JPH0520060B2 - - Google Patents
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- Publication number
- JPH0520060B2 JPH0520060B2 JP1227660A JP22766089A JPH0520060B2 JP H0520060 B2 JPH0520060 B2 JP H0520060B2 JP 1227660 A JP1227660 A JP 1227660A JP 22766089 A JP22766089 A JP 22766089A JP H0520060 B2 JPH0520060 B2 JP H0520060B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- pressure
- water
- container
- sterilization
- 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
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- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、ヘツドスペースを残して、カレー等
の液状食品が充填密封された、加熱殺菌処理のさ
い永久変形を起し易い壁部を備え、かつ自己保形
性を有する密封容器を回転式加圧加熱殺菌釜にて
殺菌処理する方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention comprises a wall portion that is easily permanently deformed during heat sterilization treatment and is filled and sealed with a liquid food such as curry, leaving a head space. The present invention also relates to a method of sterilizing a sealed container having self-shape retaining properties in a rotary pressure heating sterilization cauldron.
(従来の技術)
比較的大型の密封容器に充填された食品の加圧
加熱殺菌処理、所謂レトルト殺菌処理は比較的長
時間を要し、従つて内容食品の品質劣化を起こし
易い。そのため従来、液状食品が充填された比較
的大型の缶詰(例えば1号缶)の殺菌処理に対し
ては、加熱殺菌処理時間が比較的短かくて済む回
転式加圧加熱殺菌釜が好ましく用いられていた。(Prior Art) Pressure and heat sterilization treatment of foods packed in relatively large sealed containers, so-called retort sterilization treatment, takes a relatively long time and is therefore likely to cause quality deterioration of the food contents. Therefore, conventionally, for the sterilization of relatively large cans (for example, No. 1 cans) filled with liquid foods, a rotary pressurized heat sterilization pot, which requires a relatively short heat sterilization time, has been preferably used. was.
しかしながら、ヘツドスペースを残して液状食
品が充填された、加熱殺菌処理のさい永久変形を
起こし易い比較的低剛性の壁部を備え、かつ自己
保形性を有する密封容器に対しては回転式加圧加
熱殺菌釜は従来採用されていなかつた。 However, for sealed containers that are self-retaining and have relatively low rigidity walls that are prone to permanent deformation during heat sterilization, and are filled with liquid food with a head space left, rotary processing is not recommended. A pressure-heating sterilization kettle has not been used in the past.
その理由は次のように考えられる。加圧加熱殺
菌釜で加熱殺菌処理する場合に、容器内圧と殺菌
釜内の圧力に差を生ずると、比較的低剛性の壁部
に凸状又は凹状に永久変形が生じて商品価値が失
われ易く、特にこの圧力差が大きい場合にはヒー
トシール部が剥離して密封性が失なわれたり、極
端な場合は壁部が破裂する等のトラブルを生じ易
い。 The reason may be as follows. When heat sterilization is performed in a pressurized heat sterilization pot, if there is a difference between the internal pressure of the container and the pressure inside the sterilization pot, permanent deformation occurs in a convex or concave shape on the wall, which has relatively low rigidity, and the product value is lost. Particularly when this pressure difference is large, problems such as the heat-sealed portion peeling off and loss of sealing performance, or in extreme cases, the wall portion rupturing, are likely to occur.
このようなトラブルを防止するためには、密封
容器内圧と殺菌釜内圧の圧力差が実質的にないよ
うに、もしくは通常はこの圧力差を約0.3Kg/cm2
以内に保ちながら加熱殺菌処理する必要がある。 To prevent such troubles, the pressure difference between the internal pressure of the sealed container and the internal pressure of the sterilization pot must be reduced to virtually no, or normally this pressure difference must be reduced to approximately 0.3 kg/cm 2.
It is necessary to heat sterilize while keeping the temperature within the range.
しかし回転式加圧加熱殺菌釜の場合は、密封容
器が釜の軸の周りに公転しているため、上記のよ
うな圧力制御が事実上困難である。例えば殺菌釜
に覗き窓を設けて、作業員がこの覗き窓から壁部
の凹みや脹らみ等の僅かの変形を観察して、これ
らの変形が戻つて壁部が正常な形になるように、
殺菌釜の圧力を制御する方法が考えられる。しか
し容器が回転しているため壁部の僅かの変形の目
視による検出は困難であり、かりに可能である場
合も作業員の疲労が大きく、実作業への採用は困
難である。 However, in the case of a rotary pressurized heat sterilization kettle, since the sealed container revolves around the axis of the kettle, it is practically difficult to control the pressure as described above. For example, a viewing window may be installed in the sterilization pot, and workers can observe slight deformations such as dents and bulges in the wall through the viewing window, and make sure that these deformations are corrected and the wall returns to its normal shape. To,
One possible method is to control the pressure in the sterilization pot. However, since the container is rotating, it is difficult to visually detect slight deformation of the wall, and even if it is possible, the operator will be extremely fatigued, making it difficult to use in actual work.
(発明が解決しようとする課題)
本発明は、ヘツドスペースを残して液状食品が
充填された、加圧加熱殺菌処理のさい永久変形を
起こし易い壁部を備え、かつ自己保形性を有する
密封容器を、容器内圧と殺菌釜内圧の圧力差を、
壁部の永久変形や破裂等が起らない程度の僅少に
自動制御して、回転式加圧加熱殺菌釜で殺菌する
ことが可能な、密封容器の加熱殺菌方法を提供す
ることを目的とする。(Problems to be Solved by the Invention) The present invention provides a self-shape-retaining seal that is filled with a liquid food leaving a head space, has a wall portion that is susceptible to permanent deformation during pressure and heat sterilization treatment, and has a self-shape retention property. The pressure difference between the container internal pressure and the sterilization pot internal pressure,
The purpose of the present invention is to provide a heating sterilization method for sealed containers that can be sterilized in a rotary pressurized heating sterilization pot under automatic control to the extent that permanent deformation or rupture of the wall does not occur. .
(課題を解決するための手段)
本発明は、ヘツドスペースを残して液状食品が
充填された、加圧加熱殺菌処理のさい永久変形を
起こし易い壁部を備え、かつ自己保形性を有する
密封容器を、回転式加圧加熱殺菌釜にて殺菌する
方法であつて、該液状食品の代わりに水が充填さ
れている以外は該密封容器と同様のサンプル容器
を該殺菌釜に該密封容器と一緒に収納し、該殺菌
釜内の圧力を、該殺菌釜内の媒体温度Trが該サ
ンプル容器内の該水の温度Tw以上である期間
は、該サンプル容器内の該水の温度Twにおけ
る、ヘツドスペースの空気分圧Paと水の飽和蒸
気圧Pwの和に実質的に等しい圧力になるように、
かつ媒体温度Trが該サンプル容器内の水の温度
Twより低い期間は、該媒体温度Trにおける、該
ヘツドスペースの空気分圧Paと水の飽和蒸気圧
Pwの和に実質的に等しい圧力になるように、制
御することを特徴とする密封容器の加熱殺菌方法
を提供するものである。(Means for Solving the Problems) The present invention provides a self-shape-retaining hermetic seal that is filled with a liquid food leaving a head space, has a wall portion that is susceptible to permanent deformation during pressurized heat sterilization treatment, and has a self-shape retaining property. A method of sterilizing a container in a rotary pressure heating sterilization pot, in which a sample container similar to the sealed container except that water is filled instead of the liquid food is placed in the sterilization pot together with the sealed container. During the period when the medium temperature Tr in the sterilization pot is equal to or higher than the temperature Tw of the water in the sample container, the pressure in the sterilization pot is kept at the temperature Tw of the water in the sample container. so that the pressure is substantially equal to the sum of the air partial pressure Pa in the headspace and the saturated vapor pressure Pw of water.
and the medium temperature Tr is the temperature of the water in the sample container.
During the period lower than Tw, the air partial pressure Pa in the head space and the saturated vapor pressure of water at the medium temperature Tr are
The present invention provides a method for heat sterilizing a sealed container, which is characterized by controlling the pressure to be substantially equal to the sum of Pw.
本明細書において液状食品とは、常温や加熱殺
菌温度において液状を呈して、殺菌釜内で容器の
回転(公転)に伴ない容器内で流動し易い食品を
称し、液体のみよりなる調理食品もしくは固液混
合の調理食品(固体は通常細片又は小粒状、もし
くは賽の目状等である)等であつて、水を含んで
いる。液状食品として、スープ、ゼリー、シチユ
ー、ホワイトソース、カレー、スイートコーン
(ホールカーネル又はクリームスタイル)等が例
示される。 In this specification, liquid food refers to food that is liquid at room temperature or heat sterilization temperature and easily flows in the container as the container rotates (revolutions) in the sterilization pot, and refers to cooked food consisting only of liquid or It is a cooked food that is a solid-liquid mixture (the solid is usually in the form of pieces, small particles, dice, etc.) and contains water. Examples of liquid foods include soup, jelly, stew, white sauce, curry, and sweet corn (whole kernel or cream style).
壁部は、胴壁部の他に、蓋部および底壁部等を
含む。加熱殺菌処理のさい永久変形を起こし易い
壁部を備え、かつ自己保形性を有する密封容器と
しては、比較的薄いプラスチツクシート、もしく
はプラスチツクフイルムと金属箔よりなる積層体
等より成形された、カツプ状容器本体のフランジ
部に、プラスチツクフイルム、またはプラスチツ
クフイルムと金属箔を含む可撓性の積層体よりな
る蓋部をヒートシールしてなる成形容器、あるい
は比較的低剛性の胴壁部を有するプラスチツクボ
トル、あるいは絞り−しごき成形缶等が例示され
る。密封容器としては比較的大型のものが本発明
に好ましく適用されるが、比較的小型であつても
よい。 In addition to the body wall, the wall includes a lid, a bottom wall, and the like. A self-shape-retaining sealed container with a wall that is susceptible to permanent deformation during heat sterilization may be a cup made of a relatively thin plastic sheet or a laminate of plastic film and metal foil. A molded container in which a lid made of plastic film or a flexible laminate containing plastic film and metal foil is heat-sealed to the flange of the container body, or a plastic container having a body wall with relatively low rigidity. Examples include bottles, drawn and ironed cans, and the like. Although a relatively large sealed container is preferably applied to the present invention, a relatively small sealed container may also be used.
(作 用)
回転式加圧加熱殺菌内において、液状食品12
を収納した密封容器10は、軸9a(第2図参照)
の軸線周りに第1図aに示すように回転(公転)
して、食品12は流動撹拌され、ヘツドスペース
10cの接する主な壁部部分は、蓋部10b、胴
部10d、底部10e、胴部10dと連続的に変
化する。そしてヘツドスペース10cに接する壁
部部分の内側には液状食品12の薄層12aが形
成される。(Function) In the rotary pressure heating sterilization, liquid food 12
The sealed container 10 containing the shaft 9a (see Fig. 2)
Rotation (revolution) around the axis of as shown in Figure 1 a
As a result, the food 12 is fluidized and agitated, and the main wall portions in contact with the head space 10c change continuously to include a lid portion 10b, a body portion 10d, a bottom portion 10e, and a body portion 10d. A thin layer 12a of the liquid food 12 is formed inside the wall portion in contact with the head space 10c.
液状食品12の加熱期間、すなわちTrTF
(TW)の間(第4図参照、時間t2までの期間)
は、この薄層12aの方が液状食品12の、温度
センサ31が挿入された中心部(本明細書におい
ては正立状態の中心部に対応する位置を中心部と
称する)よりも温度上昇が速いので、ヘツドスペ
ース10cの内圧は、薄層12a中の水の飽和蒸
気圧PWとヘツドスペース10c内の空気の分圧
Paの和P1(第3図参照)にほぼ等しいと見做され
る。 Heating period of liquid food 12, i.e. TrT F
(T W ) (see Figure 4, period up to time t 2 )
The temperature of this thin layer 12a is higher than that of the center of the liquid food 12 where the temperature sensor 31 is inserted (in this specification, the position corresponding to the center of the erect state is referred to as the center). Therefore, the internal pressure in the head space 10c is equal to the saturated vapor pressure P W of water in the thin layer 12a and the partial pressure of air in the head space 10c.
It is considered to be approximately equal to the sum P 1 (see Figure 3) of P a .
サンプル容器14も第1図bに示されるよう
に、密封容器10と同じ回転をし、蓋部14b、
胴部14d、底部14e等のヘツドスペース14
cと接する壁部部分の内側に水13の薄層13a
が形成される。この場合も薄層13aの方が水中
心部よりも速く加熱されるが、水13は粘性が低
く、しかも絶えず流動撹拌されているので(薄層
13aの水は水本体に移り、水本体の水は薄層1
3a中へ移動するという過程を繰返す)、薄層1
3aの温度は水13の温度、すなわち温度センサ
16の温度と実質的に等しいと考えられる。 As shown in FIG. 1b, the sample container 14 also rotates in the same manner as the sealed container 10, and the lid part 14b,
Head space 14 including trunk 14d, bottom 14e, etc.
A thin layer 13a of water 13 is placed inside the wall portion in contact with c.
is formed. In this case as well, the thin layer 13a is heated faster than the center of the water, but since the water 13 has low viscosity and is constantly being fluidized and stirred (the water in the thin layer 13a moves to the main body of water, Water is a thin layer 1
(repeat the process of moving into layer 3a), thin layer 1
It is considered that the temperature of 3 a is substantially equal to the temperature of water 13 , that is, the temperature of temperature sensor 16 .
ところで液状食品12の薄層12a中の水の温
度は、サンプル容器14の水の薄層13aの温
度、従つて水13の温度に実質的に等しいと考え
られる。また密封容器10のヘツドスペース10
c内の平均温度も薄層12aの温度従つてサンプ
ル容器14内の水13の温度にほぼ近似できると
考えられる。従つてこの期間の密封容器10の内
圧は、サンプル容器14内の水13の温度におけ
るヘツドスペースの空気分圧Paと水の飽和蒸気
圧PWの和P1にほぼ等しいと考えられる。 However, the temperature of the water in the thin layer 12a of the liquid food product 12 is considered to be substantially equal to the temperature of the thin layer 13a of water in the sample container 14, and thus the temperature of the water 13. Also, the head space 10 of the sealed container 10
It is considered that the average temperature within c can be approximately approximated to the temperature of the thin layer 12a and therefore the temperature of the water 13 in the sample container 14. Therefore, the internal pressure of the sealed container 10 during this period is considered to be approximately equal to the sum P 1 of the air partial pressure P a in the head space and the saturated vapor pressure P W of water at the temperature of the water 13 in the sample container 14 .
液状食品12が冷却期間に入り、Tr<TWにな
つたとき、密封容器10のヘツドスペース10c
に接する壁部部分の温度が媒体(冷却水)温度
Trに接近して、その近傍のヘツドスペース部分
の温度より低くなるため、ヘツドスペース10c
内の水蒸気が薄層12aに凝結して、飽和水蒸気
圧が減少し、ヘツドスペース10cにおける飽和
水蒸気圧は媒体温度Trによつて支配される。同
様にしてヘツドスペース10cの空気分圧は媒体
温度Trによつて近似される。従つてこの期間の
密封容器10の内圧は、媒体(冷却水)温度Tr
における、ヘツドスペースの空気分圧Paと水の
飽和蒸気圧PWの和P2にほぼ等しいと考えられる。 When the liquid food 12 enters the cooling period and T r <T W , the head space 10c of the sealed container 10
The temperature of the wall part in contact with is the medium (cooling water) temperature.
The temperature of the head space 10c approaches T r and becomes lower than the temperature of the nearby head space.
The water vapor in the head space 10c condenses into a thin layer 12a, reducing the saturated water vapor pressure, and the saturated water vapor pressure in the head space 10c is dominated by the medium temperature T r . Similarly, the air partial pressure in the head space 10c is approximated by the medium temperature T r . Therefore, the internal pressure of the sealed container 10 during this period is equal to the medium (cooling water) temperature T r
It is considered to be approximately equal to the sum P 2 of the air partial pressure P a in the headspace and the saturated vapor pressure P W of water.
そのため殺菌釜1内の圧力をTrTWの期間
は、サンプル容器14内の水13の温度におけ
る、ヘツドスペースの空気分圧Paと水の飽和蒸
気圧PWの和P1に実質的に等しい圧力になるよう
に、かつTr<TWの期間は、媒体温度Trにおけ
る、ヘツドスペースの空気分圧Paと水の飽和蒸
気圧PWの和に実質的に等しい圧力P2になるよう
に制御することにより、所謂等圧制御が実現され
て、密封容器10の壁部の永久変形や破裂等のト
ラブルが起こるのが防止される。 Therefore, the period of time T r T W for the pressure inside the sterilization pot 1 is substantially equal to the sum P 1 of the air partial pressure P a in the head space and the saturated vapor pressure P W of water at the temperature of the water 13 in the sample container 14. and during the period T r <T W , the pressure P 2 is substantially equal to the sum of the air partial pressure P a in the headspace and the saturated vapor pressure P W of water at the medium temperature T r . By controlling the pressure so as to achieve so-called equal pressure control, it is possible to prevent troubles such as permanent deformation and rupture of the wall of the sealed container 10 from occurring.
(実施例)
第2図において、1は熱水タイプの回転式加圧
加熱殺菌釜(所謂回転レトルト)であつて、熱水
タンク2より送られた熱水3が空間部4を残して
収納されている。5は空間部4のエア圧を所定圧
に上昇させるための加圧エア配管、6は熱水3の
温度を加熱期に上昇させるため、および所定殺菌
温度を維持するためのスチーム配管、7は熱水3
の温度を冷却期に下降させるための冷却水配管で
ある。また8は空間部4を減圧するための排気配
管である。熱水3は、図示されない循環系統を通
つて作業中循環されて、殺菌釜1における温度分
布が一様になるようになつている。(Example) In Fig. 2, 1 is a hot water type rotary pressure heating sterilization pot (so-called rotary retort), in which hot water 3 sent from a hot water tank 2 is stored leaving a space 4. has been done. 5 is a pressurized air pipe for raising the air pressure in the space 4 to a predetermined pressure; 6 is a steam pipe for raising the temperature of the hot water 3 during the heating period and maintaining a predetermined sterilization temperature; 7 is a steam pipe for raising the temperature of the hot water 3 during the heating period; hot water 3
This is a cooling water pipe for lowering the temperature during the cooling period. Further, 8 is an exhaust pipe for reducing the pressure in the space 4. The hot water 3 is circulated during operation through a circulation system (not shown) so that the temperature distribution in the sterilization pot 1 is uniform.
9はバスケツト11を収納する回転ドラムであ
つて、バスケツト11には液状食品12が充填さ
れた密封容器10(図示は省略したが多数の)、
および水13が充填された1個のサンプル容器1
4が収納されている。回転ドラム9は、図示され
ない駆動機構に設けられたギヤ9cに噛合するギ
ア9bおよびシヤフト9aによつて、一定方向
に、または左右交互に回転(通常1〜30r.p.m.)
して、密封容器10およびサンプル容器14をシ
ヤフト9aの軸線の周りに回転(公転)するよう
に構成されている。 Reference numeral 9 denotes a rotating drum for storing baskets 11, each of which includes sealed containers 10 (not shown, but in large numbers) filled with liquid food 12;
and one sample container 1 filled with water 13
4 are stored. The rotating drum 9 is rotated in a fixed direction or alternately left and right (usually 1 to 30 rpm) by a gear 9b and a shaft 9a that mesh with a gear 9c provided in a drive mechanism (not shown).
Thus, the sealed container 10 and the sample container 14 are configured to rotate (revolution) around the axis of the shaft 9a.
15は熱水3および後述の冷却水30の温度
(すなわち媒体温度)を測定するための温度セン
サであり、16はサンプル容器14に、正立状態
における水13の中心部温度を測定可能に取付け
られた温度センサである。温度センサ15の出力
(通常mvのオーダ)は増幅器17aに入力し、温
度センサ16の出力は、シヤフト9a内を通り、
スリツプリング機構19を介して増幅器17bに
入力する。なお19aはスリツプリング、19b
は固定リングである。増幅器17aおよび17b
の出力は、プログラマブル演算器20に入力す
る。 15 is a temperature sensor for measuring the temperature (i.e., medium temperature) of the hot water 3 and cooling water 30 (described later), and 16 is attached to the sample container 14 so as to be able to measure the temperature of the center of the water 13 in an upright state. temperature sensor. The output of the temperature sensor 15 (usually on the order of mv) is input to the amplifier 17a, and the output of the temperature sensor 16 is passed through the shaft 9a.
The signal is inputted to the amplifier 17b via the slip ring mechanism 19. Note that 19a is a slip ring, 19b
is a fixed ring. Amplifiers 17a and 17b
The output is input to the programmable arithmetic unit 20.
演算器20には、媒体温度(Tr)とサンプル
容器14の水13の中心部温度(TW)と比較し
て、TrTWのとき、つまりセンサ15の出力が
センサ16の出力以上の場合は、第3図(この図
については後述する)よりTWにおける水の飽和
蒸気圧PWとヘツドスペース空気分圧Paの和P1(電
圧換算値)を出力し、Tr<TWのとき、つまり温
度センサ15の出力が温度センサ16の出力より
小さい場合は、第3図より、Trにおける水の飽
和蒸気圧PWと、ヘツドスペース空気分圧Paの和
P2(電圧換算値)を出力するよう命令するプログ
ラムが、プログラマー21より入力されている。 The computing unit 20 compares the medium temperature (T r ) with the center temperature (T W ) of the water 13 in the sample container 14 and calculates that when T r T W , that is, the output of the sensor 15 is higher than the output of the sensor 16. In this case, output the sum P 1 (voltage conversion value) of the saturated vapor pressure of water P W and the headspace air partial pressure P a at T W from Fig. 3 (this figure will be explained later), and find that T r < When T W , that is, when the output of the temperature sensor 15 is smaller than the output of the temperature sensor 16 , from FIG .
A program that instructs to output P 2 (voltage conversion value) is input from the programmer 21.
演算器20よりの出力は、信号変換器(図示さ
れない)を介して、電流−空気圧変換器22に入
力し、空気信号に変換される。変換器22の出力
は圧力コントローラ23に入力し、圧力コントロ
ーラ23は、加圧エア配管5に設けられた調節弁
25を開閉して、殺菌釜1内の圧力が、上記P1
又P2と等しくなるように制御する。 The output from the calculator 20 is input to the current-air pressure converter 22 via a signal converter (not shown) and is converted into an air signal. The output of the converter 22 is input to the pressure controller 23, and the pressure controller 23 opens and closes the control valve 25 provided in the pressurized air piping 5, so that the pressure inside the sterilization pot 1 is adjusted to the above P 1
It is also controlled to be equal to P 2 .
第3図は、サンプル容器14に20℃の水13を
充填密封した場合の、温度Tr又はTWと、ヘツド
スペース空気分圧(Pa曲線)と、水の飽和蒸気
圧(PW曲線)の関係を示す。Pa曲線は、水の熱
膨脹による影響は無視できるものとして、ボイ
ル・シヤールの法則にもとづき計算により作製し
た。 Figure 3 shows the temperature T r or T W , the headspace air partial pressure (P a curve), and the saturated vapor pressure of water (P W curve) when the sample container 14 is filled with water 13 at 20°C and sealed. ). The P a curve was created by calculation based on the Boyle-Schard law, assuming that the influence of thermal expansion of water can be ignored.
密封容器10は、カツプ状の容器本体10a
と、そのフランジ部10a1(第1図参照)にヒー
トシールされた蓋部10bを備えており、内部に
ヘツドスペース10c(通常内容積に対して約10
〜40容積%)を残して、液状食品12が、この例
においては20℃において充填密封されている。 The sealed container 10 has a cup-shaped container body 10a.
It has a lid part 10b heat-sealed to its flange part 10a 1 (see Figure 1), and has a head space 10c inside (approximately 10
~40% by volume), the liquid food product 12 is filled and sealed at 20° C. in this example.
容器本体10aは、室温においては自己保形性
は有するが、加熱殺菌処理時に外圧や内圧によつ
て永久変形を起こし易い壁部より構成されてい
る。すなわち比較的薄い、例えば厚さ約0.4〜1.0
mmの、ポリプロピレンシート、もしくはポリプロ
ピレン−カルボン酸変性ポリプロピレン−エチレ
ン・ヒニールアルコール共重合体−カルボン酸変
性ポリプロピレン−ポリプロピレンの5層よりな
る積層体等のプラスチツク積層シート、あるいは
ポリオレフイン(例えばポリプロピレン)−接着
剤層(例えばポリウレタン系の)−金属箔(例え
ばアルミニウム箔)よりなる積層体、または金属
箔単体等よりなるブランクを真空成形やプレス成
形等によつて成形することによつて形成される。
蓋部10bも前述の如き材料より形成されてい
る。 The container main body 10a has a self-shape retaining property at room temperature, but is composed of a wall portion that is susceptible to permanent deformation due to external pressure or internal pressure during heat sterilization treatment. i.e. relatively thin, e.g. about 0.4 to 1.0 thick
mm, polypropylene sheet, or a plastic laminate sheet such as a 5-layer laminate of polypropylene-carboxylic acid-modified polypropylene-ethylene/hynyl alcohol copolymer-carboxylic acid-modified polypropylene-polypropylene, or polyolefin (e.g. polypropylene)-adhesive It is formed by vacuum forming, press forming, etc., a laminate consisting of an agent layer (eg, polyurethane-based) and metal foil (eg, aluminum foil), or a blank consisting of a single metal foil.
The lid portion 10b is also made of the above-mentioned material.
本実施例の場合、密封容器10の1つに、液状
食品12の中心部温度を測定可能の温度センサ3
1が挿入されており、その出力はスリツプリング
機構19を介して、殺菌条件を設定するための温
度記録計(図示されない)に記録されるようにな
つている。実作業の場合は、既に殺菌条件は設定
されているため、必ずしも温度センサ31を挿入
する必要はない。 In the case of this embodiment, one of the sealed containers 10 is equipped with a temperature sensor 3 capable of measuring the temperature at the center of the liquid food 12.
1 is inserted, and its output is recorded via a slip ring mechanism 19 on a temperature recorder (not shown) for setting sterilization conditions. In the case of actual work, since the sterilization conditions have already been set, it is not necessarily necessary to insert the temperature sensor 31.
サンプル容器14の容器本体14aおよび蓋部
14b(第1図b参照)はそれぞれ、密封容器1
0の容器本体10aおよび蓋部10bと同一のも
のから形成されている。サンプル容器14のヘツ
ドスペース14c(第1図b)の容積も、密封容
器10のヘツドスペース10cのそれと等しい。 The container body 14a and the lid part 14b (see FIG. 1b) of the sample container 14 are respectively connected to the sealed container 1.
It is formed from the same material as the container body 10a and lid portion 10b of No. 0. The volume of the head space 14c (FIG. 1b) of the sample container 14 is also equal to that of the head space 10c of the sealed container 10.
以上の装置により、密封容器10内の液状食品
12の加熱殺菌処理は次のようにして行なわれ
る。 Using the above-described apparatus, heat sterilization of the liquid food 12 in the sealed container 10 is carried out as follows.
1個のサンプル容器14および多数の密封容器
10を収納したバスケツト11を回転式加圧加熱
殺菌釜1の回転ドラム9に装入し、温度センサ1
6および31をスリツプリング19aに接続す
る。 The basket 11 containing one sample container 14 and a large number of sealed containers 10 is loaded into the rotating drum 9 of the rotary pressure heating sterilization pot 1, and the temperature sensor 1
6 and 31 are connected to the slip ring 19a.
次に送湯弁33を開いて、熱水タンク2より殺
菌釜1に熱水3を所定レベルまで送入し、回転ド
ラム9を所定回転数で回転する。その後スチーム
配管6の開閉弁28を開いて、スチームを送つて
熱水3を加熱殺菌温度Trn(Trの最高温度;第4
図参照)まで加熱する。熱水温度がTrnに達した
ら開閉弁27を開閉して温度コントロールを行な
う。また熱水送入後から図示されない循環ポンプ
を動作させて、熱水3を循環系統(図示されな
い)を通つて殺菌釜1の中を循環させる。その間
熱水3のレベルはバスケツト11より上方の所定
レベルに保持されるようにする。 Next, the hot water supply valve 33 is opened, hot water 3 is supplied from the hot water tank 2 to the sterilizing pot 1 to a predetermined level, and the rotary drum 9 is rotated at a predetermined number of rotations. Thereafter, the on-off valve 28 of the steam pipe 6 is opened, and steam is sent to sterilize the hot water 3 at a temperature T rn (maximum temperature of T r ;
(see figure). When the hot water temperature reaches Trn , the on-off valve 27 is opened and closed to control the temperature. After the hot water is delivered, a circulation pump (not shown) is operated to circulate the hot water 3 through the sterilization pot 1 through a circulation system (not shown). During this time, the level of the hot water 3 is maintained at a predetermined level above the basket 11.
密封容器10は第1図に示すように、回転ドラ
ム9の回転と共にシヤフト9aの軸線の周りに公
転し、その中の液状食品12は流動撹拌されなが
ら加熱される。液状食品12の中心部温度(温度
センサ31の温度)が上昇し、所定の殺菌値F0
を満足する時間t2(第4図参照;密封容器の1つ
に温度センサ31を挿入しない場合の時間t2は予
め実験により定めておく)に達したら、開閉弁2
8を閉じ、冷却水配管7の開閉弁26を開いて冷
却水30を送入して、それまでの熱水3と混合し
ながら(その間熱水3を熱水タンク2に戻して)
冷却する。 As shown in FIG. 1, the sealed container 10 revolves around the axis of the shaft 9a as the rotating drum 9 rotates, and the liquid food 12 therein is heated while being fluidized and stirred. The temperature at the center of the liquid food 12 (the temperature measured by the temperature sensor 31) rises, and the predetermined sterilization value F 0
When the time t 2 (see Fig. 4; the time t 2 when the temperature sensor 31 is not inserted into one of the sealed containers is determined in advance by experiment) is reached, the on-off valve 2 is closed.
8, open the on-off valve 26 of the cooling water pipe 7 to feed the cooling water 30, and mix it with the hot water 3 (while returning the hot water 3 to the hot water tank 2).
Cooling.
この間の加熱冷却サイクルの例を第4図に示
す。密封容器10内の液状食品12の温度TFは
温度センサ31にもとづくものであるが、温度
TFの上昇が温度TWのそれより遅いのは、液状食
品12は水13よりも粘度が高いので、回転によ
る撹拌による容器壁部から食品内部までの熱伝達
が、水の場合よりも小さいことによるものと考え
られる。また温度TFの上昇曲線が波状になつて
いるのは、内容品温度が均一でないので、回転に
より温度が高い部分と低い部分がセンサに当るこ
とによると思われる。 An example of the heating/cooling cycle during this period is shown in FIG. The temperature T F of the liquid food 12 in the sealed container 10 is based on the temperature sensor 31;
The reason why T F rises slower than temperature T W is because the liquid food 12 has a higher viscosity than water 13, so the heat transfer from the container wall to the inside of the food due to rotational stirring is smaller than in the case of water. This is thought to be due to this. Also, the reason why the temperature T F rise curve is wavy is probably because the temperature of the contents is not uniform, so that high and low temperature areas hit the sensor due to rotation.
このように温度TFの上昇は温度TWのそれより
遅いので、温度TWが加熱殺菌温度Trnに達した
時点t1では温度TFはまだTrnに達しない。時点t2
まではTrTWであるが、時点t2後は、温度TWの
下降は温度Trのそれより遅れてTr<TWとなり、
温度TFの下降は温度TWのそれよりさらに遅れて
TW<TFとなる。 In this way, the temperature T F rises more slowly than the temperature T W , so at the time t 1 when the temperature T W reaches the heat sterilization temperature T rn , the temperature T F has not yet reached T rn . Time t 2
Until then, T r T W , but after time t 2 , the decrease in temperature T W lags behind that of temperature T r and becomes T r < T W.
The drop in temperature T F is even later than that in temperature T W
T W < T F.
この加熱冷却期間の密封容器10の内外の圧力
差にもとづく容器壁部の永久変形等を防止するた
め、この間プログラマブル演算器20および圧力
コントローラ23を用いて、前述の方法に従い、
殺菌釜1に送入されるエア量および殺菌釜より送
出される排気量を調節して、殺菌釜1内の圧力を
調節する。密封容器10内の液状食品12が所定
温度まで冷却された後、殺菌釜1を開き、密封容
器10およびサンプル容器14を取出す。 In order to prevent permanent deformation of the container wall due to the pressure difference between the inside and outside of the sealed container 10 during this heating and cooling period, during this period, using the programmable calculator 20 and the pressure controller 23, according to the method described above,
The pressure inside the sterilization pot 1 is adjusted by adjusting the amount of air fed into the sterilization pot 1 and the amount of exhaust air sent out from the sterilization pot 1. After the liquid food 12 in the sealed container 10 has been cooled to a predetermined temperature, the sterilization pot 1 is opened and the sealed container 10 and sample container 14 are taken out.
本発明は以上の例によつて制約されるものでな
く、例えば液状食品12および水13の充填密封
は20℃以外の温度、例えば50℃で行なつてもよ
い。ただしこの場合、ヘツドスペース部の温度が
50℃とみなせるとすると、50℃における飽和蒸気
圧PWと空気分圧Paの和P1が1気圧となるように、
第3図の空気分圧直線Paの位置を、Pa′線までず
らす必要がある。 The present invention is not limited to the above examples; for example, the filling and sealing of the liquid food 12 and water 13 may be performed at a temperature other than 20°C, for example 50°C. However, in this case, the temperature of the head space is
If it can be considered as 50℃, then the sum P 1 of saturated vapor pressure P W and air partial pressure P a at 50℃ is 1 atm.
It is necessary to shift the position of the air partial pressure straight line P a in FIG. 3 to the P a ' line.
また密封容器も、比較的薄肉のプラスチツクボ
トルを密封したものであつてもよい。さらに蒸気
−空気タイプの加圧加熱殺菌釜を用いてもよい。 The sealed container may also be a relatively thin-walled plastic bottle sealed. Furthermore, a steam-air type pressurized heat sterilization kettle may be used.
またサンプル容器14内の温度センサ16は、
水13内の適宜の位置にあつてもよい。回転のた
め水13の温度の場所による差は殆んどないから
である。 Furthermore, the temperature sensor 16 inside the sample container 14 is
It may be located at an appropriate position within the water 13. This is because there is almost no difference in the temperature of the water 13 depending on the location due to the rotation.
以下具体例について説明する。 A specific example will be explained below.
厚さ1.0mmのポリプロピレンシートより内容積
200c.c.の、カツプ状容器本体10aを形成し、20
℃においてカレー12を、50c.c.のヘツドスペース
10cを残して充填した後、フランジ部10a1に
蓋部10bをヒートシールして密封して密封容器
10を作製した。なお蓋部10bは、内層が厚さ
70μmのポリプロピレンフイルム、中間層が厚さ
9μmのアルミニウム箔、外層が厚さ12μmのポリ
エステルフイルムよりなる積層体より形成され
た。この場合蓋部10bが容器本体10aよりも
変形し易い。 Internal volume from 1.0mm thick polypropylene sheet
A cup-shaped container body 10a of 200 c.c. is formed, and 20
After filling the curry 12 with a head space 10c of 50 cc at a temperature of 10.degree. C., the lid 10b was heat-sealed to the flange 10a1 to produce a sealed container 10. Note that the inner layer of the lid portion 10b has a thickness of
70μm polypropylene film, middle layer thickness
It was formed from a laminate consisting of a 9 μm aluminum foil and an outer layer of a 12 μm thick polyester film. In this case, the lid portion 10b is more easily deformed than the container body 10a.
水13を充填した以外は前記と同様にしてサン
プル容器14を作製した。 A sample container 14 was prepared in the same manner as described above except that water 13 was filled.
サンプル容器14および密封容器10の各1個
について、それぞれ水13およびカレー12の中
心部に熱電対よりなる温度センサ16および31
を取付け、温度センサ16,31と容器壁部の間
を、アタツチメントにより密封した。 Temperature sensors 16 and 31 each consisting of a thermocouple are installed in the center of the water 13 and curry 12 for each of the sample container 14 and the sealed container 10.
was attached, and the space between the temperature sensors 16, 31 and the container wall was sealed with an attachment.
上記温度センサ付、サンプル容器14および密
封容器10、ならびに温度センサを取付けられな
い通常の同様な密封容器10を800個バスケツト
11に載置後、第2図に示すタイプの熱水式加圧
加熱殺菌釜に収納し、センサ16,31をスリツ
プリング19aに接続した。 After placing 800 of the above sample containers 14 and sealed containers 10 with temperature sensors, as well as ordinary similar sealed containers 10 to which no temperature sensor can be attached, in the basket 11, hot water pressure heating of the type shown in FIG. 2 is carried out. It was placed in a sterilized pot, and the sensors 16 and 31 were connected to the slip ring 19a.
次に熱水タンク2より殺菌釜1に熱水3を送入
した後、回転ドラム9を毎分10回の速度で回転し
ながら、スチーム配管6の弁28を開いて、スチ
ームを送つて熱水3を120℃まで加熱した。 Next, after feeding the hot water 3 from the hot water tank 2 to the sterilizing pot 1, while rotating the rotary drum 9 at a speed of 10 times per minute, the valve 28 of the steam pipe 6 is opened to send steam and heat the water. Water 3 was heated to 120°C.
サンプル容器14の水温および密封容器10の
カレー温度が120℃に達し、カレーに対する殺菌
値F0を満足する時間経過後、弁28を閉じ、弁
26を開いて冷却水を送入し、それまでの熱水と
置換した。このときの加熱冷却サイクルを第4図
に示す。その間実施例に示すようにして殺菌釜内
圧力の等圧制御を行なつた。 After the water temperature in the sample container 14 and the curry temperature in the sealed container 10 reach 120°C and the curry sterilization value F 0 is satisfied, the valve 28 is closed and the valve 26 is opened to supply cooling water, and until then, was replaced with hot water. The heating and cooling cycle at this time is shown in FIG. During this time, the pressure inside the sterilization pot was controlled to be equal to the pressure as shown in the example.
作業中殺菌釜1の扉1aの中心に設けられた覗
き窓(図示されない)から、最近接の密封容器1
0Aの蓋部10bの変形を特別の装置により観察
したが、変形は殆んど認められなかつた。カレー
12の温度がほぼ30℃になつた後、殺菌釜を開
き、密封容器10を取出したが、全数に変形等の
異常は認められなかつた。 During operation, the nearest sealed container 1 is
Deformation of the lid portion 10b of 0A was observed using a special device, but almost no deformation was observed. After the temperature of the curry 12 reached approximately 30°C, the sterilization pot was opened and the sealed containers 10 were taken out, but no abnormality such as deformation was observed in all of them.
なお比較のため、密封容器10内の温度センサ
31の出力を増幅器17aに入力し(温度センサ
16の出力は増幅器17aに入力しない)た点以
外は前記と同様にして加熱冷却した。この場合
は、加熱期間に容器内圧の方が殺菌釜圧力よりも
遥かに低くなり、冷却期には逆に高くなつたため
と考えられるが、密封容器10の全数について、
壁部の変形(底部の膨らみや胴部の凹み等の)が
発生した。 For comparison, heating and cooling were performed in the same manner as described above, except that the output of the temperature sensor 31 inside the sealed container 10 was input to the amplifier 17a (the output of the temperature sensor 16 was not input to the amplifier 17a). In this case, it is thought that the internal pressure of the container became much lower than the sterilization pot pressure during the heating period, and conversely increased during the cooling period, but for all the sealed containers 10,
Deformation of the wall (such as a bulge in the bottom or a dent in the body) occurred.
第5図の丸点は、第4図の加熱冷却サイクルの
場合について、以上に述べた本発明の方法に従つ
て計算された容器内圧を示す。一方実線による曲
線は、密封容器10Aを上記サイクルで殺菌処理
するに当り、覗き窓より蓋部10bを観察して、
その変形が起らないように手動で殺菌釜圧力を調
節した場合の、この圧力の時間的変動を示す。両
者はよく一致していることが分る。 The circle dots in FIG. 5 indicate the container internal pressure calculated according to the method of the present invention described above for the heating/cooling cycle shown in FIG. On the other hand, the solid line curve indicates that when the lid part 10b is observed through the viewing window when the sealed container 10A is sterilized in the above cycle,
This figure shows the temporal fluctuation of the pressure in the sterilization pot when it is manually adjusted to prevent the deformation. It can be seen that the two are in good agreement.
(発明の効果)
本発明の密封容器の加熱殺菌方法は、ヘツドス
ペースを残して液状食品が充填された、加圧加熱
殺菌処理のさい永久変形を起こし易い壁部を備
え、かつ自己保形性を有する密封容器を、容器内
圧と殺菌釜内圧の圧力差を、壁部の永久変形や破
裂等が起らない程度の僅少に自動制御して回転式
加圧加熱殺菌釜で殺菌することができるという効
果を奏する。そしてこのように回転式加圧加熱殺
菌ができるので、殺菌時間が短縮でき、かつ高品
質の所謂レトルト殺菌処理食品が得られるという
メリツトを有する。(Effects of the Invention) The heat sterilization method for a sealed container of the present invention has a wall portion that is filled with a liquid food leaving a head space and is easily permanently deformed during pressurized heat sterilization treatment, and is self-shape-retaining. It is possible to sterilize a sealed container with a rotary pressurized heat sterilizer by automatically controlling the pressure difference between the internal pressure of the container and the internal pressure of the sterilizer to a small level that does not cause permanent deformation or rupture of the wall. This effect is achieved. Since rotary pressure heat sterilization can be performed in this manner, it has the advantage that sterilization time can be shortened and high quality so-called retort sterilized foods can be obtained.
第1図aおよびbはそれぞれ、本発明の方法に
おいて密封容器およびサンプル容器が回転する状
態を示す説明用縦断面図、第2図は本発明を実施
するための装置の例を示す説明用図面、第3図は
容器のヘツドスペースにおける空気分圧および飽
和水蒸気圧と温度との関係の例を示す線図、第4
図は回転式加圧加熱殺菌釜内の媒体温度、サンプ
ル容器内の水温および密封容器内の液状食品の中
心部温度の関係の例を示す線図、第5図は本発明
の方法に基づいて計算された密封容器の内圧、お
よび密封容器に変形が生じない殺菌釜圧力と時間
との関係を示す線図である。
1…回転式加圧加熱殺菌釜、3…熱水(媒体)、
10…密封容器、10b…蓋部(壁部)、10c
…ヘツドスペース、10d…胴部(壁部)、10
e…底部(壁部)、12…液状食品、13…水、
14…サンプル容器、30…冷却水(媒体)。
Figures 1a and b are explanatory longitudinal cross-sectional views showing the state in which a sealed container and a sample container are rotated in the method of the present invention, respectively, and Figure 2 is an explanatory drawing showing an example of an apparatus for carrying out the present invention. , Figure 3 is a diagram showing an example of the relationship between air partial pressure and saturated water vapor pressure in the head space of the container and temperature.
The figure is a diagram showing an example of the relationship between the medium temperature in the rotary pressurized heat sterilization pot, the water temperature in the sample container, and the temperature at the center of the liquid food in the sealed container. FIG. 3 is a diagram showing the relationship between the calculated internal pressure of the sealed container and the sterilization pot pressure at which no deformation occurs in the sealed container and time. 1... Rotary pressure heating sterilization pot, 3... Hot water (medium),
10... Sealed container, 10b... Lid part (wall part), 10c
...Head space, 10d...Body (wall), 10
e...bottom (wall), 12...liquid food, 13...water,
14...Sample container, 30...Cooling water (medium).
Claims (1)
た、加圧加熱殺菌処理のさい永久変形を起こし易
い壁部を備え、かつ自己保形性を有する密閉容器
を、回転式加圧加熱殺菌釜にて殺菌する方法であ
つて、該液状食品の代わりに水が充填されている
以外は該密封容器と同様のサンプル容器を該殺菌
釜に該密封容器と一緒に収納し、該殺菌釜内の圧
力を、該殺菌釜内の媒体温度Trが該サンプル容
器内の該水の温度Tw以上である期間は、該サン
プル容器内の該水の温度Twにおける、ヘツドス
ペースの空気分圧Paと水の飽和蒸気圧Pwの和に
実質的に等しい圧力になるように、かつ媒体温度
Trが該サンプル容器内の水の温度Twより低い期
間は、該媒体温度Trにおける、該ヘツドスペー
スの空気分圧Paと水の飽和蒸気圧Pwの和に実質
的に等しい圧力になるように、制御することを特
徴とする密封容器の加熱殺菌方法。1. A closed container that is filled with liquid food leaving a head space, has a wall that is susceptible to permanent deformation during pressure and heat sterilization treatment, and has self-shape properties, is placed in a rotary pressure and heat sterilization pot. In this sterilization method, a sample container similar to the sealed container except that water is filled instead of the liquid food is stored in the sterilization pot together with the sealed container, and the pressure inside the sterilization pot is reduced. , during the period when the medium temperature Tr in the sterilization pot is higher than the temperature Tw of the water in the sample container, the air partial pressure Pa in the head space and the saturated vapor of water at the temperature Tw of the water in the sample container so that the pressure is substantially equal to the sum of the pressures Pw, and the medium temperature
During the period when Tr is lower than the temperature Tw of the water in the sample container, the pressure is substantially equal to the sum of the air partial pressure Pa and the saturated vapor pressure Pw of water in the headspace at the medium temperature Tr. A method of heat sterilization of a sealed container characterized by controlling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22766089A JPH0391468A (en) | 1989-08-31 | 1989-08-31 | Method for heating and sterilizing sealed vessel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22766089A JPH0391468A (en) | 1989-08-31 | 1989-08-31 | Method for heating and sterilizing sealed vessel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0391468A JPH0391468A (en) | 1991-04-17 |
| JPH0520060B2 true JPH0520060B2 (en) | 1993-03-18 |
Family
ID=16864342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22766089A Granted JPH0391468A (en) | 1989-08-31 | 1989-08-31 | Method for heating and sterilizing sealed vessel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0391468A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE1016086A3 (en) * | 2004-05-10 | 2006-02-07 | Dethier Livin Fernand Georges | DEVICE FOR ROLLING UP AND unwinding HOSES, CABLES OR THE LIKE. |
| EP3875953B1 (en) * | 2020-03-06 | 2023-07-12 | DMK Deutsches Milchkontor GmbH | Accelerated storage test |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53142549A (en) * | 1977-05-19 | 1978-12-12 | Toppan Printing Co Ltd | Pressure and heat pasteurizing method and apparatus |
| JP3067776B2 (en) * | 1987-10-06 | 2000-07-24 | 藤森工業株式会社 | Heat and pressure sterilization method |
| JPH01202275A (en) * | 1988-02-09 | 1989-08-15 | Steeltin Can Corp | Method and for sterilizing food at low temperature |
-
1989
- 1989-08-31 JP JP22766089A patent/JPH0391468A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0391468A (en) | 1991-04-17 |
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