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JP6036274B2 - Sterilizer - Google Patents

Sterilizer Download PDF

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JP6036274B2
JP6036274B2 JP2012280465A JP2012280465A JP6036274B2 JP 6036274 B2 JP6036274 B2 JP 6036274B2 JP 2012280465 A JP2012280465 A JP 2012280465A JP 2012280465 A JP2012280465 A JP 2012280465A JP 6036274 B2 JP6036274 B2 JP 6036274B2
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water
treatment tank
water supply
flow rate
cooling
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JP2014124094A (en
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健司 金澤
健司 金澤
暁 若狭
暁 若狭
泰三 松川
泰三 松川
松藤 幸樹
幸樹 松藤
康 田中
康 田中
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Miura Co Ltd
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Description

本発明は、レトルト食品などの加熱殺菌とその後の冷却に用いられる殺菌装置に関するものである。   The present invention relates to a sterilizer used for heat sterilization and subsequent cooling of retort foods and the like.

処理槽内に被処理物を収容して、蒸気や熱水により加熱殺菌後、冷却水により冷却する殺菌装置が知られている。この種の殺菌装置では、殺菌工程後の冷却工程の開始時に、蒸気が充満した処理槽内に冷却水が供給されることになる。   A sterilization apparatus is known in which an object to be processed is accommodated in a treatment tank, sterilized by heating with steam or hot water, and then cooled with cooling water. In this type of sterilizer, cooling water is supplied into the treatment tank filled with steam at the start of the cooling process after the sterilization process.

ところが、蒸気が充満した処理槽内に冷却水を供給すると、処理槽内の蒸気が凝縮して、処理槽内の圧力が急激に低下する。蒸気凝縮による圧力低下分を補うように処理槽内に加圧空気を導入するにしても、加圧空気の導入が追い付かず、処理槽内の圧力が急激に低下するおそれがある。その場合、被処理物の破損(たとえばレトルトパウチの破袋)を起こすおそれもある。   However, when cooling water is supplied into the treatment tank filled with steam, the steam in the treatment tank is condensed, and the pressure in the treatment tank is rapidly reduced. Even if the pressurized air is introduced into the treatment tank so as to compensate for the pressure drop due to vapor condensation, the introduction of the pressurized air may not catch up, and the pressure in the treatment tank may drop rapidly. In that case, there is a possibility of causing damage to the object to be processed (for example, bag breakage of the retort pouch).

そこで、下記特許文献1に開示されるように、処理槽内を空気で加圧することなく100%蒸気により被処理物を加熱殺菌する殺菌装置において、処理槽内下部に予め冷却水を貯留しておき、殺菌工程中、蒸気により被処理物を加熱すると共に、前記貯留した冷却水も殺菌温度まで加熱しておくことが提案されている。この場合、冷却工程では、その加熱された冷却水を被処理物に散水すると共に、処理槽内に冷却水を徐々に導入して、冷却水の温度を徐々に下げることで、被処理物の冷却が図られる。   Therefore, as disclosed in Patent Document 1 below, in a sterilizer that heats and sterilizes an object to be processed with 100% steam without pressurizing the inside of the processing tank with air, cooling water is stored in advance in the lower part of the processing tank. In addition, during the sterilization process, it is proposed that the object to be treated is heated by steam and the stored cooling water is also heated to the sterilization temperature. In this case, in the cooling step, the heated cooling water is sprinkled into the object to be treated, and the cooling water is gradually introduced into the treatment tank, and the temperature of the cooling water is gradually lowered, thereby Cooling is achieved.

また、下記特許文献2に開示されるように、蒸気により被処理物を加熱殺菌後、処理槽内に冷却水を導入してそれを加熱することで熱水を作り(温水準備工程)、その熱水を被処理物に噴射する冷却工程では、1秒以下の短時間噴射とそれより長い噴射休止とを繰り返しながら被処理物の冷却を図ることが提案されている。この場合、冷却水の短時間噴射と噴射休止とを繰り返す間、処理槽内へは冷却水は供給されない(特許文献2の図2)。その後、被処理物の冷却が進むと、処理槽内に冷却水を供給することで冷却水の温度を低下させ、被処理物のさらなる冷却が図られる。   In addition, as disclosed in Patent Document 2 below, after sterilizing the object to be treated with steam, hot water is made by introducing cooling water into the treatment tank and heating it (hot water preparation step), In the cooling step of injecting hot water onto the object to be processed, it has been proposed to cool the object to be processed while repeating a short time injection of 1 second or less and an injection pause longer than that. In this case, the cooling water is not supplied into the treatment tank while the short-time injection of the cooling water and the injection pause are repeated (FIG. 2 of Patent Document 2). Then, when cooling of a to-be-processed object progresses, the temperature of cooling water is reduced by supplying cooling water in a processing tank, and further cooling of a to-be-processed object is achieved.

特公平7−95935号公報(請求項1、第2頁右欄第38行−第3頁左欄第1行、第1図)Japanese Patent Publication No. 7-95935 (Claim 1, page 2, right column, line 38-page 3, left column, line 1, FIG. 1) 特開2010−94051号公報(請求項1、段落0009−0013、図1−図3)Japanese Patent Laying-Open No. 2010-94051 (Claim 1, paragraphs 0009-0013, FIGS. 1 to 3)

しかしながら、特許文献1に記載の発明の場合、100%蒸気で殺菌するのに処理槽内には予め冷却水を貯留しておく必要があり、またその貯留水は循環されないので温度ムラを生じやすく、その後の冷却工程において好ましくない。   However, in the case of the invention described in Patent Document 1, it is necessary to store cooling water in the treatment tank in advance in order to sterilize with 100% steam, and since the stored water is not circulated, temperature unevenness is likely to occur. In the subsequent cooling step, it is not preferable.

また、特許文献1に記載の発明の場合、100%蒸気により殺菌が行われた後、冷却工程における処理槽内への給水流量は一定である。そのため、冷却工程の開始直後において、処理槽内の蒸気の凝縮が大きく、処理槽内の圧力が急激に低下するおそれがある。あるいは、これを防止しようとして、給水流量を少なくすれば、その後の冷却工程に時間を要することになる。   In the case of the invention described in Patent Document 1, after sterilization is performed with 100% steam, the feed water flow rate into the treatment tank in the cooling process is constant. For this reason, immediately after the start of the cooling step, the condensation of the vapor in the treatment tank is large, and the pressure in the treatment tank may rapidly decrease. Alternatively, if the feed water flow rate is decreased in order to prevent this, the subsequent cooling process will take time.

一方、特許文献2に記載の発明の場合、冷却水の短時間噴射と噴射休止とを繰り返す間は、処理槽内へは新たに冷却水が供給されないので不都合はないが、その後に処理槽内へ冷却水を給水し始めると、その給水流量が一定であるため、やはり前記特許文献1に記載の発明と同様の不都合を生じる。また、そもそも、特許文献2に記載の発明の場合、処理槽内に水を貯留せずに蒸気で殺菌後、温水準備工程において処理槽内に冷却水がいきなり供給され、しかもその給水流量が一定であるため、処理槽内の蒸気凝縮による圧力急減が避けられない。   On the other hand, in the case of the invention described in Patent Document 2, there is no inconvenience since the cooling water is not newly supplied into the processing tank while repeating the short-time injection and the suspension of the cooling water. When the cooling water is started to be supplied to the water, the water supply flow rate is constant, so that the same inconvenience as the invention described in Patent Document 1 occurs. In the first place, in the case of the invention described in Patent Document 2, after sterilizing with steam without storing water in the treatment tank, the cooling water is suddenly supplied into the treatment tank in the warm water preparation step, and the water supply flow rate is constant. Therefore, a rapid decrease in pressure due to vapor condensation in the treatment tank is inevitable.

なお、特許文献2には、殺菌工程を熱水で行うことができる旨の記載はあるが、熱水で殺菌を行った場合にまで、温水準備工程や冷却工程(冷却水の短時間噴射と噴射休止との繰り返し)を同様に行うものではない。そもそも殺菌工程において処理槽内に熱水があるとすれば、その後の温水準備工程などをどのように行うか不明となるからである。   In addition, in Patent Document 2, there is a description that the sterilization process can be performed with hot water, but until the sterilization with hot water, the warm water preparation process and the cooling process (short-time injection of cooling water and (Repetition with injection stop) is not performed in the same manner. In the first place, if there is hot water in the treatment tank in the sterilization process, it is unclear how to perform the subsequent warm water preparation process.

さらに、いずれの特許文献に記載の発明でも、殺菌工程後の冷却工程において、処理槽内に冷却水を供給して冷却水の温度を徐々に下げるが、処理槽内に冷却水を供給するばかりでは、やがて被処理物が冷却水に水没して流れるおそれがある。   Furthermore, in any invention described in any of the patent documents, in the cooling step after the sterilization step, the cooling water is supplied into the treatment tank to gradually lower the temperature of the cooling water, but only the cooling water is supplied into the treatment tank. Then, there is a possibility that the object to be processed flows in the cooling water in the course of time.

本発明が解決しようとする課題は、冷却工程における処理槽内の圧力の急減を防止して、被処理物の保護を図ることができる殺菌装置を提供することにある。   The problem to be solved by the present invention is to provide a sterilizer capable of preventing a sudden decrease in pressure in a treatment tank in a cooling process and protecting a workpiece.

本発明は、前記課題を解決するためになされたもので、請求項1に記載の発明は、処理槽内に収容した被処理物へ向けて熱水を噴出して被処理物を加熱する殺菌工程後、前記処理槽内に冷却水を導入して被処理物を冷却する冷却工程を行う殺菌装置であって、被処理物が収容される前記処理槽と、この処理槽内へ給水可能で且つその給水流量を変更可能な給水手段と、前記処理槽内からの排水手段と、前記処理槽内に加圧空気を導入する加圧手段と、前記処理槽内からの排気手段と、被処理物を水没させない水位まで前記給水手段により前記処理槽内に貯留した水を、前記処理槽の底部から前記処理槽内の被処理物へ噴出させて戻す循環手段と、殺菌工程において前記循環手段による循環水を加熱する加熱手段とを備え、殺菌工程および冷却工程では、前記処理槽内を処理槽内温度相当の飽和蒸気圧力よりも高圧に維持するように、前記加圧手段および前記排気手段を制御し、前記給水手段は、小流量給水とこれより流量の多い大流量給水との二段階で流量を調整可能とされ、冷却工程では、前記循環手段により前記処理槽内の水を循環させながら、前記処理槽内に上限水位まで前記給水手段により給水後、前記排水手段により所定時間排水することを繰り返すと共に、冷却工程開始後設定時間経過前は、前記給水手段による前記処理槽内への給水は小流量給水により行う一方、設定時間経過後は大流量給水により行うことを特徴とする殺菌装置である。 The present invention has been made to solve the above-mentioned problems, and the invention according to claim 1 is a sterilization method in which hot water is jetted toward an object to be processed accommodated in a processing tank to heat the object to be processed. A sterilization apparatus that performs a cooling step of cooling the workpiece by introducing cooling water into the treatment tank after the process, and is capable of supplying water into the treatment tank in which the workpiece is accommodated. And the water supply means which can change the water supply flow rate, the drainage means from the inside of the processing tank, the pressurizing means for introducing pressurized air into the processing tank, the exhaust means from the inside of the processing tank, A circulation means for returning water stored in the treatment tank by the water supply means to a water level that does not submerge an object from the bottom of the treatment tank to an object to be treated in the treatment tank; and by the circulation means in a sterilization step Heating means for heating the circulating water, sterilization process and cooling In the process, the pressurizing means and the exhaust means are controlled so that the inside of the treatment tank is maintained at a pressure higher than the saturated vapor pressure corresponding to the temperature in the treatment tank. The flow rate can be adjusted in two stages with a large flow rate water supply with a lot of water, and in the cooling process, water is supplied by the water supply means to the upper limit water level in the treatment tank while circulating the water in the treatment tank by the circulation means. The draining means repeats draining for a predetermined time, and before the set time elapses after the start of the cooling process, the water supply means feeds water into the treatment tank by a small flow rate water supply, while the set time elapses. It is a sterilizer characterized by performing by water supply .

請求項1に記載の発明によれば、冷却工程における処理槽内への冷却水の導入量について、設定条件を満たす前の方が、設定条件を満たした後よりも抑えられる。設定条件を満たすまでの間、処理槽内への冷却水の導入量を抑えることで、冷却工程の開始直後における蒸気の凝縮量を抑えることができる。これにより、処理槽内の圧力の急減を防止して、被処理物の破損を防止することができる。   According to the first aspect of the present invention, the amount of cooling water introduced into the treatment tank in the cooling step is suppressed before the set condition is satisfied than after the set condition is satisfied. Until the setting condition is satisfied, the amount of steam condensed immediately after the start of the cooling step can be suppressed by suppressing the amount of cooling water introduced into the treatment tank. Thereby, it is possible to prevent a sudden decrease in the pressure in the processing tank and prevent the object to be processed from being damaged.

請求項1に記載の発明によれば、殺菌工程では、処理槽内の底部に貯留した水を循環手段により被処理物へ噴出させて戻すことにより循環させると共に、その循環水を加熱手段により加熱する。その後、その熱水は冷却工程において冷却水として使用され、冷却工程において徐々に水を入れ替えて水温を低下させることで、被処理物の冷却が図られる。殺菌工程における熱水をそのまま冷却工程における冷却水として使用し始めることで、工程移行時の温度差を低減し、処理槽内の蒸気の急激な凝縮を防止することができる。また、冷却工程では、単に処理槽内に冷却水を追加するのではなく、適宜排水して処理槽内の水を徐々に入れ替えるので、被処理物を水没させることなく、処理槽内の水温を徐々に低下させることができる。さらに、冷却工程開始直後における処理槽内への給水流量を少なくすることで、処理槽内の蒸気の急激な凝縮を防止することができる。このようにして、処理槽内の圧力低下速度を小さくすることで、処理槽内への加圧空気の導入が遅れることはなく、処理槽内を所望の圧力に維持することができ、被処理物の破損を防止することができる。 According to the first aspect of the present invention, in the sterilization step, the water stored at the bottom in the treatment tank is circulated by returning the water to the object to be treated by the circulation means, and the circulating water is heated by the heating means. To do. Thereafter, the hot water is used as cooling water in the cooling step, and the workpiece is cooled by gradually replacing the water in the cooling step to lower the water temperature. By starting to use the hot water in the sterilization process as it is as the cooling water in the cooling process, it is possible to reduce the temperature difference during the process transition and to prevent rapid condensation of the steam in the treatment tank. Also, in the cooling process, instead of simply adding cooling water into the treatment tank, the water in the treatment tank is gradually drained and the water in the treatment tank is gradually replaced. Can be gradually reduced. Furthermore, the rapid condensation of the vapor | steam in a processing tank can be prevented by reducing the feed water flow rate in the processing tank immediately after a cooling process start. In this way, by reducing the pressure drop rate in the treatment tank, the introduction of pressurized air into the treatment tank is not delayed, the inside of the treatment tank can be maintained at a desired pressure, Damage to the object can be prevented.

請求項1に記載の発明によれば、上限水位までの給水と、所定時間の排水とを繰り返すことで、簡易に、処理槽内の水を徐々に入れ替えることができる。また、冷却工程開始後、設定時間経過前は、処理槽内への給水を小流量で行うことで、処理槽内の蒸気の急激な凝縮を防止して、処理槽内の圧力の急減を防止することができる。 According to invention of Claim 1 , the water in a processing tank can be replaced gradually easily by repeating the water supply to an upper limit water level, and the waste_water | drain for predetermined time . In addition, after starting the cooling process and before the set time has elapsed, water supply to the treatment tank is performed at a small flow rate to prevent rapid condensation of the steam in the treatment tank and prevent a rapid decrease in the pressure in the treatment tank. can do.

本発明によれば、冷却工程における処理槽内の圧力の急減を防止して、被処理物の保護を図ることができる。   ADVANTAGE OF THE INVENTION According to this invention, the sudden fall of the pressure in the processing tank in a cooling process can be prevented, and a to-be-processed object can be aimed at.

本発明の殺菌装置の一実施例を示す概略図である。It is the schematic which shows one Example of the sterilizer of this invention.

以下、本発明の具体的実施例を図面に基づいて詳細に説明する。
図1は、本発明の殺菌装置1の一実施例を示す概略図であり、一部を断面にして示している。本実施例の殺菌装置1は、被処理物2を加熱殺菌後に冷却する装置である。被処理物2は、特に問わないが、典型的にはレトルト食品である。
Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic view showing an embodiment of the sterilizing apparatus 1 of the present invention, and a part thereof is shown in cross section. The sterilization apparatus 1 of the present embodiment is an apparatus that cools the workpiece 2 after heat sterilization. The workpiece 2 is not particularly limited, but is typically a retort food.

本実施例の殺菌装置1は、被処理物2が収容される処理槽3と、この処理槽3内への給水手段4と、処理槽3内からの排水手段5と、処理槽3内に加圧空気を導入する加圧手段6と、処理槽3内からの排気手段7と、処理槽3内の貯留水の循環手段8と、その循環水を加熱する加熱手段9と、これら各手段4〜9を制御する制御手段(図示省略)とを備える。   The sterilization apparatus 1 of the present embodiment includes a treatment tank 3 in which an object to be treated 2 is accommodated, a water supply means 4 into the treatment tank 3, a drainage means 5 from the treatment tank 3, and a treatment tank 3. Pressurizing means 6 for introducing pressurized air, exhaust means 7 from inside the processing tank 3, circulating means 8 for stored water in the processing tank 3, heating means 9 for heating the circulating water, and each of these means And control means (not shown) for controlling 4-9.

処理槽3は、被処理物2を収容する中空容器である。処理槽3は、その形状を特に問わないが、本実施例では水平に配置された円筒材を備え、この円筒材は、一方の開口部が閉塞されており、他方の開口部が扉で開閉可能とされている。従って、扉を開けることで、処理槽3に対し被処理物2を出し入れすることができ、扉を閉じることで、処理槽3の開口部を気密に閉じることができる。   The treatment tank 3 is a hollow container that accommodates the workpiece 2. The shape of the treatment tank 3 is not particularly limited. In the present embodiment, the treatment tank 3 includes a horizontally disposed cylindrical material, and this cylindrical material has one opening closed and the other opening opened and closed by a door. It is possible. Therefore, the workpiece 2 can be taken in and out of the processing tank 3 by opening the door, and the opening of the processing tank 3 can be airtightly closed by closing the door.

処理槽3には、処理槽3内の温度を検出する温度センサ10が設けられると共に、処理槽3内の水位を検出する水位検出器(図示省略)が設けられている。   The processing tank 3 is provided with a temperature sensor 10 that detects the temperature in the processing tank 3 and a water level detector (not shown) that detects the water level in the processing tank 3.

なお、図示例の場合、被処理物2は、トレー11に並べられ、そのようなトレー11が上下に積み重ねられて処理槽3内に収容されている。トレー11は、上方へ開口した浅い矩形状の容器であり、少なくとも底面に多数の開口が形成されると共に、上下のトレー11は、側面において隙間をあけて積み重ねられる。但し、被処理物2は、処理槽3内の棚に載せたり、ワゴンに載せたりして、処理槽3内に収容されてもよい。   In the case of the illustrated example, the objects to be processed 2 are arranged in a tray 11, and such trays 11 are stacked in the vertical direction and accommodated in the processing tank 3. The tray 11 is a shallow rectangular container that opens upward, and a large number of openings are formed at least on the bottom surface. The upper and lower trays 11 are stacked with gaps on the side surfaces. However, the to-be-processed object 2 may be accommodated in the processing tank 3 by mounting on the shelf in the processing tank 3, or mounting on a wagon.

給水手段4は、給水路12を介して処理槽3内へ水を供給する。給水手段4は、処理槽3内への給水流量を変更可能に構成されている。本実施例では、給水路12は、給水ポンプ13より下流(処理槽3側)において二股に分岐された後、再び合流して処理槽3に接続されている。これにより、給水路12の一部は、第一給水路12aと第二給水路12bとが並列に配置されて構成されることになる。   The water supply means 4 supplies water into the treatment tank 3 through the water supply path 12. The water supply means 4 is configured to be able to change the water supply flow rate into the treatment tank 3. In this embodiment, the water supply path 12 is bifurcated on the downstream side (processing tank 3 side) from the water supply pump 13, and then merges again and is connected to the processing tank 3. Thereby, a part of the water supply path 12 is configured by arranging the first water supply path 12a and the second water supply path 12b in parallel.

第一給水路12aには第一給水弁14が設けられ、第二給水路12bには第二給水弁15が設けられる。給水ポンプ13を作動させた状態で、一方または双方の給水弁14,15を開けることで、給水源からの水を処理槽3内へ供給することができる。この際、第一給水弁14と第二給水弁15との内、いずれを開けるかにより、または一方のみを開けるか双方を開けるかにより、処理槽3内への給水流量を二段階で調整可能とされている。   A first water supply valve 14 is provided in the first water supply path 12a, and a second water supply valve 15 is provided in the second water supply path 12b. In a state where the water supply pump 13 is operated, one or both of the water supply valves 14 and 15 are opened to supply water from the water supply source into the treatment tank 3. At this time, the water supply flow rate into the treatment tank 3 can be adjusted in two stages by opening either the first water supply valve 14 or the second water supply valve 15, or by opening only one or both. It is said that.

具体的には、本実施例の給水手段4は、小流量給水とこれより流量の多い大流量給水との二段階で給水流量を変更可能とされており、第二給水弁15を閉鎖した状態で第一給水弁14のみを開放すれば小流量給水、第一給水弁14を閉鎖した状態で第二給水弁15のみを開放すれば大流量給水で、処理槽3内へ給水できる。但し、処理槽3内への大流量給水は、第一給水弁14を閉鎖した状態で第二給水弁15のみを開放するのではなく、第一給水弁14と第二給水弁15との双方を開放することで行ってもよい。一方、第一給水弁14と第二給水弁15との双方を閉鎖すれば、処理槽3内への給水を停止できる。   Specifically, the water supply means 4 of the present embodiment is capable of changing the water supply flow rate in two stages of a small flow rate water supply and a large flow rate water supply with a higher flow rate, and the second water supply valve 15 is closed. If only the first water supply valve 14 is opened, water can be supplied into the treatment tank 3 with a small flow rate water supply, and if only the second water supply valve 15 is opened with the first water supply valve 14 closed, the water can be supplied into the treatment tank 3 with a large flow rate water supply. However, the large flow rate water supply into the treatment tank 3 does not open only the second water supply valve 15 with the first water supply valve 14 closed, but both the first water supply valve 14 and the second water supply valve 15. It may be done by opening. On the other hand, if both the 1st water supply valve 14 and the 2nd water supply valve 15 are closed, the water supply to the processing tank 3 can be stopped.

詳細は後述するが、殺菌装置1の運転開始に伴い、処理槽3内には給水手段4により水が供給され、設定水位まで水が貯留される。その設定水位は、処理槽3内のいずれの被処理物2も水没させない水位である。具体的には、処理槽3内の最下部に配置された被処理物2よりも下方において設定水位が定められ、設定水位まで水を貯留しても、処理槽3内のいずれの被処理物2も貯留水に浸漬されない。   Although details will be described later, with the start of operation of the sterilizer 1, water is supplied into the treatment tank 3 by the water supply means 4, and water is stored up to the set water level. The set water level is a water level that does not submerge any object 2 in the treatment tank 3. Specifically, even if the set water level is determined below the workpiece 2 disposed at the lowermost part in the treatment tank 3 and water is stored up to the set water level, any of the treatment objects in the treatment tank 3 is stored. 2 is not immersed in the stored water.

排水手段5は、排水路16を介して処理槽3内から水を排出する。排水路16は、処理槽3の底部に接続され、排水弁17が設けられている。排水弁17を開くことで、処理槽3内の水を外部へ排出することができる。   The drainage means 5 drains the water from the treatment tank 3 through the drainage channel 16. The drainage channel 16 is connected to the bottom of the treatment tank 3 and is provided with a drainage valve 17. By opening the drain valve 17, the water in the processing tank 3 can be discharged to the outside.

加圧手段6は、加圧路18を介して処理槽3内へ加圧空気(言い換えれば圧縮空気)を供給する。加圧路18に設けた加圧弁19を開くことで、加圧空気源からの加圧空気を処理槽3内に供給して、大気圧を超える圧力に処理槽3内を加圧することができる。   The pressurizing means 6 supplies pressurized air (in other words, compressed air) into the processing tank 3 through the pressurizing passage 18. By opening the pressurizing valve 19 provided in the pressurizing passage 18, pressurized air from a pressurized air source can be supplied into the processing tank 3, and the inside of the processing tank 3 can be pressurized to a pressure exceeding the atmospheric pressure. .

排気手段7は、大気圧を超える圧力下の処理槽3内から排気路20を介して気体を排出する。排気路20は、処理槽3の上部に接続され、処理槽3の側から順に、排気弁21と逆止弁22とが設けられている。処理槽3内が大気圧を超える圧力にある状態で、排気弁21を開くと、処理槽3内の気体は排気路20を介して外部へ排出され、処理槽3内の圧力を下げることができる。   The exhaust means 7 exhausts the gas from the inside of the processing tank 3 under a pressure exceeding the atmospheric pressure through the exhaust path 20. The exhaust path 20 is connected to the upper part of the processing tank 3, and an exhaust valve 21 and a check valve 22 are provided in order from the processing tank 3 side. When the exhaust valve 21 is opened in a state where the inside of the processing tank 3 is at a pressure exceeding the atmospheric pressure, the gas in the processing tank 3 is discharged to the outside through the exhaust path 20, and the pressure in the processing tank 3 may be lowered. it can.

循環手段8は、処理槽3内の貯留水を、処理槽3の底部から抜き出し、循環路23を介して処理槽3内の被処理物2へ噴出させて戻すことで、処理槽3内の水を循環する。循環路23には循環ポンプ24が設けられており、この循環ポンプ24を作動させることで、処理槽3内の水を循環させることができる。循環路23からの水は、処理槽3内へ戻される際、ノズル25により被処理物2へ噴出して戻される。このノズル25は、処理槽3内の側部および/または上部に設けられている。なお、図示例の場合、給水路12と循環路23とは、処理槽3の底部の側で共通の管路とされている。   The circulation means 8 draws out the stored water in the treatment tank 3 from the bottom of the treatment tank 3 and ejects the stored water in the treatment tank 3 through the circulation path 23 to return to the object 2 in the treatment tank 3. Circulate water. A circulation pump 24 is provided in the circulation path 23, and the water in the treatment tank 3 can be circulated by operating the circulation pump 24. When the water from the circulation path 23 is returned into the treatment tank 3, it is ejected and returned to the workpiece 2 by the nozzle 25. The nozzle 25 is provided on the side and / or upper part in the processing tank 3. In the case of the illustrated example, the water supply channel 12 and the circulation channel 23 are a common pipeline on the bottom side of the treatment tank 3.

加熱手段9は、循環手段8による循環水を加熱する。加熱手段9は、その構成を特に問わないが、本実施例では、循環水への給蒸手段とされている。具体的には、本実施例では、循環ポンプ24より下流において、循環路23には給蒸路26が接続されており、循環路23と給蒸路26との接続部には、循環水への蒸気の混合器27が設けられている。また、給蒸路26には給蒸弁28が設けられている。従って、給蒸弁28を開けることで、循環路23内の循環水に蒸気を吹き込んで、循環水を加熱することができる。処理槽3に設けた温度センサ10の検出温度に基づき給蒸弁28の開度を調整することで、処理槽3内の温度を所望に調整することができる。   The heating means 9 heats the circulating water from the circulation means 8. The heating means 9 is not particularly limited in its configuration, but in this embodiment, it is a means for supplying steam to the circulating water. Specifically, in this embodiment, a steam supply path 26 is connected to the circulation path 23 downstream of the circulation pump 24, and the connection between the circulation path 23 and the steam supply path 26 is connected to the circulating water. A steam mixer 27 is provided. The steam supply passage 26 is provided with a steam supply valve 28. Therefore, by opening the steam supply valve 28, steam can be blown into the circulating water in the circulation path 23 to heat the circulating water. By adjusting the opening degree of the steam supply valve 28 based on the temperature detected by the temperature sensor 10 provided in the processing tank 3, the temperature in the processing tank 3 can be adjusted as desired.

制御手段は、温度センサ10や水位検出器の検出信号や経過時間などに基づき、前記各手段4〜9を制御する制御器(図示省略)である。具体的には、給水ポンプ13、第一給水弁14、第二給水弁15、排水弁17、加圧弁19、排気弁21、循環ポンプ24、給蒸弁28の他、温度センサ10および水位検出器などは、制御器に接続されている。   The control means is a controller (not shown) that controls each of the means 4 to 9 based on the detection signal of the temperature sensor 10 and the water level detector, the elapsed time, and the like. Specifically, in addition to the water supply pump 13, the first water supply valve 14, the second water supply valve 15, the drain valve 17, the pressurizing valve 19, the exhaust valve 21, the circulation pump 24, the steam supply valve 28, the temperature sensor 10 and the water level detection. The device is connected to the controller.

制御器は、以下に述べるように、所定の手順(プログラム)に従い、処理槽3内の被処理物2の加熱殺菌と、その後の冷却を行う。典型的には、給水工程、移行工程、殺菌工程、冷却工程および排水工程を順次に実行する。以下、各工程について説明する。なお、殺菌装置1の運転に先立ち、処理槽3内には被処理物2が収容され、処理槽3の扉は閉じられる。その状態では、排気弁21は開かれ、その他の弁は閉じられており、各ポンプは停止している。   As will be described below, the controller performs heat sterilization of the workpiece 2 in the processing tank 3 and subsequent cooling in accordance with a predetermined procedure (program). Typically, a water supply process, a transition process, a sterilization process, a cooling process, and a drainage process are sequentially performed. Hereinafter, each step will be described. Prior to the operation of the sterilizer 1, the workpiece 2 is accommodated in the treatment tank 3, and the door of the treatment tank 3 is closed. In this state, the exhaust valve 21 is opened, the other valves are closed, and each pump is stopped.

(1)給水工程
給水工程では、処理槽3内の被処理物2を浸漬しない設定水位まで、給水手段4により処理槽3内に水を供給して、処理槽3内に水を貯留する。この際、大流量給水で、処理槽3内に給水することができる。具体的には、給水ポンプ13を作動させた状態で、第一給水弁14と第二給水弁15との内、第二給水弁15のみを開けるか、双方の給水弁14,15を開けばよい。この際、排水弁17および加圧弁19は閉じられており、排気弁21は開かれている。処理槽3内に設定水位まで水が貯留されたことを水位検出器により検知すると、給水弁15(,14)を閉じると共に給水ポンプ13を停止させて、給水工程を終了する。
(1) Water supply step In the water supply step, water is supplied into the treatment tank 3 by the water supply means 4 to a set water level at which the workpiece 2 in the treatment tank 3 is not immersed, and the water is stored in the treatment tank 3. At this time, water can be supplied into the treatment tank 3 with a large flow rate of water supply. Specifically, when the water supply pump 13 is operated, only the second water supply valve 15 of the first water supply valve 14 and the second water supply valve 15 is opened, or both the water supply valves 14 and 15 are opened. Good. At this time, the drain valve 17 and the pressurizing valve 19 are closed, and the exhaust valve 21 is opened. When the water level detector detects that water has been stored in the treatment tank 3 up to the set water level, the water supply valve 15 (, 14) is closed and the water supply pump 13 is stopped to end the water supply process.

(2)移行工程
移行工程では、循環手段8により処理槽3内の水を循環させながら、その循環水を加熱手段9により加熱して、処理槽3内の温度を殺菌温度(たとえば120℃)まで上昇させる。具体的には、循環ポンプ24を作動させることで、処理槽3内底部からの水を、循環路23を介して処理槽3内へ戻すことで、処理槽3の水を循環させる。また、給蒸弁28を開けて、混合器27において循環水に蒸気を吹き込むことで、循環水を加熱する。
(2) Transition Step In the transition step, the circulating water is heated by the heating means 9 while circulating the water in the treatment tank 3 by the circulation means 8, and the temperature in the treatment tank 3 is set to the sterilization temperature (for example, 120 ° C.). Raise to. Specifically, the water in the processing tank 3 is circulated by returning the water from the inner bottom of the processing tank 3 into the processing tank 3 through the circulation path 23 by operating the circulation pump 24. Further, the steam supply valve 28 is opened, and steam is blown into the circulating water in the mixer 27 to heat the circulating water.

このようにして、処理槽3内の温度を徐々に上昇させるが、それに伴い被処理物2が加熱により膨張して包装(レトルトパウチなど)が破裂するおそれがある。そこで、これを防止するために、加圧手段6により処理槽3内は徐々に加圧され、大気圧を超える圧力(処理槽内温度相当の飽和蒸気圧力よりもやや高圧)とされる。具体的には、加圧弁19と排気弁21とを制御することにより、処理槽3内の温度に応じた加圧がなされる。以後、循環手段8による水の循環と、加圧手段6による処理槽3内の加圧とは、冷却工程の終了まで引き続きなされる。   Thus, although the temperature in the processing tank 3 is raised gradually, the to-be-processed object 2 expand | swells by heating, and there exists a possibility that packaging (a retort pouch etc.) may burst. Therefore, in order to prevent this, the inside of the processing tank 3 is gradually pressurized by the pressurizing means 6 to a pressure exceeding the atmospheric pressure (slightly higher than the saturated vapor pressure corresponding to the temperature in the processing tank). Specifically, the pressurization according to the temperature in the processing tank 3 is performed by controlling the pressurization valve 19 and the exhaust valve 21. Thereafter, the water circulation by the circulation means 8 and the pressurization in the treatment tank 3 by the pressure means 6 are continued until the end of the cooling step.

(3)殺菌工程
殺菌工程では、処理槽3内の温度を殺菌温度に保持して、被処理物2を加熱して殺菌する。具体的には、循環ポンプ24により処理槽3内の水を循環させつつ、温度センサ10の検出温度を殺菌温度に維持するように、給蒸弁28の開度を調整する。処理槽3内が殺菌温度以上で殺菌時間経過すると、給蒸弁28を閉じて循環水の加熱を停止して、殺菌工程を終了する。
(3) Sterilization process In a sterilization process, the temperature in the processing tank 3 is hold | maintained at the sterilization temperature, and the to-be-processed object 2 is heated and sterilized. Specifically, the degree of opening of the steam supply valve 28 is adjusted so as to maintain the temperature detected by the temperature sensor 10 at the sterilization temperature while circulating the water in the treatment tank 3 by the circulation pump 24. When the inside of the treatment tank 3 is at or above the sterilization temperature and the sterilization time has elapsed, the steam supply valve 28 is closed, heating of the circulating water is stopped, and the sterilization process is terminated.

(4)冷却工程
冷却工程では、循環手段8により処理槽3内の水を循環させながら、給水手段4および排水手段5により処理槽3内の水を徐々に入れ替えることで、循環水の温度を徐々に低下させ、これにより処理槽3内の被処理物2の冷却を図る。具体的には、循環ポンプ24を作動させて処理槽3内の水を循環させた状態で、次のようにして処理槽3内の水を徐々に入れ替える。
(4) Cooling step In the cooling step, the water in the treatment tank 3 is circulated by the circulation means 8 and the water in the treatment tank 3 is gradually replaced by the water supply means 4 and the drainage means 5 to thereby adjust the temperature of the circulating water. By gradually lowering the temperature, the object 2 in the treatment tank 3 is cooled. Specifically, the water in the treatment tank 3 is gradually replaced as follows in a state where the circulation pump 24 is operated to circulate the water in the treatment tank 3.

つまり、冷却工程では、処理槽3内に上限水位まで給水手段4により給水する一方、その上限水位より低い下限水位まで排水手段5により排水することを繰り返す。これにより、処理槽3内の比較的高温の水が、給水手段4により新たに処理槽3内へ供給される比較的低温の水と徐々に入れ替えられて、処理槽3内の水温の低下が図られる。なお、上限水位および下限水位は水位検出器により検知され、上限水位においても、処理槽3内の最下部の被処理物2は、貯留水に浸漬されない。また、上限水位または下限水位のいずれかを、前記給水工程における前記設定水位と一致させることができる。   That is, in the cooling step, water is supplied into the treatment tank 3 by the water supply means 4 up to the upper limit water level, while the water is discharged by the drainage means 5 to a lower limit water level lower than the upper limit water level. Thereby, the relatively high temperature water in the treatment tank 3 is gradually replaced with the relatively low temperature water newly supplied into the treatment tank 3 by the water supply means 4, and the water temperature in the treatment tank 3 is lowered. Figured. The upper limit water level and the lower limit water level are detected by a water level detector, and even at the upper limit water level, the lowermost workpiece 2 in the treatment tank 3 is not immersed in the stored water. Moreover, either an upper limit water level or a lower limit water level can be made to correspond with the said setting water level in the said water supply process.

ところで、冷却工程の開始直後には、その直前の殺菌工程により処理槽3内に蒸気が充満している。その状態で、処理槽3内に給水手段4により比較的低温(典型的には常温)の冷却水を供給すると、蒸気の凝縮により、処理槽3内の圧力が急激に低下し、被処理物2の破損(レトルトパウチの破袋)を生じるおそれがある。圧力低下が生じるとそれを補うように加圧空気を導入する制御はなされているが、冷却工程の開始直後には蒸気の凝縮が多く、処理槽3内への加圧空気の供給が追い付かないおそれがある。   By the way, immediately after the start of the cooling process, the treatment tank 3 is filled with steam by the immediately preceding sterilization process. In this state, when relatively low-temperature (typically normal temperature) cooling water is supplied into the treatment tank 3 by the water supply means 4, the pressure in the treatment tank 3 rapidly decreases due to the condensation of steam, and the object to be treated. 2 damage (retort pouch bag breakage) may occur. Although control is performed to introduce pressurized air so as to compensate for a pressure drop, the steam is often condensed immediately after the start of the cooling process, and the supply of pressurized air into the treatment tank 3 cannot catch up. There is a fear.

そこで、本実施例では、給水手段4による処理槽3内への給水について、冷却工程開始後設定時間経過前には小流量給水で行い、設定時間経過後には大流量給水で行う。具体的には、処理槽3内へ給水する際、冷却工程開始後設定時間経過前には、第一給水弁14と第二給水弁15との内、第一給水弁14のみを開いて比較的小流量で給水し、設定時間経過後には、第二給水弁15のみを開くか、双方の給水弁14,15を開いて比較的大流量で給水する。   Therefore, in this embodiment, the water supply to the treatment tank 3 by the water supply means 4 is performed with a small flow rate water supply before the set time elapses after the start of the cooling process, and with a large flow rate water supply after the set time elapses. Specifically, when supplying water into the treatment tank 3, before the set time elapses after the start of the cooling process, only the first water supply valve 14 and the first water supply valve 14 are opened and compared. After the set time has elapsed, only the second water supply valve 15 is opened, or both water supply valves 14 and 15 are opened to supply water at a relatively large flow rate.

これにより、冷却工程開始直後における処理槽3内の蒸気の凝縮を抑制し、処理槽3内への加圧空気の導入が遅れるのを防止することができる。よって、処理槽3内を所望の圧力に維持して、被処理物2の破損を防止することができる。そして、冷却工程開始後、設定時間経過する頃には、処理槽3内の蒸気が加圧手段6による空気に置き換わっており、その後は大流量給水により給水しても処理槽3内の圧力を低下させることはない。   Thereby, condensation of the vapor | steam in the processing tank 3 immediately after a cooling process start can be suppressed, and it can prevent that introduction of pressurized air into the processing tank 3 is delayed. Therefore, the inside of the processing tank 3 can be maintained at a desired pressure to prevent the workpiece 2 from being damaged. When the set time elapses after the start of the cooling process, the steam in the treatment tank 3 is replaced with air by the pressurizing means 6, and thereafter the pressure in the treatment tank 3 is maintained even if water is supplied by a large flow rate water supply. There is no reduction.

冷却工程の開始から所定時間経過するか、処理槽3内の温度(または冷却水の温度)が所定温度よりも下がってから所定時間経過すると、循環手段8による循環や給水手段4による給水を停止して、冷却工程を終了する。   When a predetermined time elapses from the start of the cooling process, or when a predetermined time elapses after the temperature in the treatment tank 3 (or the temperature of the cooling water) falls below the predetermined temperature, the circulation by the circulation means 8 and the water supply by the water supply means 4 are stopped. Then, the cooling process is completed.

(5)排水工程
排水工程では、排水手段5により処理槽3内から排水する。具体的には、排水弁17を開くことで、外部へ水を排出する。加圧手段6により処理槽3内を加圧したままで排水手段5により排水すれば、処理槽3内からの排水を迅速に行うことができる。その後、加圧弁19を閉じる一方、排気弁21を開いて、処理槽3内を大気圧まで戻した後、処理槽3の扉を開けて、処理槽3内から被処理物2を取り出すことができる。
(5) Drainage process In the drainage process, the drainage means 5 drains water from the treatment tank 3. Specifically, water is discharged to the outside by opening the drain valve 17. If the drainage means 5 drains while the inside of the treatment tank 3 is pressurized by the pressurizing means 6, drainage from the treatment tank 3 can be performed quickly. Thereafter, the pressurizing valve 19 is closed, the exhaust valve 21 is opened, the inside of the processing tank 3 is returned to atmospheric pressure, the door of the processing tank 3 is opened, and the workpiece 2 is taken out from the processing tank 3. it can.

本実施例の殺菌装置1によれば、殺菌工程で使用した熱水を、そのまま冷却工程において冷却水として使用し始めることになる。これにより、工程移行時の温度差を低減し、処理槽3内の蒸気の急激な凝縮を防止することができる。また、冷却工程において、処理槽3内の水は、給水手段4による新たな水と徐々に入れ替えられるが、冷却工程開始後設定時間経過するまでは、処理槽3内への給水流量を抑えることで、処理槽3内の水温が急激に低下するのを防止し、処理槽3内の蒸気の急激な凝縮を防止することができる。このようにして、処理槽3内の圧力低下速度を小さくすることで、処理槽3内への加圧空気の導入が遅れることはなく、処理槽3内を所望の圧力に維持することができ、被処理物2の破損を防止することができる。   According to the sterilization apparatus 1 of the present embodiment, the hot water used in the sterilization process starts to be used as cooling water in the cooling process as it is. Thereby, the temperature difference at the time of a process transfer can be reduced, and the rapid condensation of the vapor | steam in the processing tank 3 can be prevented. Moreover, in the cooling process, the water in the treatment tank 3 is gradually replaced with new water by the water supply means 4, but the water supply flow rate into the treatment tank 3 is suppressed until a set time has elapsed after the start of the cooling process. Thus, it is possible to prevent the water temperature in the processing tank 3 from rapidly decreasing and to prevent the steam in the processing tank 3 from condensing rapidly. In this way, by reducing the pressure drop rate in the processing tank 3, the introduction of pressurized air into the processing tank 3 is not delayed, and the inside of the processing tank 3 can be maintained at a desired pressure. Further, it is possible to prevent the workpiece 2 from being damaged.

本発明の殺菌装置1は、前記実施例の構成に限らず、適宜変更可能である。特に、被処理物2を加熱殺菌後に冷却する殺菌装置1において、冷却工程開始後、設定条件を満たすまで、処理槽3内への冷却水の導入量を、それ以降よりも抑えるのであれば、その他の構成は適宜に変更可能である。たとえば、前記実施例では、熱水により被処理物2を加熱殺菌したが、蒸気により被処理物2を加熱殺菌してもよい。   The sterilization apparatus 1 of the present invention is not limited to the configuration of the above embodiment, and can be changed as appropriate. In particular, in the sterilization apparatus 1 that cools the workpiece 2 after heat sterilization, if the amount of cooling water introduced into the treatment tank 3 is suppressed after that until the set condition is satisfied after the start of the cooling process, Other configurations can be changed as appropriate. For example, in the said Example, although the to-be-processed object 2 was heat-sterilized with hot water, you may heat-sterilize the to-be-processed object 2 with a vapor | steam.

また、前記実施例では、冷却工程の開始から設定時間経過する前後で、処理槽3内への給水流量を変えたが、給水流量を変えるタイミングは、適宜に変更可能である。たとえば、処理槽3内の温度または処理槽3内の冷却水の温度が設定温度まで下がるまでは小流量で給水するようにしてもよい。   Moreover, in the said Example, although the feed water flow rate into the processing tank 3 was changed before and after the set time passed from the start of a cooling process, the timing which changes a feed water flow rate can be changed suitably. For example, water may be supplied at a small flow rate until the temperature in the processing tank 3 or the temperature of the cooling water in the processing tank 3 falls to a set temperature.

また、前記実施例では、給水流量は、小流量給水と大流量給水との二段階で切り替えたが、三段階以上で切り替えてもよいし、給水流量を徐々に増すように連続的に変更してもよい。たとえば、給水ポンプ13をインバータ制御したり、給水弁14(15)の開度を徐々に開けたりして、処理槽3内への給水流量を徐々に増すようにしてもよい。この場合、第一給水路12aと第二給水路12bとを並列に設ける必要はなく、いずれか一方のみで足りる。   Moreover, in the said Example, although the feed water flow rate was switched in two steps, a small flow rate feed water and a large flow rate feed water, it may be switched in three steps or more, and it is continuously changed to gradually increase the feed water flow rate. May be. For example, the feed water flow rate into the treatment tank 3 may be gradually increased by inverter-controlling the feed water pump 13 or gradually opening the opening of the feed water valve 14 (15). In this case, it is not necessary to provide the first water supply path 12a and the second water supply path 12b in parallel, and only one of them is sufficient.

また、前記実施例では、加熱手段9は、循環路23において循環水に蒸気を吹き込んだが、処理槽3内底部において貯留水に蒸気を吹き込んでもよい。あるいは、循環路23に熱交換器を設け、その熱交換器において、循環水を蒸気で間接的に加熱してもよい。   Moreover, in the said Example, although the heating means 9 injected the vapor | steam into the circulating water in the circulation path 23, you may inject a vapor | steam into the stored water in the bottom part of the processing tank 3. FIG. Alternatively, a heat exchanger may be provided in the circulation path 23, and the circulating water may be indirectly heated with steam in the heat exchanger.

さらに、前記実施例では、冷却工程において、上限水位までの給水と、下限水位までの排水とを繰り返すことで、処理槽3内の水を徐々に入れ替えて水温の低下を図ったが、上限水位までの給水後、所定時間排水することを繰り返してもよい。あるいは、処理槽3内への給水を継続した状態で、目標水位を維持するように排水手段5による排水量を調整するように制御してもよい。この際、目標水位を維持するように、排水手段5による排水量だけでなく、給水手段4による給水量の制御を行ってもよい。   Furthermore, in the said Example, in the cooling process, by repeating the water supply to the upper limit water level and the drainage to the lower limit water level, the water in the treatment tank 3 was gradually replaced to lower the water temperature. After the water supply up to, it may be repeatedly drained for a predetermined time. Or you may control so that the amount of drainage by the drainage means 5 may be adjusted so that a target water level may be maintained in the state which continued the water supply in the processing tank 3. FIG. At this time, not only the amount of drainage by the drainage means 5 but also the amount of water supply by the water supply means 4 may be controlled so as to maintain the target water level.

1 殺菌装置
2 被処理物
3 処理槽
4 給水手段
5 排水手段
6 加圧手段
7 排気手段
8 循環手段
9 加熱手段
10 温度センサ
11 トレー
12 給水路
12a 第一給水路
12b 第二給水路
13 給水ポンプ
14 第一給水弁
15 第二給水弁
16 排水路
17 排水弁
18 加圧路
19 加圧弁
20 排気路
21 排気弁
22 逆止弁
23 循環路
24 循環ポンプ
25 ノズル
26 給蒸路
27 混合器
28 給蒸弁
DESCRIPTION OF SYMBOLS 1 Sterilization apparatus 2 To-be-processed object 3 Processing tank 4 Water supply means 5 Drainage means 6 Pressurization means 7 Exhaust means 8 Circulation means 9 Heating means 10 Temperature sensor 11 Tray 12 Water supply path 12a First water supply path 12b Second water supply path 13 Water supply pump DESCRIPTION OF SYMBOLS 14 1st water supply valve 15 2nd water supply valve 16 Drainage path 17 Drainage valve 18 Pressurization path 19 Pressurization valve 20 Exhaust path 21 Exhaust valve 22 Check valve 23 Circulation path 24 Circulation pump 25 Nozzle 26 Steam supply path 27 Mixer 28 Supply Steam valve

Claims (1)

処理槽内に収容した被処理物へ向けて熱水を噴出して被処理物を加熱する殺菌工程後、前記処理槽内に冷却水を導入して被処理物を冷却する冷却工程を行う殺菌装置であって
被処理物が収容される前記処理槽と、
この処理槽内へ給水可能で且つその給水流量を変更可能な給水手段と、
前記処理槽内からの排水手段と、
前記処理槽内に加圧空気を導入する加圧手段と、
前記処理槽内からの排気手段と、
被処理物を水没させない水位まで前記給水手段により前記処理槽内に貯留した水を、前記処理槽の底部から前記処理槽内の被処理物へ噴出させて戻す循環手段と、
殺菌工程において前記循環手段による循環水を加熱する加熱手段とを備え、
殺菌工程および冷却工程では、前記処理槽内を処理槽内温度相当の飽和蒸気圧力よりも高圧に維持するように、前記加圧手段および前記排気手段を制御し
前記給水手段は、小流量給水とこれより流量の多い大流量給水との二段階で流量を調整可能とされ、
冷却工程では、前記循環手段により前記処理槽内の水を循環させながら、前記処理槽内に上限水位まで前記給水手段により給水後、前記排水手段により所定時間排水することを繰り返すと共に、冷却工程開始後設定時間経過前は、前記給水手段による前記処理槽内への給水は小流量給水により行う一方、設定時間経過後は大流量給水により行う
ことを特徴とする殺菌装置。
The sterilization which performs the cooling process which introduce | transduces cooling water into the said processing tank and cools a to-be-processed object after the sterilization process which spouts hot water toward the to-be-processed object accommodated in the processing tank, and heats a to-be-processed object A device ,
The treatment tank in which the object to be treated is accommodated;
Water supply means capable of supplying water into the treatment tank and capable of changing the water supply flow rate;
Means for draining from the treatment tank;
Pressurizing means for introducing pressurized air into the treatment tank;
Means for exhausting from the treatment tank;
Circulating means for returning the water stored in the treatment tank by the water supply means to a water level that does not submerge the treatment object from the bottom of the treatment tank and returning it to the treatment object in the treatment tank;
Heating means for heating the circulating water by the circulation means in the sterilization step,
In the sterilization step and the cooling step, the pressurizing means and the exhaust means are controlled so that the inside of the treatment tank is maintained at a pressure higher than a saturated vapor pressure corresponding to the temperature in the treatment tank ,
The water supply means is capable of adjusting the flow rate in two stages, a small flow rate water supply and a large flow rate water supply with a higher flow rate than this,
In the cooling step, while circulating the water in the processing bath by the circulating means, after the water supply by the water supply means to the upper limit water level in the processing bath, with repeated be drained predetermined time by the drainage means, starting the cooling process The sterilization apparatus according to claim 1, wherein water is supplied to the processing tank by the water supply means by a small flow rate water supply before the set time elapses, and is performed by a large flow rate water supply after the set time elapses.
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