WO2017110501A1 - Sterilization system - Google Patents

Sterilization system Download PDF

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Publication number
WO2017110501A1
WO2017110501A1 PCT/JP2016/086568 JP2016086568W WO2017110501A1 WO 2017110501 A1 WO2017110501 A1 WO 2017110501A1 JP 2016086568 W JP2016086568 W JP 2016086568W WO 2017110501 A1 WO2017110501 A1 WO 2017110501A1
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Prior art keywords
sterilized
plasma
width
active oxygen
cap
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PCT/JP2016/086568
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French (fr)
Japanese (ja)
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芳原和希
東山堅一
冨永健太
平山裕二
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 JP2017557864A priority Critical patent/JPWO2017110501A1/en
Publication of WO2017110501A1 publication Critical patent/WO2017110501A1/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
    • A61L2/14Plasma, 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
    • A61L2/20Gaseous substances, e.g. vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65BMACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
    • B65B55/00Preserving, protecting or purifying packages or package contents in association with packaging
    • B65B55/02Sterilising, e.g. of complete packages
    • B65B55/04Sterilising wrappers or receptacles prior to, or during, packaging
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65BMACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
    • B65B55/00Preserving, protecting or purifying packages or package contents in association with packaging
    • B65B55/02Sterilising, e.g. of complete packages
    • B65B55/04Sterilising wrappers or receptacles prior to, or during, packaging
    • B65B55/10Sterilising wrappers or receptacles prior to, or during, packaging by liquids or gases
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05HPLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H1/00Generating plasma; Handling plasma
    • H05H1/24Generating plasma
    • H05H1/26Plasma torches

Definitions

  • the present invention relates to a sterilization system that generates plasma and sterilizes an object to be sterilized using the obtained plasma.
  • the sterilization system is A sterilization system that generates plasma and sterilizes an object to be sterilized using the obtained plasma, A transport unit for transporting the article to be sterilized; A gas supply unit for supplying a mixed gas containing oxygen; A water vapor supply unit for supplying water vapor; A plasma generation unit for generating plasma containing ozone from the mixed gas supplied from the gas supply unit; An active oxygen generator that generates active oxygen by reacting the plasma with the water vapor supplied from the water vapor supply unit; A plurality of sterilizers provided in parallel along the conveying direction of the article to be sterilized, and a discharge unit that discharges the plasma and the active oxygen to the article to be sterilized as a sterilizing agent, A pitch stuffing mechanism is provided to pack the interval between the objects to be sterilized by the sterilizer.
  • a plurality of the sterilization apparatuses are arranged in parallel along the conveyance direction of the article to be sterilized.
  • an air spraying device that blows air against the object to be sterilized from behind in the transport direction as the pitch filling mechanism.
  • the interval between the sterilized objects can be reduced with a simple configuration in which air is blown to propel the sterilized object forward in the conveyance direction.
  • the conveyance unit is inclined downward toward the front in the conveyance direction, and the article to be sterilized is conveyed using its own weight.
  • the system configuration can be simplified without using mechanical means. Further, because of the magnitude relationship between the dynamic friction coefficient and the static friction coefficient, the object to be sterilized is further promoted in a state where the object to be sterilized advances by its own weight, compared with the force for propelling the object to be sterilized with respect to the transport unit. Since the force is small, when combined with a configuration including an air blowing device as the pitch filling mechanism, there is an advantage that pitch filling by blowing air can be easily performed.
  • the article to be sterilized has at least a first width portion having a first width and a second width portion having a second width larger than the first width
  • the transport unit is preferably configured such that the two rod-like members are arranged in parallel with each other with a width that is substantially the same as or larger than the first width and smaller than the second width. It is.
  • the object to be sterilized can be supported by the rod-shaped member by setting the width of the rod-shaped member as described above.
  • the object to be sterilized is sterilized not only on the surface to be treated with plasma and active oxygen directly from the sterilizer, but also on the part other than the surface to be treated with the plasma and active oxygen dissipated to the surroundings.
  • the part of the installation surface with the plate-shaped transport part of the object to be sterilized cannot be sterilized by the plasma and active oxygen dissipated to the surroundings, but it is sterilized by the rod-shaped member. If it is the structure which supports an object, the area
  • the first width portion has at least the first width portion having the first width and the second width portion having the second width larger than the first width.
  • the diameter may be gradually increased, for example, in a tapered shape toward the second width portion, and the change from the first width portion to the second width portion may be continuous, or the second width portion
  • the shape may protrude from the first width portion, and the change from the first width portion to the second width portion may be discontinuous.
  • the sterilization system 100 of the present embodiment sterilizes a cap 80 of a container such as a PET bottle as an example of an object to be sterilized, generates plasma, and sterilizes the cap 80 with the obtained plasma.
  • the sterilization system 100 includes a gas supply unit 30 that supplies a mixed gas containing oxygen, a water vapor supply unit 40 that supplies water vapor, and a plasma generation unit that generates ozone-containing plasma from the mixed gas supplied from the gas supply unit 30.
  • active oxygen generation unit 13 that reacts plasma and water vapor supplied from water vapor supply unit 40 to generate active oxygen (Reactive Oxygen Species (ROS), for example, OH radical or singlet oxygen), plasma and activity
  • a sterilizer 1 including a discharge unit 12 that discharges a sterilizer containing oxygen, and a transport unit 110 that transports a cap 80 are provided.
  • the sterilization system 100 is provided with a pitch filling mechanism 120 that closes the gap between the caps 80 conveyed by the conveyance unit 110. Thereby, it is possible to improve the sterilizing effect on the sterilized product while increasing the number of sterilizable products per unit time, and to efficiently sterilize using active oxygen.
  • the apparatus structure of the sterilizer 1 for performing sterilization using active oxygen is demonstrated first.
  • 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 unit 12 that discharges a bactericide 70 containing plasma and active oxygen, and active oxygen that is disposed between the plasma generation unit 11 and the discharge unit 12. And a generation unit 13.
  • 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.
  • oxygen O 2 , oxygen
  • oxygen is supplied into the plasma generation unit 11 together with air (air), and oxygen is passed through the generated electric field, thereby generating plasma containing ozone from the supplied oxygen.
  • the generated plasma is sent to the active oxygen generator 13.
  • oxygen radicals and ozone (O 3 ) are generated by the plasma, and these are sent to the active oxygen generator 13.
  • the active oxygen generation unit 13 is connected to an evaporator (corresponding to a water vapor supply unit) 40, and further water vapor is sent to the active oxygen generation unit 13.
  • the active oxygen generation unit 13 can generate active oxygen by reacting the plasma (oxygen radicals and ozone) sent from the plasma generation unit 11 with the water vapor (vapor) supplied from the evaporator 40.
  • the plasma oxygen radicals and ozone
  • hydroxy radicals .OH
  • the hydrogen radical reacts with ozone to generate a hydroxy radical and oxygen (O 2 ) as shown in the following formula (5).
  • the reaction of the above formula (6) 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 nozzle 10, a generator 21 and a transformer 22 that constitute an AC power supply 20, a gas supply machine (corresponding to a gas supply unit) 30 that supplies various gases such as oxygen to the nozzle 10 and the evaporator 40, active oxygen
  • the evaporator 40 which supplies water vapor
  • Generator 21 generates an alternating current.
  • the frequency is 13 kHz
  • the effective voltage is 350 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 unit 30 is connected to the plasma generation unit 11 and supplies oxygen together with air to the nozzle 10 (plasma generation unit 11). Further, the air for supplying the water vapor generated by the evaporator 40 to the active oxygen generator 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, the air is supplied to the nozzle 10 at 6 L / min and oxygen at 3 L / min so that the air: oxygen ratio is 2: 1. In 40, air is sent at 3 L / min.
  • the evaporator 40 is connected to the active oxygen generator 13 and sends water vapor to the active oxygen generator 13. Specifically, a built-in heating wire (not shown) is heated to 180 ° C., and water supplied from the pump 50 is heated by the heating wire to generate water vapor. Then, water vapor is mixed with the air supplied from the gas supplier 30, and the water vapor is supplied to the active oxygen generator 13 together with the air. In the present embodiment, for example, the pump 50 supplies water to the evaporator 40 at a rate of 1.2 mL / min.
  • the chiller 60 cools the nozzle 10 that generates heat when a high voltage is applied by supplying cooling water to the nozzle 10.
  • 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 plasma is the active oxygen generation unit 13.
  • the active oxygen mainly composed of hydroxy radicals is continuously generated by reacting with water vapor supplied together with air from the evaporator 40. Then, active oxygen, water vapor, and unreacted plasma continuously generated in the active oxygen generation unit 13 are continuously discharged from the discharge unit 12 as the sterilizing agent 70, thereby enabling continuous processing of the cap 80. It becomes.
  • the bactericide 70 containing plasma and active oxygen is discharged from the discharge unit 12 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. For example, when a sterilizing agent containing hydrogen peroxide is used, it is necessary to subsequently clean the sterilizing agent so that it does not remain on the article 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 sterilization system 100 includes a transport unit 110 that transports the cap 80, and a plurality of the sterilizers 1 are arranged in parallel along the transport direction T of the cap 80.
  • An air blowing device 130 that blows air against the cap 80 from the rear in the conveyance direction T is provided as a pitch filling mechanism that closes the gap between the caps 80 conveyed by the conveyance unit 110. Since a plurality (5 in this embodiment) of the sterilizers 1 are arranged in parallel along the transport direction T of the cap 80, the cap 80 is transported by the transport unit 110 without stopping the cap 80. Plasma and active oxygen can be discharged to the cap 80 in sufficient time and amount by the plurality of sterilization apparatuses 1 arranged in the transport direction T. Thereby, the quantity of the to-be-sterilized thing which can be sterilized per unit time can be increased.
  • the transport unit 110 includes two rod-shaped members 111, and the two rod-shaped members 111 are arranged in parallel with each other with a width that can support the ring portion 82 of the cap 80 from below. That is, the PET bottle cap 80 usually has a threaded portion on the inside, a main body portion (corresponding to a first width portion having a first width) 81 to be screwed with the threaded portion in the mouth portion of the bottle, and the cap. A ring portion (second width portion having a second width larger than the first width) 82 remaining on the bottle side when opening 80, and the diameter of the ring portion 82 (the second width portion). (Corresponding to the width) is designed to be larger than the diameter of the main body 81 (corresponding to the first width).
  • the width of the two rod-shaped members 111 is set to be substantially the same as or larger than the diameter of the main body portion 81 and smaller than the diameter of the ring portion 82, the cap 80 is placed on the opening surface side (that is, In the state where the ring portion 82 side is up, the two ring portions (second width portions) 82 are provided as shown in FIG. 5 by passing between the main body portion 81 and the two rod-shaped members 111. It will be in the state supported by the rod-shaped member 111 of this. In the present embodiment, as shown in FIG.
  • the width of the two rod-shaped members 111 is substantially the same as the width of the main body portion 81, so that the ring portion 82 is supported from below by the two rod-shaped members 111. It will be in a state to be.
  • the cap 80 is sterilized not only by the part to which the plasma and active oxygen are directly applied from the sterilization apparatus 1 but also other parts by the plasma and active oxygen dissipated to the surroundings. If it is the structure which supports, the area
  • the conveyance part 110 inclines below as it goes ahead of the conveyance direction T.
  • the cap 80 is not held by the conveyance unit 110 and the ring portion 82 is supported from below by the two rod-shaped members 111.
  • the cap 80 is transported forward in the transport direction T using its own weight. As a result, the cap 80 can be transported with a simple configuration in which the entire transport unit 110 is inclined.
  • the continuously transported cap 80 can be continuously sterilized by the plurality of sterilization apparatuses 1, but the inventor can continuously sterilize the object to be sterilized in this way.
  • the sterilization effect is improved by reducing the interval between the articles to be sterilized. This is because when the interval between the caps 80 is equal to or larger than a certain interval, the air flow is likely to be disturbed due to the interval, so that the plasma and the active oxygen are easily dissipated. This is because the plasma and active oxygen are not smoothly applied.
  • a plurality of air spraying devices 120 are provided.
  • the air blowing device 120 is configured to be able to blow air against the cap 80 from the rear in the transport direction T, and blows air from the rear of the cap 80 when there is an interval (pitch) between the caps 80.
  • the cap 80 is pushed forward in the transport direction T so as to close the gap.
  • the bactericidal effect with respect to a to-be-sterilized thing can be improved.
  • the air blowing device 120 may be operated at all times, or may be operated when it is detected that there is a gap between the caps 80 using an optical sensor or the like. In addition, the air blowing device 120 may be provided only in a region on the rear side in the transport direction T with respect to the sterilization device 1.
  • 3 and 4 show a state in which the gaps are narrowed until the caps 80 come into close contact with each other, but it is not always necessary to bring the caps 80 into close contact with each other.
  • the distance between the caps 80 may be close enough to make it difficult to disturb the airflow.
  • the interval varies depending on the size and shape of the object to be sterilized. For example, in the cap 80 (diameter 30 mm) of the present embodiment, if the interval between the caps 80 is within 30 mm, a favorable improvement in sterilization effect can be expected.
  • the sterilization system 100 is configured as described above, it is possible to improve the sterilization effect on the cap 80 while increasing the number of caps 80 that can be sterilized per unit time, thereby sterilizing using active oxygen. Can be performed efficiently.
  • the transport unit 110 is configured such that the two rod-shaped members 111 are separated from each other by a predetermined width and are arranged in parallel to each other, and are inclined downward toward the front in the transport direction.
  • the configuration in which the cap 80 is transported using its own weight has been described.
  • the embodiment of the present invention is not limited to this.
  • the cap 80 may be conveyed not by its own weight but by driving a conveying device such as a conveyor.
  • a conveying device such as a conveyor.
  • You may convey the cap 80 using a self-weight on a roller or a plate-shaped member.
  • the configuration using the air blowing device 120 as the pitch filling mechanism has been described as an example.
  • the embodiment of the present invention is not limited to this.
  • the cap 80 is transported using its own weight as described above, and as a pitch filling mechanism, an arbitrary cap 80 such as the top cap 80 moves at a constant speed slower than the traveling speed due to its own weight.
  • the cap 80 that moves at a constant speed catches up with the cap 80, and the gap between the cap 80 that has moved at the same speed as the cap 80 and the cap 80 that follows the cap 80 may be narrowed.
  • a damming portion for temporarily damming the cap 80 is provided at an arbitrary position upstream (backward in the conveying direction T) from the sterilizing apparatus 1, and the damped cap 80 and the cap 80 following the dammed cap 80 are provided. You may make it close
  • the cap 80 is used as an object to be sterilized, and the cap 80 has a second width larger than the first width as the first width portion having the first width.
  • the configuration having the ring portion as the second width portion has been described as an example.
  • the embodiment of the present invention is not limited to this.
  • what is used as the article to be sterilized can be changed as appropriate.
  • the first width portion having the first width and the second width portion having the second width larger than the first width are not necessarily required.
  • the configuration in which the sterilizer 1 directly discharges the sterilizer 70 containing active oxygen to the cap 80 has been described as an example.
  • the embodiment of the present invention is not limited to this.
  • the sterilizing agent 70 is discharged into the chamber through which the cap 80 passes instead of directly discharging the sterilizing agent into the cap 80, and the conveyance unit 110 is allowed to pass through the chamber so that the chamber is filled.
  • the cap 80 may be sterilized indirectly, for example, by sterilizing the cap 80 passing through the chamber with the sterilizing agent 70.
  • the present invention can be used for a sterilization system for sterilizing an object to be sterilized such as a cap.

Abstract

A sterilization system (100) that comprises a sterilization device (1) comprising a gas supply part (30) which supplies a mixed gas containing oxygen, a steam supply part (40) which supplies steam, a plasma generation part (11) which generates ozone-containing plasma from oxygen supplied by the gas supply part (30), an active oxygen generation part (13) which generates active oxygen through a reaction between the plasma and steam supplied by the steam supply part (40), and a discharge part (12) which discharges the plasma and active oxygen as a sterilizing agent (70) , and a transport part (110) which transports subjects (80) being sterilized, wherein a pitch-reducing mechanism (120) for reducing the interval between the subjects (80) being sterilized by the sterilization device (1) is provided .

Description

殺菌システムSterilization system
 本発明は、プラズマを発生させて、得られたプラズマを利用して被殺菌物を殺菌する殺菌システムに関する。 The present invention relates to a sterilization system that generates plasma and sterilizes an object to be sterilized using the obtained plasma.
 本出願人はPCT/JP2015/005185において、PETボトルのキャップ等の被殺菌物を殺菌する新たな手法として、プラズマを発生させて、そのプラズマと水蒸気とを反応させることにより生成される活性酸素を用いてプラズマとともに殺菌を行う殺菌装置を提案している。このようにして生成される活性酸素は反応性の高いヒドロキシラジカルを多く含み、そのため高い殺菌効果を奏するものであるため、これを用いて殺菌を行うことにより効果的に殺菌が行える。このため、この殺菌装置を用いた殺菌が望まれているが、この手法は新規な手法であるため、さらなる改良の余地がある。 In the PCT / JP2015 / 005185, the present applicant, as a new technique for sterilizing an object to be sterilized such as a cap of a PET bottle, generates active oxygen generated by reacting the plasma with water vapor by generating plasma. We have proposed a sterilizer that uses and sterilizes with plasma. The active oxygen produced in this way contains a large amount of highly reactive hydroxy radicals, and therefore has a high sterilizing effect. Therefore, sterilization can be performed effectively by using this. For this reason, although sterilization using this sterilizer is desired, since this method is a novel method, there is room for further improvement.
 そこで、活性酸素を用いた殺菌を効率的に行うことができる殺菌システムの実現が望まれる。 Therefore, it is desired to realize a sterilization system that can efficiently perform sterilization using active oxygen.
 本発明に係る殺菌システムは、
 プラズマを発生させて、得られたプラズマを利用して被殺菌物を殺菌する殺菌システムであって、
 前記被殺菌物を搬送する搬送部を備え、
 酸素を含む混合ガスを供給するガス供給部と、
 水蒸気を供給する水蒸気供給部と、
 前記ガス供給部から供給される前記混合ガスからオゾンを含むプラズマを生成するプラズマ生成部と、
 前記プラズマと前記水蒸気供給部から供給される前記水蒸気とを反応させて活性酸素を生成する活性酸素生成部と、
 前記プラズマと前記活性酸素とを殺菌剤として前記被殺菌物に対して吐出する吐出部と、を備える殺菌装置が前記被殺菌物の搬送方向に沿って複数並設されており、
 前記殺菌装置により殺菌される前記被殺菌物間の間隔を詰めるピッチ詰め機構が設けられている。
The sterilization system according to the present invention is
A sterilization system that generates plasma and sterilizes an object to be sterilized using the obtained plasma,
A transport unit for transporting the article to be sterilized;
A gas supply unit for supplying a mixed gas containing oxygen;
A water vapor supply unit for supplying water vapor;
A plasma generation unit for generating plasma containing ozone from the mixed gas supplied from the gas supply unit;
An active oxygen generator that generates active oxygen by reacting the plasma with the water vapor supplied from the water vapor supply unit;
A plurality of sterilizers provided in parallel along the conveying direction of the article to be sterilized, and a discharge unit that discharges the plasma and the active oxygen to the article to be sterilized as a sterilizing agent,
A pitch stuffing mechanism is provided to pack the interval between the objects to be sterilized by the sterilizer.
 発明者は、このように連続搬送される被殺菌物を殺菌する場合、被殺菌物間の間隔が一定間隔以上であると、その間隔に起因して気流の乱れが生じやすくなり、これにより、被殺菌物に対してプラズマ及び活性酸素が円滑に当たらなくなること、及び、搬送される被殺菌物間の間隔を詰めれば、気流の乱れを効果的に低減できて、その結果殺菌効果が向上することを見出した。そこで、この構成では、発明者が見出した好適な手法を採用し、搬送される被殺菌物間の間隔を詰めるピッチ詰め機構が設けられている。これにより、被殺菌物に対する殺菌効果を向上させることができる。したがって、活性酸素を用いた殺菌を効率的に行うことができる。 When the inventor continuously sterilizes the articles to be sterilized in this manner, if the interval between the articles to be sterilized is equal to or larger than a certain interval, the air flow is likely to be disturbed due to the interval. If the plasma and active oxygen are not smoothly applied to the object to be sterilized, and the interval between the objects to be sterilized is reduced, the turbulence of the air current can be effectively reduced, and as a result, the sterilization effect is improved. I found out. In view of this, in this configuration, a pitch filling mechanism that closes the interval between the articles to be sterilized by using a suitable technique found by the inventor is provided. Thereby, the bactericidal effect with respect to a to-be-sterilized thing can be improved. Therefore, sterilization using active oxygen can be performed efficiently.
 一つの態様として、前記殺菌装置が前記被殺菌物の搬送方向に沿って複数並設されていると好適である。 As one aspect, it is preferable that a plurality of the sterilization apparatuses are arranged in parallel along the conveyance direction of the article to be sterilized.
 この構成によれば、殺菌装置を被殺菌物の搬送方向に沿って複数並設するから、搬送される被殺菌物に対して複数の殺菌装置からプラズマ及び活性酸素を吐出することで、被殺菌物に当てられるプラズマ及び活性酸素の量を保ちながら単位時間あたりの殺菌可能な被殺菌物の数量を増やすことができる。 According to this configuration, since a plurality of sterilization apparatuses are arranged in parallel along the conveyance direction of the object to be sterilized, by discharging plasma and active oxygen from the plurality of sterilization apparatuses to the object to be sterilized, While maintaining the amount of plasma and active oxygen applied to the object, the number of objects to be sterilized per unit time can be increased.
 一つの態様として、前記ピッチ詰め機構として前記搬送方向の後方から前記被殺菌物に対しエアーを吹き付けるエアー吹付装置を備えると好適である。 As one aspect, it is preferable to provide an air spraying device that blows air against the object to be sterilized from behind in the transport direction as the pitch filling mechanism.
 この構成によれば、エアーを吹き付けて被殺菌物を搬送方向前方に推進させるという簡易な構成で被殺菌物間の間隔を詰めることができる。 According to this configuration, the interval between the sterilized objects can be reduced with a simple configuration in which air is blown to propel the sterilized object forward in the conveyance direction.
 一つの態様として、前記搬送部は前記搬送方向前方に向かうに従って下方に傾斜しており、前記被殺菌物の自重を利用して前記被殺菌物を搬送すると好適である。 As one aspect, it is preferable that the conveyance unit is inclined downward toward the front in the conveyance direction, and the article to be sterilized is conveyed using its own weight.
 この構成によれば、システム構成を機械的な手段を用いない簡易な構成とできる。また、動摩擦係数と静摩擦係数との大小関係から、搬送部に対して静止している被殺菌物を推進させる力に比べ、被殺菌物が自重により進んでいる状態でさらに被殺菌物を推進させる力は小さく済むため、上記のピッチ詰め機構としてエアー吹付装置を備える構成と組み合わせれば、エアーを吹き付けることによるピッチ詰めを容易に行える利点がある。 According to this configuration, the system configuration can be simplified without using mechanical means. Further, because of the magnitude relationship between the dynamic friction coefficient and the static friction coefficient, the object to be sterilized is further promoted in a state where the object to be sterilized advances by its own weight, compared with the force for propelling the object to be sterilized with respect to the transport unit. Since the force is small, when combined with a configuration including an air blowing device as the pitch filling mechanism, there is an advantage that pitch filling by blowing air can be easily performed.
 一つの態様として、前記被殺菌物は、第1の幅を有する第1の幅部分と前記第1の幅よりも大きい第2の幅を有する第2の幅部分と、を少なくとも有し、前記搬送部は、2本の棒状部材が、前記第1の幅と略同じ又はそれよりも大きく且つ前記第2の幅よりも小さい幅で離間して、互いに平行に配置されたものであると好適である。 As one aspect, the article to be sterilized has at least a first width portion having a first width and a second width portion having a second width larger than the first width, The transport unit is preferably configured such that the two rod-like members are arranged in parallel with each other with a width that is substantially the same as or larger than the first width and smaller than the second width. It is.
 この構成によれば、棒状部材の幅を上記のように設定することにより、棒状部材によって被殺菌物を支持させることができる。被殺菌物は、殺菌装置から直接プラズマ及び活性酸素が当てられる被処理面だけでなく、周囲に散逸するプラズマ及び活性酸素によって被処理面以外の部分も殺菌されるところ、例えばプレート状の搬送部上で被殺菌物を搬送する場合、被殺菌物のうち、プレート状の搬送部との設置面の部分は周囲に散逸するプラズマ及び活性酸素によっても殺菌することはできないが、棒状部材によって被殺菌物を支持する構成であれば、殺菌において搬送部が干渉する領域を極めて小さくすることができ、被殺菌物の全体を効果的に殺菌できる。 According to this configuration, the object to be sterilized can be supported by the rod-shaped member by setting the width of the rod-shaped member as described above. The object to be sterilized is sterilized not only on the surface to be treated with plasma and active oxygen directly from the sterilizer, but also on the part other than the surface to be treated with the plasma and active oxygen dissipated to the surroundings. When transporting the object to be sterilized above, the part of the installation surface with the plate-shaped transport part of the object to be sterilized cannot be sterilized by the plasma and active oxygen dissipated to the surroundings, but it is sterilized by the rod-shaped member. If it is the structure which supports an object, the area | region where a conveyance part interferes in sterilization can be made very small, and the whole to-be-sterilized object can be sterilized effectively.
 なお、ここで、第1の幅を有する第1の幅部分と第1の幅よりも大きい第2の幅を有する第2の幅部分と、を少なくとも有するものとしては、第1の幅部分から第2の幅部分に向かうにつれて例えばテーパー状に徐々に拡径し、第1の幅部分から第2の幅部分への変化が連続的なものであってもよく、また、第2の幅部分が第1の幅部分から突出した形状であり、第1の幅部分から第2の幅部分への変化が不連続なものであってもよい。 Here, the first width portion has at least the first width portion having the first width and the second width portion having the second width larger than the first width. The diameter may be gradually increased, for example, in a tapered shape toward the second width portion, and the change from the first width portion to the second width portion may be continuous, or the second width portion The shape may protrude from the first width portion, and the change from the first width portion to the second width portion may be discontinuous.
活性酸素を用いた殺菌を行う殺菌装置の概略構成図Schematic configuration diagram of a sterilizer that performs sterilization using active oxygen 活性酸素を用いた殺菌を行う殺菌装置の装置構成ブロック図Device configuration block diagram of a sterilizer that performs sterilization using active oxygen 殺菌システムの斜視図Perspective view of sterilization system 殺菌システムの側面図Side view of sterilization system 殺菌システムの正面図Front view of sterilization system
 本発明に係る殺菌システム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100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り、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。殺菌システム100は、酸素を含む混合ガスを供給するガス供給部30と、水蒸気を供給する水蒸気供給部40と、ガス供給部30から供給される混合ガスからオゾンを含むプラズマを生成するプラズマ生成部11と、プラズマと水蒸気供給部40から供給される水蒸気とを反応させて活性酸素(Reactive Oxygen Species(ROS)、例えばOH radicalやsinglet oxygenなど)を生成する活性酸素生成部13と、プラズマと活性酸素とを含む殺菌剤を吐出する吐出部12と、を備える殺菌装置1と、キャップ80を搬送する搬送部110と、を備えている。そして、殺菌システム100には、搬送部110により搬送されるキャップ80間の間隔を詰めるピッチ詰め機構120が設けられている。これにより、単位時間あたりの殺菌可能な被殺菌物の数量を増やしながらも、被殺菌物に対する殺菌効果を向上させることができて、活性酸素を用いた殺菌を効率的に行うことができる。以下ではまず、活性酸素を用いた殺菌を行うための殺菌装置1の装置構成について説明する。 Embodiments of a sterilization system according to the present invention will be described with reference to the drawings. The sterilization system 100 of the present embodiment sterilizes a cap 80 of a container such as a PET bottle as an example of an object to be sterilized, generates plasma, and sterilizes the cap 80 with the obtained plasma. The sterilization system 100 includes a gas supply unit 30 that supplies a mixed gas containing oxygen, a water vapor supply unit 40 that supplies water vapor, and a plasma generation unit that generates ozone-containing plasma from the mixed gas supplied from the gas supply unit 30. 11, active oxygen generation unit 13 that reacts plasma and water vapor supplied from water vapor supply unit 40 to generate active oxygen (Reactive Oxygen Species (ROS), for example, OH radical or singlet oxygen), plasma and activity A sterilizer 1 including a discharge unit 12 that discharges a sterilizer containing oxygen, and a transport unit 110 that transports a cap 80 are provided. The sterilization system 100 is provided with a pitch filling mechanism 120 that closes the gap between the caps 80 conveyed by the conveyance unit 110. Thereby, it is possible to improve the sterilizing effect on the sterilized product while increasing the number of sterilizable products per unit time, and to efficiently sterilize using active oxygen. Below, the apparatus structure of the sterilizer 1 for performing sterilization using active oxygen is demonstrated first.
 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とを含む殺菌剤70を吐出する吐出部12と、プラズマ生成部11と吐出部12との間に配置された活性酸素生成部13と、を備える。 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 unit 12 that discharges a bactericide 70 containing plasma and active oxygen, and active oxygen that is disposed between the plasma generation unit 11 and the discharge unit 12. And a generation unit 13.
 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、被殺菌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 is not necessary to expose to-be-sterilized material 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、本実施形態では、プラズマ生成部11内にエアー(air)とともに酸素(O、oxygen)を供給し、発生電界に酸素を通気させることにより、供給される酸素からオゾンを含むプラズマを生成する。そして、生成されたプラズマは、活性酸素生成部13へと送られる。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、これらが活性酸素生成部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. . In the present embodiment, oxygen (O 2 , oxygen) is supplied into the plasma generation unit 11 together with air (air), and oxygen is passed through the generated electric field, thereby generating plasma containing ozone from the supplied oxygen. To do. Then, the generated plasma is sent to the active oxygen generator 13. Specifically, oxygen radicals and ozone (O 3 ) are generated by the plasma, and these are sent to the active oxygen generator 13.
 活性酸素生成部13は、エバポレータ(水蒸気供給部に相当)40と接続してあり、活性酸素生成部13にはさらに水蒸気が送られる。これにより、活性酸素生成部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から供給される水蒸気(vapor)とを反応させて、活性酸素を生成できる。本実施形態では、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 active oxygen generation unit 13 is connected to an evaporator (corresponding to a water vapor supply unit) 40, and further water vapor is sent to the active oxygen generation unit 13. As a result, the active oxygen generation unit 13 can generate active oxygen by reacting the plasma (oxygen radicals and ozone) sent from the plasma generation unit 11 with the water vapor (vapor) supplied from the evaporator 40. In the present embodiment, by reacting plasma (oxygen radicals and ozone) with water vapor, hydroxy radicals (.OH) having a particularly high reactivity 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(4)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 (4).
 HO → ・H+・OH・・・・・(4) H 2 O → H + OH (4)
 また、水素ラジカルはオゾンと反応して、以下の(5)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 (5).
 ・H+O → ・OH+O・・・・・(5) ・ H + O 3 → ・ OH + O 2 (5)
 (4)式と(5)式は、次の(6)式にまとめることができる。 (4) and (5) can be combined into the following (6).
 HO+O → 2・OH+O・・・・・(6) H 2 O + O 3 → 2.OH + O 2 (6)
 つまり、プラズマと水蒸気を反応させることにより、上記(6)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(酸素ラジカルとオゾン)とが殺菌剤70として吐出部12からキャップ80に吐出されて、キャップ80の殺菌が行われる。 That is, by reacting plasma and water vapor, the reaction of the above formula (6) 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 (oxygen radicals and ozone) are discharged from the discharge unit 12 to the cap 80 as the sterilizing agent 70, and the cap 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に酸素等の各種ガスを供給するガス供給機(ガス供給部に相当)30、活性酸素生成部13に水蒸気を供給するエバポレータ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、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 nozzle 10, a generator 21 and a transformer 22 that constitute an AC power supply 20, a gas supply machine (corresponding to a gas supply unit) 30 that supplies various gases such as oxygen to the nozzle 10 and the evaporator 40, active oxygen The evaporator 40 which supplies water vapor | steam to the production | generation part 13, the pump 50 which supplies water to the evaporator 40, and the chiller 60 which supplies cooling water to the nozzle 10 are provided.
 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13kHzで、実効電圧350V、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 13 kHz, the effective voltage is 350 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、プラズマ生成部11に接続されて、ノズル10(プラズマ生成部11)に対し、エアーとともに酸素を供給する。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活性酸素生成部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:酸素が2:1となるように、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 unit 30 is connected to the plasma generation unit 11 and supplies oxygen together with air to the nozzle 10 (plasma generation unit 11). Further, the air for supplying the water vapor generated by the evaporator 40 to the active oxygen generator 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, the air is supplied to the nozzle 10 at 6 L / min and oxygen at 3 L / min so that the air: oxygen ratio is 2: 1. In 40, air is sent at 3 L / min.
 エバポレータ40は、活性酸素生成部13に接続され、活性酸素生成部13に水蒸気を送る。具体的には、内蔵された電熱線(図示しない)を180℃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活性酸素生成部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(water)を1.2mL/minで供給する。 The evaporator 40 is connected to the active oxygen generator 13 and sends water vapor to the active oxygen generator 13. Specifically, a built-in heating wire (not shown) is heated to 180 ° C., and water supplied from the pump 50 is heated by the heating wire to generate water vapor. Then, water vapor is mixed with the air supplied from the gas supplier 30, and the water vapor is supplied to the active oxygen generator 13 together with the air. In the present embodiment, for example, the pump 50 supplies water to the evaporator 40 at a rate of 1.2 mL / min.
 チラー60は、ノズル10に冷却水(cooling water)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 a 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、生成されたプラズマが活性酸素生成部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、活性酸素生成部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として吐出部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の流量で吐出部12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 plasma is the active oxygen generation unit 13. , The active oxygen mainly composed of hydroxy radicals is continuously generated by reacting with water vapor supplied together with air from the evaporator 40. Then, active oxygen, water vapor, and unreacted plasma continuously generated in the active oxygen generation unit 13 are continuously discharged from the discharge unit 12 as the sterilizing agent 70, thereby enabling continuous processing of the cap 80. It becomes. In the present embodiment, for example, the bactericide 70 containing plasma and active oxygen is discharged from the discharge unit 12 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。例えば、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. For example, when a sterilizing agent containing hydrogen peroxide is used, it is necessary to subsequently clean the sterilizing agent so that it does not remain on the article 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.
 以上が、活性酸素を用いた殺菌のための装置構成である。次に、本実施形態に係る殺菌システム100について図3~5を用いて説明する。なお、以下では、殺菌装置1によりキャップ80を殺菌する領域のみを説明し、その前後の構成については特に説明しない。その前後の構成をどのようにするかは特に限定されず、目的に応じて適宜選択可能である。 The above is the apparatus configuration for sterilization using active oxygen. Next, the sterilization system 100 according to the present embodiment will be described with reference to FIGS. In the following, only the region where the cap 80 is sterilized by the sterilization apparatus 1 will be described, and the configuration before and after that will not be specifically described. There are no particular limitations on how the configurations before and after that can be selected as appropriate according to the purpose.
 図3に示すように、殺菌システム100は、キャップ80を搬送する搬送部110を備え、殺菌装置1がキャップ80の搬送方向Tに沿って複数並設されている。そして、搬送部110により搬送されるキャップ80間の間隔を詰めるピッチ詰め機構として搬送方向Tの後方からキャップ80に対しエアーを吹き付けるエアー吹付装置130が設けられている。キャップ80の搬送方向Tに沿って殺菌装置1を複数(本実施形態では5台)並設してあるため、キャップ80を静止させることなく、搬送部110によってキャップ80を搬送しながら、キャップ80の搬送方向Tに並ぶ複数台の殺菌装置1によって、キャップ80に対してプラズマと活性酸素とを十分な時間・量で吐出することができる。これにより、単位時間あたりに殺菌可能な被殺菌物の数量を増やすことができる。 As shown in FIG. 3, the sterilization system 100 includes a transport unit 110 that transports the cap 80, and a plurality of the sterilizers 1 are arranged in parallel along the transport direction T of the cap 80. An air blowing device 130 that blows air against the cap 80 from the rear in the conveyance direction T is provided as a pitch filling mechanism that closes the gap between the caps 80 conveyed by the conveyance unit 110. Since a plurality (5 in this embodiment) of the sterilizers 1 are arranged in parallel along the transport direction T of the cap 80, the cap 80 is transported by the transport unit 110 without stopping the cap 80. Plasma and active oxygen can be discharged to the cap 80 in sufficient time and amount by the plurality of sterilization apparatuses 1 arranged in the transport direction T. Thereby, the quantity of the to-be-sterilized thing which can be sterilized per unit time can be increased.
 搬送部110は、2本の棒状部材111からなり、2本の棒状部材111がキャップ80のリング部82を下方から支持可能な幅で離間して、互いに平行に配置されている。つまり、PETボトルのキャップ80は通常、内側にネジ部を有し、ボトルの口部におけるネジ部と螺合させる本体部(第1の幅を有する第1の幅部分に相当)81と、キャップ80を開封する際、ボトル側に残るリング部(第1の幅よりも大きい第2の幅を有する第2の幅部分)82とを有するものであり、このリング部82の径(第2の幅に相当)は本体部81の径(第1の幅に相当)よりも大きく設計されている。このため、2本の棒状部材111の幅を、本体部81の径と略同じ又はそれよりも大きくし、且つ、リング部82の径よりも小さく設定すれば、キャップ80を開口面側(即ち、リング部82側)が上になる状態で、本体部81から2本の棒状部材111の間に通すことで、図5に示すように、リング部(第2の幅部分)82が2本の棒状部材111に支持される状態となる。本実施形態では、図5に示すように、2本の棒状部材111の幅は本体部81の幅と略同じにしてあり、これにより、2本の棒状部材111によりリング部82が下方から支持される状態となる。キャップ80は、殺菌装置1から直接プラズマ及び活性酸素が当てられる部位だけでなく、周囲に散逸するプラズマ及び活性酸素によってそれ以外の部分も殺菌されるところ、このように棒状部材111によってキャップ80を支持する構成であれば、殺菌において搬送部110が干渉する領域を極めて小さくすることができ、キャップ80の全体を効果的に殺菌できる。 The transport unit 110 includes two rod-shaped members 111, and the two rod-shaped members 111 are arranged in parallel with each other with a width that can support the ring portion 82 of the cap 80 from below. That is, the PET bottle cap 80 usually has a threaded portion on the inside, a main body portion (corresponding to a first width portion having a first width) 81 to be screwed with the threaded portion in the mouth portion of the bottle, and the cap. A ring portion (second width portion having a second width larger than the first width) 82 remaining on the bottle side when opening 80, and the diameter of the ring portion 82 (the second width portion). (Corresponding to the width) is designed to be larger than the diameter of the main body 81 (corresponding to the first width). For this reason, if the width of the two rod-shaped members 111 is set to be substantially the same as or larger than the diameter of the main body portion 81 and smaller than the diameter of the ring portion 82, the cap 80 is placed on the opening surface side (that is, In the state where the ring portion 82 side is up, the two ring portions (second width portions) 82 are provided as shown in FIG. 5 by passing between the main body portion 81 and the two rod-shaped members 111. It will be in the state supported by the rod-shaped member 111 of this. In the present embodiment, as shown in FIG. 5, the width of the two rod-shaped members 111 is substantially the same as the width of the main body portion 81, so that the ring portion 82 is supported from below by the two rod-shaped members 111. It will be in a state to be. The cap 80 is sterilized not only by the part to which the plasma and active oxygen are directly applied from the sterilization apparatus 1 but also other parts by the plasma and active oxygen dissipated to the surroundings. If it is the structure which supports, the area | region which the conveyance part 110 interferes in disinfection can be made very small, and the whole cap 80 can be disinfected effectively.
 そして、本実施形態では、図4に示すように、搬送部110は、搬送方向Tの前方に向かうに従って下方に傾斜している。上記したように、キャップ80は搬送部110により保持されることなく、2本の棒状部材111によりリング部82が下方から支持される状態であるため、このように傾斜することによって、キャップ80の自重を利用してキャップ80が搬送方向Tの前方に搬送される。これにより、搬送部110全体を傾斜させるだけの簡易な構成でキャップ80を搬送することができる。 And in this embodiment, as shown in FIG. 4, the conveyance part 110 inclines below as it goes ahead of the conveyance direction T. As shown in FIG. As described above, the cap 80 is not held by the conveyance unit 110 and the ring portion 82 is supported from below by the two rod-shaped members 111. The cap 80 is transported forward in the transport direction T using its own weight. As a result, the cap 80 can be transported with a simple configuration in which the entire transport unit 110 is inclined.
 このように搬送部110が構成されることにより、連続搬送されるキャップ80を複数の殺菌装置1で連続的に殺菌することができるが、発明者は、このように連続搬送される被殺菌物(キャップ80)を複数の殺菌装置1で殺菌する場合、搬送される被殺菌物間の間隔を詰めることで殺菌効果が向上することを見出した。これは、キャップ80間の間隔が一定間隔以上である場合、その間隔に起因して気流の乱れが生じやすく、このため、プラズマ及び活性酸素が散逸しやすくなり、その結果、キャップ80に対してプラズマ及び活性酸素が円滑に当たらなくなるためである。そして、本実施形態では、発明者が見出した好適な手法を採用し、殺菌装置1が設けられている範囲や殺菌装置1に対して搬送方向Tの後側の領域における搬送部110の両外側に複数のエアー吹付装置120が設けられている。このエアー吹付装置120は搬送方向Tの後方からキャップ80に対しエアーを吹き付け可能に構成されており、キャップ80間で間隔(ピッチ)が空いている場合に、キャップ80の後方からエアーを吹き付けることによって、キャップ80を搬送方向Tの前方に推進させてその間隔を詰めるようにしてある。これにより、被殺菌物に対する殺菌効果を向上させることができる。なお、エアー吹付装置120は常時運転させるようにしてもよく、又は、光学センサ等によりキャップ80間に間隔が空いてあることを検出したときに運転させるようにしてもよい。また、エアー吹付装置120は殺菌装置1に対して搬送方向Tの後側の領域にのみ設けるようにしてもよい。 By configuring the transport unit 110 as described above, the continuously transported cap 80 can be continuously sterilized by the plurality of sterilization apparatuses 1, but the inventor can continuously sterilize the object to be sterilized in this way. When the (cap 80) is sterilized with a plurality of sterilization apparatuses 1, it has been found that the sterilization effect is improved by reducing the interval between the articles to be sterilized. This is because when the interval between the caps 80 is equal to or larger than a certain interval, the air flow is likely to be disturbed due to the interval, so that the plasma and the active oxygen are easily dissipated. This is because the plasma and active oxygen are not smoothly applied. And in this embodiment, the suitable method which the inventor discovered is employ | adopted, the both sides of the conveyance part 110 in the area | region in the back direction of the conveyance direction T with respect to the range in which the sterilizer 1 is provided, or the sterilizer 1 A plurality of air spraying devices 120 are provided. The air blowing device 120 is configured to be able to blow air against the cap 80 from the rear in the transport direction T, and blows air from the rear of the cap 80 when there is an interval (pitch) between the caps 80. Thus, the cap 80 is pushed forward in the transport direction T so as to close the gap. Thereby, the bactericidal effect with respect to a to-be-sterilized thing can be improved. The air blowing device 120 may be operated at all times, or may be operated when it is detected that there is a gap between the caps 80 using an optical sensor or the like. In addition, the air blowing device 120 may be provided only in a region on the rear side in the transport direction T with respect to the sterilization device 1.
 なお、図3,4ではキャップ80どうしが密着するまで間隔を詰めた状態を示しているが、必ずしもキャップ80どうしを密着させるまで接近させる必要はない。キャップ80間の間隔を詰める場合、被殺菌物に対する殺菌効果を向上させるためには、気流の乱れが生じにくくなるように相当程度接近していればよい。その間隔は被殺菌物の大きさや形状によって変化するが、例えば本実施形態のキャップ80(径30mm)ではそのキャップ80間の間隔が30mm以内であれば殺菌効果の好適な向上が見込める。 3 and 4 show a state in which the gaps are narrowed until the caps 80 come into close contact with each other, but it is not always necessary to bring the caps 80 into close contact with each other. When the space between the caps 80 is reduced, in order to improve the sterilizing effect on the object to be sterilized, the distance between the caps 80 may be close enough to make it difficult to disturb the airflow. The interval varies depending on the size and shape of the object to be sterilized. For example, in the cap 80 (diameter 30 mm) of the present embodiment, if the interval between the caps 80 is within 30 mm, a favorable improvement in sterilization effect can be expected.
 殺菌システム100は以上のような構成であるため、単位時間あたりに殺菌可能なキャップ80の数量を増やしながらも、キャップ80に対する殺菌効果を向上させることができ、これにより、活性酸素を用いた殺菌を効率的に行うことができる。 Since the sterilization system 100 is configured as described above, it is possible to improve the sterilization effect on the cap 80 while increasing the number of caps 80 that can be sterilized per unit time, thereby sterilizing using active oxygen. Can be performed efficiently.
〔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、搬送部110が、2本の棒状部材111が所定の幅で離間して、互いに平行に配置されたものであり、且つ、搬送方向前方に向かうに従って下方に傾斜しており、キャップ80の自重を利用してキャップ80を搬送する構成を例に説明した。しかし、本発明の実施形態はこれに限定されない。例えば自重ではなくコンベア等の搬送装置を駆動させることによりキャップ80を搬送させてもよい。また、自重により搬送させる場合でも、上記の実施形態の構成に限らず、ローラーやプレート状の部材の上で自重を利用してキャップ80を搬送させてもよい。 (1) In the above-described embodiment, the transport unit 110 is configured such that the two rod-shaped members 111 are separated from each other by a predetermined width and are arranged in parallel to each other, and are inclined downward toward the front in the transport direction. In the above description, the configuration in which the cap 80 is transported using its own weight has been described. However, the embodiment of the present invention is not limited to this. For example, the cap 80 may be conveyed not by its own weight but by driving a conveying device such as a conveyor. Moreover, even when conveying by self-weight, it is not restricted to the structure of said embodiment, You may convey the cap 80 using a self-weight on a roller or a plate-shaped member.
(2)上記の実施形態では、ピッチ詰め機構としてエアー吹付装置120を用いた構成を例に説明した。しかし、本発明の実施形態はこれに限定されない。例えば、基本的にはキャップ80を上記のように自重を利用して搬送しつつ、ピッチ詰め機構として先頭のキャップ80など任意のキャップ80だけ自重による進行速度よりも遅い一定速度で進むようにして、その一定速度で進むキャップ80及びそのキャップ80に追いつきそのキャップ80と同一の速度で進むこととなったキャップ80とこれらに後続するキャップ80との間隔を詰めるようにしてもよい。また、ピッチ詰め機構として殺菌装置1より上流(搬送方向Tの後方側)の任意の箇所でキャップ80を一時せき止めるせき止め部を設けて、せき止められたキャップ80とそれに後続するキャップ80との間の間隔を詰めるようにしてもよい。このように、キャップ80間の間隔を詰めることができるものであれば特に限定されない。 (2) In the above embodiment, the configuration using the air blowing device 120 as the pitch filling mechanism has been described as an example. However, the embodiment of the present invention is not limited to this. For example, basically, the cap 80 is transported using its own weight as described above, and as a pitch filling mechanism, an arbitrary cap 80 such as the top cap 80 moves at a constant speed slower than the traveling speed due to its own weight. The cap 80 that moves at a constant speed, catches up with the cap 80, and the gap between the cap 80 that has moved at the same speed as the cap 80 and the cap 80 that follows the cap 80 may be narrowed. Further, as a pitch filling mechanism, a damming portion for temporarily damming the cap 80 is provided at an arbitrary position upstream (backward in the conveying direction T) from the sterilizing apparatus 1, and the damped cap 80 and the cap 80 following the dammed cap 80 are provided. You may make it close | close a space | interval. Thus, there is no particular limitation as long as the gap between the caps 80 can be reduced.
(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、そのキャップ80が第1の幅を有する第1の幅部分として本体部81と第1の幅よりも大きい第2の幅を有する第2の幅部分としてリング部とを有している構成を例に説明した。しかし、本発明の実施形態はこれに限定されない。例えば、被殺菌物として何を用いるかは適宜変更可能である。また、必ずしも、第1の幅を有する第1の幅部分と第1の幅よりも大きい第2の幅を有する第2の幅部分と、を少なくとも有するものでなくともよい。 (3) In the above embodiment, the cap 80 is used as an object to be sterilized, and the cap 80 has a second width larger than the first width as the first width portion having the first width. The configuration having the ring portion as the second width portion has been described as an example. However, the embodiment of the present invention is not limited to this. For example, what is used as the article to be sterilized can be changed as appropriate. In addition, the first width portion having the first width and the second width portion having the second width larger than the first width are not necessarily required.
(4)上記の実施形態では、ガス供給機30からプラズマ生成部11に対してエアーとともに酸素のみを供給する構成を例に説明した。しかし、本発明の実施形態はこれに限定されない。酸素の他に他の成分を含むものであってもよく、酸素を含むものであれば特に限定されない。 (4) In the above-described embodiment, the configuration in which only oxygen is supplied together with air from the gas supply unit 30 to the plasma generation unit 11 has been described as an example. However, the embodiment of the present invention is not limited to this. It may contain other components in addition to oxygen, and is not particularly limited as long as it contains oxygen.
(5)上記の実施形態では、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例に説明した。しかし、本発明の実施形態はこれに限定されない。例えば、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を吐出するようにするとともに、搬送部110がチャンバー内を通過するようにし、チャンバー内に充満させた殺菌剤70によりチャンバー内を通過するキャップ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。 (5) In the above embodiment, the configuration in which the sterilizer 1 directly discharges the sterilizer 70 containing active oxygen to the cap 80 has been described as an example. However, the embodiment of the present invention is not limited to this. For example, the sterilizing agent 70 is discharged into the chamber through which the cap 80 passes instead of directly discharging the sterilizing agent into the cap 80, and the conveyance unit 110 is allowed to pass through the chamber so that the chamber is filled. The cap 80 may be sterilized indirectly, for example, by sterilizing the cap 80 passing through the chamber with the sterilizing agent 70.
(6)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。 (6) Regarding other configurations, 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システムに利用することができる。 The present invention can be used for a sterilization system for sterilizing an object to be sterilized such as a cap.
1     殺菌装置
11    プラズマ生成部
12    吐出部
13    活性酸素生成部
30    ガス供給機(ガス供給部)
40    エバポレータ(水蒸気供給部)
80    キャップ(被殺菌物)
81    本体部(第1の幅部分)
82    リング部(第2の幅部分)
100   殺菌システム
110   搬送部
111   棒状部材
120   エアー吹付装置(ピッチ詰め機構)
T     搬送方向
DESCRIPTION OF SYMBOLS 1 Sterilizer 11 Plasma production | generation part 12 Discharge part 13 Active oxygen production | generation part 30 Gas supply machine (gas supply part)
40 Evaporator (steam supply part)
80 cap (object to be sterilized)
81 Body (first width part)
82 Ring part (second width part)
100 Sterilization system 110 Conveying section 111 Bar-shaped member 120 Air spraying device (pitch filling mechanism)
T Transport direction

Claims (5)

  1.  プラズマを発生させて、得られたプラズマを利用して被殺菌物を殺菌する殺菌システムであって、
     酸素を含む混合ガスを供給するガス供給部と、
     水蒸気を供給する水蒸気供給部と、
     前記ガス供給部から供給される前記混合ガスからオゾンを含むプラズマを生成するプラズマ生成部と、
     前記プラズマと前記水蒸気供給部から供給される前記水蒸気とを反応させて活性酸素を生成する活性酸素生成部と、
     前記プラズマと前記活性酸素とを殺菌剤として吐出する吐出部と、を備える殺菌装置と、
     前記被殺菌物を搬送する搬送部と、を備え、
     前記殺菌装置により殺菌される前記被殺菌物間の間隔を詰めるピッチ詰め機構が設けられている殺菌システム。
    A sterilization system that generates plasma and sterilizes an object to be sterilized using the obtained plasma,
    A gas supply unit for supplying a mixed gas containing oxygen;
    A water vapor supply unit for supplying water vapor;
    A plasma generation unit for generating plasma containing ozone from the mixed gas supplied from the gas supply unit;
    An active oxygen generator that generates active oxygen by reacting the plasma with the water vapor supplied from the water vapor supply unit;
    A sterilizer comprising: a discharge unit that discharges the plasma and the active oxygen as a sterilant;
    A transport unit for transporting the article to be sterilized,
    The sterilization system provided with the pitch filling mechanism which packs the space | interval between the said to-be-sterilized objects sterilized by the said sterilizer.
  2.  前記殺菌装置が前記被殺菌物の搬送方向に沿って複数並設されている請求項1に記載の殺菌システム。 The sterilization system according to claim 1, wherein a plurality of the sterilization apparatuses are arranged in parallel along a conveyance direction of the article to be sterilized.
  3.  前記ピッチ詰め機構として前記搬送方向の後方から前記被殺菌物に対しエアーを吹き付けるエアー吹付装置を備える請求項1又は2に記載の殺菌システム。 The sterilization system according to claim 1 or 2, further comprising an air spray device that blows air against the object to be sterilized from behind in the transport direction as the pitch filling mechanism.
  4.  前記搬送部は前記搬送方向前方に向かうに従って下方に傾斜しており、前記被殺菌物の自重を利用して前記被殺菌物を搬送する請求項1~3のいずれか一項に記載の殺菌システム。 The sterilization system according to any one of claims 1 to 3, wherein the transport unit is inclined downward toward the front in the transport direction, and transports the sterilized material using its own weight. .
  5.  前記被殺菌物は、第1の幅を有する第1の幅部分と前記第1の幅よりも大きい第2の幅を有する第2の幅部分と、を少なくとも有し、
     前記搬送部は、2本の棒状部材が、前記第1の幅と略同じ又はそれよりも大きく且つ前記第2の幅よりも小さい幅で離間して、互いに平行に配置されたものである請求項4に記載の殺菌システム。
    The article to be sterilized has at least a first width portion having a first width and a second width portion having a second width larger than the first width,
    In the transport unit, two rod-shaped members are arranged in parallel to each other, spaced apart by a width substantially equal to or larger than the first width and smaller than the second width. Item 5. The sterilization system according to Item 4.
PCT/JP2016/086568 2015-12-25 2016-12-08 Sterilization system WO2017110501A1 (en)

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