H 2 O + O 3 → 2.OH + O 2 (3)
 つまり、酸素プラズマと水蒸気を反応させることにより、上記(3)式の反応を生じさせて効率的にヒドロキシラジカル(・OH)を生成することができる。その結果、生成される活性酸素は、ヒドロキシラジカルを主として含むこととなる。特に反応性の高いヒドロキシラジカルを主として含むことにより、高い殺菌効果を奏することができる。そして、このように生成された活性酸素と水蒸気と未反応のプラズマとが殺菌剤70として吐出口12から被殺菌物80に吐出されて、被殺菌物80の殺菌が行われる。 That is, by reacting oxygen plasma with water vapor, the reaction of the above formula (3) can be caused to generate hydroxy radicals (.OH) efficiently. As a result, the generated active oxygen mainly contains hydroxy radicals. In particular, a high bactericidal effect can be achieved by mainly including highly reactive hydroxy radicals. Then, the generated active oxygen, water vapor, and unreacted plasma are discharged from the discharge port 12 to the sterilized object 80 as the sterilizing agent 70, and the sterilized object 80 is sterilized.
 次に、図2に示された活性酸素を用いて殺菌を行う殺菌装置1の装置構成を説明する。殺菌装置1は、ノズル10のほか、交流電源20を構成するジェネレーター21とトランスフォーマー22、ノズル10やエバポレータ40に各種ガスを供給するガス供給機30、中継部13に水蒸気を送るエバポレータ40、エバポレータ40に水を供給するポンプ50、ノズル10に冷却水を供給するチラー60と、を備える。 Next, the device configuration of the sterilizer 1 that performs sterilization using the active oxygen shown in FIG. 2 will be described. The sterilizer 1 includes a generator 21 and a transformer 22 that constitute an AC power source 20 in addition to the nozzle 10, a gas supply device 30 that supplies various gases to the nozzle 10 and the evaporator 40, an evaporator 40 that sends water vapor to the relay unit 13, and an evaporator 40. And a chiller 60 for supplying cooling water to the nozzle 10.
 ジェネレーター21は交流電流を発生する。例えば、本実施形態では、周波数が14kHzで、実効電圧300V、実効電流11Aの条件のものを用いている。そして、ジェネレーター21から供給された交流電流の電圧をトランスフォーマー22にて300Vから20kVまで昇圧する。これにより、プラズマ生成部11における内部電極11aと外部電極11bとの間に20kVの高電圧を印加する。 Generator 21 generates an alternating current. For example, in this embodiment, the frequency is 14 kHz, the effective voltage is 300 V, and the effective current is 11 A. The voltage of the alternating current supplied from the generator 21 is increased from 300 V to 20 kV by the transformer 22. Thereby, a high voltage of 20 kV is applied between the internal electrode 11a and the external electrode 11b in the plasma generation unit 11.
 ガス供給機30は、ノズル10に対し、エアーとともに酸素(O)を送る。また、エバポレータ40に対し、エバポレータ40で生成された水蒸気を中継部13に送るためのエアーを供給する。ガス供給機30は、コントロールパネル31を有する。このコントロールパネル31を操作することで、各種ガスの対象への供給量を調整することができる。本実施形態では、コントロールパネル31を操作することにより、例えば、ノズル10に対してはエアーを6L/minで酸素を3L/minで送り、エバポレータ40にはエアーを3L/minで送るようにしてある。 The gas supply machine 30 sends oxygen (O 2 ) to the nozzle 10 together with air. Further, the air for supplying the water vapor generated by the evaporator 40 to the relay unit 13 is supplied to the evaporator 40. The gas supply machine 30 has a control panel 31. By operating the control panel 31, the supply amount of various gases to the target can be adjusted. In this embodiment, by operating the control panel 31, for example, air is sent to the nozzle 10 at 6 L / min and oxygen is sent at 3 L / min, and air is sent to the evaporator 40 at 3 L / min. is there.
 エバポレータ40は、内蔵された電熱線(図示しない)を300℃に加熱し、ポンプ50から供給される水を電熱線により加熱して水蒸気を発生させる。そして、ガス供給機30から供給されるエアーに水蒸気が混合されて、エアーとともに水蒸気が中継部13に供給される。なお、本実施形態では、例えば、ポンプ50はエバポレータ40に水を1.2mL/minで供給する。 The evaporator 40 heats a built-in heating wire (not shown) to 300 ° C., and heats water supplied from the pump 50 by the heating wire to generate water vapor. And water vapor is mixed with the air supplied from the gas supply machine 30, and water vapor is supplied to the relay part 13 with air. In the present embodiment, for example, the pump 50 supplies water to the evaporator 40 at 1.2 mL / min.
 チラー60は、ノズル10に冷却水を供給することにより、高電圧が印加されることにより発熱するノズル10を冷却する。 The chiller 60 cools the nozzle 10 that generates heat when high voltage is applied by supplying cooling water to the nozzle 10.
 上記のように構成された殺菌装置1では、ガス供給機30からノズル10に対してエアーとともに供給される酸素がノズル10のプラズマ生成部11でプラズマ化し、生成された酸素プラズマが中継部13においてエバポレータ40からエアーとともに供給される水蒸気と反応してヒドロキシラジカルを主とする活性酸素が連続的に生成される。そして、中継部13で連続的に生成される活性酸素と水蒸気と未反応のプラズマとが殺菌剤70として吐出口12から連続的に吐出されて、これにより、キャップ80の連続処理が可能となる。本実施形態では、例えば、プラズマと活性酸素を含む殺菌剤70が50~80℃の温度で、50000mm/secの流量で吐出口から吐出される。 In the sterilization apparatus 1 configured as described above, oxygen supplied together with air from the gas supply device 30 to the nozzle 10 is turned into plasma by the plasma generation unit 11 of the nozzle 10, and the generated oxygen plasma is generated in the relay unit 13. It reacts with water vapor supplied together with air from the evaporator 40 to continuously generate active oxygen mainly composed of hydroxyl radicals. Then, the active oxygen, water vapor, and unreacted plasma continuously generated in the relay unit 13 are continuously discharged from the discharge port 12 as the sterilizing agent 70, thereby enabling continuous processing of the cap 80. . In this embodiment, for example, the bactericide 70 containing plasma and active oxygen is discharged from the discharge port at a temperature of 50 to 80 ° C. and a flow rate of 50000 mm / sec.
 活性酸素を用いた殺菌を行うことにより、次のような利点がある。過酸化水素を含む殺菌剤を用いた場合、殺菌剤が被殺菌物に残留しないようにその後洗浄する必要がある。しかし、洗浄によって全ての殺菌剤を除去することは困難であり、殺菌剤が被殺菌物に残留するリスクがある。また、殺菌剤噴霧やその後の洗浄は主として高温下で行われるため、被殺菌物が樹脂素材などの熱収縮が生じる素材である場合、過剰な熱収縮や変形を防ぐためにその殺菌工程に種々の制約を抱えることになる。これに対し、活性酸素は時間経過に伴い消滅するため残留することがなく、かつ、活性酸素を用いた殺菌は被殺菌物に対して熱収縮を生じさせるほどの熱を与える必要はない。したがって、上記した殺菌剤残留や被殺菌物の熱収縮・変形の問題を回避できる。 The following advantages are obtained by sterilization using active oxygen. When a sterilizing agent containing hydrogen peroxide is used, it is necessary to wash the sterilizing agent afterwards so that the sterilizing agent does not remain on the object to be sterilized. However, it is difficult to remove all the sterilizing agent by washing, and there is a risk that the sterilizing agent remains on the article to be sterilized. In addition, since the sterilizing agent spray and the subsequent cleaning are mainly performed at a high temperature, when the material to be sterilized is a material that causes heat shrinkage such as a resin material, various sterilization processes are performed in order to prevent excessive heat shrinkage and deformation. There will be constraints. On the other hand, active oxygen does not remain because it disappears with the passage of time, and sterilization using active oxygen does not need to give heat to the object to be sterilized so as to cause heat shrinkage. Therefore, it is possible to avoid the above-mentioned problem of the sterilizing agent residue and the heat shrinkage / deformation of the sterilized material.
 次に、本実施形態に係る殺菌システム100Aの構成について説明する。本実施形態に係る殺菌システム100Aは、図3に示すように、プラズマ殺菌手段120に加え、プラズマ殺菌手段120とは異なる方法でキャップ80の殺菌を行う他の殺菌手段130が、キャップ80を搬送する搬送ライン110上に併設されている。本実施形態に係る殺菌システム100Aでは、プラズマ殺菌手段110と他の殺菌手段130とは、搬送ライン110上に並列に設けられている。次に、殺菌システム100Aの各部の構成について説明する。 Next, the configuration of the sterilization system 100A according to this embodiment will be described. In the sterilization system 100A according to the present embodiment, as shown in FIG. 3, in addition to the plasma sterilization means 120, another sterilization means 130 that sterilizes the cap 80 by a method different from the plasma sterilization means 120 conveys the cap 80. On the transfer line 110. In the sterilization system 100 </ b> A according to the present embodiment, the plasma sterilization unit 110 and the other sterilization unit 130 are provided in parallel on the transport line 110. Next, the configuration of each part of the sterilization system 100A will be described.
 搬送ライン110は、例えばコンベアなどで構成されている。そして、第1切替点111で、第1分岐ライン112と第2分岐ライン113とに分岐する。第1分岐ライン112にプラズマ殺菌手段120が設けられており、第2分岐ライン113に他の殺菌手段130が設けられている。また、この第1切替点111において、その上流側から搬送されるキャップ80を、第1分岐ライン112と第2分岐ライン113とのいずれで搬送するかを切り替え可能に構成してある。また、第1分岐ライン112と第2分岐ライン113とは、第2切替点114において合流し、第2切替点114は、第1分岐ライン112と第2分岐ライン113とのいずれを、その下流側のライン115と接続するかを切り替え可能にしてある。つまり、殺菌システム100Aでは、プラズマ殺菌手段120と他の殺菌手段130とのいずれによりキャップ80の殺菌を行うかを切り替え可能にしてある。なお、第1分岐ライン112のプラズマ殺菌手段120の下流側112aと、第1分岐ライン112のプラズマ殺菌手段120の下流側112aと、第2切替点114と、第2切替点114より下流側のライン115とでは、殺菌後のキャップ80が搬送されることとなるため、無菌環境としてある。また、第1切替点111と第2切替点114とにおけるライン切替は、例えばコントロールセンターにおけるスイッチ操作により行うものや、コンピューターが自動的に行うものなどの手動又は自動による遠隔操作であってもよく、また、人が直接現場で切替を行うことも考えられる。ただし、第2切替点114については無菌環境とする必要があるため、リモコンによるスイッチ操作などの遠隔操作による切替が好ましい。 The conveyance line 110 is constituted by, for example, a conveyor. Then, the first branch line 112 and the second branch line 113 are branched at the first switching point 111. Plasma sterilizing means 120 is provided on the first branch line 112, and other sterilizing means 130 is provided on the second branch line 113. In addition, at the first switching point 111, the cap 80 conveyed from the upstream side can be switched between the first branch line 112 and the second branch line 113. Further, the first branch line 112 and the second branch line 113 merge at the second switching point 114, and the second switching point 114 is connected to either the first branch line 112 or the second branch line 113 downstream thereof. The connection to the line 115 on the side can be switched. That is, in the sterilization system 100A, it is possible to switch between the plasma sterilization means 120 and the other sterilization means 130 to sterilize the cap 80. In addition, the downstream 112a of the plasma sterilization means 120 of the first branch line 112, the downstream 112a of the plasma sterilization means 120 of the first branch line 112, the second switching point 114, and the downstream of the second switching point 114. Since the sterilized cap 80 is conveyed with the line 115, it is aseptic environment. Further, the line switching between the first switching point 111 and the second switching point 114 may be a manual or automatic remote operation such as one performed by a switch operation at a control center or one automatically performed by a computer. It is also conceivable that a person switches directly on site. However, since the second switching point 114 needs to be an aseptic environment, switching by remote operation such as switch operation by a remote controller is preferable.
 プラズマ殺菌手段120では、プラズマ殺菌装置1が第1切替ライン112に沿って複数配置されている(図3では、省略してノズル10のみを図示してある)。また、キャップ80の殺菌は無菌環境で行う必要があるため、プラズマ殺菌手段120は無菌チャンバー121を有しており、無菌チャンバー121内でキャップ80の殺菌が行われる。 In the plasma sterilization means 120, a plurality of plasma sterilization apparatuses 1 are arranged along the first switching line 112 (in FIG. 3, only the nozzle 10 is shown by omission). In addition, since the cap 80 needs to be sterilized in an aseptic environment, the plasma sterilization means 120 includes the aseptic chamber 121, and the cap 80 is sterilized in the aseptic chamber 121.
 他の殺菌手段130では、プラズマ殺菌手段120とは異なる方法でキャップ80の殺菌を行う。異なる方法としては、既に一般的に用いられておりその殺菌効率や運転の確実性(不良なく運転するか)が実証されている従来から行われている方法によるものが好ましい。例えば、過酸化水素による殺菌や、電子線照射による殺菌、過酢酸系殺菌剤を用いた殺菌などが挙げられる。そして、他の殺菌手段130も同様に無菌チャンバー131を有しており、無菌チャンバー131内でキャップ80の殺菌が行われる。 In the other sterilization means 130, the cap 80 is sterilized by a method different from that of the plasma sterilization means 120. As a different method, a method that has been conventionally used and that has already been generally used and has proven its sterilization efficiency and operation reliability (whether it operates without defects) is preferable. Examples include sterilization with hydrogen peroxide, sterilization with electron beam irradiation, and sterilization with a peracetic acid-based sterilizer. The other sterilizing means 130 also has a sterile chamber 131, and the cap 80 is sterilized in the sterile chamber 131.
 また、図4に示すように、プラズマ殺菌手段120には、プラズマ殺菌装置1の下流側の第1切替ライン112上に、殺菌後のキャップ80を収縮させる収縮手段としてのホットエアーノズル(加熱手段に相当)122が設けられている。つまり、プラズマ殺菌手段120による活性酸素を用いた殺菌はキャップ80に対して熱収縮を生じさせるほどの熱を与える必要はなく、そのためプラズマ殺菌手段120による殺菌ではキャップ80に熱収縮は起こりにくい。一方、他の殺菌手段130で行う従来から用いられている殺菌手段(例えば過酸化水素の含む殺菌剤による殺菌)は、キャップ80に収縮が生じるものが主流である。このため、プラズマ殺菌手段120と他の殺菌手段130との間でキャップ80の大きさにばらつきが生じうる。そこで、このホットエアーノズル122からホットエアー123をキャップ80に吹き込むことにより、殺菌後のキャップ80を加熱することができ、キャップ80の(熱)収縮を生じさせることが可能である。これにより、プラズマ殺菌手段120と他の殺菌手段130との間での殺菌後のキャップ80の大きさのばらつきを効果的に抑制してある。また、キャップ80にごみやほこりが付着している場合に、これを除去できる。 Further, as shown in FIG. 4, the plasma sterilization means 120 includes a hot air nozzle (heating means) as a contraction means for contracting the sterilized cap 80 on the first switching line 112 on the downstream side of the plasma sterilization apparatus 1. 122) is provided. That is, the sterilization using active oxygen by the plasma sterilization unit 120 does not need to apply heat to the cap 80 so as to cause thermal shrinkage. Therefore, the sterilization by the plasma sterilization unit 120 is unlikely to cause thermal contraction in the cap 80. On the other hand, conventionally used sterilization means (for example, sterilization using a hydrogen peroxide-containing sterilizing agent) performed by the other sterilization means 130 is one in which the cap 80 contracts. For this reason, the size of the cap 80 may vary between the plasma sterilization means 120 and the other sterilization means 130. Therefore, by blowing the hot air 123 from the hot air nozzle 122 into the cap 80, the sterilized cap 80 can be heated, and the (heat) shrinkage of the cap 80 can be caused. Thereby, the variation in the size of the cap 80 after sterilization between the plasma sterilization means 120 and the other sterilization means 130 is effectively suppressed. Further, when dust or dust adheres to the cap 80, it can be removed.
 本実施形態に係る殺菌システム100Aは次のような場合に有効である。つまり、新規な殺菌方法である活性酸素を用いた殺菌方法を設備に導入する場合、導入実績が欠けているために、実際にその設備で運転を行うことについて、予期せぬエラーにより運転が停止したり、機器に不具合が生じるなどのリスクを包含したものとなる。そこで、殺菌システム100Aでは、活性酸素を用いた殺菌を行うプラズマ殺菌手段120と他の殺菌手段130とのいずれによりキャップ80の殺菌を行うかを切り替え可能にしてあり、これにより、プラズマ殺菌手段120による殺菌を行っている間に、上記したリスクを抱えたプラズマ殺菌手段120に何らかの不具合が生じたとしても、キャップ80の殺菌をプラズマ殺菌手段120から他の殺菌手段130に切り替えれば、継続してキャップ80の殺菌を行うことができる。 The sterilization system 100A according to the present embodiment is effective in the following cases. In other words, when introducing a new sterilization method using active oxygen, which is a new sterilization method, due to lack of track record of introduction, operation is actually stopped due to an unexpected error. Or the risk that the equipment will malfunction. Therefore, in the sterilization system 100A, it is possible to switch between the plasma sterilization unit 120 that performs sterilization using active oxygen and the other sterilization unit 130 to perform the sterilization of the cap 80. Even if any trouble occurs in the plasma sterilization means 120 having the above risk during the sterilization by the above, if the sterilization of the cap 80 is switched from the plasma sterilization means 120 to another sterilization means 130, it will continue. The cap 80 can be sterilized.
 そのための本実施形態に係る殺菌システム100Aの運転方法としては、具体的には次のものが考えられる。まず、活性酸素を用いた殺菌を行うべく、第1及び第2切替点111,114を第1分岐ライン112側に設定しておく。そして、他の殺菌手段130の運転は停止させておき、プラズマ殺菌手段120のみを運転し、プラズマ殺菌手段120によりキャップ80に対して活性酸素を用いた殺菌を行う。その後、何も問題が生じなければ、この状態を保って運転を継続するが、プラズマ殺菌手段120に何らかの不具合が生じた場合には、第1及び第2切替点111,114を第2分岐ライン113側に切り替え、プラズマ殺菌手段120の運転を停止するとともに、他の殺菌手段130の運転を開始し、他の殺菌手段130によりキャップ80を殺菌する。その後、プラズマ殺菌手段120の不具合が解消された場合には、再び、第1及び第2切替点111,114を第2分岐ライン113側に切り替え、他の殺菌手段130の運転を停止するとともに、プラズマ殺菌手段120の運転を開始し、再度、プラズマ殺菌手段120によりキャップ80に対して活性酸素を用いた殺菌を行う。 Therefore, as an operation method of the sterilization system 100A according to the present embodiment for that purpose, the following can be specifically considered. First, the first and second switching points 111 and 114 are set on the first branch line 112 side in order to perform sterilization using active oxygen. Then, the operation of the other sterilization means 130 is stopped, only the plasma sterilization means 120 is operated, and the plasma sterilization means 120 sterilizes the cap 80 using active oxygen. Thereafter, if no problem occurs, the operation is continued while maintaining this state. However, if any trouble occurs in the plasma sterilization means 120, the first and second switching points 111 and 114 are connected to the second branch line. The operation is switched to the 113 side to stop the operation of the plasma sterilization means 120 and the operation of the other sterilization means 130 is started, and the cap 80 is sterilized by the other sterilization means 130. After that, when the trouble of the plasma sterilization means 120 is resolved, the first and second switching points 111 and 114 are switched to the second branch line 113 side again, and the operation of the other sterilization means 130 is stopped, The operation of the plasma sterilization means 120 is started, and the plasma sterilization means 120 again sterilizes the cap 80 using active oxygen.
 また、本実施形態に係る殺菌システム100Aによれば、活性酸素を用いた殺菌を行うプラズマ殺菌手段110と他の殺菌方法により殺菌を行う他の殺菌手段130とは別ライン112,113上に配置されることになるから、他の殺菌手段130が殺菌を行っている場合の他の殺菌手段130における殺菌剤がプラズマ殺菌手段120まで及んでプラズマ殺菌手段120中に逆流してしまうといった事態が効果的に抑制される。 Further, according to the sterilization system 100A according to the present embodiment, the plasma sterilization means 110 that performs sterilization using active oxygen and the other sterilization means 130 that performs sterilization by other sterilization methods are arranged on separate lines 112 and 113. Therefore, when the other sterilizing means 130 is sterilizing, the sterilizing agent in the other sterilizing means 130 reaches the plasma sterilizing means 120 and flows back into the plasma sterilizing means 120. Is suppressed.
〔第2の実施形態〕
 本発明に係る殺菌システムの第2の実施形態について、図5を参照して説明する。本実施形態では、プラズマ殺菌手段120と他の殺菌手段130との搬送ライン110上の配置が第1の実施形態と異なっている。以下、本実施形態に係る殺菌システム100Bについて、主に第1の実施形態との相違点について説明する。なお、特に明記しない点に関しては、第1の実施形態と同様であり、同一の符号を付して詳細な説明は省略する。
[Second Embodiment]
A second embodiment of the sterilization system according to the present invention will be described with reference to FIG. In the present embodiment, the arrangement of the plasma sterilizing means 120 and the other sterilizing means 130 on the transfer line 110 is different from that of the first embodiment. Hereinafter, differences between the sterilization system 100B according to the present embodiment and the first embodiment will be mainly described. Note that the points not particularly specified are the same as those in the first embodiment, and the same reference numerals are given and detailed description thereof is omitted.
 本実施形態の殺菌システム100Bでは、プラズマ殺菌手段120と他の殺菌手段130とは、搬送ライン110上に直列に設けられている。また、本実施形態では、プラズマ殺菌手段120及び他の殺菌手段130はそれぞれ別の無菌チャンバー121,131を有し、各チャンバー121,131内で殺菌を行う。本実施形態の殺菌システム100Bでは、第1実施形態の殺菌システム100Aのようなライン切替を行うことなく、プラズマ殺菌手段120と他の殺菌手段130とのいずれか一方のみを運転させることにより、プラズマ殺菌手段120のみによるキャップ80の殺菌、又は、他の殺菌手段130のみによるキャップ80の殺菌を可能にしてある。これにより、例えば、活性酸素を用いた殺菌を優先的に行うべく、基本的には、他の殺菌手段130の運転は停止してプラズマ殺菌手段120のみを運転し、プラズマ殺菌手段120のみによるキャップ80の殺菌を行いつつ、プラズマ殺菌手段120に何らかの不具合が生じた場合には、プラズマ殺菌手段120の運転を停止して代わりに他の殺菌手段130の運転を開始し、他の殺菌手段130によりキャップ80を殺菌する、という運転を行うことができる。 In the sterilization system 100B of this embodiment, the plasma sterilization means 120 and the other sterilization means 130 are provided in series on the transport line 110. In this embodiment, the plasma sterilization means 120 and the other sterilization means 130 have separate sterilization chambers 121 and 131, respectively, and perform sterilization in the chambers 121 and 131. In the sterilization system 100B of the present embodiment, the plasma sterilization means 120 and the other sterilization means 130 are operated without switching the line as in the sterilization system 100A of the first embodiment, so that the plasma The cap 80 can be sterilized only by the sterilizing means 120, or the cap 80 can be sterilized only by the other sterilizing means 130. Thus, for example, in order to preferentially perform sterilization using active oxygen, basically, the operation of the other sterilization means 130 is stopped, only the plasma sterilization means 120 is operated, and the cap only by the plasma sterilization means 120 is used. If any trouble occurs in the plasma sterilization means 120 while performing the sterilization of 80, the operation of the plasma sterilization means 120 is stopped and the operation of the other sterilization means 130 is started instead. An operation of sterilizing the cap 80 can be performed.
 また、プラズマ殺菌手段120と他の殺菌手段130との両方を運転させて、プラズマ殺菌手段120と他の殺菌手段130とでキャップ80の殺菌を行うことも可能である。これにより、キャップ80に対する殺菌効果を高めることもできる。そして、このときも、プラズマ殺菌手段120に何らかの不具合が生じた場合には、プラズマ殺菌手段120の運転を停止して他の殺菌手段130のみを運転をして殺菌を行えばよい。特に、本実施形態では、プラズマ殺菌手段120を他の殺菌手段130よりも上流側に配置して、プラズマ殺菌手段120による殺菌に対する予備的・補足的な殺菌手段としても他の殺菌手段130を利用できる。 It is also possible to sterilize the cap 80 with the plasma sterilization means 120 and the other sterilization means 130 by operating both the plasma sterilization means 120 and the other sterilization means 130. Thereby, the bactericidal effect with respect to the cap 80 can also be improved. At this time, if any trouble occurs in the plasma sterilization means 120, the operation of the plasma sterilization means 120 may be stopped and only the other sterilization means 130 may be operated for sterilization. In particular, in the present embodiment, the plasma sterilization means 120 is disposed upstream of the other sterilization means 130, and the other sterilization means 130 is also used as a preliminary and supplemental sterilization means for sterilization by the plasma sterilization means 120. it can.
〔第3の実施形態〕
 本発明に係る殺菌システムの第3の実施形態について、図6を参照して説明する。本実施形態の殺菌システム100Cでは、プラズマ殺菌手段120と他の殺菌手段130とが同一の無菌チャンバー140内で殺菌を行う点で第2の実施形態と異なっている。以下、本実施形態に係る殺菌システムについて、主に第2の実施形態との相違点について説明する。なお、特に明記しない点に関しては、第2の実施形態と同様であり、同一の符号を付して詳細な説明は省略する。
[Third Embodiment]
A third embodiment of the sterilization system according to the present invention will be described with reference to FIG. The sterilization system 100C of this embodiment is different from the second embodiment in that the plasma sterilization means 120 and other sterilization means 130 perform sterilization in the same aseptic chamber 140. Hereinafter, differences between the sterilization system according to the present embodiment and the second embodiment will be mainly described. Note that points not particularly specified are the same as those in the second embodiment, and the same reference numerals are given and detailed description thereof is omitted.
 本実施形態の殺菌システム100Cは、図6に示すように、プラズマ殺菌手段120側の無菌チャンバー140aと他の殺菌手段130側の無菌チャンバー140bとが一体となった無菌チャンバー140内で殺菌を行う構成にしてある。これにより、両方の殺菌手段を別々の無菌チャンバー内に設けるのに比べ、省スペース化を図ることができる。この場合でも、第2実施形態の殺菌システム100Bと同様に、プラズマ殺菌手段120と他の殺菌手段130とのいずれか一方のみを運転させることにより、プラズマ殺菌手段120のみによるキャップ80の殺菌、又は、他の殺菌手段130のみによるキャップ80の殺菌が可能である。また、プラズマ殺菌手段120と他の殺菌手段130との両方を運転させて、プラズマ殺菌手段120と他の殺菌手段130とでキャップ80の殺菌を行うことも可能である。 As shown in FIG. 6, the sterilization system 100C of this embodiment performs sterilization in a sterilization chamber 140 in which a sterilization chamber 140a on the plasma sterilization means 120 side and a sterilization chamber 140b on the other sterilization means 130 side are integrated. It is configured. Thereby, space saving can be achieved compared with providing both sterilization means in a separate aseptic chamber. Even in this case, similarly to the sterilization system 100B of the second embodiment, by operating only one of the plasma sterilization means 120 and the other sterilization means 130, the cap 80 is sterilized only by the plasma sterilization means 120, or The cap 80 can be sterilized only by the other sterilization means 130. It is also possible to operate both the plasma sterilization means 120 and the other sterilization means 130 and sterilize the cap 80 with the plasma sterilization means 120 and the other sterilization means 130.
 ただし、両方の殺菌手段120,130が同じ無菌チャンバー140内にあると、他の殺菌手段130のみが運転している場合、他の殺菌手段130で使用される殺菌剤が、プラズマ殺菌手段120まで及んでプラズマ殺菌手段120における各プラズマ殺菌装置1中に逆流してしまう虞がある。そこで、本実施形態の殺菌システム100Cは、他の殺菌手段130のみが殺菌を行っているときは、第1プラズマ殺菌手段120における各プラズマ殺菌装置1に殺菌剤70の吐出口12から逆流防止用のエアーを噴出させる制御部(図示しない)を備えている。そして、他の殺菌手段130のみが殺菌を行っているときは、プラズマ殺菌手段120については逆流防止用のエアーを噴出させて、他の殺菌手段130の殺菌剤がプラズマ殺菌装置1中に逆流してしまうことを抑止してある。 However, if both sterilization means 120 and 130 are in the same sterilization chamber 140, when only the other sterilization means 130 is operating, the sterilizing agent used in the other sterilization means 130 is up to the plasma sterilization means 120. There is a possibility that the plasma sterilization means 120 may flow back into each plasma sterilization apparatus 1. Therefore, when only the other sterilization means 130 is sterilizing, the sterilization system 100C of this embodiment is used for preventing backflow from the discharge port 12 of the sterilizing agent 70 to each plasma sterilization apparatus 1 in the first plasma sterilization means 120. A control unit (not shown) for ejecting the air is provided. When only the other sterilizing means 130 is sterilizing, the plasma sterilizing means 120 is jetted with air for preventing backflow, and the sterilizing agent of the other sterilizing means 130 flows back into the plasma sterilizing apparatus 1. It is deterring.
〔第4の実施形態〕
 本発明に係る殺菌システムの第4の実施形態として、プラズマ殺菌手段の変形例について、図7を参照して説明する。第1~第3の実施形態の殺菌システム100A~100Cでは、無菌チャンバー121,140a内にプラズマ殺菌手段120が設けられている構成を示したが、図7に示すように、無菌チャンバー121外にプラズマ殺菌手段120を設け、且つ、無菌チャンバー121に吐出口12を接続した状態とし、キャップ80を通過させる無菌チャンバー121中に殺菌剤70を吐出して、無菌チャンバー121内に充満させた殺菌剤70により間接的にキャップ80を殺菌するようにしてもよい。
[Fourth Embodiment]
As a fourth embodiment of the sterilization system according to the present invention, a modified example of the plasma sterilization means will be described with reference to FIG. In the sterilization systems 100A to 100C of the first to third embodiments, the configuration in which the plasma sterilization means 120 is provided in the sterilization chambers 121 and 140a is shown. However, as shown in FIG. The disinfectant provided with the plasma disinfection means 120 and the discharge port 12 connected to the aseptic chamber 121, disinfecting the disinfectant 70 into the aseptic chamber 121 through which the cap 80 passes, and filling the aseptic chamber 121. The cap 80 may be sterilized indirectly by 70.
〔その他の実施形態〕
 最後に、本発明に係る殺菌システムのその他の実施形態について説明する。なお、以下のそれぞれの実施形態で開示される構成は、矛盾が生じない限り、他の実施形態で開示される構成と組み合わせて適用することも可能である。
[Other Embodiments]
Finally, other embodiments of the sterilization system according to the present invention will be described. Note that the configurations disclosed in the following embodiments can be applied in combination with the configurations disclosed in other embodiments as long as no contradiction arises.
(1)上記の実施形態では、プラズマ殺菌手段120に、殺菌後のキャップ80を収縮させる収縮手段としてのホットエアーノズル122が設けられている構成を例として説明した。しかし、本発明の実施形態はこれに限定されない。例えば、ホットエアーノズル122に限らず、蒸気など他の加熱手段であってもよく、加熱によりキャップ80を殺菌するものに限らず、電子線照射などの他の収縮手段を用いても良い。また、収縮手段を設ける位置は、プラズマ殺菌装置1の下流側に限らず、プラズマ殺菌装置1の上流側に配置して、殺菌前のキャップ80を収縮させるようにしても良い。その他にも、収縮手段を用いない構成としても良い。 (1) In the above embodiment, the configuration in which the plasma air sterilizing unit 120 is provided with the hot air nozzle 122 as a contracting unit that contracts the cap 80 after sterilization has been described as an example. However, the embodiment of the present invention is not limited to this. For example, it is not limited to the hot air nozzle 122 but may be other heating means such as steam, and is not limited to sterilizing the cap 80 by heating, and other contraction means such as electron beam irradiation may be used. Further, the position where the contracting means is provided is not limited to the downstream side of the plasma sterilization apparatus 1 but may be disposed upstream of the plasma sterilization apparatus 1 so that the cap 80 before sterilization is contracted. In addition, it is good also as a structure which does not use a contraction means.
 また、上記の実施形態では、収縮手段は、他の殺菌手段130とは別にプラズマ殺菌手段120に設けた構成を例として説明したが、本発明はこれに限定されない。上記の第2及び第3実施形態のように、プラズマ殺菌手段120と他の殺菌手段130とを直列に設けることの一形態として、他の殺菌手段130を加熱による殺菌や電子線照射による殺菌も可能な収縮手段とし、殺菌システムを、プラズマ殺菌手段120に加えて収縮手段が設けられたものとしてもよい。つまり、殺菌システムとしては、プラズマを発生させて、得られた前記プラズマを照射して被殺菌物を殺菌するプラズマ殺菌手段を備え、前記プラズマ殺菌手段には、水蒸気が供給され、前記プラズマ殺菌手段は、発生させた前記プラズマと、供給される前記水蒸気と前記プラズマとが反応して生成される活性酸素と、を含む殺菌剤を前記被殺菌物に対して吐出するものであり、前記プラズマ殺菌手段に加え、前記被殺菌物を収縮させる収縮手段が設けられている殺菌システム、も考えられる。この場合、収縮手段は、例えば、該殺菌手段に隣接してその下流側又は上流側に設けたりするなど、搬送ライン上の任意箇所に設ければよい。また、収縮手段は、被殺菌物の収縮のみを目的としていてもよい。 In the above embodiment, the contraction means is described as an example of the configuration provided in the plasma sterilization means 120 separately from the other sterilization means 130, but the present invention is not limited to this. As in the second and third embodiments, the plasma sterilization means 120 and the other sterilization means 130 are provided in series, and the other sterilization means 130 may be sterilized by heating or electron beam irradiation. As a possible contraction means, the sterilization system may be provided with a contraction means in addition to the plasma sterilization means 120. That is, the sterilization system includes plasma sterilization means for generating plasma and irradiating the obtained plasma to sterilize an object to be sterilized. The plasma sterilization means is supplied with water vapor, and the plasma sterilization means Is for discharging a sterilizing agent containing the generated plasma and active oxygen generated by a reaction between the supplied water vapor and the plasma to the object to be sterilized. In addition to the means, a sterilization system provided with contraction means for contracting the article to be sterilized is also conceivable. In this case, the contraction means may be provided at an arbitrary location on the transport line, for example, adjacent to the sterilization means or provided downstream or upstream thereof. Further, the contraction means may be intended only for contraction of the article to be sterilized.
(2)上記の第2及び第3実施形態では、プラズマ殺菌手段120を他の殺菌手段130の上流側に配置した構成を示した。しかし、本発明の実施形態はこれに限定されず、プラズマ殺菌手段120を他の殺菌手段130の下流側に配置してもよい。 (2) In the second and third embodiments, the configuration in which the plasma sterilizing unit 120 is arranged on the upstream side of the other sterilizing unit 130 is shown. However, the embodiment of the present invention is not limited to this, and the plasma sterilization means 120 may be arranged downstream of the other sterilization means 130.
(3)上記の実施形態では、被殺菌物としてキャップ80を用いた構成を示した。しかし、本発明の実施形態はこれに限定されず、被殺菌物としてそれ以外のものを用いることができる。 (3) In the above embodiment, the configuration using the cap 80 as the article to be sterilized is shown. However, the embodiment of the present invention is not limited to this, and other things can be used as sterilized items.
 その他の構成に関しても、本明細書において開示された実施形態は全ての点で例示であって、本発明の範囲はそれらによって限定されることはないと理解されるべきである。当業者であれば、本発明の趣旨を逸脱しない範囲で、適宜改変が可能であることを容易に理解できるであろう。従って、本発明の趣旨を逸脱しない範囲で改変された別の実施形態も、当然、本発明の範囲に含まれる。 Regarding other configurations as well, it should be understood that the embodiments disclosed herein are illustrative in all respects and that the scope of the present invention is not limited thereby. Those skilled in the art will readily understand that modifications can be made as appropriate without departing from the spirit of the present invention. Accordingly, other embodiments modified without departing from the spirit of the present invention are naturally included in the scope of the present invention.
 本発明は、例えばキャップなどの被殺菌物を殺菌するための殺菌装置に利用することができる。 The present invention can be used in a sterilization apparatus for sterilizing an object to be sterilized such as a cap.
12   吐出口
70   殺菌剤
80   被殺菌物
110  搬送ライン
120  プラズマ殺菌手段(プラズマ殺菌手段)
122  ホットエアーノズル(加熱手段、収縮手段)
130  他の殺菌手段
140  無菌チャンバー
12 Discharge port 70 Disinfectant 80 Object to be sterilized 110 Transport line 120 Plasma sterilization means (plasma sterilization means)
122 Hot air nozzle (heating means, shrinking means)
130 Other sterilization means 140 Aseptic chamber

Claims (8)

  1.  プラズマを発生させて、得られた前記プラズマにより被殺菌物を殺菌するプラズマ殺菌手段を備え、
     前記プラズマ殺菌手段には、水蒸気が供給され、
     前記プラズマ殺菌手段は、発生させた前記プラズマと、供給される前記水蒸気と前記プラズマとが反応して生成される活性酸素と、を含む殺菌剤を吐出するものであり、
     前記プラズマ殺菌手段に加え、前記プラズマ殺菌手段とは異なる方法で前記被殺菌物の殺菌を行う他の殺菌手段が、前記被殺菌物を搬送する搬送ライン上に併設されている殺菌システム。
    Plasma sterilization means for generating plasma and sterilizing the object to be sterilized with the obtained plasma,
    The plasma sterilizing means is supplied with water vapor,
    The plasma sterilizing means discharges a sterilizing agent containing the generated plasma, and active oxygen generated by the reaction between the supplied water vapor and the plasma,
    A sterilization system in which, in addition to the plasma sterilization means, another sterilization means for sterilizing the article to be sterilized by a method different from the plasma sterilization means is provided on a conveyance line for conveying the article to be sterilized.
  2.  前記プラズマ殺菌手段と前記他の殺菌手段とのいずれにより前記被殺菌物の殺菌を行うかを切り替え可能にしてある請求項1に記載の殺菌システム。 The sterilization system according to claim 1, wherein the sterilization means can be switched by either the plasma sterilization means or the other sterilization means.
  3.  前記プラズマ殺菌手段と前記他の殺菌手段とは、前記搬送ライン上に並列に設けられている請求項2に記載の殺菌システム。 The sterilization system according to claim 2, wherein the plasma sterilization means and the other sterilization means are provided in parallel on the transfer line.
  4.  前記プラズマ殺菌手段と前記他の殺菌手段とは、前記搬送ライン上に直列に設けられている請求項2に記載の殺菌システム。 The sterilization system according to claim 2, wherein the plasma sterilization means and the other sterilization means are provided in series on the transfer line.
  5.  前記プラズマ殺菌手段と前記他の殺菌手段とは、同じ無菌チャンバー内に設けられている請求項4に記載の殺菌システム。 The sterilization system according to claim 4, wherein the plasma sterilization means and the other sterilization means are provided in the same aseptic chamber.
  6.  前記他の殺菌手段のみが殺菌を行っているときは、前記プラズマ殺菌手段に前記殺菌剤の吐出口から逆流防止用のエアーを噴出させる制御部を備える請求項5に記載の殺菌システム。 6. The sterilization system according to claim 5, further comprising a control unit that causes the plasma sterilization unit to eject air for preventing backflow from the discharge port of the sterilant when only the other sterilization unit performs sterilization.
  7.  前記プラズマ殺菌手段には、前記被殺菌物を収縮させる収縮手段が設けてられている請求項1~6のいずれか1項に記載の殺菌システム。 The sterilization system according to any one of claims 1 to 6, wherein the plasma sterilization means is provided with contraction means for contracting the article to be sterilized.
  8.  前記収縮手段は、前記被殺菌物を加熱する加熱手段である請求項7に記載の殺菌システム。
     
    The sterilization system according to claim 7, wherein the contraction means is a heating means for heating the article to be sterilized.
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