JP2779341B2 - Rotary spray type retort sterilization method and apparatus - Google Patents

Rotary spray type retort sterilization method and apparatus

Info

Publication number
JP2779341B2
JP2779341B2 JP8027808A JP2780896A JP2779341B2 JP 2779341 B2 JP2779341 B2 JP 2779341B2 JP 8027808 A JP8027808 A JP 8027808A JP 2780896 A JP2780896 A JP 2780896A JP 2779341 B2 JP2779341 B2 JP 2779341B2
Authority
JP
Japan
Prior art keywords
product
spray
trays
sterilization
rotating 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 - Lifetime
Application number
JP8027808A
Other languages
Japanese (ja)
Other versions
JPH09215733A (en
Inventor
善謙 福田
隆一 堤
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.)
HISAKA SEISAKUSHO KK
Original Assignee
HISAKA SEISAKUSHO KK
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 HISAKA SEISAKUSHO KK filed Critical HISAKA SEISAKUSHO KK
Priority to JP8027808A priority Critical patent/JP2779341B2/en
Publication of JPH09215733A publication Critical patent/JPH09215733A/en
Application granted granted Critical
Publication of JP2779341B2 publication Critical patent/JP2779341B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、食品や医薬品等の
内容物を容器(パウチ、缶詰、ビン詰等)内に密封充填
した製品を昇温、加熱、冷却のレトルトサイクルプロセ
スで加熱殺菌処理する回転型スプレー式レトルト殺菌方
法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat sterilization treatment of a product in which contents such as food and medicine are sealed in a container (pouch, can, bottle, etc.) by a retort cycle process of heating, heating and cooling. The present invention relates to a rotating spray type retort sterilizing method and apparatus.

【0002】[0002]

【従来の技術】従来、この種の加熱殺菌処理には、スプ
レー式レトルト殺菌機が提供されている。このスプレー
式レトルト殺菌機は、製品を載置したトレーを複数段積
み重ねて殺菌槽内に収容し、トレー間の隙間に向けて配
置したスプレーノズルから熱水あるいは蒸気等を噴霧し
て製品を加熱殺菌した後、スプレーノズルから冷却水を
噴霧して製品を冷却するものである(実公平3−319
7号公報等参照)。
2. Description of the Related Art Conventionally, a spray type retort sterilizer has been provided for this type of heat sterilization. This spray-type retort sterilizer stacks a plurality of trays on which products are placed and stores them in a sterilization tank. After sterilization, cooling water is sprayed from a spray nozzle to cool the product (Japanese Utility Model Publication 3-319).
No. 7).

【0003】[0003]

【発明が解決しようとする課題】従来のスプレー式レト
ルト殺菌機は、殺菌槽内で製品を水平に静置して加熱殺
菌処理を行っているため、容器内の内容物への伝熱促進
効果が低い。特に、大型容器で粘度の高い液が入ってい
る場合、中心部の温度変化が大幅に遅くなる。このよう
な場合、加熱殺菌処理は内容物全体に施すことが必要で
あるため、中心部の温度が目標値に達するまでスプレー
ノズルから熱水等を噴霧し続ける必要があり、処理時間
が長くなっていた。
The conventional spray-type retort sterilizer heats and sterilizes the product by standing the product horizontally in a sterilization tank, and thus has an effect of promoting heat transfer to the contents in the container. Is low. In particular, when a highly viscous liquid is contained in a large container, the temperature change in the central portion is significantly slowed down. In such a case, since the heat sterilization treatment needs to be performed on the entire contents, it is necessary to continuously spray hot water or the like from the spray nozzle until the temperature in the central portion reaches the target value, which increases the processing time. I was

【0004】本発明の目的は、容器内の内容物への伝熱
促進効果を高めて殺菌処理時間を短縮し得る回転型スプ
レー式レトルト殺菌方法及び装置を提供することにあ
る。
An object of the present invention is to provide a rotary spray retort sterilization method and apparatus capable of enhancing the effect of promoting heat transfer to the contents in a container and shortening the sterilization processing time.

【0005】[0005]

【課題を解決するための手段】本発明の方法は、上述の
目的を達成するために、製品を載置したトレーを複数段
積み重ねて殺菌槽内に収容し、トレー間の隙間に向けて
配置したスプレーノズルから熱水あるいは蒸気等を噴霧
して製品を加熱殺菌した後、スプレーノズルから冷却水
を噴霧して製品を冷却するスプレー式レトルト殺菌方法
において、製品の加熱殺菌及び冷却処理中、製品を載置
したトレー及びスプレーノズルを殺菌槽内で回転させて
容器内の内容物への伝熱促進効果を高めて殺菌処理する
ものである。
According to the method of the present invention, in order to achieve the above-mentioned object, trays on which products are placed are stacked in a plurality of stages, accommodated in a sterilization tank, and arranged toward a gap between the trays. The product is heated and sterilized by spraying hot water or steam from the spray nozzle that has been sprayed, and then cooled by spraying cooling water from the spray nozzle to cool the product. The tray and the spray nozzle on which are placed are rotated in the sterilization tank to enhance the effect of promoting heat transfer to the contents in the container for sterilization.

【0006】また、本発明の装置は、製品を載置したト
レーを複数段積み重ねて殺菌槽内に収容し、トレー間の
隙間に向けて配置したスプレーノズルから熱水あるいは
蒸気等を噴霧して製品を加熱殺菌した後、スプレーノズ
ルから冷却水を噴霧して製品を冷却するスプレー式レト
ルト殺菌装置において、複数段に積み重ねられたトレー
を殺菌槽内で回転可能に保持する回転体と、トレー間の
隙間に向けて熱水、蒸気、冷却水を噴霧するスプレーノ
ズルを有し、回転体と一緒に回転するように配置したヘ
ッダーパイプと、回転体及びヘッダーパイプを殺菌槽内
で回転させる回転駆動手段とを具備させ、製品の加熱殺
菌及び冷却処理中、製品を載置したトレー及びヘッダー
パイプを回転駆動手段により殺菌槽内で回転させて容器
内の内容物への伝熱促進効果を高めて殺菌処理するよう
になしたものである。
In the apparatus of the present invention, a plurality of trays on which products are placed are stacked and accommodated in a sterilization tank, and hot water or steam is sprayed from a spray nozzle disposed toward a gap between the trays. In a spray-type retort sterilizer that cools products by spraying cooling water from spray nozzles after heating and sterilizing the products, a rotating body that holds the trays stacked in multiple stages rotatably in the sterilization tank, A spray pipe that sprays hot water, steam, and cooling water toward the gap between the header pipe and the header pipe that is arranged to rotate together with the rotating body, and a rotary drive that rotates the rotating body and the header pipe in the sterilization tank During the heat sterilization and cooling treatment of the product, the tray on which the product is placed and the header pipe are rotated in the sterilization tank by the rotation drive means to transfer the product to the contents in the container. It is obtained without to sterilization increase the promoting effect.

【0007】[0007]

【発明の実施の形態】図1は本発明の方法の実施に使用
する殺菌装置の要部の概略構造を示す縦断正面図、図2
の(A)(B)は回転途中の状態を示す動作状態の説明
図、図3の(A)は回転体の概略構造を示す斜視図、
(B)はトレーの概略斜視図、図4の(A)は回転駆動
手段の第1実施例を示す概略側面図、(B)は回転駆動
手段の第2実施例を示す概略側面図、(C)はその縦断
正面図を示している。
FIG. 1 is a longitudinal sectional front view showing a schematic structure of a main part of a sterilization apparatus used for carrying out the method of the present invention.
3A and 3B are explanatory views of an operation state showing a state in the middle of rotation, FIG. 3A is a perspective view showing a schematic structure of a rotating body,
4B is a schematic perspective view of the tray, FIG. 4A is a schematic side view showing a first embodiment of the rotary drive unit, FIG. 4B is a schematic side view showing a second embodiment of the rotary drive unit, C) shows a longitudinal front view thereof.

【0008】図1〜図4において、1は殺菌槽、2は回
転体、3はトレー、4はヘッダーパイプ、5は回転駆動
手段、aは製品を示す。
1 to 4, reference numeral 1 denotes a sterilization tank, 2 denotes a rotating body, 3 denotes a tray, 4 denotes a header pipe, 5 denotes a rotation driving means, and a denotes a product.

【0009】殺菌槽1は、図1及び図4に示すように、
基台6上に水平状態で固定支持された円筒状をなし、そ
の両端には蓋部材1a、1bが気密に取り付けられ、前
側の蓋部材1aは、製品aを載置したトレー3を搬入・
搬出するために開閉可能に装着されている。
As shown in FIGS. 1 and 4, the sterilization tank 1
It has a cylindrical shape fixed and supported on a base 6 in a horizontal state, and lid members 1a and 1b are hermetically attached to both ends thereof. The front lid member 1a carries a tray 3 on which a product a is placed.
It is installed to be able to open and close to carry it out.

【0010】回転体2は、図3の(A)に最もよく示す
ように、複数の円板2aと、各円板2aを適宜の間隔で
連結する複数の連結バー2bと、トレー3を段積みした
台車3aを収納するため各円板2aに形成された略矩形
の開口部2cと、各円板2aの略矩形の開口部2cの間
に亘って配設され、トレー3を段積みした台車3aを搬
入・搬出可能に保持する底部案内レール2dと、側面案
内ロール2eと、台車3aに段積みされたトレー3の最
上段のものを上から押えるトレー押え部材2fとを具備
し、殺菌槽1内に支持コロ2gを介して回転可能に支持
され、又は、前端側を支持コロ2gで支持し、後端側を
後述する回転軸5eにより殺菌槽1の後端側の蓋部材1
bの中央部に軸受を介して回転可能に支持させている。
底部案内レール2dは、台車3aの搬入・搬出を容易に
するためコロコンベアで構成されているが、単にレール
構造でもよい。また、側面案内ロール2eは、台車3a
に段積みされたトレー3の全体を両側面から案内保持す
るためのもので、各円板2aの間に1列ないし複数列で
設置されている。さらに、トレー押え部材2fは、各円
板2aの間の上部にエアシリンダその他の適宜の手段2
hによって上下操作可能に設置され、パンチングメタル
等で構成されている。また、支持コロ2gは、回転体2
の各円板2aに対応して、或いは、適宜の円板2aに対
応して殺菌槽1の一部に回転可能に設置され、円板2a
の円周上を下方の2点を含む複数箇所で支持するように
配置されている。
As best shown in FIG. 3A, the rotating body 2 comprises a plurality of disks 2a, a plurality of connecting bars 2b for connecting the disks 2a at appropriate intervals, and a tray 3. The trays 3 are stacked between substantially rectangular openings 2c formed in the respective disks 2a for storing the stacked carts 3a and substantially rectangular openings 2c of the respective disks 2a. It has a bottom guide rail 2d for holding the carriage 3a so that it can be carried in and out, a side guide roll 2e, and a tray pressing member 2f for pressing the uppermost one of the trays 3 stacked on the carriage 3a from above. The lid member 1 is rotatably supported in the tank 1 via a support roller 2g, or the front end side is supported by the support roller 2g, and the rear end side is a rear end side lid member 1 of the sterilization tank 1 by a rotating shaft 5e described later.
It is rotatably supported at the center of b through a bearing.
The bottom guide rail 2d is formed of a roller conveyor to facilitate loading and unloading of the carriage 3a, but may be simply a rail structure. In addition, the side guide roll 2e is a cart 3a.
For guiding and holding the entirety of the trays 3 stacked on both sides from one side to the other, and is installed in one or more rows between the discs 2a. Further, the tray holding member 2f is provided with an air cylinder or other appropriate means 2 on the upper portion between the disks 2a.
h so that it can be operated up and down, and is made of punching metal or the like. In addition, the supporting roller 2g is
Corresponding to each disk 2a, or corresponding to an appropriate disk 2a, rotatably installed in a part of the sterilization tank 1, and
Are arranged so as to be supported at a plurality of points including the lower two points on the circumference of.

【0011】トレー3は、図3の(B)に最もよく示す
ように、台車3a上に段積み可能で、それぞれ複数個の
製品aを相互に重ならず、移動しないように仕切り板3
bで区画して位置決め保持し、かつ、段積みされた各ト
レー3の周囲から熱水等を噴霧可能とするために窓孔3
cが形成されており、また、底部からの排水を可能とす
るためにパンチングメタル等の適宜の排水構造が採用さ
れている。
As best shown in FIG. 3B, the tray 3 can be stacked on a truck 3a, and a plurality of products a do not overlap with each other and do not move.
b for positioning and holding, and for allowing hot water or the like to be sprayed from around each of the stacked trays 3.
c is formed, and an appropriate drainage structure such as punching metal is employed to enable drainage from the bottom.

【0012】ヘッダーパイプ4は、図1に最もよく示す
ように、多数のスプレーノズル4aを有し、回転体2内
に搬入された段積み状態の各トレー3の間の窓孔3cか
ら製品aに向けて熱水等を噴霧するためのもので、回転
体2の各円板2a間に縦方向又は横方向に配置され、回
転体2内に搬入された段積み状態のトレー3と一体的に
回転するように構成されている。
As best shown in FIG. 1, the header pipe 4 has a large number of spray nozzles 4a, and a product a through a window 3c between the trays 3 stacked in the rotating body 2 and stacked. For spraying hot water or the like toward the surface of the rotating body 2, which is arranged vertically or horizontally between the disks 2 a of the rotating body 2, and is integrated with the tray 3 in a stacked state carried into the rotating body 2. It is configured to rotate.

【0013】ヘッダーパイプ4への熱水又は冷却水の供
給は、図1、図3の(A)、図4の(A)に示すよう
に、回転体2の両側に配設された主配管4bから分岐管
4cを介してそれぞれ分岐供給され、この両側の主配管
4bは、回転体2の後端において回転体2の中心軸線上
で合流管4dにより合流せしめられ、殺菌槽1の後端側
の蓋部材1bの中心部に配置された供給口管4eに回転
継手4fを介して接続されている。この供給口管4eに
は、図1に示すように、循環ポンプ7及び熱交換器8を
備えた熱水又は冷却水の循環供給配管9が接続されてい
る。循環ポンプ7の吸入管9aは、殺菌槽1の底部に接
続されており、循環ポンプ7の吐出管9bは、熱交換器
8の入口に接続され、熱交換器8の出口は、循環供給配
管9を介して前記供給口管4eに接続されている。熱交
換器8は、殺菌槽1の底部に滞留する水その他適宜の液
体を加熱蒸気s又は冷却水cにより加熱又は冷却(熱交
換)して熱水又は冷却水を作り出すためのものであっ
て、熱交換用の加熱蒸気と冷却水とが配管10、11か
ら切換弁12、13を介して切換供給され、また、冷却
水出口配管14と蒸気ドレン配管15が切換弁16、1
7を介して切換可能に接続されている。また、殺菌槽1
には、必要に応じて真空脱気手段18と乾燥用熱風供給
及び排気手段19が接続される(図1参照)。なお、ヘ
ッダーパイプ4への熱水又は冷却水の供給は、図1の実
施例のような熱交換器8を介さずに直接、供給口管4e
へ加熱蒸気又は冷却水を切換え供給させるようにしても
よい。
As shown in FIGS. 1, 3A, and 4A, the main pipes disposed on both sides of the rotating body 2 supply hot water or cooling water to the header pipe 4. The main pipes 4b on both sides are joined at a rear end of the rotating body 2 on a central axis of the rotating body 2 by a merging pipe 4d, and the rear end of the sterilizing tank 1 is provided. It is connected via a rotary joint 4f to a supply port tube 4e arranged at the center of the side lid member 1b. As shown in FIG. 1, a circulating supply pipe 9 provided with a circulation pump 7 and a heat exchanger 8 is connected to the supply port pipe 4e. The suction pipe 9a of the circulation pump 7 is connected to the bottom of the sterilization tank 1, the discharge pipe 9b of the circulation pump 7 is connected to the inlet of the heat exchanger 8, and the outlet of the heat exchanger 8 is connected to a circulation supply pipe. 9 is connected to the supply port tube 4e. The heat exchanger 8 heats or cools (heat exchanges) water or other appropriate liquid staying at the bottom of the sterilization tank 1 with the heating steam s or the cooling water c to produce hot water or cooling water. Heated steam for heat exchange and cooling water are switched and supplied from pipes 10 and 11 via switching valves 12 and 13, and a cooling water outlet pipe 14 and a steam drain pipe 15 are connected to switching valves 16 and 1.
7 are switchably connected. In addition, sterilization tank 1
Is connected to a vacuum degassing means 18 and a hot air supply and exhaust means 19 for drying as required (see FIG. 1). The supply of the hot water or the cooling water to the header pipe 4 is directly performed without passing through the heat exchanger 8 as in the embodiment of FIG.
The heating steam or the cooling water may be switched and supplied.

【0014】回転駆動手段5は、2つの実施例があり、
その1つは、図4の(A)に示すように、殺菌槽1の一
端外部の基台6上に設置したモータ5aから減速機5
b、歯車5c、5dを介して回転体2の一端に固着した
回転軸5eを回転させるように構成されている。この場
合、回転軸5eは、中空軸であって、その中心部を貫通
して回転体2のヘッダーパイプ4へ熱水又は冷却水が供
給されるものである。また、回転軸5eは、殺菌槽1の
後端側の蓋部材1bに回転可能に支持されている。
The rotation driving means 5 has two embodiments.
One of them is, as shown in FIG. 4 (A), a motor 5a installed on a base 6 outside one end of the sterilizing tank 1 and a speed reducer 5 mounted on the base 6.
b, the rotating shaft 5e fixed to one end of the rotating body 2 via the gears 5c and 5d is configured to rotate. In this case, the rotating shaft 5e is a hollow shaft through which hot water or cooling water is supplied to the header pipe 4 of the rotating body 2 through its center. The rotating shaft 5e is rotatably supported by the lid member 1b on the rear end side of the sterilization tank 1.

【0015】もう1つの実施例は、図4の(B)(C)
に示すように、殺菌槽1の外周一部にモータ5fを設
置し、回転体2の一部に環状歯車5gを固着し、前記モ
ータ5fからピニオン5hを介して環状歯車5gを噛合
回転させて回転体2を回転させるようにしたものであ
る。
Another embodiment is shown in FIGS. 4B and 4C.
As shown in FIG. 5, a motor 5f is installed on a part of the outer periphery of the sterilizing tank 1, an annular gear 5g is fixed to a part of the rotating body 2, and the motor 5f is rotated by meshing the annular gear 5g via a pinion 5h. The rotating body 2 is rotated.

【0016】本発明は、以上の構成からなり、次にその
動作を説明する。先ず、殺菌槽1の前側の蓋部材1aを
開放し、製品aを載置したトレー3を台車3a上に積み
重ねた状態で搬入コンベア(図示省略)等により回転体
2内に順次収納し、蓋部材1aを閉じる。そして、トレ
ー押え部材2fを降下動作させて最上部のトレー3を押
圧保持させる。これにより、各トレー3の積み重ね体
は、回転体2内で、上下方向にはトレー押え部材2fと
底部案内レール2dとにより、また、両側方向には側部
案内ロール2eによりそれぞれ保持される。この状態で
熱交換器8に加熱蒸気を供給し、循環ポンプ7を運転し
て殺菌槽1内のヘッダーパイプ4に熱水を供給する。こ
れと同時に、回転駆動手段5を駆動して回転体2を所定
の回転数、製品a内に含まれる液体分の粘性を考慮し
て、例えば、5〜30rpm、多くは20rpmで回転
させる。図2の(A)は回転体2を反時計方向へ45°
回転させた時の製品aの容器内における内容物の移動状
態を示し、図2の(B)は回転体2をさらに反時計方向
へ270°回転させた時の製品aの容器内における内容
物の移動状態を示している。
The present invention is configured as described above, and the operation will be described next. First, the lid member 1a on the front side of the sterilization tank 1 is opened, and the trays 3 on which the products a are placed are sequentially stored in the rotating body 2 by a carry-in conveyor (not shown) in a state of being stacked on the carriage 3a. The member 1a is closed. Then, the tray holding member 2f is moved down to press and hold the uppermost tray 3. Thereby, the stacked body of each tray 3 is held in the rotating body 2 by the tray pressing member 2f and the bottom guide rail 2d in the vertical direction, and by the side guide rolls 2e in the both sides. In this state, heated steam is supplied to the heat exchanger 8, and the circulation pump 7 is operated to supply hot water to the header pipe 4 in the sterilization tank 1. At the same time, the rotation driving means 5 is driven to rotate the rotating body 2 at a predetermined number of rotations, for example, at 5 to 30 rpm, most often at 20 rpm in consideration of the viscosity of the liquid contained in the product a. FIG. 2A shows the rotating body 2 at 45 ° counterclockwise.
FIG. 2B shows the state of movement of the contents of the product a in the container when rotated, and FIG. 2B shows the contents of the product a in the container when the rotating body 2 is further rotated 270 ° counterclockwise. Shows the moving state of.

【0017】殺菌槽1内で回転体2を回転駆動手段5に
より上記のように回転させることにより、各トレー3に
載置されている製品aは、トレー3と共に回転しながら
ヘッダーパイプ4の多数のスプレーノズル4aから噴霧
される熱水により加熱される。この場合、製品a内に含
まれる液体分が上記の回転により、図2の(A)(B)
に示すように、容器内で左右に移動し、容器中心部の内
容物が容器周縁部と絶えず入れ替え移動せしめられ、容
器内の内容物全体が早期に均一に加熱される。加熱処理
後の冷却工程でも上記と同様に回転させて処理させるこ
とにより、各部均一に、しかも、短時間で冷却すること
ができる。
By rotating the rotator 2 in the sterilization tank 1 by the rotation driving means 5 as described above, the product a placed on each tray 3 is rotated with the tray 3 by a large number of header pipes 4. Is heated by hot water sprayed from the spray nozzle 4a. In this case, the liquid contained in the product a is rotated by the above-described rotation, so that the liquid components shown in FIGS.
As shown in (1), the container moves left and right in the container, the contents in the center of the container are constantly replaced with the container peripheral portion, and the entire contents in the container are heated quickly and uniformly. In the cooling step after the heat treatment, each part can be uniformly cooled in a short period of time by rotating and treating in the same manner as described above.

【0018】図5の(A)〜(D)は、本発明の効果を
確認するために製作した実験装置の説明図であって、殺
菌槽の代用となる処理槽20と、この処理槽20内に収
容した回転体の代用となる製品載置台21と、この製品
載置台21上に製品の代用となるパウチ22を上下から
パンチング板23、23で挟んでボルト24により周囲
を固定し、処理槽20内の上部にスプレーノズル25を
設け、このスプレーノズル25には循環ポンプ26から
処理槽20内底部の滞留水を途中でスチーム加えて昇温
させつつ供給し、製品載置台21のパウチ22に上から
熱水を噴霧させると共に、製品載置台21を図5の
(E)に示すように、回転数6rpmで回転させ、パウ
チ22内の溶液中に含まれる固形物の昇温状態を測定し
た。なお、ず5の(A)において、符号27は回収スト
ップ弁を示しており、上記処理中は閉鎖させている。こ
の場合、温度センサ28をパウチ22の3箇所(図5の
(B)(C)(D)参照)に略等間隔にセットし、それ
ぞれの検出温度をT2、T3、T4で表示するように
し、パウチ22内各部の固形物温度が所定温度(120
℃)に達するまで実験を行った。処理槽20内は密閉状
態とし、内部の温度T1は別の温度センサ(図示省略)
で測定し、圧力P1の変化を圧力計(図示省略)で測定
した。なお、温度センサ28のパウチ22へのセット方
法は、溶液温度を測定する場合には、図5の(F)
(G)に示すようにシリコンゴム等の耐熱材料で円錐栓
形状としたセンサ保持部材29の中心孔に貫通させて先
端の感温部を液中に露出保持させ、パウチ22の上面や
底面に接触しないようにする。また、溶液内に含まれる
固形物の温度変化を測定する場合には、図5の(H)
(I)(J)に示すように、シリコンゴム等の耐熱材料
からなる立方体(他形状でも可)によりダミー固形物3
0を温度センサ28の先端の感温部に差し込み装着し、
ダミー固形物30の内部の昇温状態を測定させるように
する。パウチ22の寸法は、図5の(K)に示す数値
(mm)の通りである。パウチ22内の溶液は、CMC
溶液(1.5wt%)を使用しており、この溶液の粘度
特性は、JISのB型粘度計のローター回転数と温度と
に対して図6の(A)の検出データ表及び(B)のグラ
フに示すような傾向のものを使用した。
FIGS. 5A to 5D are explanatory views of an experimental apparatus manufactured to confirm the effect of the present invention, and show a processing tank 20 as a substitute for a sterilizing tank and this processing tank 20. A product mounting table 21 serving as a substitute for a rotating body accommodated therein, and a pouch 22 serving as a product substitute on the product mounting table 21 are sandwiched from above and below by punching plates 23, 23, and the periphery thereof is fixed by bolts 24. A spray nozzle 25 is provided in the upper part of the tank 20, and the stagnant water in the bottom part of the processing tank 20 is supplied from the circulation pump 26 to the spray nozzle 25 while increasing the temperature while being heated. The product mounting table 21 is rotated at a rotation speed of 6 rpm as shown in FIG. 5E, and the temperature rise state of the solid matter contained in the solution in the pouch 22 is measured. did. In FIG. 5 (A), reference numeral 27 denotes a collection stop valve, which is closed during the above processing. In this case, the temperature sensors 28 are set at substantially equal intervals at three places on the pouch 22 (see (B), (C), and (D) in FIG. 5), and the detected temperatures are displayed as T2, T3, and T4. , The solid matter temperature of each part in the pouch 22 is set to a predetermined temperature (120
C)). The inside of the processing tank 20 is sealed, and the internal temperature T1 is measured by another temperature sensor (not shown).
And the change in pressure P1 was measured with a pressure gauge (not shown). When the temperature of the solution is measured, the temperature sensor 28 is set on the pouch 22 as shown in FIG.
As shown in (G), the sensor holding member 29 made of a heat-resistant material such as silicone rubber or the like and having a conical plug shape is penetrated through the center hole to expose and hold the temperature-sensitive portion at the tip in the liquid. Avoid contact. When measuring the temperature change of the solid matter contained in the solution, FIG.
(I) As shown in (J), a dummy solid 3 is formed by a cube (other shapes are also possible) made of a heat-resistant material such as silicon rubber.
0 into the temperature sensing part at the tip of the temperature sensor 28,
The temperature rise state inside the dummy solid 30 is measured. The dimensions of the pouch 22 are as shown in the numerical values (mm) shown in FIG. The solution in the pouch 22 is CMC
A solution (1.5 wt%) is used. The viscosity characteristics of this solution are shown in the detection data table of FIG. 6A and the rotor data of FIG. The trend shown in the graph was used.

【0019】図7は、前記実験装置により、レトルトカ
レーのような固形物を含む溶液を内容物とする製品を想
定して、製品載置台21を静置した状態で処理した場合
(A)と、製品載置台21を回転させて処理した場合
(B)とにおける固形物の内部の温度変化(T2、T
3、T4)と、この温度変化に基づいて求めたF値(殺
菌度を表示する数値で、4以上でボツリヌス菌が死滅す
る)の分布(F2、F3、F4)を示す比較実験データ
を示している。
FIG. 7 shows a case where a product containing a solid-containing solution such as retort curry as a content is processed by the experimental apparatus in a state where the product mounting table 21 is left stationary (A). , The temperature change (T2, T2) inside the solid in the case where the processing is performed by rotating the product mounting table 21 (B).
3, T4) and comparative experimental data showing the distribution (F2, F3, F4) of the F value (a numerical value indicating the degree of sterilization, botulinum kills at 4 or more) obtained based on this temperature change. ing.

【0020】静置処理の場合:図7(A)参照 F2=16.9 F3= 8.2 F4=13.4 図7の(A)に示す静置処理の場合、処理槽内の温度上
昇カーブT1に比べ、パウチ内各部の温度上昇カーブT
2、T3、T4が緩やかで、かつ、バラツキがあり、し
かも、全体が所定温度(約120℃)に達する前(11
8℃付近)にF値が目標値をクリヤーして加熱が終了
し、この加熱終了時点(処理開始から約1時間35分経
過)から、直ちに冷却工程に移行し、処理槽内の温度T
1が約30℃付近まで急降下して(この間に2〜3分の
タイムラグあり)冷却が開始され、この冷却工程でも静
置処理の場合では処理槽内の冷却温度カーブT1に比
べ、パウチ内各部の冷却温度カーブT2、T3、T4が
緩やかで、かつ、バラツキがあり、冷却終了時点におけ
る処理槽内温度T1≒40℃に対し、T2≒60℃、T
3≒70℃、T4≒72℃と約20℃〜32℃高温とな
っており、冷却開始時点(処理開始から約1時間38分
経過)から冷却終了時点(処理開始から約1時間58分
経過)までの冷却所要時間も約20分を要している。そ
の結果、F値は、F2=16.9、F3=8.2、F4
=13.4と大きくバラツキを生じている。要するに、
静置処理の場合では、加熱時間が約1時間35分、冷却
時間が約20分、全体の処理時間は、約1時間58分程
度かかっており、パウチ内の各部への伝熱作用のバラツ
キが大きく、その結果、F値のバラツキも大きくなって
いる。
In the case of stationary processing: see FIG. 7A. F2 = 16.9 F3 = 8.2 F4 = 13.4 In the case of static processing shown in FIG. Temperature rise curve T of each part in the pouch compared to curve T1
2, T3 and T4 are moderate and uneven, and before the whole reaches a predetermined temperature (about 120 ° C.) (11
At about 8 ° C.), the F value clears the target value, and the heating is completed. From the end of the heating (approximately 1 hour and 35 minutes after the start of the processing), the process immediately shifts to the cooling step, and the temperature T in the processing tank is reduced.
1 rapidly drops to about 30 ° C. (with a time lag of 2 to 3 minutes during this period), and cooling is started. In this cooling step, in the case of still processing, each part in the pouch is compared with the cooling temperature curve T1 in the processing tank. The cooling temperature curves T2, T3, and T4 are gradual and varied, and the temperature T2 at approximately 60 ° C.
3 ≒ 70 ° C., T4 ≒ 72 ° C., about 20 ° C. to 32 ° C., high temperature, and from the start of cooling (about 1 hour and 38 minutes after the start of processing) to the end of cooling (about 1 hour and 58 minutes after the start of processing) It takes about 20 minutes to cool down to (2). As a result, the F value is F2 = 16.9, F3 = 8.2, F4
= 13.4. in short,
In the case of the stationary treatment, the heating time is about 1 hour and 35 minutes, the cooling time is about 20 minutes, and the entire processing time is about 1 hour and 58 minutes, and the variation of the heat transfer action to each part in the pouch is varied. Is large, and as a result, the variation of the F value is also large.

【0021】回転処理の場合:図7(B)参照 F2=13.9 F3=12.9 F4=13.7 図7の(B)に示す回転処理の場合、処理槽内の温度上
昇カーブT1に対して、パウチ内各部の温度上昇カーブ
T2、T3、T4が急激で、処理開始から約33分経過
した時点で全体が所定温度(約120℃)に達してお
り、その後F値が目標値をクリヤーして加熱が終了する
時点(処理開始から約43分経過=加熱所要時間)か
ら、直ちに冷却工程に移行し、処理槽内の温度が約30
℃付近まで急降下して(この間に2〜3分のタイムラグ
あり)冷却が開始され、この冷却工程でも回転処理によ
り各部の冷却温度カーブT2、T3、T4が急激に降下
しており、冷却開始時点(処理開始から約48分経過)
から冷却終了時点(処理開始から約58分経過)までの
所要時間が約10分となっており、冷却終了時点での処
理槽内の温度T1≒40℃に対して、パウチ内各部の温
度はT2≒53℃、T3≒55℃、T4≒54℃と温度
差が13℃〜15℃と小さい。このように、回転処理の
場合は、パウチ内各部への伝熱作用が向上し、バラツキ
も少なく、加熱時間が約43分に短縮され、かつ、冷却
時間も約10分に短縮され、全体の処理時間は約58分
に短縮されており、F値についても、F2=13.9、
F3=12.9、F4=13.7とバラツキが小さい。
なお、図7の(A)(B)において、処理槽20内の温
度T1は、約120℃に設定され、また、圧力P1は約
2kg/cm2に設定されている。
In the case of rotation processing: see FIG. 7 (B) F2 = 13.9 F3 = 12.9 F4 = 13.7 In the case of rotation processing shown in FIG. 7 (B), the temperature rise curve T1 in the processing tank On the other hand, the temperature rise curves T2, T3, and T4 of each part in the pouch are sharp, and the entire temperature has reached a predetermined temperature (about 120 ° C.) about 33 minutes after the start of the processing. Immediately after the heating is completed (about 43 minutes have elapsed since the start of the treatment = the required heating time), the process immediately proceeds to the cooling step, and the temperature in the treatment tank is reduced to about 30 minutes.
℃, and the cooling is started (there is a time lag of 2 to 3 minutes during this period). In this cooling process, the cooling temperature curves T2, T3, T4 of each part are rapidly lowered by the rotation process. (Approximately 48 minutes have passed since the start of processing)
The required time from the start to the end of cooling (approximately 58 minutes after the start of processing) is about 10 minutes. In contrast to the temperature T1 in the processing tank at the end of cooling of about 40 ° C. The temperature difference between T2、53 ° C., T3 ≒ 55 ° C. and T4 ≒ 54 ° C. is as small as 13 ° C. to 15 ° C. As described above, in the case of the rotation processing, the heat transfer action to each part in the pouch is improved, the dispersion is small, the heating time is reduced to about 43 minutes, and the cooling time is also reduced to about 10 minutes, and The processing time was reduced to about 58 minutes, and the F value was also F2 = 13.9,
F3 = 12.9 and F4 = 13.7, which are small variations.
In FIGS. 7A and 7B, the temperature T1 in the processing tank 20 is set to about 120 ° C., and the pressure P1 is set to about 2 kg / cm 2 .

【0022】図7の(A)(B)に示す比較実験データ
から明らかな通り、静置処理の場合(A)では、パウチ
内各部の温度変化(T2、T3、T4)及びF値の分布
(F2、F3、F4)に大きいバラツキがあり、処理時
間も長くかかているが、回転処理の場合(B)では、パ
ウチ内各部の温度変化(T2、T3、T4)及びF値の
分布(F2、F3、F4)のバラツキが小さく、処理時
間も短い。
As is clear from the comparative experiment data shown in FIGS. 7A and 7B, in the case of the stationary treatment (A), the temperature change (T2, T3, T4) and the distribution of the F value in each part in the pouch. There is a large variation in (F2, F3, F4) and a long processing time, but in the case of the rotation processing (B), the temperature change (T2, T3, T4) of each part in the pouch and the distribution of the F value The dispersion of (F2, F3, F4) is small and the processing time is short.

【0023】[0023]

【発明の効果】本発明によれば、製品の加熱・冷却処理
中、製品を回転させながら熱水又は冷却水を製品に噴霧
するようになしたため、容器内の内容物が絶えず移動せ
しめられ、容器中心部まで一様かつ迅速に熱伝達され、
容器内の内容物への伝熱促進効果を高めて殺菌処理時間
を短縮することができる。
According to the present invention, during the heating / cooling process of a product, the product is rotated and the hot water or the cooling water is sprayed on the product, so that the contents in the container are constantly moved, Heat is uniformly and quickly transferred to the center of the container,
The effect of promoting heat transfer to the contents in the container can be enhanced, and the sterilization time can be reduced.

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

【図1】本発明の方法の実施に使用する殺菌装置の要部
の概略構造を示す縦断正面図である。
FIG. 1 is a longitudinal sectional front view showing a schematic structure of a main part of a sterilization apparatus used for carrying out the method of the present invention.

【図2】(A)(B)は回転体を回転させた状態を示す
内容物の移動状態の説明図である。
FIGS. 2A and 2B are explanatory diagrams of a moving state of contents showing a state in which a rotating body is rotated.

【図3】(A)は回転体の概略構造を示す斜視図、
(B)はトレーの概略斜視図である。
FIG. 3A is a perspective view showing a schematic structure of a rotating body,
(B) is a schematic perspective view of a tray.

【図4】(A)は回転駆動手段の第1実施例を示す概略
側面図、(B)は回転駆動手段の第2実施例を示す概略
側面図、(C)はその縦断正面図を示している。
FIG. 4A is a schematic side view showing a first embodiment of the rotary drive unit, FIG. 4B is a schematic side view showing a second embodiment of the rotary drive unit, and FIG. ing.

【図5】(A)は本発明の実験装置全体の構成を示す概
略図、(B)は前記実験装置における処理槽と製品載置
台とパウチとの関係を示す横断平面図、(C)は縦断側
面図、(D)は縦断正面図、(E)は製品載置台の回転
処理条件説明図、(F)は実験に使用するパウチ内の液
温測定要領の概略説明図、(G)は温度センサー保持部
材の斜視図、(H)はパウチ内の固形物の温度を測定す
る場合の概略説明図、(I)はダミー固形物の斜視図、
(J)はダミー固形物の側面図、(K)は実験に使用す
るパウチ寸法の説明図である。
5A is a schematic diagram showing the configuration of the entire experimental apparatus of the present invention, FIG. 5B is a cross-sectional plan view showing the relationship between a processing tank, a product mounting table and a pouch in the experimental apparatus, and FIG. (D) is a vertical sectional front view, (E) is an explanatory view of a rotation processing condition of a product mounting table, (F) is a schematic explanatory view of a liquid temperature measuring procedure in a pouch used for an experiment, and (G) is a schematic explanatory view. Perspective view of a temperature sensor holding member, (H) is a schematic explanatory view when measuring the temperature of a solid in a pouch, (I) is a perspective view of a dummy solid,
(J) is a side view of a dummy solid, and (K) is an explanatory view of a pouch size used in an experiment.

【図6】(A)はパウチ内に充填したCMC溶液(1.
5wt%)のJIS−B型粘度計のローター回転数と温
度とに対する粘度特性の検出データ図表であり、(B)
はその傾向を示すグラフである。
FIG. 6 (A) shows a CMC solution filled in a pouch (1.
5B is a detection data chart of viscosity characteristics of the JIS-B type viscometer (5 wt%) with respect to the rotor rotation speed and the temperature.
Is a graph showing the tendency.

【図7】(A)は内容物が固形物を含む製品の静置処理
状態の処理特性図、(B)は同じ製品の回転処理状態の
処理特性図である。
FIG. 7 (A) is a processing characteristic diagram of a product in which the contents include a solid material in a stationary processing state, and FIG. 7 (B) is a processing characteristic diagram of a rotation processing state of the same product.

【符号の説明】[Explanation of symbols]

1 殺菌槽 2 回転体 3 トレー 4 ヘッダーパイプ 4a スプレーノズル 5 回転駆動手段 a 製品 DESCRIPTION OF SYMBOLS 1 Sterilization tank 2 Rotating body 3 Tray 4 Header pipe 4a Spray nozzle 5 Rotation drive means a Product

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) A61L 2/04 - 2/06 A23L 3/10──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) A61L 2/04-2/06 A23L 3/10

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 製品を載置したトレーを複数段積み重ね
て殺菌槽内に収容し、トレー間の隙間に向けて配置した
スプレーノズルから熱水あるいは蒸気等を噴霧して製品
を加熱殺菌した後、スプレーノズルから冷却水を噴霧し
て製品を冷却するスプレー式レトルト殺菌方法におい
て、 製品の加熱殺菌及び冷却処理中、製品を載置したトレー
及びスプレーノズルを殺菌槽内で回転させて処理するこ
とを特徴とする回転型スプレー式レトルト殺菌方法。
1. After stacking a plurality of trays on which products are placed and storing them in a sterilization tank, the product is heated and sterilized by spraying hot water or steam from a spray nozzle arranged toward a gap between the trays. The spray retort sterilization method of spraying cooling water from a spray nozzle to cool the product, wherein during the heat sterilization and cooling of the product, the tray on which the product is placed and the spray nozzle are rotated in the sterilization tank to perform the processing. A rotary spray type retort sterilization method characterized by the above-mentioned.
【請求項2】 製品を載置したトレーを複数段積み重ね
て殺菌槽内に収容し、トレー間の隙間に向けて配置した
スプレーノズルから熱水あるいは蒸気等を噴霧して製品
を加熱殺菌した後、スプレーノズルから冷却水を噴霧し
て製品を冷却するスプレー式レトルト殺菌装置におい
て、 複数段に積み重ねられたトレーを殺菌槽内で回転可能に
保持する回転体と、 トレー間の隙間に向けて熱水、蒸気、冷却水を噴霧する
スプレーノズルを有し、回転体と一緒に回転するように
配置したヘッダーパイプと、 回転体及びヘッダーパイプを殺菌槽内で回転させる回転
駆動手段とを具備していることを特徴とする回転型スプ
レー式レトルト殺菌装置。
2. After stacking a plurality of trays on which the products are placed and storing them in a sterilization tank, the products are heated and sterilized by spraying hot water or steam from a spray nozzle arranged toward a gap between the trays. In a spray-type retort sterilizer that cools products by spraying cooling water from spray nozzles, a rotating body that holds multiple stacked trays rotatably in a sterilization tank and heat toward a gap between the trays It has a spray pipe for spraying water, steam and cooling water, and includes a header pipe arranged to rotate together with the rotating body, and a rotation drive means for rotating the rotating body and the header pipe in the sterilization tank. A rotary spray type retort sterilizer, characterized in that:
JP8027808A 1996-02-15 1996-02-15 Rotary spray type retort sterilization method and apparatus Expired - Lifetime JP2779341B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8027808A JP2779341B2 (en) 1996-02-15 1996-02-15 Rotary spray type retort sterilization method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8027808A JP2779341B2 (en) 1996-02-15 1996-02-15 Rotary spray type retort sterilization method and apparatus

Publications (2)

Publication Number Publication Date
JPH09215733A JPH09215733A (en) 1997-08-19
JP2779341B2 true JP2779341B2 (en) 1998-07-23

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2398501B (en) * 2003-02-24 2005-03-16 Patrick Brian Clayton Device for cleaning and sterilising dental equipment
JP4684026B2 (en) * 2005-07-04 2011-05-18 越後製菓株式会社 Food heat treatment method and food heat treatment apparatus
JP4824962B2 (en) 2005-07-25 2011-11-30 越後製菓株式会社 Centrifugal dehydrator
US20070280044A1 (en) * 2006-06-02 2007-12-06 Persoons Gustaaf M L Process fluid application system for agitating retorts
DE102007045720A1 (en) * 2007-09-24 2009-04-09 Sig Technology Ag Apparatus for sterilizing parallelepiped carton / plastic composite packagings in an autoclave and pack suitable for this purpose
JP5136269B2 (en) * 2008-08-04 2013-02-06 東洋製罐株式会社 Temperature measuring method and temperature measuring jig for pouch-packed fluid food
JP5748360B2 (en) * 2012-12-25 2015-07-15 株式会社日阪製作所 Oscillating sterilizer
JP6131238B2 (en) * 2014-12-01 2017-05-17 株式会社日阪製作所 Steam sterilizer
CN105146674A (en) * 2015-09-09 2015-12-16 泉州市南方食品机械有限公司 Rotary spraying and sterilization device for canned foods
KR102086967B1 (en) 2019-09-19 2020-03-09 장광양 Rotating type retort sterilization apparatus with basket fixing unit
KR102481536B1 (en) * 2020-03-02 2022-12-26 씨제이제일제당 (주) Sterilizer
KR102455201B1 (en) * 2020-03-02 2022-10-18 씨제이제일제당 (주) Sterilizing module
CN114304259B (en) * 2022-01-21 2023-09-01 浙江大学中原研究院 Continuous type ration spraying structure of disinfecting after fruit is adopted

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