JP2916726B2 - Vacuum heat treatment equipment - Google Patents
Vacuum heat treatment equipmentInfo
- Publication number
- JP2916726B2 JP2916726B2 JP4061405A JP6140592A JP2916726B2 JP 2916726 B2 JP2916726 B2 JP 2916726B2 JP 4061405 A JP4061405 A JP 4061405A JP 6140592 A JP6140592 A JP 6140592A JP 2916726 B2 JP2916726 B2 JP 2916726B2
- Authority
- JP
- Japan
- Prior art keywords
- heat treatment
- liquid
- heat
- treatment chamber
- leg
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Cookers (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- General Preparation And Processing Of Foods (AREA)
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 method for heat-treating an object to be heat-treated with a heating fluid supplied in a heat-treating chamber 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, a technique disclosed in Japanese Patent Publication No. 57-56855 has been used. This is done by arranging a conveyor that transports the heat treatment target in a steam tunnel provided with an air discharge duct that communicates with the atmosphere, installing a steam blowing pipe below the conveyor, and installing an automatic temperature control valve, etc., on this pipe. A constant temperature controller set is connected, and an automatic steam-water separator set and an automatic pressure reducing valve set are attached to required portions of the steam pipe. Steam reduced to a relatively low pressure by an automatic pressure reducing valve set,
By supplying the steam from the steam blow-out pipe into the steam tunnel through the automatic constant temperature controller set to 9
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 after heating the object to be heat-treated is low due to natural heat radiation. In addition, in order to perform cooling with cooling water, a separate cooling water tank is required, so that there is a problem that a large installation space is required and equipment costs are increased. Many foods must be cooled after the heat treatment in order to quickly proceed 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 steam temperature of less than about. This is because the inside of the steam tunnel is in an atmospheric pressure state, and the pressure and temperature of the steam are uniquely determined, and the steam becomes almost 100 ° C. under the atmospheric pressure, so that low-temperature steam cannot be produced. Depending on the type of food, if it is not more than 90 ° C., it may cause scorching or heat damage, and the above 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。Accordingly, a technical object of the present invention is to make it possible to perform heat treatment with steam to a low temperature of 90 ° C. or less, and to be able to efficiently cool with simple equipment 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。熱処理室に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、熱処理室を
減圧ポンプと接続して、熱処理室内を搬送手段としての
無端コンベアで搬送される被熱処理物を熱処理室内空間
で熱処理するものにおいて、熱処理室と空間を介してそ
の一端開放口が連通した所望高さを有する脚状連設部を
形成し、当該脚状連設部の他端開放口を上記無端コンベ
アの入口と出口とすると共に、当該脚状連設部の他端開
放口の入口側と出口側にそれぞれ液溜容器を配置し、当
該それぞれの液溜容器内に上記熱処理のための流体と同
一状の液体を溜置き、当該液体内に上記脚状連設部の他
端開放口を配置して、当該液溜容器内の液体で熱処理室
内の減圧度に応じて上記他端開放口の脚状連設部に液柱
を形成し、上記液溜容器の内少なくとも出口側の液溜容
器に冷却液供給通路を接続して当該出口側の液溜容器内
に冷却液を溜置いて被熱処理物が当該冷却液内を通過す
る間に冷却されるものである。The constitution of the reduced pressure heat treatment apparatus of the present invention is as follows. With connecting fluid supply passage for supplying the fluid for the heat treatment heat treatment chamber, by connecting the heat treatment chamber and <br/> vacuum pump, as the conveying means to a heat treatment chamber
The object to be heat treated conveyed by the endless conveyor is placed inside the heat treatment room.
Heat treatment in the heat treatment room and through the space
A leg-shaped connecting portion having a desired height to which one end opening of the
And the other end opening of the leg-shaped connecting portion is connected to the endless conveyor.
And the other end of the leg-shaped connection
Dispose reservoirs on the inlet and outlet sides of the outlet, respectively.
In each of the liquid reservoirs, the same fluid as the heat treatment is used.
A liquid is stored in the liquid, and the liquid other than the leg-shaped connecting portion is stored in the liquid.
An open end is placed, and the liquid in the reservoir is filled with heat in the heat treatment chamber.
A liquid column is attached to the leg-like connecting portion of the other end opening according to the degree of decompression inside.
Forming a reservoir volume of at least the outlet side of the fluid reservoir container
Connect the coolant supply passage bowl the outlet side of the reservoir in the container
The liquid to be heat treated is passed through the cooling liquid
It is cooled during the process.
【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。[Action] Since the inlet and the outlet are connected in a leg shape and a liquid reservoir is provided at the lower part, when the pressure in the heat treatment chamber is reduced by a vacuum pump,
A liquid column is formed in the leg portion in accordance with the degree of pressure reduction, and the inside of the heat treatment chamber is brought into a predetermined reduced pressure state. The object to be heat-treated is transferred from the liquid reservoir on the inlet side to the heat-treating chamber via the inlet by the transfer means. In this case, when a heating fluid, for example, steam is supplied from the fluid supply passage into the heat treatment chamber, the heat treatment target is heated. When a low-temperature steam or a low-pressure steam at or below the atmospheric pressure is supplied as a heating fluid, the temperature of the heat treatment chamber is reduced, so that the steam temperature is in accordance with the reduced pressure, and the steam can be heated at an arbitrary temperature of 90 ° C. or less. The object to be 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 transport means. In the liquid reservoir on the outlet side, a cooling liquid supply passage is provided, so that the cooling liquid is stored therein. When the object to be heat-treated passes therethrough, heat is taken by the cooling liquid and cooled.
【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。BRIEF DESCRIPTION OF THE DRAWINGS FIG. In FIG. 1, a box-shaped heat treatment chamber 1, an endless conveyor 2 as a conveying means, a heating steam supply passage 3, a cooling liquid supply passage 4,
A combined vacuum pump 5 as a vacuum pump constitutes a vacuum heat treatment apparatus.
【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 desired heights are formed at left and right ends, and only lower ends of the spaces 6 and 7 are opened. Let the inlet 8 and outlet 9 of the chamber 1 be. The lower part 10 of the heat treatment chamber 1 has an entrance 8
Provide a lower gradient toward the side. Inlet 8 and outlet 9 are liquid reservoir 1
The liquids 13 and 14 stored in the liquids 1 and 12 are disposed. The coolant supply passage 4 is connected to the liquid reservoir 12 on the outlet 9 side via valves 30 and 31. When water is used for the liquids 13 and 14, the heights of the spaces 6 and 7 are 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 placed on the conveyor 2 (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,
A pump 17 has a suction side connected to a tank 18, a discharge side connected to an ejector 16, and a diffuser 19 of the ejector 16.
Is connected to the upper space of the tank 18, and connects the ejector 16 and the inside of the heat treatment chamber 1 via a valve 20. In the combination pump 5, the water in the tank 18 is supplied to the ejector 16 by the operation of the pump 17, and the ejector 16 is caused to suction to return to the tank 18. The tank 18 can be supplied with cooling water from the cooling liquid supply passage 4 through a valve 26 so that the suction force generated by the ejector 16 can be controlled. Also,
A surplus water discharge passage 22 is connected to a part of the circulation path 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。Heated steam supply passage 3 as a fluid supply passage
Is provided with an on-off valve 23 and a steam pressure reducing valve 25. The pressure reducing valve 25 is configured as shown in FIG.
The inlet 50 and the outlet 51 can be cut off by a valve 54. The diaphragm 52, which receives the pressure of the outlet 51 on the lower surface by a communication hole 53 with the outlet 51, is pulled upward by a coil spring 56 of a tensile action via a spring receiver 55. It is the one that is energized. Therefore, the pressure on the outlet 51 side is
When the pressure falls below the pressure corresponding to the tensile load of the coil spring 56, the diaphragm 52 is displaced downward, and at the same time, the valve element 54 is opened. When the pressure is restored to the pressure corresponding to the pressure, the diaphragm 52 is displaced upward and returns to the original position. At the same time, the supply of steam is stopped by closing the valve body 54. The tensile load of the coil spring 56 can be adjusted by moving the connection shaft 58 up and down by the electric motor 57. In the present embodiment, an example in which a self-acting pressure reducing valve as shown in FIG. 2 is used as the pressure reducing valve 25 has been described, but a conventionally known pressure control valve or the like may be used.
【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 coolant may be supplied from the coolant supply passage 4 into the heat treatment chamber 1 through the valve 24. By doing so, when the temperature inside the heat treatment chamber 1 rises above a predetermined temperature, a 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 the object to be heat-treated on the conveyor 2 is heated, the valve 23 of the steam supply passage 3 is opened, and the tension of the coil spring 56 of the pressure reducing valve 25 is set to a required pressure. Supply low-pressure steam inside. The interior of the heat treatment chamber 1 is depressurized by the combination pump 5, and a desired pressure is reduced by generating liquid columns in the spaces 6 and 7 in accordance with the degree of depressurization. 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 of 235 mmHg by the combination pump 5 and supplying steam of substantially the same pressure from the pressure reducing valve 25, the steam temperature is reduced to about 70
Degree C. The steam deprived of heat by heating the object to be heat-treated is condensed and condensed, and is condensed.
It flows down into the liquid reservoir 11 on the inlet 8 side along a gradient of zero.
【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 conveyed to the outside via the outlet 9 and the inside of the liquid reservoir 12 through the space 7 by the conveyor 2. The coolant is supplied to the liquid reservoir 12 from the coolant supply passage 4 via the valves 30 and 31, and the heat-treating object passing therethrough is deprived of heat and cooled. Liquid reservoir 12
The excess liquid accumulated inside is discharged out of 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, an example is shown in which the combination pump 5 is used as a pressure reducing pump. However, 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 steam-heated under reduced pressure below the atmospheric pressure, and the heating temperature can be arbitrarily set by adjusting the degree of reduced pressure. Therefore,
Steam heating can be performed even at a low temperature of 90 ° C. or less, and the object to be heat-treated can be cooled efficiently and with simple equipment by the liquid reservoir provided with the cooling liquid supply passage at 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 steam pressure reducing valve of FIG. 1;
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 DESCRIPTION OF SYMBOLS 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 Vacuum pressure reducing valve
Claims (1)
る流体供給通路を接続すると共に、熱処理室を減圧ポン
プと接続して、熱処理室内を搬送手段としての無端コン
ベアで搬送される被熱処理物を熱処理室内空間で熱処理
するものにおいて、熱処理室と空間を介してその一端開
放口が連通した所望高さを有する脚状連設部を形成し、
当該脚状連設部の他端開放口を上記無端コンベアの入口
と出口とすると共に、当該脚状連設部の他端開放口の入
口側と出口側にそれぞれ液溜容器を配置して、当該それ
ぞれの液溜容器内に上記熱処理のための流体と同一状の
液体を溜置き、当該液体内に上記脚状連設部の他端開放
口を配置して、当該液溜容器内の液体で熱処理室内の減
圧度に応じて上記他端開放口の脚状連設部に液柱を形成
し、上記液溜容器の内少なくとも出口側の液溜容器に冷
却液供給通路を接続して当該出口側の液溜容器内に冷却
液を溜置いて被熱処理物が当該冷却液内を通過する間に
冷却されるをことを特徴とする減圧熱処理装置。1. A with connecting fluid supply passage for supplying the fluid for the heat treatment heat treatment chamber, the heat treatment chamber connected to the vacuum pump, an endless con as conveying means a heat treatment chamber
Heat treatment of the object to be heat-transferred by the bare inside the heat treatment room
To open one end through the heat treatment chamber and space
Forming a leg-shaped connecting portion having a desired height with which the outlet communicates ,
Open the other end of the leg-shaped continuous part to the entrance of the endless conveyor.
As well as the outlet, and the inlet of the other
Dispose the liquid reservoirs on the mouth side and the outlet side, respectively.
In each of the reservoirs, the same
Liquid is stored and the other end of the leg-shaped connecting portion is opened in the liquid.
Arrange the opening to reduce the heat inside the heat treatment chamber with the liquid in the reservoir.
A liquid column is formed in the leg-like connecting portion of the above-mentioned other opening according to the pressure
A cooling liquid supply passage is connected to at least the liquid storage container on the outlet side of the liquid storage container to cool the liquid storage container on the outlet side.
While the liquid is stored and the object to be heat treated passes through the cooling liquid,
A vacuum heat treatment apparatus characterized by being cooled .
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 JPH05227928A (en) | 1993-09-07 |
| JP2916726B2 true 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) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ITTO20040664A1 (en) * | 2004-10-05 | 2005-01-05 | R E A S N C Di Sassi E Baudin | APPARATUS FOR PASTEURIZATION OF FOOD PRODUCTS |
| JP5482677B2 (en) * | 2011-01-25 | 2014-05-07 | 東芝ホームテクノ株式会社 | rice cooker |
-
1992
- 1992-02-14 JP JP4061405A patent/JP2916726B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05227928A (en) | 1993-09-07 |
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