JP2569201B2 - Spray sterilizer with gas replacement mechanism and sterilization method - Google Patents
Spray sterilizer with gas replacement mechanism and sterilization methodInfo
- Publication number
- JP2569201B2 JP2569201B2 JP2103714A JP10371490A JP2569201B2 JP 2569201 B2 JP2569201 B2 JP 2569201B2 JP 2103714 A JP2103714 A JP 2103714A JP 10371490 A JP10371490 A JP 10371490A JP 2569201 B2 JP2569201 B2 JP 2569201B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- processing
- processing tank
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007921 spray Substances 0.000 title claims description 18
- 230000001954 sterilising effect Effects 0.000 title claims description 15
- 238000004659 sterilization and disinfection Methods 0.000 title claims description 12
- 238000000034 method Methods 0.000 title claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 123
- 239000007789 gas Substances 0.000 claims description 36
- 239000011261 inert gas Substances 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000011084 recovery Methods 0.000 claims description 10
- 230000005587 bubbling Effects 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 8
- 239000000498 cooling water Substances 0.000 claims description 3
- 239000008236 heating water Substances 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 239000012071 phase Substances 0.000 description 4
- 235000013305 food Nutrition 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明はバブリングを行なう貯水槽を併設したガス置
換機構付スプレー式殺菌装置及びこの装置を用いたガス
置換スプレー式殺菌処理方法に関するものである。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a spray disinfection device equipped with a gas replacement mechanism provided with a water tank for performing bubbling, and a gas replacement spray disinfection method using the device.
従来の技術 従来、不活性ガスを用いた処理方法としては、特開昭
57−206447号公報及び特開昭59−78674号公報が知られ
ている。これら刊行物に示される技術の主目的は、処理
物の酸化を防止して、高品質の製品を得ることにある。2. Description of the Related Art Conventionally, as a processing method using an inert gas,
JP-A-57-206447 and JP-A-59-78674 are known. The main purpose of the technology described in these publications is to obtain a high quality product by preventing the oxidation of the processed product.
発明が解決しようとする課題 しかし、上記のようない従来例では、例えば30分〜90
分程度の1バッチ処理で使用される不活性ガスは、毎回
そのまま全部消費され、多大の経費を発生すること及び
それらの貯蔵設備が大となること、排気時の騒音や多量
の不活性ガスの排気による作業環境の安全面にも好まし
くない等の問題点があった。Problems to be Solved by the Invention However, in the conventional examples not described above, for example, 30 minutes to 90 minutes
The inert gas used in one batch process of about one minute is consumed as it is every time, which causes a great expense and a large storage facility, noise at the time of exhaustion and a large amount of the inert gas. There have been problems such as the unfavorable safety of the working environment due to the exhaust.
又、運転中に処理槽内の圧力調整を不活性ガスで行な
うため、この点の排気コスト及び作業環境面の問題点も
あった。In addition, since the pressure in the processing tank is adjusted with an inert gas during operation, there are also problems in terms of exhaust cost and work environment in this respect.
本発明の目的はバブリングにより気相及び液相内の脱
気を図り、高温時に通気性が大きくなるようなプラスチ
ック容器に収納された食品や薬品の酸化が防止できると
共に圧力調整を行なわず自然昇圧及び自然降圧下で処理
することができ、処理終了後、不活性ガスの回収及び脱
気置換された水の回収を可能としたガス置換機構付スプ
レー式殺菌装置及び殺菌処理方法を提供しようとするも
のである。The object of the present invention is to degas the gas phase and the liquid phase by bubbling, thereby preventing the oxidation of foods and chemicals contained in plastic containers that increase air permeability at high temperatures, and increasing the pressure naturally without adjusting the pressure. The present invention aims to provide a spray-type sterilizing apparatus with a gas replacement mechanism and a sterilizing method capable of recovering an inert gas and recovering degassed and replaced water after the processing is completed. Things.
課題を解決するための手段 本発明は上記目的を達成するため、第1発明として、
スプレー管を内蔵し、上端にバルブを介して給排気口を
有する処理槽と、バブリング管を内蔵した貯水槽と、前
記処理槽の上端と前記貯水槽の上端とをバルブを介して
連通したガス供給管と、前記処理槽の下部と前記貯水槽
の下部とをバルブ及びポンプを介して連通した給水管
と、前記処理槽の下部と間接加熱型の熱交換器とをバル
ブ及びポンプを介して連結し、前記熱交換器よりバルブ
を介して処理槽内のスプレー管と連結した処理液循環路
と、から成るガス置換機構付スプレー式殺菌装置とし
た。Means for Solving the Problems In order to achieve the above object, the present invention provides, as a first invention,
A processing tank having a built-in spray pipe and having a supply / exhaust port through a valve at the upper end, a water storage tank having a built-in bubbling pipe, and a gas communicating the upper end of the processing tank with the upper end of the water storage tank through a valve. A supply pipe, a water supply pipe communicating a lower part of the processing tank and a lower part of the water storage tank via a valve and a pump, and a lower part of the processing tank and an indirect heating type heat exchanger through a valve and a pump. And a treatment liquid circulation path connected to a spray pipe in the treatment tank from the heat exchanger via a valve.
また、第1発明の装置を用いて殺菌処理する第2発明
として、処理槽へ被処理物を装填し、密閉する装填工程
と、処理槽下端よりあらかじめ準備した貯水槽の水を満
水にして給排気口より排気する給水工程と、処理槽の上
端と貯水槽の上端とをガス供給管で連通し、貯水槽に準
備された不活性ガスを処理槽へ送り込むと共に処理槽の
水を貯水槽へ戻すガス置換工程と、貯水槽の水の一部を
処理槽へ戻し、処理槽を密閉すると共に一切の圧力調整
を行なわず自然昇圧及び自然降圧条件下でポンプ及び熱
交換器を介して処理槽内のスプレー管への加熱水又は冷
却水を一定時間強制循環させる間に殺菌から冷却までを
行なう処理工程と、前記ガス供給管を連通させて、貯水
槽の水を処理槽内へ送り込み、処理槽から貯水槽へ不活
性ガスを回収するガス回収工程と、前記給水管を開いて
処理槽内の水を貯水管へ戻す水回収工程と、処理槽から
被処理物を出す取出工程と、から成るガス置換スプレー
式殺菌処理方法とした。Further, as a second invention for sterilizing treatment using the apparatus of the first invention, a treatment tank is loaded with an object to be treated and hermetically sealed, and a water supply tank prepared from the lower end of the treatment tank is filled with water and supplied. The water supply step of exhausting from the exhaust port, the upper end of the treatment tank and the upper end of the water tank are connected by a gas supply pipe, and the inert gas prepared in the water tank is sent to the treatment tank and the water in the treatment tank is sent to the water tank. Return gas replacement process, return part of the water in the water storage tank to the processing tank, seal the processing tank, and do not perform any pressure adjustments. A process of performing sterilization to cooling while forcibly circulating heating water or cooling water to the spray pipe for a certain period of time, and communicating the gas supply pipe to send water in a water storage tank into the processing tank to perform processing. Gas to recover inert gas from tank to water tank A recovery step, the water recovery step of returning the water in the open water supply pipe processing bath into the water storage pipe, and the retrieval step of issuing an object to be processed from the processing tank, and the gas replacement spray sterilization process comprising.
作 用 第1発明では、貯水槽にバブリング管を有するので、
満水に給水後、密閉して不活性ガスを供給することによ
り、気相及び液相内の脱気が行なわれる。この不活性ガ
スと脱気された水を用いて、処理槽と配水管とを上端及
び下端で連結するガス供給管と給水管により、処理槽内
を脱気して給水し、上端から不活性ガスを供給すること
ができるようになっている。また間接加熱型の熱交換器
を設けて、処理槽の下端と処理槽内のスプレー管とを連
結した処理液循環路を設けているので、前記脱気された
水が処理槽とポンプと熱交換器、そしてスプレー管との
間で循環することができ、その間に熱交換器による加熱
及び冷却による処理が可能となっている。加熱殺菌処理
終了後では、処理槽と貯水槽との間の給水管とガス供給
管とにより貯水槽の水を処理槽へ送って、不活性ガスを
貯水槽へ回収し、その後前記給排気口を開いて処理槽上
端から空気を入れると共に給水管によって水を貯水槽へ
回収することができるようになった。Operation In the first invention, since the water storage tank has the bubbling pipe,
After supplying water to the full water, the interior of the gas phase and the liquid phase is deaerated by supplying an inert gas in a sealed state. Using this inert gas and degassed water, the inside of the treatment tank is degassed and supplied with water by a gas supply pipe and a water supply pipe connecting the treatment tank and the water distribution pipe at the upper and lower ends, and inert from the upper end. Gas can be supplied. Further, since a heat exchanger of an indirect heating type is provided and a processing liquid circulation path connecting the lower end of the processing tank and the spray pipe in the processing tank is provided, the degassed water is heated by the processing tank, the pump and the heat. It can circulate between the exchanger and the spray tube, during which processing by heating and cooling by the heat exchanger is possible. After the heat sterilization treatment, the water in the water storage tank is sent to the processing tank by a water supply pipe and a gas supply pipe between the processing tank and the water storage tank, and the inert gas is collected in the water storage tank. Was opened, air was introduced from the upper end of the treatment tank, and water could be collected into the water storage tank by a water supply pipe.
上記装置を用いる第2発明では、処理槽へ被処理物を
装填し、貯水槽内であらかじめ準備された不活性ガスと
脱気された水とを利用して、加熱殺菌及び冷却までの一
環した処理が行なわれる。すなわち、処理槽と貯水槽の
下端で連結されている給水管により貯水槽の水を処理槽
へ送り込み、給排気口から排気することにより給水工程
が行なわれ、ガス供給管によって前記不活性ガスを処理
槽へ送り、給水管より処理槽の水を貯水槽は戻すガス置
換工程ができる。さらに貯水槽の水を一部処理槽へ戻
し、この水をポンプと熱交換器とスプレー管を介して循
環させることにより、間接的な熱交換による加熱から冷
却に至る処理工程が行なわれる。この処理工程中は処理
槽は密閉され、一切の圧力調節を行なわず加熱・冷却に
よる自然昇圧と自然降圧となっている。処理終了後は貯
水槽の水を処理槽へ送り込み、ガス供給管を介して処理
槽内の不活性ガスを貯水槽へ回収するガス回収工程が行
なわれる。又、この工程の後給排気口を開いて処理槽内
の水を貯水槽へ戻して水回収工程が行なわれ、被処理物
を取出すことができるようになる。In the second invention using the above-mentioned apparatus, an object to be treated is loaded into a treatment tank, and an inert gas and degassed water prepared in advance in a water tank are used to perform heat sterilization and cooling. Processing is performed. That is, a water supply step is performed by sending water in the water storage tank to the processing tank by a water supply pipe connected at a lower end of the processing tank and the water storage tank, and exhausting the water from a water supply / exhaust port. A gas replacement step can be performed in which the water is sent to the treatment tank and the water in the treatment tank is returned from the water supply pipe to the water storage tank. Further, a part of the water in the water storage tank is returned to the processing tank, and the water is circulated through the pump, the heat exchanger, and the spray pipe, whereby a processing step from heating to cooling by indirect heat exchange is performed. During this processing step, the processing tank is closed, and the pressure is not adjusted at all, and the pressure is naturally increased and decreased by heating and cooling. After the treatment is completed, a gas recovery step is performed in which water in the water storage tank is sent to the processing tank, and an inert gas in the processing tank is recovered to the water storage tank via a gas supply pipe. After this step, the supply / exhaust port is opened to return the water in the treatment tank to the water storage tank, and the water recovery step is performed, so that the object to be treated can be taken out.
実施例 以下、実施例としての殺菌装置及び殺菌処理方法を図
面に従って説明する。Example Hereinafter, a sterilizing apparatus and a sterilizing method as an example will be described with reference to the drawings.
第1図において、1は処理槽で、上端にバルブ(V1)
を介して給排気口2を有し、内部にはスプレー管3を内
蔵している。4は貯水槽で、内部にバブリング管5を有
する。6はガス供給及び回収管で、処理槽1の上端と貯
水槽5の上端とをバルブ(V2)を介して連通している。
7は給水及び回収管で、処理槽1の下部と貯水槽4の下
部とをバルブ(V3)及びポンプ8を介して連通してい
る。9は間接加熱型の熱交換器、10は処理液循環路で、
処理槽1の下部からバルブ(V4)及びポンプ11を介して
熱交換器9を通り、バルブ(V5)を介して処理槽1内の
スプレー管3に接続され、ポンプ11によって処理液を強
制循環されるようになっている。間接加熱型の熱交換器
9には水又は蒸気を伝熱板を介して熱交換できるよう供
給される。In FIG. 1, 1 is a processing tank, and a valve (V 1 ) is provided at the upper end.
And a supply / exhaust port 2 through which a spray pipe 3 is incorporated. Reference numeral 4 denotes a water storage tank having a bubbling pipe 5 therein. Reference numeral 6 denotes a gas supply and recovery pipe, which connects the upper end of the treatment tank 1 and the upper end of the water storage tank 5 via a valve (V 2 ).
Reference numeral 7 denotes a water supply and recovery pipe, which connects the lower part of the treatment tank 1 and the lower part of the water storage tank 4 via a valve (V 3 ) and a pump 8. 9 is an indirect heating type heat exchanger, 10 is a processing liquid circulation path,
The lower part of the processing tank 1 passes through the heat exchanger 9 via a valve (V 4 ) and a pump 11 and is connected to the spray pipe 3 in the processing tank 1 via a valve (V 5 ). It is forcibly circulated. Water or steam is supplied to the indirect heating type heat exchanger 9 through a heat transfer plate so that heat can be exchanged.
(V6)〜(V9)はそれぞれバルブを示す。 (V 6) ~ (V 9 ) respectively show a valve.
上記の構成において、先ず貯水槽4で処理槽1で用い
られる処理液が準備される。バルブ(V6)を開いて排気
をしつつ貯水槽4内に満水になるまで給水される。次い
で(V6)を閉じて下部より水抜きをして所定液面まで下
げて上面を真空とさせる。バブリング管5より、例えば
N2ガスによりバブリング(bubbling)を始め、水中及び
上面気相のガス置換を行ない一定時間後(V6)を開いて
排気し、排気完了後再度これを繰返して水中及び上面気
相のガス置換を完成させる。In the above configuration, first, a processing liquid used in the processing tank 1 is prepared in the water storage tank 4. Water is supplied to the water storage tank 4 until the water tank 4 is full while opening the valve (V 6 ) to exhaust air. Next, (V 6 ) is closed, water is drained from the lower part, the level is lowered to a predetermined level, and the upper surface is evacuated. From the bubbling tube 5, for example,
Bubbling with N 2 gas is started, gas replacement of water and upper gas phase is performed, and after a certain time (V 6 ), the gas is opened and evacuated. To complete.
以後この脱気ガス置換した水を利用して殺菌処理を行
なう。Thereafter, sterilization treatment is performed using the degassed gas-replaced water.
(イ)処理槽1への被処理物を装填し密閉する装填工
程、 (ロ)処理槽1下端より、給水管7を介して処理槽1へ
あらかじめ貯水槽4に準備された水を供給し(V1)を開
いて排気し満水になれば(V1)を閉じる給水工程(第2
図参照)、 (ハ)処理槽1上端と貯水槽4の上端を連通するガス供
給管6により、(V2)を開とし貯水槽4上部空間に準備
された不活性ガスを処理槽1へ送り込むと共に処理槽1
の水を貯水槽4へ戻すガス置換工程(第3図参照)、 (ニ)貯水槽4の水の一部を処理槽へ戻し、処理槽を密
閉すると共に処理液循環路をポンプ11によって強制循環
させる処理工程、この先熱交換器の熱水又は冷却水によ
って間接的に加熱・冷却され、スプレー管3よりのスプ
レーによって被処理物の処理が行なわれる。この間、処
理槽内圧は自然昇圧及び自然降圧となり一切の圧力調整
は行なわれない(第4図参照)。(A) A loading step of loading and sealing an object to be treated into the processing tank 1, and (b) supplying water previously prepared in the water storage tank 4 from the lower end of the processing tank 1 to the processing tank 1 via the water supply pipe 7. (V 1) Close if the exhaust and filled with water by opening the (V 1) water supply step (the second
(Refer to the figure), (c) The gas supply pipe 6 communicating the upper end of the processing tank 1 and the upper end of the water storage tank 4 opens (V 2 ) and sends the inert gas prepared in the upper space of the water storage tank 4 to the processing tank 1. Processing tank 1
(D) A part of the water in the water storage tank 4 is returned to the processing tank, the processing tank is sealed, and the processing liquid circulation path is forced by the pump 11. In the circulating process, the workpiece is heated and cooled indirectly by hot water or cooling water from the preheat exchanger, and the workpiece is processed by spraying from the spray pipe 3. During this time, the internal pressure of the processing tank becomes a natural pressure increase and a natural pressure decrease, and no pressure adjustment is performed (see FIG. 4).
(ホ)処理終了後、ガス供給管6を連通させて、貯水槽
4の水を処理槽1内へ送り込み、処理槽から貯水槽へ不
活性ガスを回収するガス回収工程(第5図参照)。(E) After the treatment, the gas supply pipe 6 is communicated, the water in the water storage tank 4 is sent into the processing tank 1, and the inert gas is recovered from the processing tank to the water storage tank (see FIG. 5). .
(ヘ)さらに、給排気口2を開き、給水管7を介して、
処理槽1内の水を貯水槽4へ戻す水回収工程(第6図参
照)、 (ト)処理の終了として処理槽から被処理物を出す取出
工程、 によって全工程を終了する。(F) Further, the air supply / exhaust port 2 is opened, and through the water supply pipe 7,
All steps are completed by a water collecting step of returning the water in the processing tank 1 to the water storage tank 4 (see FIG. 6), and (g) a step of taking out an object to be processed from the processing tank as the end of the processing.
発明の効果 本発明装置では貯水槽によって脱気ガス置換された水
と不活性ガスを準備することができ、処理槽と貯水槽と
の間を連通するガス供給管と給水管とによって、処理槽
内の脱気と水の供給が行なわれ、処理液循環路を介して
間接加熱された水による被処理物の加熱・殺菌が行なわ
れ冷却に至る処理全体が、脱気ガス置換された水と不活
性ガス存在下での処理が可能となり、且つ不活性ガスの
回収と脱気ガス置換された水の回収が可能となり、次回
処理に再利用することができるようになったので、毎回
不活性ガスを消費することがなくなった。Effect of the Invention In the apparatus of the present invention, the water and the inert gas, which have been degassed and replaced by the water storage tank, can be prepared, and the processing tank is provided by the gas supply pipe and the water supply pipe communicating between the processing tank and the water storage tank. The deaeration and supply of water are performed, and the whole process up to the cooling and heating of the object to be processed by the water indirectly heated through the processing liquid circulation path is performed with degassed gas-replaced water. Processing in the presence of inert gas is possible, and the collection of inert gas and the water that has been replaced with degassed gas becomes possible, making it possible to reuse it for the next processing. Gas is no longer consumed.
従って、プラスチック容器に包装された食品や薬品で
酸化を嫌うものに対しても安心して安定した加熱殺菌処
理ができるようになった。Accordingly, stable heat sterilization treatment can be performed with respect to foods and medicines that are not oxidized in plastic containers.
又、処理中は処理槽は密閉とし、外部から加圧・減圧
(排気)を一切行なわない自然昇圧及び自然降圧システ
ムとしたので運転中に加圧・排気される不活性ガスの消
耗も一切不要となった。In addition, the processing tank is sealed during processing, and a natural pressure increase and decrease system that does not pressurize or depressurize (exhaust) from outside is used, so there is no need to consume any inert gas that is pressurized and exhausted during operation. It became.
又、本発明方法においては、貯水槽における気相及び
液相内の脱気を確実に行なうと共に、この水と不活性ガ
スを利用して処理槽と貯水槽間の水及び不活性ガスの交
換によって、酸化を防止した加熱殺菌処理が実現できる
ようになった。熱交換器として間接加熱型を用いること
によって、加熱及び冷却が自由にでき、脱気された処理
液に悪影響を与えることがなく、プラスチック容器に内
装した食品や薬品の処理が安定して実行できる効果があ
る。Further, in the method of the present invention, the degassing in the gas phase and the liquid phase in the water storage tank is reliably performed, and the water and the inert gas are exchanged between the processing tank and the water storage tank by using the water and the inert gas. As a result, the heat sterilization treatment preventing oxidation can be realized. By using an indirect heating type as a heat exchanger, heating and cooling can be performed freely, without adversely affecting the degassed processing liquid, and the processing of foods and chemicals contained in plastic containers can be performed stably. effective.
第1図は本発明装置の説明図、第2図〜第6図は各工程
を示す説明図である。 1……処理槽、2……給排気口、3……スプレー管、4
……貯水槽、5……バブリング管、6……ガス供給及び
回収管、7……給水及び回収管、8、11……ポンプ、9
……熱交換器、10……処理液循環路FIG. 1 is an explanatory view of the apparatus of the present invention, and FIGS. 2 to 6 are explanatory views showing respective steps. 1 ... processing tank, 2 ... supply / exhaust port, 3 ... spray pipe, 4
... water storage tank, 5 ... bubbling pipe, 6 ... gas supply and recovery pipe, 7 ... water supply and recovery pipe, 8, 11 ... pump, 9
…… Heat exchanger, 10 …… Treatment liquid circulation path
Claims (2)
て給排気口を有する処理槽と、バブリング管を内蔵した
貯水槽と、前記処理槽の上端と前記貯水槽の上端とをバ
ルブを介して連通したガス供給管と、前記処理槽の下部
と前記貯水槽の下部とをバルブ及びポンプを介して連通
した給水管と、前記処理槽の下部と間接加熱型の熱交換
器とをバルブ及びポンプを介して連結し、前記熱交換器
よりバルブを介して処理槽内のスプレー管と連結した処
理液循環炉と、から成るガス置換機構付スプレー式殺菌
装置。1. A processing tank having a spray pipe built therein and having a supply / exhaust port at its upper end via a valve, a water storage tank having a bubbling pipe built therein, and a valve connected to the upper end of the processing tank and the upper end of the water storage tank. A gas supply pipe that communicates with a gas supply pipe, a water supply pipe that communicates a lower part of the treatment tank with the lower part of the water storage tank via a valve and a pump, and a valve that connects the lower part of the treatment tank and an indirect heating type heat exchanger. And a processing liquid circulation furnace connected to the spray pipe in the processing tank from the heat exchanger via a valve and a pump from the heat exchanger.
工程と、処理槽下端よりあらかじめ準備した貯水層の水
を満水にして給排気口より排気する給水工程と、処理槽
の上端と貯水槽の上端とをガス供給管で連通し、貯水層
に準備された不活性ガスを処理槽へ送り込むと共に処理
槽の水を貯水槽へ戻すガス置換工程と、貯水槽の水の一
部を処理槽へ戻し、処理槽を密閉すると共に一切の圧力
調整を行なわず自然昇圧及び自然降圧条件下でポンプ及
び熱交換器を介して処理槽内のスプレー管へ加熱水又は
冷却水を一定時間強制循環させる間に殺菌から冷却まで
を行なう処理工程と、前記ガス供給管を連通させて、貯
水槽の水を処理槽内へ送り込み、処理槽から貯水槽へ不
活性ガスを回収するガス回収工程と、前記給水管を開い
て処理槽内の水を貯水管へ戻す水回収工程と、処理槽か
ら被処理物を出す取出工程と、から成るガス置換スプレ
ー式殺菌処理方法。2. A loading step for loading an object to be treated into a processing tank and sealing it, a water supply step of filling the water in a storage layer prepared in advance from a lower end of the processing tank and exhausting the water from a supply / exhaust port, and an upper end of the processing tank. A gas supply pipe connects the upper end of the water tank with the gas supply pipe, sends the inert gas prepared in the water tank to the processing tank and returns the water in the processing tank to the water tank, and a part of the water in the water tank. Is returned to the treatment tank, the treatment tank is sealed, and without any pressure adjustment, heating water or cooling water is supplied to the spray pipe in the treatment tank through the pump and heat exchanger for a certain period of time under the conditions of natural pressure increase and decrease. A processing step of performing sterilization to cooling during forced circulation, and a gas recovery step of communicating the gas supply pipe to feed water from a water storage tank into the processing tank, and recovering an inert gas from the processing tank to the water storage tank. Open the water supply pipe and drain the water in the treatment tank A water recovery step of returning to the water tube, take-out step and the gas replacement spray sterilization treatment method consisting of issuing an object to be processed from the processing tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2103714A JP2569201B2 (en) | 1990-04-19 | 1990-04-19 | Spray sterilizer with gas replacement mechanism and sterilization method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2103714A JP2569201B2 (en) | 1990-04-19 | 1990-04-19 | Spray sterilizer with gas replacement mechanism and sterilization method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH042349A JPH042349A (en) | 1992-01-07 |
| JP2569201B2 true JP2569201B2 (en) | 1997-01-08 |
Family
ID=14361381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2103714A Expired - Fee Related JP2569201B2 (en) | 1990-04-19 | 1990-04-19 | Spray sterilizer with gas replacement mechanism and sterilization method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2569201B2 (en) |
-
1990
- 1990-04-19 JP JP2103714A patent/JP2569201B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH042349A (en) | 1992-01-07 |
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