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JPS6017539B2 - Continuous sterilization method - Google Patents

Continuous sterilization method

Info

Publication number
JPS6017539B2
JPS6017539B2 JP55122219A JP12221980A JPS6017539B2 JP S6017539 B2 JPS6017539 B2 JP S6017539B2 JP 55122219 A JP55122219 A JP 55122219A JP 12221980 A JP12221980 A JP 12221980A JP S6017539 B2 JPS6017539 B2 JP S6017539B2
Authority
JP
Japan
Prior art keywords
sterilized
gas phase
sterilization
dish
main body
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
Application number
JP55122219A
Other languages
Japanese (ja)
Other versions
JPS5749452A (en
Inventor
好己 寺島
洋 穐利
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Seikan Group Holdings Ltd
Original Assignee
Toyo Seikan Kaisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyo Seikan Kaisha Ltd filed Critical Toyo Seikan Kaisha Ltd
Priority to JP55122219A priority Critical patent/JPS6017539B2/en
Publication of JPS5749452A publication Critical patent/JPS5749452A/en
Publication of JPS6017539B2 publication Critical patent/JPS6017539B2/en
Expired legal-status Critical Current

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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)

Description

【発明の詳細な説明】 この発明は、可榛性包装容器に食品などを充填した可榛
性包装体(レトルトパウチ)からなる被殺菌物を100
℃以上の殺菌温度で、大気圧以上の圧力により連続的に
殺菌する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION This invention is a method of sterilizing an object to be sterilized consisting of a flexible packaging body (retort pouch) in which a flexible packaging container is filled with food or the like.
It relates to a method of continuous sterilization using a sterilization temperature of ℃ or higher and a pressure of atmospheric pressure or higher.

一般に、可榛性包装体は、鎚語などと異なり、可榛・性
包装容器が損傷し易いので、可捺性包装体を被殺菌物と
して連続殺菌する場合には、被殺菌物を皿状容器に収容
し、皿状容器を上下複数段に積重ねた状態で搬送しつつ
加熱殺菌した後、冷却することにより、可裸性包装容器
の損傷を防いでいる。
In general, flexible packaging containers are easily damaged, unlike plastic packaging containers, so when continuously sterilizing flexible packaging as objects to be sterilized, the objects to be sterilized must be shaped like dishes. Damage to the peelable packaging container is prevented by storing it in a container and heating and sterilizing it while transporting the dish-shaped containers stacked in multiple tiers, followed by cooling.

このような連続殺菌方法として、可榛性包装体からなる
被殺菌物を収容した皿状容器を上下複数段に積重ねたも
のを、装置本体外から装置本体内に設けた搬送用コンベ
アに供給し、この搬送用コンベアにより前記皿状容器を
水平に保って搬送し、冷却水に満された冷却水中から装
置本体内上部の気相部を経て殺菌室に満たされた熱水中
に導き、熱水で被殺菌物を加熱殺菌した後、装置本体内
上部の前記気相部と仕切った他の気相部を経て冷却室に
満された冷却水中に導き冷却水で冷却し、その後皿状容
器を装置本体外に送出すものが、既に提案されている。
しかし、この連続殺菌方法では、被殺菌物を収容して上
下複数段に積重ねた皿状容器は、冷却水から下段の皿状
容器が上段のものに比べ遅れて気相部に出て先に熱水中
に導かれ、また熱水から遅れて気相部に出て先に冷却水
中に導かれ、上段の皿状容器は下段の皿状容器の場合の
逆になる。このため、上、下段の皿状容器に収容された
被殺菌物の熱水中での加熱殺菌時間に差ができ、したが
って微生物の死滅の程度を示すF値にも差ができてしま
う。とくに、殺菌温度が145午0、殺菌時間2分間な
ど、高温短時間殺菌の場合に、前述のF値が重要な問題
となる。この発明は、上下に積重ねられた皿状容器のど
の位置にある被殺菌物でも、同機な時間と条件で殺菌が
できるようにして、F値の不均一性をなくし、良好な連
続殺菌が行えるようにすることを目的とするものである
。この目的を達するために、この発明は、前述した連続
殺菌方法において、装置本体内の気相部のいずれか一方
に加熱用気体を供給し、被殺菌物を熱水での加熱殺菌と
実質的に同様な条件で加熱殺菌することを要旨とするも
のである。
In this continuous sterilization method, dish-shaped containers made of flexible packaging containing objects to be sterilized are stacked in multiple tiers, one above the other, and are fed from outside the device body to a conveyor installed inside the device body. The dish-shaped container is transported while being held horizontally by this transport conveyor, and is guided from the cooling water filled with the cooling water through the gas phase at the upper part of the device main body into the hot water filling the sterilization chamber. After the object to be sterilized is heated and sterilized with water, it is introduced into the cooling water filled in the cooling chamber through another gas phase section separated from the above-mentioned gas phase section in the upper part of the device main body, and then cooled with the cooling water, and then placed in a dish-shaped container. There have already been proposals for sending out the information outside the main body of the device.
However, in this continuous sterilization method, the dish-shaped containers that contain the objects to be sterilized and are stacked up and down in multiple tiers, the cooling water in the lower tier of the dish-shaped containers enters the gas phase later than the upper tier. It is introduced into the hot water, and after leaving the hot water, it exits into the gas phase and is first introduced into the cooling water, so that the upper dish-shaped container is the opposite of the lower dish-shaped container. For this reason, there is a difference in the heating sterilization time of the objects to be sterilized in the hot water stored in the upper and lower dish-shaped containers, and therefore there is also a difference in the F value indicating the degree of killing of microorganisms. In particular, in the case of high-temperature, short-time sterilization, such as at a sterilization temperature of 145 pm and a sterilization time of 2 minutes, the above-mentioned F value becomes an important issue. This invention makes it possible to sterilize objects to be sterilized at any position in dish-shaped containers stacked one above the other in the same time and under the same conditions, eliminates non-uniformity in F value, and enables good continuous sterilization. The purpose is to do so. In order to achieve this object, the present invention supplies a heating gas to either one of the gas phase parts in the apparatus main body in the continuous sterilization method described above, so that the object to be sterilized can be sterilized by heating with hot water. The gist is to heat sterilize under the same conditions as before.

以下、この発明の一実施態様につき図を参照して説明す
る。
Hereinafter, one embodiment of the present invention will be described with reference to the drawings.

第1図はこの発明による連続殺菌方法を行う装置を示す
FIG. 1 shows an apparatus for carrying out the continuous sterilization method according to the present invention.

第1図において、1は装置本体で、こ,の装置本体1内
には熱水が満たされる殺菌室2が形成され、この殺菌室
2の上面が開放された箱形室壁3が断熱材で構成され、
この室壁3外には冷却水が満される冷却室4が形成され
、装置本体1の上壁内面に設けられた仕切り10の下端
部が殺菌室2内の熱水中に浸簿されて、装置本体1内の
上部に仕切り10で仕切られた気相部9a,9bが形成
されている。装置本体1内には搬送用コンベア5が設け
られ、このコンベア5は、一部が駆動用スプロケットを
兼ねた多数のガイドホイール6に無端チェーン7が側面
ほぼ凹字形に掛けられ、無端チェーン7には多数の被殺
菌物受8が所定間隔で回動可能に吊下げられかつ常に垂
直状態が保持され、これらの被殺菌物受8が冷却室4の
冷却水−一方の気相部9a一殺菌室2の熱水−他方の気
相部.9b−冷却室4の冷却水の経路で循環されるよう
になっている。11はロータリバルプ式の圧力遮断機横
で、装置本体1の右側端整に固定されたケーシング12
のロータ13が競合自在に接合され、このロータ13に
は被殺菌物の鉄合凹所13aが円周方向に等間隔で複数
個所に形成され、ロー夕13は図示しない強制排出機構
を有している。
In Fig. 1, reference numeral 1 denotes the main body of the apparatus. A sterilization chamber 2 filled with hot water is formed in the main body 1 of the apparatus, and a box-shaped chamber wall 3 with an open upper surface is made of heat insulating material. It consists of
A cooling chamber 4 filled with cooling water is formed outside the chamber wall 3, and the lower end of a partition 10 provided on the inner surface of the upper wall of the apparatus main body 1 is immersed in hot water in the sterilization chamber 2. Gas phase portions 9a and 9b separated by a partition 10 are formed in the upper part of the apparatus main body 1. A transport conveyor 5 is provided in the main body 1 of the apparatus, and an endless chain 7 is hung around a large number of guide wheels 6, some of which also serve as drive sprockets, in a substantially concave shape on the side. A large number of objects to be sterilized 8 are rotatably suspended at predetermined intervals and are always maintained vertically. Hot water in chamber 2 - the other gas phase. 9b - The cooling water is circulated through the cooling water path of the cooling chamber 4. 11 is a casing 12 fixed to the right edge of the device body 1 next to a rotary valve type pressure breaker.
A rotor 13 is joined in a competitive manner, and a plurality of recesses 13a for objects to be sterilized are formed at equal intervals in the circumferential direction, and the rotor 13 has a forced ejection mechanism (not shown). ing.

装置本体1内の搬送用コンベア5と圧力遮断機機11と
の間の上部には送込手段14が、下部には送出手段15
がそれぞれ配設されている。圧力遮断機機11の外方に
は水槽16が設置され、この水槽16内に供給兼排出コ
ンベア17が圧力遮断機横11側が下方に位置するよう
に設けられている。圧力遮断機機1 1と供給兼排出コ
ンベァ17との間の上部には外部送込機構18が、下部
には外部送出機横19がそれぞれ設けられている。また
、20は気相部温度制御機構で、気相部9a,9bに温
度検知素子21a,21bが挿入され、これらによる検
知信号を入力として動作し、かつ演算器を組込んだ温度
、圧力制御部22が装置本体1外に設置され、右側の気
相部9aには冷却用空気管23が、左側の気相部9bに
は水蒸気および加圧空気の供給管24,25と排気管2
6が、それぞれ関口され、これらの管には前記制御部2
2からの信号で開閉される弁27,28,29,30が
それぞれ設けられている。
A feeding means 14 is provided in the upper part between the transport conveyor 5 and the pressure breaker 11 in the apparatus main body 1, and a sending means 15 is provided in the lower part.
are arranged respectively. A water tank 16 is installed outside the pressure breaker 11, and a supply/discharge conveyor 17 is provided in the water tank 16 so that the side 11 of the pressure breaker is located below. An external feed mechanism 18 is provided in the upper part between the pressure breaker machine 11 and the supply/discharge conveyor 17, and an external feed mechanism 19 is provided in the lower part. Reference numeral 20 denotes a gas phase temperature control mechanism, in which temperature detection elements 21a and 21b are inserted into the gas phase portions 9a and 9b, and the temperature and pressure control mechanism is operated by inputting detection signals from these elements and incorporates a computing unit. A cooling air pipe 23 is installed in the gas phase part 9a on the right side, and supply pipes 24 and 25 for water vapor and pressurized air, and an exhaust pipe 2 are installed in the gas phase part 9b on the left side.
6 are connected to each other, and these pipes are connected to the control section 2.
Valves 27, 28, 29, and 30 which are opened and closed by signals from 2 are provided, respectively.

なお、搬送用コンベア5、圧力遮断機横11のロータ1
3、供給兼排出コンベア17、送込手段14、送出手段
15、外部送込機構18、外部送出機機19の可動部は
周期駆動されるようになっている。
In addition, the conveyor 5, the rotor 1 next to the pressure breaker 11
3. The movable parts of the supply/discharge conveyor 17, the feed means 14, the feed means 15, the external feed mechanism 18, and the external feed machine 19 are driven periodically.

また、殺菌室2は100qo以上の熱水が、冷却室4お
よび水槽16には冷却水がそれぞれ導入、排出されるよ
うになっている。第2図、第3図は、扇平な可榛I性包
装体の搬送具の一例を示す。
Further, hot water of 100 qo or more is introduced into the sterilization chamber 2, and cooling water is introduced into and discharged from the cooling chamber 4 and the water tank 16, respectively. FIGS. 2 and 3 show an example of a conveyor for a fan-flat flexible package.

この搬送具31は可榛性包装体からなる被殺菌物を1個
ずつ仕切って複数個水平に収容した皿状容器32が上下
複数段に積重ねて着脱可能に装填される枠体33を備え
、この枠体33の両端面に回転自在に車輪34を設け、
これらの車輪34を連結棒35で連結すると共に、枠体
33の底に鍵36を固定して、常に皿状容器32が水平
に保持されるようにしたものである。次に、第1図に示
す連続殺菌装置により、第2図、第3図に示す搬送具を
用いて、連続殺菌する方法につき説明する。虎平な可榛
性包装体からなる被殺菌物を皿状容器32に収容し、こ
れらを上下複数段に積重ねて搬送臭31の枠体33に装
填する。このようにして被殺菌物を収容した搬送具31
を供給兼排出コンベア17に供給し、このコンベア17
の駆動により、前記搬送臭31を外部送込機構18を介
して圧力遮断機横11のロータ13に設けた鼓合凹所1
3aに送込む。前記ロー夕13の反時計万向の回動によ
り、搬送具31を装置本体1内に導き、ロータ13に設
けた強制排出機構により送込手段14に送込み、この送
込手段14を介して搬送用コンベア5の被殺菌物受8に
送込む。被殺菌物受8に送込まれた搬送具31は、搬送
用コソベァ5の駆動によって、皿状容器32および被殺
菌物を水平かつ上下転倒しないように保って搬送し、冷
却室4の冷却水中から気相部9aを経て殺菌室2の熱水
中に導き、この熱水で被殺菌物を加熱殺菌し、その後気
相部9bを経て冷却室4の冷却水中に導き、この冷却水
で冷却する。被殺菌物が冷却された搬送具31は、被殺
菌物受8から送出手段15に受緩され、この送出手段1
5によって圧力遮断機機11のロータ13の空の鉄合凹
所13aに送込まれる。なお、この鉄合凹所13aは殺
菌前の被殺菌物を収容した搬送具を押出して空になった
ものである。競合凹所13aに送込まれた被殺菌物の殺
菌、冷却後の搬送臭31はロータ13の回転によって装
置本体1外に導かれ、ロータ13の強制排出機構の動作
により外部送出機構19に受渡され、外部送出機構19
の動作によって供給兼排出コンベア17に送込まれ、こ
のコンベア17によって所定の場所に排出される。そし
て、搬送具の枠体から皿状容器を敗出し、さらに皿状容
器から被殺菌物を取出す。以上1つの搬送具に注目して
被殺菌物の加熱殺菌、冷却について述べたが、多数の搬
送臭について前述した加熱殺菌、冷却が連続して行われ
る。そして、前述したように搬送コンベア5によって皿
状容器および被殺菌物が常に水平状態で搬送されるので
、被殺菌物を収容して上下複数段に積重ねた状態で搬送
具31に装填された皿状容器32は、冷却水から下段の
皿状容器32が上段のものより遅れて気相部9aに出て
先に熱水中に導かれ、また熱水から遅れて気相部9bに
出て先に冷却水中に導かれることになり・、したがって
、下段の皿状容器32が上段のものに比べて熱水中に長
時間あることになる。
This conveyance tool 31 includes a frame 33 in which a plurality of dish-shaped containers 32, each containing a plurality of partitioned and horizontally housed objects to be sterilized made of flexible packaging, are stacked and removably loaded in a plurality of upper and lower stages. Wheels 34 are rotatably provided on both end faces of this frame 33,
These wheels 34 are connected by a connecting rod 35, and a key 36 is fixed to the bottom of the frame 33, so that the dish-shaped container 32 is always held horizontally. Next, a method for continuous sterilization using the continuous sterilization apparatus shown in FIG. 1 and the conveyor shown in FIGS. 2 and 3 will be explained. Objects to be sterilized made of flat flexible packaging bodies are housed in a dish-shaped container 32, stacked vertically in a plurality of tiers, and loaded into a frame 33 of a transport odor 31. The transport tool 31 containing the objects to be sterilized in this way
is supplied to the supply/discharge conveyor 17, and this conveyor 17
, the conveyed odor 31 is transferred to the drum recess 1 provided in the rotor 13 next to the pressure breaker 11 via the external feeding mechanism 18.
Send it to 3a. By counterclockwise rotation of the rotor 13, the conveying tool 31 is guided into the apparatus main body 1, and is sent to the feeding means 14 by a forced ejection mechanism provided on the rotor 13, and then transported through the feeding means 14. It is sent to the object to be sterilized receiver 8 of the transport conveyor 5. The conveying tool 31 sent into the object receiver 8 transports the dish-shaped container 32 and the object to be sterilized horizontally and without falling over by the drive of the transporting Kosobear 5, and transports the object into the cooling water in the cooling chamber 4. The material is introduced into the hot water in the sterilization chamber 2 through the gas phase section 9a, and the object to be sterilized is heated and sterilized with this hot water, and then introduced into the cooling water in the cooling chamber 4 through the gas phase section 9b, and cooled with this cooling water. do. The transport tool 31 with the cooled object to be sterilized is received by the delivery means 15 from the object receiver 8, and the delivery means 1
5 into the empty iron fitting recess 13a of the rotor 13 of the pressure breaker 11. It should be noted that this iron fitting recess 13a is emptied by extruding a carrier containing objects to be sterilized before sterilization. The conveyance odor 31 after sterilization and cooling of the object to be sterilized that has been sent into the competition recess 13a is led out of the apparatus main body 1 by the rotation of the rotor 13, and is delivered to the external delivery mechanism 19 by the operation of the forced discharge mechanism of the rotor 13. External delivery mechanism 19
It is sent to the supply/discharge conveyor 17 by the operation of , and is discharged to a predetermined location by this conveyor 17. Then, the dish-shaped container is removed from the frame of the carrier, and the object to be sterilized is taken out from the dish-shaped container. The heating sterilization and cooling of the object to be sterilized has been described above with attention to one transport tool, but the heating sterilization and cooling described above are performed continuously for a large number of transport odors. As described above, the conveyor 5 always transports the dish-shaped containers and the objects to be sterilized in a horizontal state, so that the dishes containing the objects to be sterilized and stacked up and down in multiple stages are loaded into the transport tool 31. The lower plate-shaped containers 32 from the cooling water exit the gas phase section 9a later than the upper ones and are led into the hot water first, and the lower dish-shaped containers 32 from the hot water exit into the gas phase section 9b later from the hot water. It is led into the cooling water first, and therefore the lower dish-shaped container 32 remains in the hot water for a longer period of time than the upper one.

そこで、皿状容器32が熱水から出て冷却水中に導かれ
る側の気相部9bに、水蒸気および加圧空気をこれらの
供給管24,25から吹込むと共に、排気管26から気
相部9b内の気体の一部を排出することにより、皿状容
器32に収容された被殺菌物を気相部9bでも加熱殺菌
する。この加熱殺菌は、温度検知素子21bによって気
相部9bの温度を検知し、この検知信号に塞き温度、圧
力制御部22から供給管24,25、排気管26の弁2
8,29,30‘こ信号を出し、これらの開度を制御す
ることにより、気相部9bの温度と圧力を所定の状態に
保持し、被殺菌物を熱水での加熱殺菌と実質的に同機な
条件で加熱殺菌する。この条件としては、121℃の熱
水で加熱殺菌する場合に、水蒸気80%以上、空気20
%以下の混合物を用いて気相部9bで加熱することより
、熱水と同様に被殺菌物を加熱殺菌することができる。
そして、殺菌室2の熱水と、気相部9bの水蒸気および
加圧空気とで連続的に加熱殺菌することにより、前述し
たように下段の皿状容器32が上段のものより先に熱水
中に入り先に気相部9bから冷却水中に入るため、それ
ぞれの搬送臭31‘こ装填された四状容器32は、上段
のものも下段のものも同じ時間だけ加熱殺菌が行われ、
加熱殺菌後には直ちに冷却水によって冷却されることに
なり、加熱殺菌が均一に行われる。また、皿状容器32
が冷却水から出て熱水中に導かれる側の気相部9aに、
冷却用空気管23から冷却用空気を供給することにより
、気相部9aで被殺菌物が加熱されないようにし、これ
によっても上段の皿状容器32と下段の皿状容器との不
均一な加熱を防止すると共に、経時変化による気相部9
a内の気体の温度上昇による過剰加熱殺菌を抑制してい
る。
Therefore, water vapor and pressurized air are blown into the gas phase portion 9b on the side where the dish-shaped container 32 comes out of the hot water and is led into the cooling water from these supply pipes 24 and 25, and the gas phase portion is blown from the exhaust pipe 26. By discharging a part of the gas in 9b, the object to be sterilized accommodated in the dish-shaped container 32 is also heated and sterilized in the gas phase part 9b. In this heat sterilization, the temperature of the gas phase section 9b is detected by the temperature detection element 21b, and the temperature and pressure control section 22, the supply pipes 24, 25, and the valve 2 of the exhaust pipe 26 are detected by blocking this detection signal.
By outputting the signals 8, 29, and 30' and controlling their opening degrees, the temperature and pressure of the gas phase section 9b can be maintained at a predetermined state, and the object to be sterilized can be sterilized by heating with hot water. Heat sterilize under the same conditions as before. When heat sterilizing with hot water at 121℃, the conditions are 80% or more of water vapor and 20% air.
By heating in the gas phase section 9b using a mixture of 5% or less, the object to be sterilized can be sterilized by heating in the same manner as hot water.
Then, by successively heating and sterilizing the hot water in the sterilization chamber 2 and the steam and pressurized air in the gas phase section 9b, the lower dish-shaped containers 32 are exposed to the hot water before the upper ones, as described above. Since the cooling water first enters the gas phase section 9b, the four-shaped containers 32 loaded with the respective transport odors 31' are heated and sterilized for the same amount of time for both the upper and lower tiers.
After heat sterilization, it is immediately cooled with cooling water, so that heat sterilization is uniformly performed. In addition, the dish-shaped container 32
In the gas phase part 9a on the side where the gas comes out of the cooling water and is led into the hot water,
By supplying cooling air from the cooling air pipe 23, the objects to be sterilized are prevented from being heated in the gas phase section 9a, and this also prevents uneven heating between the upper tray-shaped container 32 and the lower tray-shaped container. In addition to preventing the gas phase part 9 due to aging,
Excessive heating and sterilization due to the rise in temperature of the gas inside a is suppressed.

なお、気相部9aの温度および圧力制御も、気相部9b
の場合とほぼ同機にして行うものであり、また気相部9
aにも弁を有する排気管を設けて、気相部9aの圧力を
制御することが好ましい。この発明において、前述の実
施例では冷却水から熱水中に入る気相部には冷却空気を
供給し、熱水から冷却水中に入る気相部には水蒸気と加
圧空気とを供給するようにしたが、これを逆にして前者
の気相部に水蒸気と加圧空気とを供給し、後者の気相部
に冷却空気を供給するようにしてもよい。
Note that the temperature and pressure control of the gas phase portion 9a is also performed by the gas phase portion 9b.
This is done using almost the same machine as in the case of , and the gas phase section 9
It is preferable that an exhaust pipe having a valve is also provided in a to control the pressure in the gas phase portion 9a. In this invention, in the above-mentioned embodiment, cooling air is supplied to the gas phase where the cooling water enters the hot water, and water vapor and pressurized air are supplied to the gas phase where the hot water enters the cooling water. However, this may be reversed so that water vapor and pressurized air are supplied to the former gas phase, and cooling air is supplied to the latter gas phase.

また、この発明において、気相部に供給する加熱用気体
は水蒸気だけにしてもよく、また冷却空気に代えて室温
の空気とスプレー状の冷却水を供給するようにしてもよ
い。
Further, in the present invention, the heating gas supplied to the gas phase portion may be only water vapor, or room temperature air and sprayed cooling water may be supplied instead of cooling air.

さらに、この発明では、搬送用コンベアによる被殺菌物
の搬送速度を変更して気相部での加熱気体による加熱殺
菌を考慮した加熱殺菌時間が得られるようにするもので
ある。
Further, in the present invention, the conveyance speed of the object to be sterilized by the conveyor is changed to obtain a heat sterilization time that takes into account heat sterilization by heated gas in the gas phase.

以上説明したように、この発明によれば、可榛性包装体
からなる被殺菌物を収容した皿状容器を上下複数段に積
重ねたものを、搬送用コンベアによって前記皿状容器を
水平状態に保ち、冷却水中から気相部を経て熱りK中に
導いて被殺菌物を加熱殺菌した後、前記気相部と仕切っ
た他の気相部を経て冷却水に導いて冷却する場合に、前
記気相部のいずれか一方に加熱気体を供給し、被殺菌物
を熱水での加熱殺菌と実質的に同様な条件で加熱殺菌す
ることにより、積重ねた皿状容器の上段のものに収容さ
れた被殺菌物と下段のものに収容された被殺菌物とを、
同様な加熱殺菌条件で殺菌するものであるため、F値を
均一にすることができ、良好な連続殺菌を行うことがで
き、とくに高温短時間殺菌に好適するという効果が得ら
れる。
As explained above, according to the present invention, a plurality of stacked dish-like containers containing objects to be sterilized made of flexible packaging bodies are stacked one above the other, and the dish-like containers are brought into a horizontal state by a conveyor. In the case where the object to be sterilized is heated and sterilized by being guided from the cooling water into the hot K through the gas phase section, and then guided to the cooling water through another gas phase section separated from the gas phase section for cooling, By supplying heated gas to either one of the gas phase parts and heat sterilizing the object under conditions substantially similar to heat sterilization with hot water, the object is stored in the upper layer of the stacked dish-shaped containers. The objects to be sterilized and the objects to be sterilized stored in the lower row are
Since sterilization is carried out under similar heat sterilization conditions, the F value can be made uniform, good continuous sterilization can be performed, and the effect is particularly suitable for high-temperature short-time sterilization.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明による連続殺菌方法を行う殺菌装置の
一例を示す概略側断面図、第2図はこの発明による連続
殺菌方法に用いる搬送具の一例を示す正面図、3図は同
側面図である。 1…・・・装置本体、2・・・…殺菌室、4……冷却室
、5・・・・・・搬送用コンベア、9a,9b・・…・
気相部、10・・・・・・仕切り、11・・・・・・圧
力遮断機機、20・・・・・・気相部温度制御機構、2
4,25・・・・・・水蒸気、加圧空気の供給管、26
…・・・排気管。 第1図第2図 第3図
Fig. 1 is a schematic side sectional view showing an example of a sterilizer for carrying out the continuous sterilization method according to the present invention, Fig. 2 is a front view showing an example of a carrier used in the continuous sterilization method according to the invention, and Fig. 3 is a side view of the same. It is. 1... Apparatus body, 2... Sterilization chamber, 4... Cooling room, 5... Transport conveyor, 9a, 9b...
Gas phase section, 10... Partition, 11... Pressure breaker, 20... Gas phase temperature control mechanism, 2
4, 25... Water vapor, pressurized air supply pipe, 26
…···Exhaust pipe. Figure 1 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】 1 可撓性包装体からなる被殺菌物を収容した皿状容器
を上下複数段に積重ねたものを、装置本体外から装置本
体内に設けた搬送用コンベアに供給し、この搬送用コン
ベアにより前記皿状容器を水平状態に保つて搬送し、冷
却室に満たされた冷却水中から装置本体内上部の気相部
を経て殺菌室に満たされた熱水中に導き、熱水で被殺菌
物を加熱殺菌した後、装置本体内上部の前記気相部と仕
切つた他の気相部を経て冷却室に満たされた冷却水中に
導き冷却水で冷却し、その後皿状容器を装置本体外に送
出す連続殺菌方法において、前記気相部のいずれか一方
に加熱用気体を供給し、被殺菌物を熱水での加熱殺菌と
実質的に同様な条件で加熱殺菌することを特徴とする連
続殺菌方法。 2 前記気相部の加熱用気体を供給しない他方に冷却用
流体を供給して被殺菌物を冷却する特許請求の範囲第1
項記載の連続殺菌方法。
[Scope of Claims] 1. A plurality of stacked dish-shaped containers made of flexible packaging containing objects to be sterilized are stacked up and down in multiple tiers, and are fed from outside the device main body to a conveyor provided inside the device main body, This conveyor transports the dish-shaped container while keeping it in a horizontal state, and guides it from the cooling water filled in the cooling chamber through the gas phase in the upper part of the device main body into the hot water filled in the sterilization chamber. After the object to be sterilized is heated and sterilized with water, it is introduced into the cooling water filled in the cooling chamber through another gas phase section separated from the above-mentioned gas phase section in the upper part of the main body of the device, and then cooled with the cooling water, and then placed in a dish-shaped container. In a continuous sterilization method in which the sterilization material is sent out of the apparatus main body, a heating gas is supplied to either one of the gas phase parts, and the object to be sterilized is heat sterilized under substantially the same conditions as heat sterilization with hot water. A continuous sterilization method characterized by: 2. Claim 1, in which the object to be sterilized is cooled by supplying a cooling fluid to the other gas phase part to which heating gas is not supplied.
Continuous sterilization method described in section.
JP55122219A 1980-09-05 1980-09-05 Continuous sterilization method Expired JPS6017539B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55122219A JPS6017539B2 (en) 1980-09-05 1980-09-05 Continuous sterilization method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55122219A JPS6017539B2 (en) 1980-09-05 1980-09-05 Continuous sterilization method

Publications (2)

Publication Number Publication Date
JPS5749452A JPS5749452A (en) 1982-03-23
JPS6017539B2 true JPS6017539B2 (en) 1985-05-04

Family

ID=14830489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55122219A Expired JPS6017539B2 (en) 1980-09-05 1980-09-05 Continuous sterilization method

Country Status (1)

Country Link
JP (1) JPS6017539B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6461043B1 (en) * 2000-05-24 2002-10-08 Colgate Palmolive Company Reclosable bag

Also Published As

Publication number Publication date
JPS5749452A (en) 1982-03-23

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