JPS5966865A - Retort processing method - Google Patents
Retort processing methodInfo
- Publication number
- JPS5966865A JPS5966865A JP57173969A JP17396982A JPS5966865A JP S5966865 A JPS5966865 A JP S5966865A JP 57173969 A JP57173969 A JP 57173969A JP 17396982 A JP17396982 A JP 17396982A JP S5966865 A JPS5966865 A JP S5966865A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- retort
- temperature
- internal
- heat 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.)
- Granted
Links
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は、比較的薄い壁を有する包装容器内に密封され
た内容物、特に内部に空間を残して密封された内容物を
、容器の変形無しに加圧加熱殺菌する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides pressure and heat sterilization for the contents sealed in a packaging container having a relatively thin wall, especially the contents sealed with a space left inside, without deforming the container. Regarding how to.
加圧加熱によって包装容器内に密封された内容物を殺菌
する方法は、従来から缶詰、ビン詰食品に多く用いられ
て来ており、近年紙を基材とした酸素バリア性に優れた
レトルト可能な容器ラミコンカップ(東洋製缶(株)登
録商標)、ハイフックス(東洋製缶(株)登録商標)等
に包装された食品や、更にプラスチックビン詰医薬品等
にも漸次使用されるようになって来た。しかしながら、
紙を基材とした酸素バリア性に優れたレトルト可能な容
器、ラミコンカップ、ハイフレックス等の比較的変形し
易い壁を有する包装容器や、プラスチックビンのように
加熱時変形の生じ易い包装容器は、加圧加熱殺菌時容器
の破壊乃至変形の問題があるためその使用には制限が多
かった。The method of sterilizing the contents sealed in packaging containers by applying pressure and heating has traditionally been widely used for canned and bottled foods. Containers such as Lamicon Cups (registered trademark of Toyo Seikan Co., Ltd.) and Hyhooks (registered trademark of Toyo Seikan Co., Ltd.) have gradually come to be used for foods packaged in such containers, as well as pharmaceuticals packed in plastic bottles. It's here. however,
Packaging containers with walls that are relatively easily deformed such as paper-based retortable containers with excellent oxygen barrier properties, lamicon cups, and hyflex, and packaging containers that easily deform when heated such as plastic bottles, Due to the problem of destruction or deformation of the container during pressure and heat sterilization, there were many restrictions on its use.
加圧加熱殺菌時の包装容器の変形乃至破壊の原因は、包
装容器の内部圧力とレトルトの内部圧力との差によるも
ので、このような包装容器の変形は、内部に空間を残し
て内容物を密封した包装体(以下含気包装体しいう)に
特に発生し易い。このような問題を解決するため、従来
レトルト食品等では殆んど脱気をした状態で包装するこ
とが行なわれて来たが、商品によっては脱気包装を行う
ことが実際上困難なものが多かった。The cause of deformation or destruction of packaging containers during pressurized heat sterilization is due to the difference between the internal pressure of the packaging container and the internal pressure of the retort. This is particularly likely to occur in sealed packages (hereinafter referred to as air-containing packages). In order to solve this problem, retort foods and the like have traditionally been packaged in a deaerated state, but for some products it is actually difficult to deaerate the packaging. There were many.
このような脱気包装を行うことが困難な含気包装体の加
圧加熱殺菌法としては、従来次のような提案がある。特
公昭54−38190号によれば、加圧時と冷却時にお
いてレトルト内圧力と容器内圧力の適当なバランスを保
って加圧加熱殺菌を行う方法が提案されているが、この
方法によるときは加圧加熱殺菌に時間がかかりすぎ大量
生産に適しないという欠点があった。また特公昭56−
12100号によれば、昇温−殺菌−冷却時の包装容器
の内圧を検出し、レトルト圧を包装容器内圧より一定の
差圧だけ高く保たせながら加圧加熱殺菌を行う方法が提
供され、包装容器の内圧検出法として特公昭55−68
52号及び特公昭556853号が開示されている。As a method for pressurizing and heating sterilization of air-containing packages that are difficult to deaerate, the following proposals have been made. According to Japanese Patent Publication No. 54-38190, a method is proposed in which pressure and heat sterilization is performed by maintaining an appropriate balance between the pressure inside the retort and the pressure inside the container during pressurization and cooling. The disadvantage is that pressure and heat sterilization takes too much time and is not suitable for mass production. Also, special public service in 1982-
According to No. 12100, a method is provided in which the internal pressure of a packaging container is detected during heating, sterilization, and cooling, and pressure and heat sterilization is performed while maintaining the retort pressure higher than the packaging container internal pressure by a certain pressure difference. Special Publication 1986-1983 as a method for detecting the internal pressure of containers
No. 52 and Japanese Patent Publication No. 556853 are disclosed.
しかしながら、上記の包装容器の内圧を検出して、レト
ルトの内圧を制御する方法は優れた着想ではあるが、実
際問題としてなお包装体の変形が屡々発生し十分問題を
解決したものとはいい難いものであった。その原因の一
つは、含気包装体の包装容器の内部圧力の検出が比較的
熱容量の大きい金属製剛体(特公昭55−6852参照
)に内装されたモデル包装容器について行なわれ、この
ようにして検出された圧力は必しも殺菌処理される他の
多くの包装容器内の圧力と一致しにくいためと推定され
る。However, although the above-mentioned method of detecting the internal pressure of the packaging container and controlling the internal pressure of the retort is an excellent idea, in practice, deformation of the packaging still occurs frequently, and it is difficult to say that it has sufficiently solved the problem. It was something. One of the reasons for this is that the internal pressure of the air-containing packaging container is detected using a model packaging container that is built into a rigid metal body with a relatively large heat capacity (see Japanese Patent Publication No. 55-6852). It is presumed that this is because the pressure detected in this case does not necessarily match the pressure inside many other packaging containers that are sterilized.
本発明によれば、上記の従来法にみられたような包装容
器の変形が無く、しかも処理操作が極めて簡便な加圧加
熱殺菌法が提供される。According to the present invention, there is provided a pressure and heat sterilization method that does not cause deformation of the packaging container as seen in the above-mentioned conventional methods and is extremely simple in processing operations.
本発明は、レトルトの内部圧力を包装容器の内部圧力と
凡そ平衡に保つよう制御する包装内容物の加圧加熱殺菌
法において、包装容器の内部温度を検出し、検出された
温度に基いてレトルトの内部圧力を制御する包装内容物
の加熱殺菌法に関する。The present invention detects the internal temperature of the packaging container in a pressure and heat sterilization method for packaging contents, which controls the internal pressure of the retort to approximately maintain equilibrium with the internal pressure of the packaging container. This invention relates to a method for heat sterilization of package contents by controlling the internal pressure of the package.
本明細書で、レトルトの内部圧力を包装容器の内部圧力
と「凡そ平衡に保つ」とは、レトルトの内部圧力を包装
容器の内部圧力の+1Okg/cm2〜−3kg/cm
2の範囲内、好ましくは+5kg/cm2〜−2kg/
cm2の範囲内、最も好ましくは+0.2kg/cm2
〜−02kg/cm2の範囲内に保つ意味で用いるもの
である。レトルトの内部圧力が包装容器の内部圧力の+
10kg/cm2を越えて高すぎたり、また−3kg/
cm2未満と低すぎては包装容器に永久変形を生じるの
で好ましくない。In this specification, "maintaining the internal pressure of the retort approximately in equilibrium" with the internal pressure of the packaging container means that the internal pressure of the retort is +10 kg/cm2 to -3 kg/cm of the internal pressure of the packaging container.
Within the range of 2, preferably +5kg/cm2 to -2kg/cm2
cm2, most preferably +0.2 kg/cm2
It is used to maintain the weight within the range of ~-02 kg/cm2. The internal pressure of the retort is + the internal pressure of the packaging container.
Too high, exceeding 10kg/cm2, or -3kg/cm2
If it is too low, less than cm2, the packaging container will be permanently deformed, which is not preferable.
本発明で包装容器の内部温度を検出する方法は、熱電対
、抵抗温度計、磁性温度計、電気容量温度計、トランジ
スタIC温度計、弾性温度計、放射温度計、熱雑音利用
温度計、螢光温度計等による方法が用いられるが、中で
も熱電対を用いる方法が好ましい。The method of detecting the internal temperature of a packaging container in the present invention includes a thermocouple, a resistance thermometer, a magnetic thermometer, a capacitance thermometer, a transistor IC thermometer, an elastic thermometer, a radiation thermometer, a thermometer using thermal noise, and a firefly thermometer. A method using a light thermometer or the like is used, but a method using a thermocouple is particularly preferred.
本発明では、熱電対等によって測定された包装容器の内
部温度における包装容器の内部圧力を、予め準備してお
いた温度−圧カの変換曲線により求め、この値にレトル
トの内部圧力を保つものである。このような変換曲線は
、包装容器の種類、包装内容物の種類及び内容物の充填
率(内容物が包装容器に占める容積占有率%)によって
も異なるので、加圧加熱殺菌が施される包装体毎に設定
される。In the present invention, the internal pressure of the packaging container at the internal temperature of the packaging container measured by a thermocouple or the like is determined from a temperature-pressure conversion curve prepared in advance, and the internal pressure of the retort is maintained at this value. be. Such conversion curves vary depending on the type of packaging container, the type of packaging contents, and the filling rate of the contents (% of the volume occupied by the contents in the packaging container). Set for each body.
変換曲線の設定は、レトルトの内部圧力が包装容器の内
部圧力と凡そ平衡を保つものであれば、どの様な方法に
よって設定されてもよい。例えば、包装体の包装容器の
一部(例えば蓋等、以下変形部という)を可逆的に変形
容易材料で構成したモデル包装体を、内部を肉眼観察で
きるレトルト内に入れ、20℃より5℃毎に昇温加熱し
、各温度において上記変形部が変形を起さないレトルト
圧を実測しその上限と下限の圧力の平均値を求め、その
温度に於ける包装容器の内部圧力(近似値)とする。こ
のようにし20℃〜160℃の間に亘って5℃毎に温度
−圧力の変換曲線が求められる。The conversion curve may be set by any method as long as the internal pressure of the retort is approximately balanced with the internal pressure of the packaging container. For example, a model package in which a part of the packaging container (for example, a lid, etc., hereinafter referred to as the deformable part) is made of a reversibly deformable material is placed in a retort where the inside can be observed with the naked eye, and the package is heated to 5°C from 20°C. Measure the retort pressure at which the deformation part does not deform at each temperature, calculate the average value of the upper and lower limit pressures, and calculate the internal pressure of the packaging container at that temperature (approximate value). shall be. In this way, a temperature-pressure conversion curve is obtained every 5°C from 20°C to 160°C.
本発明の好適な実施態様においては、変換曲線は上記の
ように実験的に求める必要は必しもなく、次の様な変換
曲線が好適に用いられる。即ちここでT;圧力制御卸用
熱電対の検出温度(°K)P:温度Tにおけるレトルト
釜内圧力
(kg/cm2)
ρ293;293°Kにおける水の密度ρT;温度Tに
おける水の密度
Aw;充填内容品の水分活性
PWT;温度Tにおける飽和水蒸気圧(atm)H;包
装容器の容量(1とする)に対するヘッドスペースの比
率である。In a preferred embodiment of the present invention, the conversion curve does not necessarily need to be determined experimentally as described above, and the following conversion curve is preferably used. That is, here, T: Temperature detected by the pressure control wholesale thermocouple (°K) P: Pressure inside the retort pot (kg/cm2) at temperature T ρ293; Density of water at 293°K ρT; Density of water Aw at temperature T ; Water activity PWT of the filled contents; Saturated water vapor pressure (atm) H at temperature T; Ratio of the head space to the capacity of the packaging container (assumed to be 1).
で表わされる曲線によって、包装容器の内部温度Pに対
応するレトルトの内部圧力Pが容易に求められる。The internal pressure P of the retort corresponding to the internal temperature P of the packaging container can be easily determined from the curve represented by .
更に好適な態様においては、変換曲線は水の温度−蒸気
圧曲線において蒸気圧値をn倍にした曲線であり、nは
包装容器の種類、包装内容物の種類及び内容物の充填率
等によって異なるので、殺菌される含気包装体毎に最適
な数字が選ばれるが、nの範囲は一般には0.5〜3.
0好ましくは0.7〜2.7、最も好ましくは0.75
〜2.5である。最適なnの選択は、前記の実験的に変
換曲線を求める方法により一点又は二点以上の適宜の温
度におけるレトルト内部圧を求め、これと水の温度−蒸
気圧曲線との相関より容易にnの数値を算出することが
できる。In a further preferred embodiment, the conversion curve is a temperature-vapor pressure curve of water, in which the vapor pressure value is multiplied by n, where n is determined by the type of packaging container, the type of package contents, the filling rate of the contents, etc. Since the number is different, the optimum number is selected for each air-containing package to be sterilized, but the range of n is generally 0.5 to 3.
0 preferably 0.7 to 2.7, most preferably 0.75
~2.5. The optimum value of n can be easily selected by determining the internal pressure of the retort at one or more appropriate temperatures using the method of experimentally determining the conversion curve described above, and by correlating this with the water temperature-vapor pressure curve. can be calculated.
本発明で包装容器の内部温度の測定は、包装内容物(固
体或いは液体)の温度の測定又は容器内のヘッドスペー
スの温度の測定によってもよいが、好ましくは、容器内
のヘッドスペースの温度の測定による。ヘッドスペース
内の気体によって測定した温度に基づき、変換曲線によ
りレトルト内部圧力を制御した方が、包装容器の変形が
より有効に防止される故である。In the present invention, the internal temperature of the packaging container may be measured by measuring the temperature of the packaged contents (solid or liquid) or by measuring the temperature of the head space within the container, but preferably by measuring the temperature of the head space within the container. By measurement. This is because deformation of the packaging container is more effectively prevented by controlling the internal pressure of the retort using a conversion curve based on the temperature measured by the gas in the head space.
次に本発明の加圧加熱殺菌法の操作の一例を第1図及び
第2図を用い具体的に説明する。Next, an example of the operation of the pressure heat sterilization method of the present invention will be specifically explained using FIGS. 1 and 2.
内容物を包装容器に密封した包装体19を、レトルト本
体1に入れ、レトルトを密閉した後、蒸気弁3を開いて
加圧蒸気を蒸気導入管2からレトルト本体1に導入して
、殺菌棚18に置かれた被殺菌包装体19の加熱を開始
する。熱電対20をヘッドスペースに装着したモデル被
殺菌包装体22の温度上昇が始まったならば、熱電対の
検出端に発生した電圧を変換器21により変換曲線(包
装容器の内温−レトルトの内圧の変換曲線)に基づいた
レトルト本体1の内圧を指示する電圧に変換する。昇温
工程ではレトルト内圧が所定内圧より高くなりすぎると
減圧弁7が自動的に作動して減圧管6から排気が行なわ
れ、一方レトルト内圧が所再内圧より低すぎると加圧弁
5が自動的に作動して空気加圧管4から圧搾空気が供給
されレトルト内圧を上昇させる。この様な操作が自動的
に繰り返されることにより、昇温工程及び殺菌工程にお
けるレトルト内圧が包装容器内圧に凡そ平衡するように
自動的に制御される。なお、レトルト内の温度の均一性
を向上させるために蒸気攪拌用ファン8が設置されてお
り、昇温工程及び殺菌工程で好適に用いられる。After putting the package 19 with the contents sealed in the packaging container into the retort main body 1 and sealing the retort, the steam valve 3 is opened to introduce pressurized steam from the steam introduction pipe 2 into the retort main body 1, and the sterilization shelf is filled. Heating of the package 19 to be sterilized placed at 18 is started. When the temperature of the model package 22 to be sterilized with the thermocouple 20 attached to the headspace begins to rise, the voltage generated at the detection end of the thermocouple is converted into a conversion curve (internal temperature of the packaging container - internal pressure of the retort) by the converter 21. The internal pressure of the retort main body 1 based on the conversion curve (conversion curve) is converted into an indicated voltage. In the temperature raising process, if the retort internal pressure becomes too high than a predetermined internal pressure, the pressure reducing valve 7 is automatically operated to exhaust air from the pressure reducing pipe 6. On the other hand, if the retort internal pressure is too low than the predetermined internal pressure, the pressurizing valve 5 is automatically activated. The compressed air is supplied from the air pressurizing pipe 4 to increase the internal pressure of the retort. By automatically repeating such operations, the internal pressure of the retort during the temperature raising process and the sterilization process is automatically controlled so as to approximately balance with the internal pressure of the packaging container. Note that a steam stirring fan 8 is installed in order to improve the uniformity of temperature within the retort, and is suitably used in the temperature raising process and the sterilization process.
殺菌工程は所定温度で所定時間、例えば120℃で15
分間行なわれる。殺菌工程を終ると、蒸気弁8が閉じて
、一次給水弁10が開き一次給水管9から冷却水が側壁
冷却管11に供給され、冷却水はシャワー状にレトルト
本体の側壁のみを主に冷却する。レトルト本体の底部に
溜った冷却水の水位が水位センサー12に達したとき、
一次給水弁10が自動的に閉じて二次給水弁14が自動
的に開き二次給水管18から冷却水がシャワー冷却管1
5に供給され、冷却水はシャワー状に降下して被殺菌包
装体19を均一に冷却する。この際レトルト底部に溜っ
た冷却水位を水位センサーによって水位センサー12の
位置に保つよう、排水弁17が自動的に開閉を繰り返す
。The sterilization process is carried out at a predetermined temperature for a predetermined time, for example at 120°C for 15
It takes place for a minute. When the sterilization process is finished, the steam valve 8 is closed, the primary water supply valve 10 is opened, and cooling water is supplied from the primary water supply pipe 9 to the side wall cooling pipe 11, and the cooling water mainly cools only the side wall of the retort body in a shower-like manner. do. When the water level of the cooling water accumulated at the bottom of the retort body reaches the water level sensor 12,
The primary water supply valve 10 automatically closes and the secondary water supply valve 14 automatically opens, allowing cooling water to flow from the secondary water supply pipe 18 to the shower cooling pipe 1.
5, the cooling water falls like a shower and uniformly cools the package 19 to be sterilized. At this time, the drain valve 17 automatically repeats opening and closing so that the cooling water level accumulated at the bottom of the retort is maintained at the position of the water level sensor 12 by the water level sensor.
この冷却工程においても、熱電対20の検出端に発生す
る電圧は、変換器21により変換曲線(包装容器の内温
−レトルト内圧の変換曲線)に基づくレトルト本体1の
内圧を指示する電圧に変換される。レトルト内圧か所定
内圧より低すぎると、加圧電磁弁5が自動的に作動して
空気加圧管4から圧搾空気が送り込まれ、レトルト内圧
が所定内圧より高すぎると減圧電磁弁7が自動的に作動
して減圧管6から排気されて減圧される。このような操
作が繰り返されて冷却工程中レトルト本体1の内圧は包
装容器1の内圧に凡そ平衡に保たれる。Also in this cooling step, the voltage generated at the detection end of the thermocouple 20 is converted by the converter 21 into a voltage indicating the internal pressure of the retort body 1 based on the conversion curve (conversion curve of packaging container internal temperature - retort internal pressure). be done. If the retort internal pressure is too low than a predetermined internal pressure, the pressurizing solenoid valve 5 will automatically operate and compressed air will be sent from the air pressurizing pipe 4. If the retort internal pressure is too high than the predetermined internal pressure, the pressure reducing solenoid valve 7 will automatically operate. When activated, exhaust is exhausted from the pressure reducing pipe 6 and the pressure is reduced. By repeating such operations, the internal pressure of the retort body 1 is kept approximately in equilibrium with the internal pressure of the packaging container 1 during the cooling process.
上記変換器21は、次のような原理に基づくものである
。The converter 21 is based on the following principle.
熱電対式温度測定センサー(銅−コンスタンタン)から
の温度信号(起電力、DCmV)は起電力伝送器により
DC電圧信号に変換され伝送される。このDC電圧信号
を特性変換器で入出力信号間の非直線特性をリニアライ
ズする。すなわち温度−圧力変換を行う。この出力信号
を、温度−圧力変換曲線をm倍して使用する場合は、感
圧調節付増幅器でm倍増幅し、かつ、または、差圧力を
加減する場合は、演算器にて加減算を行う。ここで得ら
れた信号が設定圧力信号となり、通常の電子式PID圧
力詞節装置を経て、操作量が電−空変換され、空気圧式
操作バルブを操作する。A temperature signal (electromotive force, DC mV) from a thermocouple temperature measurement sensor (copper-constantan) is converted into a DC voltage signal and transmitted by an electromotive force transmitter. This DC voltage signal is used to linearize the non-linear characteristics between the input and output signals using a characteristic converter. That is, temperature-pressure conversion is performed. When using this output signal by multiplying the temperature-pressure conversion curve by m, amplify it by m times using an amplifier with pressure-sensitive adjustment, and/or when adding or subtracting the differential pressure, add or subtract using a calculator. . The signal obtained here becomes a set pressure signal, and the operating amount is electro-pneumatically converted through a normal electronic PID pressure control device to operate the pneumatic operating valve.
なお、本発明の加圧加熱殺菌法の操作は、特公昭54−
88190号第4頁第1図に示されるレトルトを用いて
も有効に実施することが出来る。The operation of the pressurized heat sterilization method of the present invention is described in Japanese Patent Publication No. 1983-
The retort shown in FIG. 1, page 4 of No. 88190 may also be used to effectively carry out the process.
本発明の加圧加熱殺菌法が好適に応用される包装容器と
しては、プラスチックカップ状容器、紙を主体とした成
形容器、プラスチックトレイ、ラミネートトレー、プラ
スチックビン、プラスチックチューブ、薄肉金属缶、ア
ルミ蓋金属缶等であり、内容物としては、おしるこ、コ
ーヒー、ゼリー、プリン等の嗜好品類;スーブ、みそ汁
等の汁もの類:チャーハン、チキンライス、赤飯等の米
飯類;焼そば、マカロニ、日本そば等の麺類;野菜うま
に、魚大和煮、茶わんむし、春巻等の惣菜用:蒲焼、若
鶏ももやき、ミートボール、ハンバーグ等の魚の肉加工
品類;みかん、桃等の加工果物類、貝の煮付け、焼きと
り等の酒肴類;及び上記食品の外に、リンゲル液、ぶど
う糖、グルクトース等の糖液、アミノ酸液、テキストラ
ン液等の医薬用液等がある。Packaging containers to which the pressure and heat sterilization method of the present invention is suitably applied include plastic cup-shaped containers, paper-based molded containers, plastic trays, laminate trays, plastic bottles, plastic tubes, thin-walled metal cans, and aluminum lids. These are metal cans, etc., and the contents include luxury items such as oshiruko, coffee, jelly, and pudding; soups such as soup and miso soup; cooked rice such as fried rice, chicken rice, and sekihan; fried noodles, macaroni, Japanese soba, etc. Noodles; For side dishes such as vegetable umami, Yamato simmered fish, Chawanmushi, and spring rolls; Processed fish meat products such as kabayaki, young chicken momoyaki, meatballs, and hamburgers; Processed fruits such as mandarin oranges and peaches, and shellfish. In addition to the above-mentioned foods, there are also sugar solutions such as Ringer's solution, glucose, and gluctose, and pharmaceutical solutions such as amino acid solutions and Textran solutions.
実施例1.
内容積250ml、高さ85mmのポリプロピレンとエ
チレン−ビニルアルコール共重合体の積層体よりなる円
錐台形薄肉容器(東洋製缶(株)製、商品名ラミコンカ
ップ)にコーンポタージュスープ200ml充填し、ポ
リエステル−アルミフォイル−ポリプロピレンのラミネ
ート成形落し蓋(東洋製缶(株)製品)を熱圧着シール
した。該包装体を120個調製し、そのうち40個は本
発明による温度−圧力変換圧力制御方式のレトルト処理
に供した。(残りの40個は特公昭56−12100記
載の実施例と同じく剛体容器に包装体を収納し、この圧
力をレトルト釜外部で検知することにより圧力制御を行
う加圧加熱殺菌処理〔比較例1〕に、残りの40個は従
来の一定圧力方式のレトルト処理〔比較例2〕に供した
。)
まず、本発明の温度−圧力変換圧力制御レトルトを行っ
た。被殺菌包装体のうち1つには温度−圧力変換圧力制
御を行うための温度測定に用いる熱電対固定用パッキン
ググランド(エラブ社製、商品名、TCG31−1.2
)を熱電対の温度測定部位がヘッドスペースになるよう
装着し、又、もう1つには加熱殺菌に必要な温度履歴曲
線を得るための熱電対固定用パッキンググランドを熱電
対の温度測定部位が食品部になるよう装着した。Example 1. A truncated conical thin-walled container (manufactured by Toyo Seikan Co., Ltd., trade name: Lamicon Cup) made of a laminate of polypropylene and ethylene-vinyl alcohol copolymer, with an internal volume of 250 ml and a height of 85 mm, was filled with 200 ml of corn potage soup, and polyester-aluminum A foil-polypropylene laminate molded drop lid (manufactured by Toyo Seikan Co., Ltd.) was heat-pressed and sealed. 120 such packages were prepared, and 40 of them were subjected to retort treatment using the temperature-pressure conversion pressure control system according to the present invention. (The remaining 40 pieces were subjected to pressurized heat sterilization treatment in which the package was housed in a rigid container and the pressure was controlled by detecting this pressure outside the retort pot, as in the example described in Japanese Patent Publication No. 56-12100 [Comparative Example 1 ], and the remaining 40 pieces were subjected to conventional constant pressure retort treatment [Comparative Example 2].) First, the temperature-pressure conversion pressure controlled retort of the present invention was performed. One of the packages to be sterilized was equipped with a packing gland for fixing a thermocouple (manufactured by Elab, trade name, TCG31-1.2) used for temperature measurement to perform temperature-pressure conversion pressure control.
) is attached so that the temperature measurement part of the thermocouple is in the head space, and the other is a packing gland for fixing the thermocouple to obtain the temperature history curve necessary for heat sterilization. It was attached to become the food section.
該包装体を温度−圧力変換圧力制御装置を備えたレトル
トに収納した。熱電対固定用パッキンググランドを装着
した包装体には、圧力制御用熱電対(銅−コンスタンタ
ン:エラブ社製、商品名、DCK33−1.2)と温度
測定用熱電対(銅−コンスタンタン:エラブ社製、商品
名、DCK33−1.2)を挿入固定した。熱電対はシ
リコンゴムで被覆されたリード線でレトルトの外に出し
、圧力制御装置と温度記録計(エラブ社製、商品名、Z
4FD)に接続した。The package was placed in a retort equipped with a temperature-pressure conversion pressure control device. The package equipped with the packing gland for fixing the thermocouple contains a thermocouple for pressure control (copper-constantan, manufactured by Elab, trade name: DCK33-1.2) and a thermocouple for temperature measurement (copper-constantan, manufactured by Elab). (trade name, DCK33-1.2) was inserted and fixed. The thermocouple was connected to the outside of the retort using a lead wire covered with silicone rubber, and a pressure control device and temperature recorder (manufactured by Elab, trade name, Z
4FD).
レトルトを密閉したのち、加圧蒸気をレトルト本体に導
入し、蒸気攪拌用ファンを回転させ、加圧加熱殺菌を開
始した。殺菌工程は120℃、40分行った。このとき
圧力制御に用いた温度−圧力変換曲線は水蒸気性曲線を
1.3倍(n=1.3)した曲線(第3図の曲線α)で
ある。殺菌工程終了後、加圧蒸気の導入と蒸気攪拌用フ
ァンの回転を停止し冷却工程に移行した。冷却はまず1
次冷却として、冷却水のレトルト本体への導入により生
ずる圧力制御系外の蒸気凝縮に起因の急激な圧力降下を
防止するために、レトルト本体の内側壁のみ冷却した。After the retort was sealed, pressurized steam was introduced into the retort body, a steam stirring fan was rotated, and pressurized heat sterilization was started. The sterilization process was performed at 120°C for 40 minutes. The temperature-pressure conversion curve used for pressure control at this time was a curve (curve α in FIG. 3) obtained by multiplying the water vapor curve by 1.3 times (n=1.3). After the sterilization process was completed, the introduction of pressurized steam and the rotation of the steam stirring fan were stopped, and the cooling process began. Cooling first
In the subsequent cooling, only the inner wall of the retort body was cooled in order to prevent a sudden pressure drop caused by steam condensation outside the pressure control system caused by the introduction of cooling water into the retort body.
次に2次冷却としてレトルト上部の給水管よりシャワー
状に給水し被殺菌包装体を均一に冷却した。Next, as secondary cooling, water was supplied in a shower form from the water supply pipe at the top of the retort to uniformly cool the packages to be sterilized.
このレトルト処理時におけるレトルト釜内温度(第4図
曲線1)と包装体内温度(第4図曲線2)は第4図に示
す如く終始し、又、レトルト釜内圧力は第5図に示す如
き圧力変化を示した。During this retort processing, the temperature inside the retort pot (curve 1 in Figure 4) and the temperature inside the package (curve 2 in Figure 4) are as shown in Figure 4, and the pressure inside the retort is as shown in Figure 5. It showed pressure change.
レトルト圧力が0kg/cm2になり、包装体内温度も
充分冷却された時点で冷却を終了して、排水工程を経て
全レトルト処理工程を完了した。レトルト釜から取り出
した包装体40個は全数処理前と全く同じ状態(0.5
mm以上の変形が全くなし)であった。When the retort pressure became 0 kg/cm2 and the temperature inside the package was sufficiently cooled, cooling was terminated, and the entire retort treatment process was completed through a drainage process. The 40 packages taken out from the retort pot were in exactly the same state as before they were processed (0.5
There was no deformation of more than mm).
比較例1. 特公昭56−12100記載のレトルト処理を行った。Comparative example 1. The retort treatment described in Japanese Patent Publication No. 56-12100 was carried out.
実施例と同様の貯湯タンクを上部に備え、レトルト本体
と給湯管と環湯管で連絡してなり、本体には加圧蒸気管
、給水管、排水管、加圧管、減圧管を有するレトルトで
、黄銅製の剛体容器に包装体を収納し、この圧力をレト
ルト釜外部で検知する如き圧力検知装置を備えたレトル
トに該包装体を収納した。The retort is equipped with a hot water storage tank similar to the example in the upper part, and is connected to the retort main body through a hot water supply pipe and a hot water ring pipe, and the main body has a pressurized steam pipe, a water supply pipe, a drain pipe, a pressurizing pipe, and a pressure reducing pipe. The package was housed in a rigid container made of brass, and the package was housed in a retort equipped with a pressure detection device for detecting this pressure outside the retort pot.
レトルトを密閉後、予め100℃に熱した熱水を貯湯タ
ンクからレトルト本体へ給湯した。給湯終了後のレトル
ト内の熱水の温度は85℃となった。その後加圧蒸気管
より加圧蒸気を導入して設定温度まで上昇させた。圧力
制御は圧力検知装置より検知した圧力に0.5kg/c
m2を加えて行った。After the retort was sealed, hot water preheated to 100°C was supplied from the hot water storage tank to the retort body. After the hot water supply was completed, the temperature of the hot water in the retort was 85°C. After that, pressurized steam was introduced from the pressurized steam pipe to raise the temperature to the set temperature. Pressure control is 0.5kg/c based on the pressure detected by the pressure detection device.
m2 was added.
ちなみに包装食品の温度が100℃のときのレトルト釜
内の圧力は2.1kg/cm2であった。Incidentally, when the temperature of the packaged food was 100°C, the pressure inside the retort pot was 2.1 kg/cm2.
120℃、30分の殺菌工程終了後、レトルト釜内の熱
水を一部環湯管で貯湯タンクに充し、給水管を通してレ
トルト釜内に冷却水を送り込んだ。After completing the sterilization process at 120° C. for 30 minutes, the hot water in the retort pot was partially filled into the hot water storage tank through the hot water pipe, and cooling water was sent into the retort pot through the water supply pipe.
このとき、釜内の温度は急速に低下し、それにともない
包装体内の温度も低下した。しかしながら、圧力検知装
置より検知された圧力はそれほど低下を示さなかった。At this time, the temperature inside the pot rapidly decreased, and the temperature inside the package also decreased accordingly. However, the pressure detected by the pressure sensing device did not show a significant decrease.
冷却を引続き行い包装体内の温度が30℃以下になって
も釜の圧力は0.5kg/cm2にまで低下しなかった
。冷却水を排水し、全レトルト工程を終了し、包装体を
レトルト釜内より取り出し検査した。包装容器の変形の
状況を第7図に示した。Xは蓋部の膨み(mm)を示し
、yは伸壁部のへこみ(mm)を示す。検査結果は下表
のようであった。Even though cooling was continued and the temperature inside the package became 30° C. or lower, the pressure in the pot did not drop to 0.5 kg/cm 2 . The cooling water was drained, the entire retort process was completed, and the package was taken out from the retort pot and inspected. Figure 7 shows the deformation of the packaging container. X indicates the bulge (mm) of the lid, and y indicates the dent (mm) of the extended wall. The test results were as shown in the table below.
・側壁部のへこみは、1個の包装体につき6個所に現れ
た。- There were 6 dents in the side wall for each package.
比較例2.
次に従来の一定圧力方式のレトルト処理を行った。該包
装体40個をレトルト本体に収納し、レトルトを密閉後
、加圧蒸気をレトルト本体に導入した。レトルト釜内の
温度が90℃に到達した時点で減圧弁を閉じて、加圧管
より空気加圧を開始した。加圧条件は1.5kg/cm
2である。温度−時間条件は120℃、80分で処理を
行った。殺菌工程終了後、加圧蒸気弁を閉じて冷却工程
へと移行した。冷却工程は冷却効率を良くするために1
次冷却としてレトルト内上部よりシャワー状に給水し残
存蒸気を完全に凝縮させた。このときレトルト圧力の急
激な低下が観察されたが瞬時に1.5kg/cm2に復
帰した。Comparative example 2. Next, conventional constant pressure retort processing was performed. Forty of the packages were housed in a retort body, and after the retort was sealed, pressurized steam was introduced into the retort body. When the temperature inside the retort pot reached 90° C., the pressure reducing valve was closed and air pressurization was started from the pressure tube. Pressure condition is 1.5kg/cm
It is 2. The temperature-time conditions were 120°C and 80 minutes. After the sterilization process was completed, the pressurized steam valve was closed and the cooling process started. The cooling process requires 1 to improve cooling efficiency.
For the next cooling, water was supplied from the upper part of the retort in the form of a shower to completely condense the remaining steam. At this time, a sudden drop in retort pressure was observed, but it instantly returned to 1.5 kg/cm2.
続いて2次冷却を行った。レトルト内下部より給水を迅
速に行って冷却した。包装体内温度が充分に冷却された
のを確認したのち排水を開始した。Subsequently, secondary cooling was performed. Water was rapidly supplied from the lower part of the retort to cool it. After confirming that the temperature inside the package had cooled down sufficiently, drainage was started.
このときレトルト釜圧力も急速に低Fし、0kg/cm
2となった。排水が終わりレトルト処理が完了し、包装
体をレトルトから取り出したところ包装体40個の全数
に著しい永久変形が見られた。検査結果を下表に示す。At this time, the retort pot pressure also rapidly decreased to 0 kg/cm.
It became 2. When the water was drained and the retort treatment was completed, the packages were removed from the retort, and significant permanent deformation was observed in all 40 packages. The test results are shown in the table below.
・側壁部のへこみは、1個の包装体につき6個所に現れ
た。- There were 6 dents in the side wall for each package.
実施例2.
内容積250ml、高さ85mmのポリプロピレンとエ
チレンービニルアルコール共重合体の積層体よりなる円
錐台形薄肉容器(東洋製缶(株)製、商品名ラミコンカ
ップ)に小倉ぜんさい150g、白玉餅(10g」)3
個充填し、ポリエステル、アルミフォイル、ポリプロピ
レンのラミネート成形落し蓋(東洋製缶(株)製、商品
)を熱圧着シールした。このとき該包装体の充填率は6
0%であった。前記の包装体を40個調製し、うち1個
は圧力制御用熱電対の固定用バッキンググランド(エラ
ブ社製、商品名、TCG31−1.2)を熱電対の温度
測定部位がヘッドスペースになるよう装着した。Example 2. A truncated conical thin-walled container (manufactured by Toyo Seikan Co., Ltd., trade name: Lamicon Cup) made of a laminate of polypropylene and ethylene-vinyl alcohol copolymer with an internal volume of 250 ml and a height of 85 mm contains 150 g of Ogura Zensai and 10 g of Shiratama mochi. )3
They were filled individually and sealed with thermocompression with polyester, aluminum foil, and polypropylene laminate molded drop lids (manufactured by Toyo Seikan Co., Ltd.). At this time, the filling rate of the package is 6
It was 0%. Forty of the above-mentioned packages were prepared, one of which had a backing gland for fixing the pressure control thermocouple (manufactured by Elab, trade name, TCG31-1.2), and the temperature measurement part of the thermocouple was in the head space. I installed it like this.
該包装体を実施例1の本発明による温度−圧力変換圧力
制御方式のレトルト処理と回様に処理を行った。このと
きの圧力制御に用いた温度−圧力変換曲線は水蒸気圧曲
線を1.2倍(n=1.2)した曲線(第3図の曲線b
)である。全レトルト処理工程完了後、レトルト釜より
取り出した包装体40個は全数処理前と全く同じであり
、極めて優れた薄肉容器詰レトルト食品が得られた。The package was subjected to the retort treatment using the temperature-pressure conversion pressure control method according to the present invention in Example 1. The temperature-pressure conversion curve used for pressure control at this time is a curve obtained by multiplying the water vapor pressure curve by 1.2 times (n = 1.2) (curve b in Figure 3).
). After all the retort processing steps were completed, the 40 packages taken out from the retort pot were completely the same as before the processing, and an extremely excellent retort food packaged in thin-walled containers was obtained.
実施例3.
内容量710mlのポリプロピレンとエチレン−ビニル
アルコール共重合体の積層体よりなる瓶にリンゲル液5
30ml充填し、ゴムキャップで栓をしてアルミシール
した。該包装体を40個調製し、そのうち1個は圧力制
御用であり、圧力制御用熱電対の温度測定部位は液相に
なるように熱電対固定パッキンググランド(エラブ社製
、商品名、TCG31−1.2)を固定した。Example 3. Ringer's solution 5 was placed in a bottle made of a laminate of polypropylene and ethylene-vinyl alcohol copolymer with a content of 710 ml.
It was filled with 30ml, sealed with a rubber cap, and sealed with aluminum. 40 such packages were prepared, one of which was for pressure control, and a thermocouple fixing packing gland (manufactured by Elab, trade name, TCG31- 1.2) was fixed.
該包装体を、温度−圧力変換曲線を
ここでT;圧力制御用熱電対の検出温度(°K)P;温
度Tにおけるレトルト釜内圧力
(kg/cm2)
ρ293;0.998
ρT;温度Tにおける水の密度
Aw;1.0
PWT;温度Tにおける飽和水蒸気圧(atm)H;0
.25
で表わされる曲線(第6図)で圧力制御を行い、115
℃で60分の滅菌処理を実施例1の本発明による温度−
圧力変換圧力制御方式のレトルト処理と同様に処理を行
った。全レトルト処理工程完了後、レトルト釜より取り
出した包装体40個は全数処理前と同じであった。Here, the temperature-pressure conversion curve of the package is T; temperature detected by the pressure control thermocouple (°K) P; pressure inside the retort pot at temperature T (kg/cm2) ρ293; 0.998 ρT; temperature T Density of water Aw at 1.0 PWT; Saturated water vapor pressure at temperature T (atm) H; 0
.. Pressure control is performed using the curve represented by 25 (Fig. 6), and 115
The temperature according to the invention of Example 1 was sterilized for 60 minutes at -
Processing was performed in the same manner as retort processing using the pressure conversion pressure control method. After completing all the retort processing steps, the 40 packages taken out from the retort pot were the same as before the processing.
実施例4.
内容積100ml、高さ20mmのポリプロピレンとエ
チレン−ビニルアルコール共重合体の積層体よりなる薄
肉トレー(東洋製缶(株)製;商品)に、メンマ45g
充填して、ポリエステル、アルミフォイル、ポリプロピ
レンのラミネート成形落し蓋(東洋製缶(株)製;商品
)を熱圧着シールした。Example 4. 45 g of bamboo shoots was placed in a thin-walled tray (manufactured by Toyo Seikan Co., Ltd.; product) made of a laminate of polypropylene and ethylene-vinyl alcohol copolymer with an internal volume of 100 ml and a height of 20 mm.
After filling, a laminate molded drop lid (manufactured by Toyo Seikan Co., Ltd.; product) of polyester, aluminum foil, and polypropylene was sealed by thermocompression.
該包装体の充填率は30%であった。前記の包装体を1
28個調整し、そのうち1個は圧力制御用熱電対の固定
用パッキンググランド(エラブ社製;商品名、TCG3
1−1.2)を熱電対の温度測定部位がヘッドスペース
になるよう装着した。The filling rate of the package was 30%. 1 of the above packages
28 pieces were adjusted, one of which was a packing gland for fixing the thermocouple for pressure control (manufactured by Elab; trade name, TCG3).
1-1.2) was attached so that the temperature measurement site of the thermocouple was in the head space.
該包装体を、内部を肉眼観察できるレトルト内で可逆的
に変形するモデル包装体を用いて実験的に求めた温度−
圧力変換曲線で圧力の制御を行い、120℃、20分の
殺菌処理を実施例1の本発明による温度−圧カ変換圧力
制御方式のレトルト処理と同様に処理を行った。全レト
ルト工程終了後、レトルト釜より取り出した包装体8個
は全数処理前と全く同じ状態であった。Temperature determined experimentally using a model package in which the package is reversibly deformed in a retort whose interior can be observed with the naked eye.
The pressure was controlled using a pressure conversion curve, and sterilization treatment at 120° C. for 20 minutes was carried out in the same manner as the retort treatment using the temperature-pressure conversion pressure control method according to the present invention in Example 1. After all the retort steps were completed, the 8 packages taken out from the retort pot were in exactly the same condition as before they were all processed.
第1図は本発明の加圧加熱殺菌法に用いられる蒸気式レ
トルトの横断面模式図であり、第2図は同レトルトの縦
断面模図である。
1:レトルト本体
2:蒸気導入管
4:空気加圧管
9:一次給水管
11:側壁冷却管
12:水位センサー
13:二次給水管
15:シャワー冷却管
16:排水管
19:被殺菌包装体
20:熱電対
21:変換器
第3図は実施例1及び実施例2で夫々用いたn=1.3
及びn=1.2の温度−圧力変換曲線a及びbを示す。
曲線cは飽和蒸気圧曲線である。
第4図は、実施例1におけるレトルト釜内温度と包装体
内温度の時間的変化の経過を示し、第5図は実施例1に
おけるレトルト釜内圧力の時間的変化の経過を示す。
第6図は、実施例3で用いた温度−圧力変換曲線を示す
。
第7図は、比較例2及び3のレトルト処理後の包装容器
の断面図で、点線は、蓋部及び側壁部の変形の状況を示
す。
特許出願人 岸本 昭
代理人 弁理士 小田島 平吉
ほかそ名
第3図
包装V路の内虻温&(℃)
乞茨宕器−内叶系度 (°C)
時 間(分)
時間(刑
手続補正書:(口部)″。
昭和57年11月、18日
特許庁長冨 若 杉 オロ 夫 殿1、事件の表示
HjJ4u57 qlE’辱、7i’1lli;Mi
173969号2、発明の名称
レトルトAすL工→j法
3、補正をする渚
事件との関係 特許出願人
4代 理 人〒107′
明11Mの発明の詳・、11)な説7明の11刊7、補
正の内容
別紙のと))・り
唾、 fl、1.ll、II:、、、、明什J、?i:
@ :す、19〜11行QC(”・・イフツク、1ス」
とある想□
「ハイフ゛レックス」
、5市正1−る。
’呻1 :l1flflO4Q、、1.1行に1f、’
r、A1(イ+ 4.q Jとある螢、Ti(へ品」
□と訂正する。
(3) 同第7白未行に102F、Q / :ni
Jとll)る♀1” 0.2 Kp/ :rl J
に訂正する。
(4)同v、16自〒か64〜3行K [グルクト〜ス
1とある−
「フラ:り、・5=ス」
・ と〕工正す、る。
、 ti+ 171第2t*;i’<s行に130
分」とあるを□、140分」
に訂正する。
(6) 同第23頁第4行に「30分」と矛ンるケ「
40分j
に訂11:する。
□
手、続補正書(自発)
昭和58年4月28日
特許庁長官 若 杉 和 夫 殿
l事件の表示
昭和57年特許願第173969号 ′□2
、発明の名称
レトルト処理法
、 、事件と、、の関係 、、特t7 U+lfi
□人01’ T’J(神奈川県横浜市金沢区釜利谷町
4439番地の26名 称 岸 本 −昭
(氏 ン゛、)1
4代 理 人〒1tJ7
詳細な説明の欄
□″7.補□正の内容 y;+1m。とおゎ
゛ハ別 紙
(1+ 明細書の特許請求の範囲の欄の記載を以ドの
ように訂正する。
「〔特許請求の範囲]
1、 レトルトの内部圧力を包装容器の内部圧力と凡そ
平衡に保つよう制御する包装内容物の加圧加熱殺菌法に
おいて、包装容器の内部温度を検出し、検出された温度
に基いてレトルトの内部圧力を制御する包装内容物の加
圧加熱殺菌法。
2 包装容器の内部温度とレトルトの内部圧力との関係
を示す変換曲線を該包装内容物の加圧加熱殺菌処理に先
立って予め設定しておき、検出された包装容器の内部温
度に対応するレトルトの内部圧力を該変換曲線より求め
、求められた内部圧力にl/トルトの内部圧力を保つこ
とにより、レトノ[トの内部圧力を包装容器の内部圧力
と凡そ平衡に保つ特許請求の範囲第1項記載の加圧加熱
殺菌法。
3 変換曲線が水の温度−蒸気圧曲線において蒸気圧値
をn倍したものであるlr¥iYI請求の範囲第2項記
載の加圧加熱殺菌法。
4 変換曲線が式
ここで7’ : L力制御用熱電対の検出温度(°K)
P;温度1″い−おけるレトルを釜内圧力(kg 7−
)
ρ203 ; 293’J(における水の密1にρ7
・;温度7′(・でおける水の密度’tv;介、填内容
品のノド、分宿1テ1P ;温度Tl((おし)るF
li+和本カ(気1’TE (、a、 f nt )T
Jl;包装上7器の容量(1とする)に対−する−\ソ
ドスベ スの比率である
で表わされる曲線である特許請求の範囲第1)項記載の
加圧加熱殺菌法。
5 変換曲線が、変形容易なモデル包装体と内部観察可
能なt−トルトを用い、特定温度において包装容器に変
形を4[−しないレトルト内部圧力を実験的に逐次求め
たものである特許請求の範囲第2項記載の加圧加熱殺菌
法。。
6 該内部温度の検出が、包装容器のヘノドスベスで温
度測定を特徴とする特許請求の範囲第1〜5項の何れか
に記載の加圧加熱殺菌法。
7、加熱用の蒸気導入手段、加圧用の空気導入手段減圧
用の排気手段及び冷却用の水導入手段を有する加圧加熱
殺菌用レトルトにおいて、被殺菌包装体の容器内の内部
温度を検出する手段と検出された内部温度をしl・ルト
内部圧力に変換する変換手段とによつ1、該内部温度に
基いてレトルトの内部圧力を制御することを特徴とする
加圧加熱殺菌用レトルト1、J
(2)明細ν)第1O頁第1行及第26貞第6行にとあ
るを、
にI1正−i 、7. 。FIG. 1 is a schematic cross-sectional view of a steam retort used in the pressurized heat sterilization method of the present invention, and FIG. 2 is a schematic vertical cross-sectional view of the same retort. 1: Retort main body 2: Steam introduction pipe 4: Air pressurization pipe 9: Primary water supply pipe 11: Side wall cooling pipe 12: Water level sensor 13: Secondary water supply pipe 15: Shower cooling pipe 16: Drain pipe 19: Sterilized package 20 : Thermocouple 21: Converter Figure 3 shows n=1.3 used in Example 1 and Example 2, respectively.
and temperature-pressure conversion curves a and b for n=1.2. Curve c is a saturated vapor pressure curve. FIG. 4 shows the course of changes over time in the temperature inside the retort pot and the temperature inside the package in Example 1, and FIG. 5 shows the course of changes over time in the pressure inside the retort pot in Example 1. FIG. 6 shows the temperature-pressure conversion curve used in Example 3. FIG. 7 is a cross-sectional view of the packaging containers of Comparative Examples 2 and 3 after retort treatment, and dotted lines indicate deformation of the lid and side wall. Patent applicant Akira Kishimoto Agent Patent attorney Heikichi Odajima et al. Written amendment: (mouth)''. November 18, 1981 Tomi Wakasugi Oro, Director of the Patent Office 1, Indication of the incident HjJ4u57 qlE'humiliation, 7i'1lli; Mi
No. 173969 No. 2, Name of the invention Retort A S L → J Law 3, Relation to the Nagisa case to be amended Patent applicant 4 representative Attorney Person 〒107' Details of the invention of Ming 11M, 11) Explanation of Ming 7 11th issue 7, attached sheet of amendments))・Risui, fl, 1. ll, II:,,,,Akihito J,? i:
@: Su, lines 19-11 QC ("...iftsuku, 1st"
A Certain Thought □ ``High Flex'', 5 City Hall 1-1. 'Moaning 1: l1flflO4Q,, 1f in 1.1 line,'
r, A1 (I + 4.q J and a certain firefly, correct it as Ti (Heshina) □. (3) 102F, Q / :ni in the same No. 7 white line
J and ll)ru♀1" 0.2 Kp/ : rl Correct to J. (4) Same v, 16 〒 or 64-3 K =S” ・〕 》 , ti+ 171 2nd t*; 130 in i'<s row
□, correct the text "minutes" to "140 minutes". (6) On page 23, line 4, there is a statement that contradicts “30 minutes.”
Revised 11:40 minutes. □ Hand, continuation amendment (voluntary) April 28, 1980 Commissioner of the Japan Patent Office Kazuo Wakasugi Indication of the case 1982 Patent Application No. 173969'□2
, Name of the invention, Retort processing method, , Relationship between the incident, , Special t7 U+lfi
□Person 01'T'J (26th address, 4439 Kamaritani-cho, Kanazawa-ku, Yokohama-shi, Kanagawa Prefecture Name Kishimoto-Aki (Mr. N゛,)1 4th generation Toshihito〒1tJ7 Detailed explanation column□″7.Additional□ Positive content y;+1m.
゛Attachment (1+) The statement in the claims column of the specification is corrected as follows: “[Claims] 1. Maintaining the internal pressure of the retort approximately in equilibrium with the internal pressure of the packaging container In the pressure and heat sterilization method of the packaged contents, the internal temperature of the packaging container is detected and the internal pressure of the retort is controlled based on the detected temperature.2. A conversion curve showing the relationship between the internal temperature of the packaging container and the internal pressure of the retort is set in advance prior to the pressure heat sterilization treatment of the package contents, and the internal pressure of the retort corresponding to the detected internal temperature of the packaging container is determined. is determined from the conversion curve, and the internal pressure of the container is maintained at the determined internal pressure of 1/tort, thereby keeping the internal pressure of the container approximately in equilibrium with the internal pressure of the packaging container. Pressure heat sterilization method. 3 Pressure heat sterilization method according to claim 2, wherein the conversion curve is obtained by multiplying the vapor pressure value by n in the temperature-vapor pressure curve of water. 4 The pressure heat sterilization method according to claim 2. Here, 7': Detected temperature of thermocouple for L force control (°K)
P: The retort is placed at a temperature of 1" and the pressure inside the pot is (kg 7-
) ρ203 ; 293'J (ρ7 to water density 1 in
・;Density of water at temperature 7'
A patent claim that is a curve expressed by li+Japanese power (ki 1'TE (, a, f nt) T Jl; the ratio of -\sodosbeth to the capacity of the 7 containers on the packaging (assumed to be 1) The pressure and heat sterilization method described in item 1). 5. The conversion curve is obtained by experimentally successively determining the retort internal pressure that does not cause deformation of the packaging container at a specific temperature using a model package that is easily deformable and a T-tort whose interior can be observed. The pressure and heat sterilization method described in Scope 2. . 6. The pressurized and heat sterilization method according to any one of claims 1 to 5, wherein the internal temperature is measured by temperature measurement using a henodesbeth of a packaging container. 7. In a pressurized heat sterilization retort having steam introduction means for heating, air introduction means for pressurization, exhaust means for depressurization, and water introduction means for cooling, detecting the internal temperature inside the container of the packaged object to be sterilized. A retort for pressure and heat sterilization 1, characterized in that the internal pressure of the retort is controlled based on the internal temperature by a converting means for converting the detected internal temperature into an internal pressure. , J (2) Specification ν) It is written in the 1st line of page 1O and the 6th line of 26th page. .
Claims (7)
衡に保つよう制御する包装内容物の加圧加熱殺菌法にお
いて、包装容器の内部温度を検出し、検出された温度に
基いてレトルトの内部圧力を制御する包装内容物の加圧
加熱殺菌法1. In the pressurized and heat sterilization method for packaging contents, which controls the internal pressure of the retort to approximately maintain equilibrium with the internal pressure of the packaging container, the internal temperature of the packaging container is detected, and the internal pressure of the retort is adjusted based on the detected temperature. Controlled pressure and heat sterilization method for packaged contents
を示す変換曲線を該包装内容物の加圧加熱殺菌処理に先
立って予め設定しておき、検出された包装容器の内部温
度に対応するレトルトの内部圧力を該変換曲線より求め
、求められた内部圧力にレトルトの内部圧力を保つこと
により、レトルトの内部圧力を包装容器の内部圧力と凡
そ平衡に保つ特許請求の範囲第1項記載の加圧加熱殺菌
法。2. A conversion curve showing the relationship between the internal temperature of the packaging container and the internal pressure of the retort is set in advance prior to the pressure heat sterilization treatment of the package contents, and the conversion curve of the retort corresponding to the detected internal temperature of the packaging container is set in advance. Pressurization according to claim 1, in which the internal pressure of the retort is kept approximately in equilibrium with the internal pressure of the packaging container by determining the internal pressure from the conversion curve and maintaining the internal pressure of the retort at the determined internal pressure. Heat sterilization method.
をn倍したものである特許請求の範囲第2項記載の加圧
加熱殺菌法。3. 3. The pressure heat sterilization method according to claim 2, wherein the conversion curve is obtained by multiplying the vapor pressure value by n in the temperature-vapor pressure curve of water.
度Tにおけるレトルト釜内圧力 (kg/cm2) ρ293;293°Kにおける水の密度ρT;温度7’
における水の密度 Aw;充填内容品の水分活性 PWT;温度Tにおける飽和水蒸気圧(atm)H;包
装容器の容量(Iとする)に対するヘッドスペースの比
率である で表わされる曲線である特許請求の範囲第2項記載の加
圧加熱殺菌法。4. The conversion curve is expressed by the following formula: T: Temperature detected by the pressure control thermocouple (°K) P: Pressure inside the retort pot at temperature T (kg/cm2) ρ293; Density of water at 293°K ρT; Temperature 7'
The density of water at Aw; water activity PWT of the filled contents; saturated water vapor pressure (atm) H at temperature T; The pressure and heat sterilization method described in Scope 2.
能なレトルトを用い、特定温度において包装容器に変形
を生じないレトルト内部圧力を実験的に逐次求めたもの
である特許請求の範囲第2項記載の加圧加熱殺菌法。5. Claim 2, wherein the conversion curve is obtained by experimentally determining the internal pressure of the retort that does not cause deformation of the packaging container at a specific temperature using a model packaging body that is easily deformable and a retort whose interior can be observed. Pressure heat sterilization method.
温度測定を特徴とする特許請求の範囲第1〜5項の何れ
かに記載の加圧加熱殺菌法。6. 6. The pressure and heat sterilization method according to any one of claims 1 to 5, wherein the detection of the internal temperature involves temperature measurement in the head space of the packaging container.
用の排気手段及び冷却用の水導入手段を有する加圧加熱
殺菌用レトルトにおいて、被殺菌包装体の容器内の内部
温度を検出する手段と検出された内部温度をレトルト内
部圧力に変換する変換手段とによって、該内部温度に基
いてレトルトの内部圧力を制御することを特徴とする加
圧加熱殺菌用レトルト。7. In a pressurized heat sterilization retort having steam introduction means for heating, air introduction means for pressurization, exhaust means for decompression, and water introduction means for cooling, means for detecting the internal temperature inside the container of the package to be sterilized; A retort for pressure and heat sterilization, characterized in that the internal pressure of the retort is controlled based on the internal temperature by means of a conversion means that converts the detected internal temperature into the retort internal pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57173969A JPS5966865A (en) | 1982-10-05 | 1982-10-05 | Retort processing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57173969A JPS5966865A (en) | 1982-10-05 | 1982-10-05 | Retort processing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5966865A true JPS5966865A (en) | 1984-04-16 |
JPH0351391B2 JPH0351391B2 (en) | 1991-08-06 |
Family
ID=15970383
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57173969A Granted JPS5966865A (en) | 1982-10-05 | 1982-10-05 | Retort processing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5966865A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS611371A (en) * | 1984-06-12 | 1986-01-07 | House Food Ind Co Ltd | Pressure-controlling process |
JPS62138158A (en) * | 1985-12-11 | 1987-06-20 | House Food Ind Co Ltd | Production of noodles put in container |
JPS62210971A (en) * | 1986-03-12 | 1987-09-17 | Hisaka Works Ltd | Cooking and sterilization of canned food |
JPH0195754A (en) * | 1987-10-06 | 1989-04-13 | Fujimori Kogyo Kk | Heat and pressure sterilization treatment method |
JPH03280954A (en) * | 1990-03-28 | 1991-12-11 | Hisaka Works Ltd | Method for preventing whitening during sterilization of infusion containers |
WO1992015335A1 (en) * | 1991-03-11 | 1992-09-17 | Hisaka Works Limited | Spray type retort sterilizer |
JPH06312012A (en) * | 1993-04-28 | 1994-11-08 | Chiyoda Manufacturing Co Ltd | Method for controlling temperature of heat sterilizing apparatus |
JP2007097524A (en) * | 2005-10-06 | 2007-04-19 | Shikoku Kakoki Co Ltd | Method for production of chilled daily dish packaged together with nitrogen-rich air |
ES2364917A1 (en) * | 2010-03-05 | 2011-09-16 | Tanio, S.A. (Solicitud Unipersonal) | Procedure for packaging and sterilizing olives and product of packed olives in packaged and sterilized salmon in metal container. (Machine-translation by Google Translate, not legally binding) |
JP2012526023A (en) * | 2009-05-08 | 2012-10-25 | ゲティンゲ ステラリゼイション アクチボラゲット | Sterilization method by controlled cooling |
-
1982
- 1982-10-05 JP JP57173969A patent/JPS5966865A/en active Granted
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS611371A (en) * | 1984-06-12 | 1986-01-07 | House Food Ind Co Ltd | Pressure-controlling process |
US4874580A (en) * | 1984-06-12 | 1989-10-17 | House Food Industrial Company Limited | Pressure-controlling method |
JPS62138158A (en) * | 1985-12-11 | 1987-06-20 | House Food Ind Co Ltd | Production of noodles put in container |
JPS62210971A (en) * | 1986-03-12 | 1987-09-17 | Hisaka Works Ltd | Cooking and sterilization of canned food |
JPH0195754A (en) * | 1987-10-06 | 1989-04-13 | Fujimori Kogyo Kk | Heat and pressure sterilization treatment method |
JPH03280954A (en) * | 1990-03-28 | 1991-12-11 | Hisaka Works Ltd | Method for preventing whitening during sterilization of infusion containers |
WO1992015335A1 (en) * | 1991-03-11 | 1992-09-17 | Hisaka Works Limited | Spray type retort sterilizer |
US5527516A (en) * | 1991-03-11 | 1996-06-18 | Hisaka Works Limited | Spray type retort sterilizer |
JPH06312012A (en) * | 1993-04-28 | 1994-11-08 | Chiyoda Manufacturing Co Ltd | Method for controlling temperature of heat sterilizing apparatus |
JP2007097524A (en) * | 2005-10-06 | 2007-04-19 | Shikoku Kakoki Co Ltd | Method for production of chilled daily dish packaged together with nitrogen-rich air |
JP2012526023A (en) * | 2009-05-08 | 2012-10-25 | ゲティンゲ ステラリゼイション アクチボラゲット | Sterilization method by controlled cooling |
EP2427221A4 (en) * | 2009-05-08 | 2014-06-04 | Getinge Sterilization Ab | Sterilization process with controlled cooling |
ES2364917A1 (en) * | 2010-03-05 | 2011-09-16 | Tanio, S.A. (Solicitud Unipersonal) | Procedure for packaging and sterilizing olives and product of packed olives in packaged and sterilized salmon in metal container. (Machine-translation by Google Translate, not legally binding) |
Also Published As
Publication number | Publication date |
---|---|
JPH0351391B2 (en) | 1991-08-06 |
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