JP2002345446A - Heat sterilizer for gas-containing vessel for carrying out preheating - Google Patents

Heat sterilizer for gas-containing vessel for carrying out preheating

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Publication number
JP2002345446A
JP2002345446A JP2001162309A JP2001162309A JP2002345446A JP 2002345446 A JP2002345446 A JP 2002345446A JP 2001162309 A JP2001162309 A JP 2001162309A JP 2001162309 A JP2001162309 A JP 2001162309A JP 2002345446 A JP2002345446 A JP 2002345446A
Authority
JP
Japan
Prior art keywords
temperature
sterilization
gas
container
aerated
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.)
Pending
Application number
JP2001162309A
Other languages
Japanese (ja)
Inventor
Hiroshi Mori
寛 森
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SAMSON CO Ltd
Original Assignee
SAMSON CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SAMSON CO Ltd filed Critical SAMSON CO Ltd
Priority to JP2001162309A priority Critical patent/JP2002345446A/en
Publication of JP2002345446A publication Critical patent/JP2002345446A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To prevent deformation of a gas-containing vessel and breaking of a bag caused by temperature difference between respective gas-containing vessels in a heat sterilizer for heat sterilizing the gas-containing vessels by a batch type operation. SOLUTION: In the heat sterilizer for sterilizing a food, and the like, in the gas-containing vessel 6 by carrying out a sterilization treatment comprising a heat-up process for raising the temperature of the gas-containing vessel 6 to the sterilization temperature after housing the gas-containing vessel 6 in which the food, and the like, are sealed with a gas in a treatment tank 7, a sterilization process for maintaining the gas-containing vessels at the sterilization temperature for a predetermined time and a cooling process for cooling them after sterilization, when carrying out the sterilization treatment, at first, a preheating for heating the gas-containing vessels to a temperature equal to or higher than the filling temperature of the gas-containing vessels and lower than 80 deg.C is carried out to bring the temperatures of respective vessels to be uniform and, after finishing the pre-heating, each process of the sterilization treatment is carried out.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、予備加熱を行う含気容
器用加熱殺菌装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating and sterilizing apparatus for pre-heating a gas-containing container.

【0002】[0002]

【従来の技術】密封包装した食品を処理槽内に収容し、
処理槽内を加熱することで食品を殺菌し、常温での保存
を可能にしているレトルト食品が広く普及している。そ
して食品を包装する際に食品とともに気体を充填してお
き、含気充填カップ容器を殺菌する場合がある。含気レ
トルト食品の製造工程は、食品を調理する調理工程、調
理した食品を気体とともに容器詰めする充填工程、含気
容器を処理槽内へ収容する搬入工程、処理槽内を殺菌温
度まで加熱し、含気容器を殺菌温度まで昇温させる昇温
工程、殺菌温度で設定時間維持する殺菌工程、殺菌した
含気容器を冷却する冷却工程、処理の終わった含気容器
を処理槽内から取り出す搬出工程からなる。
2. Description of the Related Art A hermetically packed food is stored in a processing tank,
2. Description of the Related Art Retort foods that sterilize foods by heating the inside of a treatment tank and enable storage at room temperature are widely used. When packing the food, the gas may be filled together with the food, and the air-filled cup container may be sterilized. The manufacturing process of the aerated retort food includes a cooking process of cooking the food, a filling process of packing the cooked food with gas, a loading process of storing the aerated container in the processing tank, and heating the processing tank to the sterilization temperature. , A heating step of raising the temperature of the aerated container to the sterilization temperature, a sterilization step of maintaining the set temperature at the sterilization temperature, a cooling step of cooling the sterilized aerated container, and taking out the treated aerated container from the processing tank. Process.

【0003】含気容器を殺菌する場合、含気容器内の気
体圧力は温度によって変化する。含気容器内の圧力が処
理槽内の圧力より高くなると容器が膨張し、含気容器内
の圧力が処理槽内の圧力より低くなると容器が収縮する
ことにより、容器に変形や破袋が発生することことがあ
る。そのため、含気容器を加熱殺菌する場合には、含気
容器内圧力とその周囲圧力が等しくなるように、処理槽
内の圧力を調節する必要がある。含気容器内の圧力P
は、下式によって求めることができる。 P={(273+t2)/(273+t1)}×(10
1.3−Pw1)+Pw2 P :含気容器内圧(kPa) t1 :充填温度(℃) t2 :処理中の含気容器内温度(℃) Pw1:t1に対する飽和蒸気圧(kPa) Pw2:t2に対する飽和蒸気圧(kPa) 処理槽内の圧力は、上記式にて求まる含気容器内圧とほ
ぼ等しくなるように制御することで、容器の変形や破袋
を防止することができる。
When sterilizing an air-containing container, the gas pressure in the air-containing container changes depending on the temperature. When the pressure in the aerated container becomes higher than the pressure in the processing tank, the container expands, and when the pressure in the aerated container becomes lower than the pressure in the processing tank, the container shrinks, causing deformation or bag breakage in the container. May be done. Therefore, when heat-sterilizing the gas-containing container, it is necessary to adjust the pressure in the processing tank so that the pressure in the gas-containing container is equal to the surrounding pressure. Pressure P in the aerated container
Can be obtained by the following equation. P = {(273 + t2) / (273 + t1)} × (10
1.3-Pw1) + Pw2 P: Internal pressure of the aerated container (kPa) t1: Filling temperature (° C.) t2: Temperature of the aerated container during processing (° C.) Pw1: Saturated vapor pressure for t1 (kPa) Pw2: For t2 Saturated Vapor Pressure (kPa) By controlling the pressure in the treatment tank to be substantially equal to the internal pressure of the aerated container determined by the above equation, deformation of the container and bag breakage can be prevented.

【0004】ところが、加熱殺菌装置はバッチ式に処理
しており、大型機種では1000個以上の含気容器を1
度に処理しているため、昇温開始時点での含気容器温度
にばらつきが生じる。その状態で昇温工程を行うと、各
含気容器内温度のばらつきによって各含気容器内圧が異
なり、ある含気容器に合わせて処理槽内の圧力を調節し
ていても、一部の含気容器内圧は処理槽内圧に比べて大
きく相違し、低強度の容器を使用した場合には容器の変
形等が生じることがあった。これは、充填工程時の含気
容器温度は一定であるが、充填工程から殺菌処理開始ま
での時間は含気容器毎に異なり、充填温度からの温度低
下量が異なることが原因であった。1度に殺菌処理する
グループの内、早い段階で充填を行った初期充填分は、
殺菌処理の開始時点では温度が大きく低下しているが、
殺菌処理開始直前に充填を行った終期充填分は、殺菌処
理開始時点でも充填温度のままであるため、温度差が発
生していた。
[0004] However, the heat sterilizer is processed in a batch system.
Temperature, the temperature of the gas-containing container at the time of starting the temperature rise varies. If the temperature raising step is performed in this state, the internal pressure of each air-containing container varies due to the variation in the temperature inside each air-containing container. The internal pressure of the gas container is largely different from the internal pressure of the processing tank, and when a low-strength container is used, the container may be deformed. This is because the temperature of the gas-containing container during the filling process is constant, but the time from the filling process to the start of the sterilization treatment differs for each gas-containing container, and the amount of temperature decrease from the filling temperature is different. Of the group that sterilizes at once, the initial filling that was done at an early stage
At the start of the sterilization process, the temperature has dropped significantly,
The final filling, which was filled immediately before the start of the sterilization treatment, was still at the filling temperature even at the start of the sterilization treatment, so that a temperature difference occurred.

【0005】図4は、バッチ式で殺菌を行う加熱殺菌装
置において、昇温工程開始時点で含気容器温度に差があ
った場合の温度変化の状況を示したものであり、図5は
図4の場合における含気容器内圧力の変化を示したもの
である。ここでは、充填時の温度は50℃であり、昇温
工程開始時点の時間T0では、終期充填分は50℃であ
るが初期充填分の含気容器は20℃まで低下していると
する。時間T0から時間T6の各時点における温度及び
圧力を、初期充填分は黒丸で表し、終期充填分は白三角
で表しており、図4には処理槽内の雰囲気温度を2点鎖
線で表している。
[0005] Fig. 4 shows a state of a temperature change when there is a difference in the temperature of the air-containing vessel at the start of the temperature raising step in a heat sterilization apparatus that performs sterilization in a batch system. 4 shows a change in the pressure inside the air-containing container in the case of No. 4. Here, it is assumed that the temperature at the time of filling is 50 ° C., and at time T0 at the start of the temperature raising step, the final filling amount is 50 ° C., but the aerated container for the initial filling has dropped to 20 ° C. The temperature and the pressure at each time point from the time T0 to the time T6 are shown by a black circle for the initial filling, a white triangle for the last filling, and an atmosphere temperature in the processing tank by a two-dot chain line in FIG. I have.

【0006】昇温工程開始時点の時間T0では、初期充
填分の温度は20℃であり、終期充填分の温度は50℃
である。昇温工程では、処理槽内の雰囲気温度を殺菌温
度の120℃まで高めておき、処理槽内に収容した含気
容器の温度を高める。この時、初期充填分と終期充填分
の温度差は、時間の経過によって縮小していくが、両方
とも上昇していくために温度差はすぐにはなくならな
い。ここでは、時間T0から時間T6までの温度が、初
期充填分の場合は20℃→40℃→65℃→90℃→1
05℃→115℃→120℃の順に変化し、終期充填分
の場合は50℃→65℃→85℃→105℃→115℃
→120℃→120℃の順に変化しているとする。
At time T0 at the start of the temperature raising step, the temperature of the initial filling is 20 ° C. and the temperature of the final filling is 50 ° C.
It is. In the temperature raising step, the ambient temperature in the processing tank is increased to a sterilization temperature of 120 ° C., and the temperature of the aerated container housed in the processing tank is increased. At this time, the temperature difference between the initial filling amount and the final filling amount decreases with the passage of time, but the temperature difference does not disappear immediately because both rise. Here, the temperature from time T0 to time T6 is 20 ° C. → 40 ° C. → 65 ° C. → 90 ° C. → 1 for the initial filling.
It changes in the order of 05 ° C → 115 ° C → 120 ° C, and 50 ° C → 65 ° C → 85 ° C → 105 ° C → 115 ° C for the final filling
It is assumed that the temperature changes in the order of → 120 ° C. → 120 ° C.

【0007】前記の各温度における含気容器内圧を、前
記の含気容器内圧算出式にて求めると、図5に記載の通
りとなる。この場合、時間T0から時間T6における初
期充填分の含気容器内圧力と終期充填分の含気容器内圧
力の差は、18kPa→24kPa→38kPa→55kPa→51
kPa→31kPa→0kPaとなる。温度差は昇温工程初期の
方が大きいが、含気容器内の圧力差は時間T3まで増加
してその後は減少しており、個々の含気容器における圧
力差によって変形が発生するとすれば、圧力差のピーク
を迎える昇温工程中期に発生することが予測できる。
When the internal pressure of the air-containing container at each of the above-mentioned temperatures is determined by the above-described equation for calculating the internal pressure of the air-containing container, the result is as shown in FIG. In this case, the difference between the pressure inside the gas-filled container for the initial filling and the pressure inside the gas-filled container for the final filling from time T0 to time T6 is 18 kPa → 24 kPa → 38 kPa → 55 kPa → 51
kPa → 31 kPa → 0 kPa. Although the temperature difference is larger at the beginning of the temperature raising step, the pressure difference in the aerated container increases until time T3 and thereafter decreases, and if the pressure difference in each of the aerated containers causes deformation, It can be predicted that this will occur in the middle stage of the heating process, where the pressure difference peaks.

【0008】[0008]

【発明が解決しようとする課題】本発明が解決しようと
する課題は、含気容器をバッチ式で加熱殺菌する加熱殺
菌装置において、各含気容器の温度差に起因する含気容
器の変形や破袋を防止することにある。
SUMMARY OF THE INVENTION The object of the present invention is to provide a heat sterilization apparatus for heat sterilization of an air-containing container in a batch system. The purpose is to prevent bag breakage.

【0009】[0009]

【課題を解決するための手段】請求項1に記載の発明
は、食品等を気体とともに密封した含気容器を処理槽内
に収容しておき、含気容器を殺菌温度まで昇温する昇温
工程、殺菌温度で所定時間維持する殺菌工程、殺菌終了
後に含気容器を冷却する冷却工程からなる殺菌処理を行
うことで、含気容器内の食品等を殺菌する加熱殺菌装置
において、殺菌処理を行う場合、まず各含気容器の温度
を均一化するために含気容器の充填温度以上であって8
0℃未満の温度で加熱する予備加熱を行い、予備加熱終
了後に殺菌処理の各工程を行うものである。予備加熱を
行うことで各含気容器の温度を均一化することができ、
各含気容器温度が均一な状態で昇温工程を行うのであれ
ば、個々の含気容器に圧力差が発生することがなくなる
ため、含気容器の変形や破袋を防ぐことができる。
According to a first aspect of the present invention, there is provided a temperature increasing method in which an aerated container in which food or the like is sealed together with a gas is accommodated in a treatment tank, and the aerated container is heated to a sterilization temperature. Process, a sterilization process of maintaining a predetermined time at the sterilization temperature, by performing a sterilization process consisting of a cooling process of cooling the aerated container after the completion of the sterilization, in a heat sterilization device for sterilizing food and the like in the aerated container, sterilization process First, in order to equalize the temperature of each aerated container, the temperature must be higher than the filling temperature of the aerated container.
Preheating is performed by heating at a temperature lower than 0 ° C., and after the preheating, each step of the sterilization treatment is performed. By performing preheating, the temperature of each aerated container can be made uniform,
If the temperature raising step is performed in a state where the temperatures of the air-containing containers are uniform, no pressure difference is generated between the individual air-containing containers, so that deformation and breakage of the air-containing containers can be prevented.

【0010】請求項2に記載の発明は、前記の予備加熱
を行う含気容器用加熱殺菌装置において、予備加熱の温
度を含気容器の充填温度と等しくしたものである。予備
加熱の温度を高くすれば、予備加熱を行っている間に各
含気容器の圧力差が拡大し、含気容器の変形などが発生
する恐れが生じるが、予備加熱を充填温度と等しくすれ
ば、予備加熱を行っている間に各含気容器の圧力差が拡
大することはなく、含気容器の変形などは確実に防止で
きる。
According to a second aspect of the present invention, in the heat sterilization apparatus for an aerated container for performing the preheating, the temperature of the preheating is set equal to the filling temperature of the aerated container. If the temperature of the preheating is increased, the pressure difference between the aerated containers increases during the preheating, which may cause deformation of the aerated container. For example, the pressure difference between the aerated containers does not increase during the preheating, and the deformation of the aerated container can be reliably prevented.

【0011】[0011]

【発明の実施の形態】本発明の一実施例を図面を用いて
説明する。図1は本発明を実施する加熱殺菌装置のフロ
ー図、図2は一実施例における含気容器内温度の説明
図、図3は図2における含気容器内圧の説明図である。
加熱殺菌装置は円筒形の処理槽7内に含気容器6を多数
収容し、処理槽7内を加熱加圧することで含気容器6内
の食品を殺菌するものである。処理槽7には、処理槽底
部より循環水を取り出し、その後処理槽内の含気容器6
へ循環水を噴射する循環配管を設ける。循環配管の途中
には、循環水を流動させる循環ポンプ9と、循環水を加
熱する熱交換器8を設けておき、熱交換器8への蒸気供
給を制御する加熱制御弁2を設ける。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a flowchart of a heat sterilization apparatus for carrying out the present invention, FIG. 2 is an explanatory diagram of the temperature in an aerated container in one embodiment, and FIG. 3 is an explanatory diagram of the internal pressure of an aerated container in FIG.
The heat disinfection apparatus accommodates a large number of aerated containers 6 in a cylindrical processing tank 7 and sterilizes the food in the aerated container 6 by heating and pressurizing the processing tank 7. Circulating water is taken out of the processing tank 7 from the bottom of the processing tank 7, and then the aerated container 6
A circulating pipe for injecting circulating water into A circulation pump 9 for flowing the circulating water and a heat exchanger 8 for heating the circulating water are provided in the middle of the circulation pipe, and a heating control valve 2 for controlling the supply of steam to the heat exchanger 8 is provided.

【0012】処理槽7の上部には、コンプレッサー10
からの加圧空気を処理槽7へ送る加圧配管を設け、加圧
配管の途中に処理槽7への加圧空気供給を制御する加圧
弁5を設ける。処理槽7の上部に、処理槽7内から空気
を排出する減圧配管を設け、減圧配管の途中には、処理
槽7からの排気を制御する減圧弁4を設ける。処理槽7
内の圧力を検出する圧力測定装置3を設け、圧力測定装
置3と接続した運転制御装置1を設けておき、運転制御
装置1は、減圧弁4・加圧弁5・循環ポンプ9・加熱制
御弁2とも接続する。運転制御装置1が、減圧弁4・加
圧弁5・循環ポンプ9・加熱制御弁2の作動を制御す
る。
At the top of the processing tank 7, a compressor 10
A pressurized pipe for sending pressurized air from the tank to the processing tank 7 is provided, and a pressurizing valve 5 for controlling the supply of pressurized air to the processing tank 7 is provided in the middle of the pressurized pipe. A pressure reducing pipe for discharging air from inside the processing tank 7 is provided above the processing tank 7, and a pressure reducing valve 4 for controlling exhaust from the processing tank 7 is provided in the middle of the pressure reducing pipe. Processing tank 7
A pressure measuring device 3 for detecting the internal pressure is provided, and an operation control device 1 connected to the pressure measuring device 3 is provided. The operation control device 1 includes a pressure reducing valve 4, a pressurizing valve 5, a circulation pump 9, and a heating control valve. Also connect 2. The operation control device 1 controls operations of the pressure reducing valve 4, the pressurizing valve 5, the circulation pump 9, and the heating control valve 2.

【0013】レトルト食品の製造工程は、食品を調理す
る調理工程、調理した食品を空気などの気体とともに容
器詰めする充填工程、含気容器を処理槽内へ収容する搬
入工程、含気容器の温度を均一化する予備加熱工程、含
気容器を殺菌温度まで加熱する昇温工程、殺菌温度で設
定時間維持する殺菌工程、殺菌工程終了後に含気容器を
冷却する冷却工程、処理槽内から含気容器を取り出す搬
出工程からなる。
The manufacturing process of the retort food includes a cooking process of cooking the food, a filling process of packing the cooked food in a container with a gas such as air, a carrying-in process of storing the aerated container in the treatment tank, and a temperature of the aerated container. Preheating step to homogenize, heating step to heat the aerated container to the sterilization temperature, sterilization step to maintain the set temperature at the sterilization temperature, cooling step to cool the aerated container after the sterilization step, and air from the treatment tank It consists of an unloading process for taking out the container.

【0014】充填工程の場合は1つずつ行い、殺菌処理
は多量の含気容器を一括して行うため、充填工程から殺
菌処理までの待ち時間はそれぞれ異なり、待ち時間の間
に低下する温度もそれぞれで異なることになる。含気容
器を殺菌する場合、運転制御装置1は昇温工程を開始す
る前に予備加熱を行う。運転制御装置1は、多数の含気
容器を処理槽7内に収容した状態で、循環ポンプ9の作
動と加熱制御弁2を開く制御を行う。熱交換器8に蒸気
を供給し、熱交換器8で熱を吸収した熱水を処理槽7内
へ噴射することで、処理槽7内を加熱する。予備加熱の
場合、処理槽7内の雰囲気温度は、含気容器の殺菌温度
より低い所定の温度を保つように加熱制御弁2の操作を
行い、各含気容器6の温度差をなくする。
In the case of the filling step, the filling step is carried out one by one, and the sterilization treatment is performed in a large amount of aerated containers at a time. Therefore, the waiting time from the filling step to the sterilization treatment is different, and the temperature which decreases during the waiting time is also different. Each will be different. When sterilizing the air-containing container, the operation control device 1 performs preheating before starting the temperature raising step. The operation control device 1 controls the operation of the circulation pump 9 and the opening of the heating control valve 2 in a state in which a large number of aerated containers are accommodated in the processing tank 7. Steam is supplied to the heat exchanger 8, and hot water having absorbed heat in the heat exchanger 8 is injected into the processing tank 7 to heat the processing tank 7. In the case of preheating, the heating control valve 2 is operated so that the atmospheric temperature in the processing tank 7 is maintained at a predetermined temperature lower than the sterilization temperature of the gas-containing container, and the temperature difference between the gas-containing containers 6 is eliminated.

【0015】図2は、充填温度は50℃であり、殺菌処
理開始時点の時間T0では、初期充填分は20℃まで低
下している場合である。時間T0から時間T1の各時点
における温度を、初期充填分は黒丸で表し、終期充填分
は白三角で表しており、処理槽内の雰囲気温度は2点鎖
線で表している。予備加熱の場合、運転制御装置1は、
処理槽7内雰囲気温度を充填温度と等しい50℃に保つ
ように加熱制御弁2の操作を行い、初期充填分の含気容
器温度を50℃まで上昇させる。終期充填分の温度は充
填温度と変わらず、初期充填分の温度は充填温度から大
きく低下していたため、時間T0の時点では終期充填分
と初期充填分に温度差があったが、処理槽7内雰囲気温
度を充填温度である50℃に加熱して維持すると、終期
充填分は温度変化せず、初期充填分は温度上昇するた
め、各含気容器6における温度差がなくなる。予備加熱
を行うことで、図3に記載のように初期充填分と終期充
填分での圧力差はなくなる。
FIG. 2 shows a case where the filling temperature is 50 ° C. and the initial filling amount has dropped to 20 ° C. at the time T0 at the start of the sterilization treatment. The temperature at each time point from the time T0 to the time T1 is represented by a black circle for the initial filling, a white triangle for the final filling, and a two-dot chain line for the atmosphere temperature in the treatment tank. In the case of preheating, the operation control device 1
The heating control valve 2 is operated so as to maintain the atmosphere temperature in the processing tank 7 at 50 ° C. which is equal to the filling temperature, and the temperature of the aerated container for the initial filling is raised to 50 ° C. Since the temperature of the final filling was not different from the filling temperature, and the temperature of the initial filling was significantly lower than the filling temperature, there was a temperature difference between the final filling and the initial filling at time T0. If the internal atmosphere temperature is heated to and maintained at 50 ° C., which is the filling temperature, the temperature of the final filling does not change and the temperature of the initial filling rises, so that the temperature difference between the aerated containers 6 disappears. By performing the preheating, the pressure difference between the initial charge and the final charge as shown in FIG. 3 is eliminated.

【0016】時間T2となり予備加熱に設定しておいた
時間が終了すると、運転制御装置1は予備加熱を終了し
て昇温工程を開始する。昇温工程では、処理槽7内雰囲
気温度を殺菌温度である120℃となるように加熱制御
弁2の開閉を制御し、含気容器6を殺菌温度まで加熱す
る。また、運転制御装置1は処理槽7内の圧力が含気容
器6内の圧力に近い値で変化する用に、加圧弁5及び減
圧弁4の制御を行う。この場合、予備加熱によって各含
気容器の温度差をなくしているため、全含気容器はほぼ
同じ温度で上昇し、各含気容器間の圧力差はわずかとな
る。そのため、全含気容器内圧とほぼ等しい圧力に処理
槽内圧を制御することができ、処理槽内圧力から外れた
圧力となる含気容器はなくなる。
When the time set for the preheating is reached at the time T2, the operation control device 1 ends the preheating and starts the temperature raising step. In the temperature increasing step, the opening and closing of the heating control valve 2 is controlled so that the atmosphere temperature in the processing tank 7 becomes the sterilization temperature of 120 ° C., and the aerated container 6 is heated to the sterilization temperature. Further, the operation control device 1 controls the pressurizing valve 5 and the pressure reducing valve 4 so that the pressure in the processing tank 7 changes at a value close to the pressure in the aerated container 6. In this case, since the temperature difference between the aerated containers is eliminated by preheating, all the aerated containers rise at substantially the same temperature, and the pressure difference between the aerated containers becomes small. Therefore, the internal pressure of the processing tank can be controlled to a pressure substantially equal to the internal pressure of the entire aerated container, and there is no aerated container having a pressure outside the internal pressure of the processing tank.

【0017】その後、時間T7となり含気容器6の温度
が殺菌温度の120℃に達すると、運転制御装置1は昇
温工程から殺菌工程に移行し、含気容器6を殺菌温度に
所定時間維持することで殺菌を行う。殺菌が終了する
と、処理槽7内を冷却する冷却工程を行い、処理槽7内
から含気容器6を取り出すことで殺菌処理の工程を終了
する。
Thereafter, at time T7, when the temperature of the aerated container 6 reaches the sterilization temperature of 120 ° C., the operation control device 1 shifts from the temperature raising step to the sterilization step, and maintains the aerated container 6 at the sterilization temperature for a predetermined time. To sterilize. When the sterilization is completed, a cooling step for cooling the inside of the processing tank 7 is performed, and the sterilization processing step is completed by removing the aerated container 6 from the inside of the processing tank 7.

【0018】予備加熱を行わず、含気容器に温度差があ
る状態で昇温工程を行うと、図5に記載のように昇温工
程の中盤で圧力差が大きくなっていたが、含気容器の温
度を高める前に温度差をなくすことで、昇温工程時に各
含気容器の温度差による圧力差が発生することがなくな
り、含気容器に変形や破袋が発生することを防止でき
る。
When the temperature raising step was performed in a state where there was a temperature difference in the gas-containing container without performing the preheating, the pressure difference increased in the middle stage of the temperature raising step as shown in FIG. By eliminating the temperature difference before increasing the temperature of the container, a pressure difference due to the temperature difference of each aerated container does not occur at the time of the temperature raising step, and it is possible to prevent the deformation and breakage of the aerated container. .

【0019】なお、本実施例では予備加熱の温度を充填
温度と等しくしたが、別の値を採用してもよい。予備加
熱温度を充填温度と等しくしておいた場合は、各含気容
器での圧力差は時間T0の時点より大きくなることがな
いため、容器の変形などを確実に防止できるが、時間T
0の時点よりも圧力差が少し大きくなっても容器の変形
などが生じないのであれば、別の値を採用することがで
きる。ただし、充填温度よりも高い温度とした場合、温
度が高すぎると予備加熱の温度まで含気容器の温度を上
昇させる間に含気容器の変形が発生する恐れが発生する
ため、予備加熱の温度は圧力差が大きくなるよりも低い
温度とする必要があり、予備加熱の温度は80℃よりも
低い温度とする。また、充填温度より低い温度とした場
合、予備加熱の間に、予備加熱温度より高い温度であっ
た終期充填分を予備加熱温度まで冷却するという無駄が
生じるため、充填温度より低い温度とするのは避けた方
が方がよい。
In this embodiment, the preheating temperature is set equal to the filling temperature, but another value may be adopted. When the preheating temperature is set equal to the filling temperature, the pressure difference in each aerated container does not become larger than that at the time T0, so that deformation of the container can be reliably prevented.
Another value can be adopted as long as the container does not deform even if the pressure difference becomes slightly larger than the time point of zero. However, when the temperature is higher than the filling temperature, if the temperature is too high, the deformation of the aerated container may occur while the temperature of the aerated container is raised to the preheating temperature. Needs to be lower than the pressure difference increases, and the preheating temperature is lower than 80 ° C. Further, when the temperature is lower than the filling temperature, during the preheating, the final filling which has been higher than the preheating temperature is wasted to be cooled to the preheating temperature. Should be avoided.

【0020】[0020]

【発明の効果】本発明を実施することで、含気容器をバ
ッチ式で加熱殺菌する加熱殺菌装置において、各含気容
器の温度差に起因する含気容器の変形や破袋を防止する
ことができる。
According to the present invention, in a heat sterilization apparatus for heat-sterilizing an air-containing container in a batch system, deformation and breakage of the air-containing container caused by a temperature difference between the air-containing containers can be prevented. Can be.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明を実施する加熱殺菌装置のフロー図FIG. 1 is a flow chart of a heat sterilization apparatus for implementing the present invention.

【図2】 本発明の一実施例における温度変化の説明図FIG. 2 is an explanatory diagram of a temperature change in one embodiment of the present invention.

【図3】 図2における圧力変化の説明図FIG. 3 is an explanatory diagram of a pressure change in FIG. 2;

【図4】 従来例における温度変化の説明図FIG. 4 is an explanatory diagram of a temperature change in a conventional example.

【図5】 図4における圧力変化の説明図FIG. 5 is an explanatory diagram of a pressure change in FIG.

【符号の説明】[Explanation of symbols]

1 運転制御装置 2 加熱制御弁 3 圧力測定装置 4 減圧弁 5 加圧弁 6 含気容器 7 処理槽 8 熱交換器 9 循環ポンプ 10 コンプレッサー REFERENCE SIGNS LIST 1 operation control device 2 heating control valve 3 pressure measuring device 4 pressure reducing valve 5 pressurizing valve 6 aerated container 7 treatment tank 8 heat exchanger 9 circulation pump 10 compressor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 食品等を気体とともに密封した含気容器
を処理槽内に収容しておき、含気容器を殺菌温度まで昇
温する昇温工程、殺菌温度で所定時間維持する殺菌工
程、殺菌終了後に含気容器を冷却する冷却工程からなる
殺菌処理を行うことで、含気容器内の食品等を殺菌する
加熱殺菌装置において、殺菌処理を行う場合、まず各含
気容器の温度を均一化するために、含気容器の充填温度
以上であって80℃未満の温度で加熱する予備加熱を行
い、予備加熱終了後に殺菌処理の各工程を行うことを特
徴とする予備加熱を行う含気容器用加熱殺菌装置。
1. An air-containing container in which foods and the like are sealed together with a gas are accommodated in a treatment tank, and a heating step of raising the temperature of the air-containing container to a sterilization temperature; a sterilization step of maintaining the sterilization temperature at a sterilization temperature for a predetermined time; By performing a sterilization process consisting of a cooling step of cooling the air-containing container after completion, when performing a sterilization process in a heat sterilization device that sterilizes foods and the like in the air-containing container, first, equalize the temperature of each air-containing container. In order to perform the preheating, the preheating is performed by heating at a temperature equal to or higher than the filling temperature of the aerated container and lower than 80 ° C., and the sterilization process is performed after the completion of the preheating. For heat sterilization equipment.
【請求項2】 請求項1に記載の予備加熱を行う含気容
器用加熱殺菌装置において、予備加熱の温度を含気容器
の充填温度と等しくしたことを特徴とする予備加熱を行
う含気容器用加熱殺菌装置。
2. The preheated air-sterilized container according to claim 1, wherein the preheating temperature is equal to the filling temperature of the air-containing container. For heat sterilization equipment.
JP2001162309A 2001-05-30 2001-05-30 Heat sterilizer for gas-containing vessel for carrying out preheating Pending JP2002345446A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001162309A JP2002345446A (en) 2001-05-30 2001-05-30 Heat sterilizer for gas-containing vessel for carrying out preheating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001162309A JP2002345446A (en) 2001-05-30 2001-05-30 Heat sterilizer for gas-containing vessel for carrying out preheating

Publications (1)

Publication Number Publication Date
JP2002345446A true JP2002345446A (en) 2002-12-03

Family

ID=19005459

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001162309A Pending JP2002345446A (en) 2001-05-30 2001-05-30 Heat sterilizer for gas-containing vessel for carrying out preheating

Country Status (1)

Country Link
JP (1) JP2002345446A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011055748A (en) * 2009-09-08 2011-03-24 Toyo Seikan Kaisha Ltd Batch type retort sterilization method and apparatus
JP2013074879A (en) * 2011-09-16 2013-04-25 Tomoda Selling Kk Retort sterilization apparatus, heating apparatus, heat sterilization method, and heat treatment method
US8808638B2 (en) 2011-09-16 2014-08-19 Tomoda Selling & Sailing Co., Ltd. Retort sterilization device, heating device, heat sterilization method, and heat treatment method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011055748A (en) * 2009-09-08 2011-03-24 Toyo Seikan Kaisha Ltd Batch type retort sterilization method and apparatus
JP2013074879A (en) * 2011-09-16 2013-04-25 Tomoda Selling Kk Retort sterilization apparatus, heating apparatus, heat sterilization method, and heat treatment method
US8808638B2 (en) 2011-09-16 2014-08-19 Tomoda Selling & Sailing Co., Ltd. Retort sterilization device, heating device, heat sterilization method, and heat treatment method
US9125428B2 (en) 2011-09-16 2015-09-08 Tomoda Selling & Sailing Co., Ltd. Retort sterilization device, heating device, heat sterilization method and heat treatment method

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