JPH05227928A - Vacuum heat treatment unit - Google Patents
Vacuum heat treatment unitInfo
- Publication number
- JPH05227928A JPH05227928A JP4061405A JP6140592A JPH05227928A JP H05227928 A JPH05227928 A JP H05227928A JP 4061405 A JP4061405 A JP 4061405A JP 6140592 A JP6140592 A JP 6140592A JP H05227928 A JPH05227928 A JP H05227928A
- Authority
- JP
- Japan
- Prior art keywords
- heat treatment
- outlet
- heat
- inlet
- steam
- 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)
- General Preparation And Processing Of Foods (AREA)
- Cookers (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、熱処理室内を減圧状態
にして供給した加熱流体により被熱処理物を熱処理する
ものに関する。具体的には、各種食品の加熱殺菌や滅
菌、冷却、あるいは凝固や解凍等を行う減圧熱処理装置
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat treatment apparatus for heat-treating an object to be heat-treated with a heating fluid supplied under reduced pressure. Specifically, the present invention relates to a reduced pressure heat treatment apparatus for performing heat sterilization, sterilization, cooling, coagulation and thawing of various foods.
【0002】[0002]
【従来技術】従来の食品の熱処理装置として、例えば特
公昭57−56855号公報に示された技術が用いられ
ていた。これは、大気に連通する空気排出ダクトを設け
たスチ―ムトンネル内に熱処理対象物を搬送するコンベ
アを配置し、コンベアの下側に蒸気吹出しパイプを設
け、このパイプに温度調節弁等からなる自動恒温制御器
セットを連通すると共に、蒸気配管の所要箇所に自動気
水分離器セットと自動減圧弁セットを取付けたものであ
る。自動減圧弁セットで比較的低圧に減圧した蒸気を、
自動恒温制御器セットを介して蒸気吹出しパイプからス
チ―ムトンネル内に供給することにより87度Cから9
8度C程度の蒸気温度でもって熱処理ができるものであ
る。2. Description of the Related Art As a conventional food heat treatment apparatus, for example, the technique disclosed in Japanese Patent Publication No. 57-56855 is used. This is a conveyor that conveys the object to be heat-treated is placed in a steam tunnel equipped with an air discharge duct that communicates with the atmosphere, a steam outlet pipe is installed under the conveyor, and this pipe is equipped with a temperature control valve, etc. A constant temperature controller set is communicated with, and an automatic steam separator set and an automatic pressure reducing valve set are installed at required locations in the steam pipe. Steam reduced to a relatively low pressure with an automatic pressure reducing valve set,
By supplying steam into the steam tunnel from the steam outlet pipe through the automatic constant temperature controller set, the temperature will change from 87 ° C to 9 ° C.
The heat treatment can be performed at a steam temperature of about 8 ° C.
【0003】[0003]
【本発明が解決しようとする課題】上記従来の熱処理装
置では、被熱処理物の加熱後の冷却を自然放熱によるた
めに冷却効率が悪い問題があった。また、冷却を冷却水
により行うためには別途冷却水槽が必要となり、大きな
設置スペ―スが必要となったり、設備費が嵩む問題があ
った。多くの食品においては、加熱処理後に次工程に速
やかに移行するために冷却しなければならないものが多
々あるのである。In the above-mentioned conventional heat treatment apparatus, there is a problem that the cooling efficiency is poor because the cooling after heating the object to be heat treated is done by natural heat radiation. Further, in order to perform cooling with cooling water, a separate cooling water tank is required, and there is a problem that a large installation space is required and equipment costs increase. Many foods must be cooled after the heat treatment in order to quickly move to the next step.
【0004】また上記従来の熱処理装置では、90度C
程度以下の低温蒸気温度では精度良く熱処理できない問
題があった。これはスチ―ムトンネル内を大気圧状態と
しているためで、蒸気は圧力と温度が一義的に定まり大
気圧下ではほぼ100度Cとなり低温蒸気たり得ないた
めである。食品の種類によっては、90度C以下でなけ
れば焦げや熱損傷を来たしてしまうものがあり、この様
なものには上記従来の熱処理装置は使用できないのであ
る。In the above conventional heat treatment apparatus, 90 ° C.
There was a problem that the heat treatment could not be performed accurately at a low temperature of low temperature steam. This is because the inside of the steam tunnel is under atmospheric pressure, and the pressure and temperature of steam are uniquely determined, and under atmospheric pressure, the temperature is almost 100 ° C. and cannot be low-temperature steam. Depending on the type of food, if it is not lower than 90 ° C., it may cause charring or heat damage, and the conventional heat treatment apparatus cannot be used for such food.
【0005】従って本発明の技術的課題は、90度C以
下の低温まで蒸気により熱処理ができるようにすると共
に、加熱後に簡単な設備で効率良く冷却することもでき
るようにすることである。Therefore, a technical object of the present invention is to make it possible to perform heat treatment by steam up to a low temperature of 90 ° C. or less, and also to efficiently cool it with a simple facility after heating.
【0006】[0006]
【課題を解決する為の手段】本発明の減圧熱処理装置の
構成は次の通りである。被熱処理物の入口と出口を設け
た熱処理室を形成し、該熱処理室に被熱処理物を搬送す
る搬送手段を配置して熱処理のための流体を供給する流
体供給通路を接続すると共に減圧ポンプを接続し、上記
入口と出口を所望高さを有する脚状に連設し、該脚状連
設部の下部に液溜を設けて、該液溜の内少なくとも出口
側の液溜に被熱処理物を冷却するための冷却液供給通路
を設けたものである。The structure of the reduced pressure heat treatment apparatus of the present invention is as follows. A heat treatment chamber having an inlet and an outlet of the heat treatment object is formed, a conveying means for conveying the heat treatment object is arranged in the heat treatment chamber, a fluid supply passage for supplying a fluid for heat treatment is connected, and a decompression pump is provided. Connected, the inlet and the outlet are continuously connected in a leg shape having a desired height, a liquid reservoir is provided in the lower part of the leg-shaped continuous portion, and the object to be heat treated is at least in the liquid reservoir on the outlet side of the liquid reservoir. A cooling liquid supply passage for cooling the liquid is provided.
【0007】[0007]
【作用】入口と出口を脚状に連設して下部に液溜を設け
たことにより、熱処理室内を減圧ポンプで減圧すると、
その減圧度に応じて脚状部に液柱を生じて熱処理室内は
所定の減圧状態となる。被熱処理物は入口側の液溜から
入口を経て熱処理室内に搬送手段により搬送される。こ
の場合熱処理室内に流体供給通路から加熱流体、例えば
蒸気、を供給すると被熱処理物は加熱処理される。加熱
流体として低温蒸気あるいは大気圧以下の低圧蒸気を供
給すると熱処理室内は減圧状態故に、その減圧値に応じ
た蒸気温度となり、90度C以下の任意の温度で蒸気加
熱することができる。熱処理室内で加熱処理された被熱
処理物は、搬送手段により出口側の液溜及び出口を経て
外部に搬出される。出口側の液溜には、冷却液供給通路
が設けられているために冷却液が溜置かれており、被熱
処理物がここを通ることにより冷却液に熱を奪われて冷
却される。[Operation] By depressurizing the heat treatment chamber with the depressurizing pump by providing the inlet and the outlet in a leg shape and providing the liquid reservoir in the lower portion,
Depending on the degree of pressure reduction, a liquid column is generated in the leg portion, and the heat treatment chamber is brought into a predetermined pressure reduction state. The object to be heat-treated is conveyed from the liquid reservoir on the inlet side through the inlet into the heat treatment chamber by the conveying means. In this case, when the heating fluid, such as steam, is supplied from the fluid supply passage into the heat treatment chamber, the object to be heat treated is heated. When low-temperature steam or low-pressure steam below atmospheric pressure is supplied as the heating fluid, the heat treatment chamber has a depressurized state, so that the steam temperature corresponds to the depressurized value, and steam heating can be performed at any temperature of 90 ° C. or less. The object to be heat-treated, which has been heat-treated in the heat-treatment chamber, is carried out to the outside through the liquid reservoir on the outlet side and the outlet by the conveying means. Since the cooling liquid supply passage is provided in the liquid reservoir on the outlet side, the cooling liquid is stored in the liquid reservoir, and the object to be heat-treated is cooled by being deprived of heat by the cooling liquid.
【0008】[0008]
【実施例】図示の実施例を詳細に説明する。図1におい
て、箱型の熱処理室1と、搬送手段としての無端コンベ
ア2と、加熱蒸気供給通路3と、冷却液供給通路4と、
減圧ポンプとしての組合せポンプ5とで減圧熱処理装置
を構成する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The illustrated embodiment will be described in detail. In FIG. 1, a box-shaped heat treatment chamber 1, an endless conveyor 2 as a transfer means, a heating steam supply passage 3, a cooling liquid supply passage 4,
A decompression heat treatment apparatus is configured with the combination pump 5 as a decompression pump.
【0009】熱処理室1は、左右の端部に所望高さを有
する脚状の空間6,7を形成し、空間6,7の下端のみ
を開放状態にし、この空間6,7の下端を熱処理室1の
入口8と出口9とする。熱処理室1の下部10は入口8
側ほど低い勾配を設ける。入口8と出口9は液溜容器1
1,12内に溜置いた液体13,14内に配置する。出
口9側の液溜容器12には弁30,31を介して冷却液
供給通路4を接続する。液体13,14に水を使用する
場合は、空間6,7の高さは10メ―トル以下とする。
無端コンベア2はそれぞれロ―ラ15により保持あるい
は移動可能に設け、コンベア2上に図示はしていないが
被熱処理物を配置する。In the heat treatment chamber 1, leg-shaped spaces 6 and 7 having a desired height are formed at the left and right ends, only the lower ends of the spaces 6 and 7 are opened, and the lower ends of the spaces 6 and 7 are heat-treated. There are an inlet 8 and an outlet 9 of the chamber 1. The lower part 10 of the heat treatment chamber 1 has an inlet 8
The lower the slope, the lower the slope. Inlet 8 and outlet 9 are liquid container 1
The liquids 13 and 14 stored in the liquids 1 and 12 are arranged. The cooling liquid supply passage 4 is connected to the liquid reservoir 12 on the outlet 9 side via valves 30 and 31. When water is used as the liquids 13 and 14, the height of the spaces 6 and 7 is set to 10 meters or less.
Each of the endless conveyors 2 is provided so as to be held or movable by a roller 15, and an object to be heat-treated is arranged on the conveyor 2 though not shown.
【0010】減圧ポンプとしての組合せポンプ5はエゼ
クタ16とポンプ17とタンク18を組合せたもので、
ポンプ17がタンク18に吸込側を接続され吐出側をエ
ゼクタ16に接続し、エゼクタ16のディフュ―ザ19
がタンク18の上部空間に接続された構成のものであ
り、エゼクタ16と熱処理室1内を弁20を介して接続
する。この組合せポンプ5は、ポンプ17の作動により
タンク18内の水をエゼクタ16に供給して、エゼクタ
16部に吸引作用をさせてタンク18に戻すようになっ
ている。タンク18には冷却液供給通路4から弁26を
介して冷却水を補給できるようにして、エゼクタ16で
生じる吸引力をコントロ―ルできるようにする。また、
組合せポンプ5の循環路の一部に弁21を介して余剰水
排出通路22を接続する。The combination pump 5 as a decompression pump is a combination of an ejector 16, a pump 17 and a tank 18,
The pump 17 has a suction side connected to the tank 18 and a discharge side connected to the ejector 16, and the diffuser 19 of the ejector 16 is connected.
Is connected to the upper space of the tank 18, and the ejector 16 and the inside of the heat treatment chamber 1 are connected via a valve 20. The combination pump 5 supplies the water in the tank 18 to the ejector 16 by the operation of the pump 17, and causes the ejector 16 part to suck and return it to the tank 18. The tank 18 can be replenished with the cooling water from the cooling liquid supply passage 4 through the valve 26 so that the suction force generated in the ejector 16 can be controlled. Also,
An excess water discharge passage 22 is connected to a part of the circulation passage of the combination pump 5 via a valve 21.
【0011】流体供給通路としての加熱蒸気供給通路3
には、開閉弁23を設けると共に蒸気用減圧弁25を取
付ける。減圧弁25は図2に構成原理図を示すように、
入口50と出口51を弁体54で連通遮断できるもの
で、出口51部との連通孔53により出口51側圧力を
下面に受けるダイヤフラム52をバネ受け55を介して
引張り作用のコイルバネ56で上方向に付勢しているも
のである。従って、出口51側の圧力がコイルバネ56
の引張り荷重に相当する圧力よりも低下すると、ダイヤ
フラム52が下方向に変位し、同時に弁体54が開弁す
ることにより、入口50側の蒸気が出口51側に補給さ
れ、コイルバネ56の引張り荷重に相当する圧力まで回
復するとダイヤフラム52が上方向に変位して元の位置
に戻り、同時に弁体54が閉弁することにより蒸気の供
給は停止するものである。コイルバネ56の引張り荷重
は、電気モ―タ57により接続軸58を上下に移動する
ことにより調節することができるものである。本実施例
においては、減圧弁25として図2に示すような自力式
の減圧弁を用いた例を示したが、その他従来周知の圧力
制御弁等を用いることもできる。Heating steam supply passage 3 as a fluid supply passage
An on-off valve 23 is provided and a pressure reducing valve 25 for steam is attached thereto. The pressure reducing valve 25, as shown in FIG.
The inlet 50 and the outlet 51 can be disconnected by the valve body 54, and the diaphragm 52 which receives the pressure on the outlet 51 side on the lower surface by the communication hole 53 with the outlet 51 part is pulled upward by the coil spring 56 of the pulling action via the spring receiver 55. It is urged to. Therefore, the pressure on the outlet 51 side is the coil spring 56.
When the pressure is lower than the pressure corresponding to the tensile load, the diaphragm 52 is displaced downward, and the valve body 54 is opened at the same time, so that the steam on the inlet 50 side is replenished to the outlet 51 side and the tensile load on the coil spring 56 is increased. When the pressure corresponding to the pressure is recovered, the diaphragm 52 is displaced upward and returns to its original position, and at the same time, the valve body 54 is closed, so that the supply of steam is stopped. The tensile load of the coil spring 56 can be adjusted by moving the connecting shaft 58 up and down by the electric motor 57. In the present embodiment, the pressure reducing valve 25 is a self-reducing pressure reducing valve as shown in FIG.
【0012】冷却液供給通路4からは弁24を介して熱
処理室1内に冷却液の一部を供給することができるよう
にしても良い。こうすることにより熱処理室1内が所定
温度よりも昇温した場合に冷却液を供給して温度を下げ
ることができる。A part of the cooling liquid may be supplied into the heat treatment chamber 1 from the cooling liquid supply passage 4 through the valve 24. By doing so, when the temperature in the heat treatment chamber 1 rises above a predetermined temperature, the cooling liquid can be supplied to lower the temperature.
【0013】コンベア2上の被熱処理物を加熱する場合
は、蒸気供給通路3の弁23を開弁し、減圧弁25のコ
イルバネ56の引張り荷重を必要とする圧力に設定し
て、熱処理室1内に低圧蒸気を供給する。熱処理室1内
は組合せポンプ5により減圧され、減圧度に応じて空間
6,7に液柱を生じることにより所望の減圧状態となっ
ており、蒸気圧力は大気圧以下すなわち100度C以下
の蒸気となって、被熱処理物を加熱する。この場合の加
熱温度は、減圧弁25の設定圧力と組合せポンプ5の減
圧度を調節することにより任意に設定することができ
る。例えば、熱処理室1内を235ミリHgの減圧状態
に組合せポンプ5によって維持して、ほぼ同圧の蒸気を
減圧弁25から供給することにより、蒸気温度を約70
度Cとすることができる。被熱処理物を加熱して熱を奪
われた蒸気は凝縮して復水となり、熱処理室1の下部1
0の勾配に沿って入口8側の液溜容器11内に流下す
る。When heating the object to be heat-treated on the conveyor 2, the valve 23 of the steam supply passage 3 is opened, and the tension load of the coil spring 56 of the pressure reducing valve 25 is set to the required pressure, and the heat treatment chamber 1 Low-pressure steam is supplied inside. The inside of the heat treatment chamber 1 is decompressed by the combination pump 5, and a desired decompression state is created by producing liquid columns in the spaces 6 and 7 according to the degree of decompression. Then, the object to be heat treated is heated. The heating temperature in this case can be arbitrarily set by adjusting the set pressure of the pressure reducing valve 25 and the degree of pressure reduction of the combination pump 5. For example, by maintaining the inside of the heat treatment chamber 1 at a reduced pressure state of 235 mmHg by the combination pump 5 and supplying the vapor of approximately the same pressure from the pressure reducing valve 25, the vapor temperature becomes about 70.
It can be C. The steam from which the heat is removed by heating the object to be heat-treated condenses and becomes condensed water, and the lower part 1 of the heat-treatment chamber 1
It flows down along the gradient of 0 into the liquid reservoir 11 on the inlet 8 side.
【0014】加熱された被熱処理物は、コンベア2によ
り空間7を通り出口9及び液溜容器12内を経て外部に
搬出される。液溜容器12には、冷却液供給通路4から
弁30,31を介して冷却液が供給されており、通過す
る被熱処理物は熱を奪われて冷却される。液溜容器12
内に溜った余剰液は弁32または33から系外に排除さ
れる。The heated object to be heat-treated is carried out by the conveyor 2 to the outside through the space 7 and the outlet 9 and the liquid reservoir 12. The liquid reservoir 12 is supplied with the cooling liquid from the cooling liquid supply passage 4 via the valves 30 and 31, and the heat-treating object passing therethrough is deprived of heat and cooled. Liquid container 12
Excess liquid accumulated inside is removed from the system through the valve 32 or 33.
【0015】本実施例においては、減圧ポンプとして組
合せポンプ5を用いた例を示したが、もちろんその他従
来公知の真空ポンプを用いることができる。In this embodiment, the combination pump 5 is used as the decompression pump, but of course, other conventionally known vacuum pumps can be used.
【0016】[0016]
【発明の効果】本発明によれば、被熱処理物を大気圧以
下の減圧状態で蒸気加熱することができ、減圧度を調節
することにより加熱温度を任意に設定できる。従って、
90度C以下の低温であっても蒸気加熱することができ
ると共に、脚状出口の冷却液供給通路を設けた液溜によ
り、被熱処理物を効率良く且つ簡単な設備で冷却するこ
ともできる。According to the present invention, the object to be heat treated can be vapor-heated under a reduced pressure below atmospheric pressure, and the heating temperature can be set arbitrarily by adjusting the degree of reduced pressure. Therefore,
Steam heating can be performed even at a low temperature of 90 ° C. or lower, and the heat treatment target can be efficiently cooled with simple equipment by the liquid reservoir provided with the cooling liquid supply passage of the leg-shaped outlet.
【図1】本発明の減圧熱処理装置の実施例の構成図であ
る。FIG. 1 is a configuration diagram of an embodiment of a reduced pressure heat treatment apparatus of the present invention.
【図2】図1の蒸気用減圧弁の概略構成図である。FIG. 2 is a schematic configuration diagram of the pressure reducing valve for steam of FIG.
1 熱処理室 2 コンベア 3 蒸気供給通路 4 冷却液供給通路 5 組合せポンプ 6,7 脚状空間 8 入口 9 出口 11,12 液溜容器 16 エゼクタ 17 ポンプ 18 タンク 25 蒸気用減圧弁 1 Heat Treatment Room 2 Conveyor 3 Steam Supply Passage 4 Coolant Supply Passage 5 Combination Pump 6,7 Leg Space 8 Inlet 9 Outlet 11,12 Liquid Reservoir 16 Ejector 17 Pump 18 Tank 25 Steam Pressure Reducing Valve
Claims (1)
室を形成し、該熱処理室に被熱処理物を搬送する搬送手
段を配置して熱処理のための流体を供給する流体供給通
路を接続すると共に減圧ポンプを接続し、上記入口と出
口を所望高さを有する脚状に連設し、該脚状連設部の下
部に液溜を設けて、該液溜の内少なくとも出口側の液溜
に被熱処理物を冷却するための冷却液供給通路を設けた
減圧熱処理装置。1. A heat treatment chamber having an inlet and an outlet of a heat treatment object is formed, and a conveying means for conveying the heat treatment object is arranged in the heat treatment chamber to connect a fluid supply passage for supplying a fluid for heat treatment. In addition, a decompression pump is connected, the inlet and the outlet are continuously connected in a leg shape having a desired height, and a liquid reservoir is provided at the lower part of the leg-shaped connecting portion, and at least the outlet side liquid of the liquid reservoir is provided. A decompression heat treatment apparatus having a reservoir provided with a cooling liquid supply passage for cooling an object to be heat treated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4061405A JP2916726B2 (en) | 1992-02-14 | 1992-02-14 | Vacuum heat treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4061405A JP2916726B2 (en) | 1992-02-14 | 1992-02-14 | Vacuum heat treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05227928A true JPH05227928A (en) | 1993-09-07 |
JP2916726B2 JP2916726B2 (en) | 1999-07-05 |
Family
ID=13170198
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4061405A Expired - Fee Related JP2916726B2 (en) | 1992-02-14 | 1992-02-14 | Vacuum heat treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2916726B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1645199A1 (en) * | 2004-10-05 | 2006-04-12 | R.E.A. s.n.c. di Sassi e Baudin & C. | Foodstuff pasteurisation apparatus. |
JP2011078844A (en) * | 2011-01-25 | 2011-04-21 | Toshiba Home Technology Corp | Rice cooker |
-
1992
- 1992-02-14 JP JP4061405A patent/JP2916726B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1645199A1 (en) * | 2004-10-05 | 2006-04-12 | R.E.A. s.n.c. di Sassi e Baudin & C. | Foodstuff pasteurisation apparatus. |
JP2011078844A (en) * | 2011-01-25 | 2011-04-21 | Toshiba Home Technology Corp | Rice cooker |
Also Published As
Publication number | Publication date |
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JP2916726B2 (en) | 1999-07-05 |
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