JPH037534A - Device for treating food raw material under pressure - Google Patents

Device for treating food raw material under pressure

Info

Publication number
JPH037534A
JPH037534A JP20353989A JP20353989A JPH037534A JP H037534 A JPH037534 A JP H037534A JP 20353989 A JP20353989 A JP 20353989A JP 20353989 A JP20353989 A JP 20353989A JP H037534 A JPH037534 A JP H037534A
Authority
JP
Japan
Prior art keywords
pressure
chamber
vessel
food materials
processed
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
Application number
JP20353989A
Other languages
Japanese (ja)
Other versions
JPH0757159B2 (en
Inventor
Takeshi Kanda
剛 神田
Yasuhiko Inoue
康彦 井上
Yoshihiko Sakashita
由彦 坂下
Masahisa Sawada
昌久 澤田
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP1203539A priority Critical patent/JPH0757159B2/en
Publication of JPH037534A publication Critical patent/JPH037534A/en
Publication of JPH0757159B2 publication Critical patent/JPH0757159B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Processing Of Meat And Fish (AREA)

Abstract

PURPOSE:To make it possible to operate a device under pressure conditions of thousands kgf/cm<2> by providing a pressure medium feeding and pressure feeding device and providing a pressure vessel capable of feeding a material to be heat-treated and free piston packed into the vessel. CONSTITUTION:A required definite amount of food raw material containing an animal protein consisting of fish meat as a main ingredient is fed into each chamber 21a, 21b and 21c. Then a pressure medium in a pressure medium tank 12 is fed from each through hole 31a to 31c of each closing member 3a to 3c through a pressure control valve 11 and opening and closing valve 9 into each chamber 6a to 6c in required pressure using a pressure pump 8 by a pressure medium feeding and pressure controlling device 7. As a result, free pistons 4a to 4c are pressurized and moved and pressure action is exerted to each material to be treated in chambers 21a to 21c and simultaneously material to be treated in chambers 21a to 21c of each pressure vessel 1a is subjected to heating action in parallel with the pressure action.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、食品素材、特には魚肉等から成る動物性蛍白
を主成分とする食品素材を、加圧下で溶融するための装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to an apparatus for melting food materials under pressure, particularly food materials whose main component is animal fluorescent material such as fish meat.

(従来の技術) 従来魚肉等は、その加工製品としては周知のように蒲鉾
、竹輪等の練り製品として供用されるか、あるいは魚粉
として知られるように、粉体状の熱変性魚肉として、飼
料等に供用されることがほとんどであり、これらの加工
に際して用いられる物理的状態変数としては、温度を中
心としてその技術展開が行われてきた。しかるに最近で
は、高圧下における蛋白変性等を利用する食品加工技術
が開発され、新技術として注目を浴びるとともに、多種
の応用が試みられつつある処で、このような食品加工へ
の圧力利用に関しては、例えば相違通する双円筒断面の
シリンダ内に一対のスクリュ軸乃至ブレード軸を可回動
に並設する型式の二軸エクストルーダが1例として認め
られるが、同装置の場合、あくまで温度と撹拌、混練、
剪断等の機械的作用効果により、当該食品素材の変性、
組織化を行なおうとするものであり、その圧力は意図的
にコントロールされるものでなく、その素材物性によっ
て変化する不安定なものであり、また例えば1(101
(10O/c4のような高圧力を作用させる訳にはゆか
ないもであった。
(Prior art) Conventionally, fish meat, etc., has been used as processed products such as paste products such as kamaboko and chikuwa, or as feed, etc. as powdered heat-denatured fish meat, known as fish meal. The technology has mainly been developed with temperature as the physical state variable used in these processes. However, recently, food processing technology that utilizes protein denaturation under high pressure has been developed, and it has attracted attention as a new technology, and various applications are being attempted. For example, a two-screw extruder in which a pair of screw shafts or blade shafts are rotatably arranged side by side in cylinders with different bicylindrical cross sections is recognized as an example, but in the case of this device, temperature, stirring, kneading,
Due to mechanical effects such as shearing, denaturation of the food material,
The pressure is not intentionally controlled, but is unstable and changes depending on the physical properties of the material.For example, 1 (101
(It was not possible to apply a high pressure such as 10O/c4.

一方圧力の存在が食品加工、とりわけ魚肉等から成る動
物性蛋白を主成分とする食品素材の加工に有効であるこ
とは、特開昭62−40255号公報あるいは特開昭6
2−40267号公報に開示される通りである。即ち、
魚肉すり身あるいは熱変性魚肉に対し、1(10〜2(
10°Cで加熱処理を施すことを1〜5分間持続するこ
とにより、溶融体が得られることが開示されており、特
に圧力の存在下において従来になかった効果が引出され
ることは注目に値する点である。
On the other hand, the presence of pressure is effective in food processing, especially in the processing of food materials whose main component is animal protein, such as fish meat, as disclosed in JP-A-62-40255 and JP-A-6.
This is as disclosed in Japanese Patent No. 2-40267. That is,
For minced fish meat or heat-denatured fish meat, add 1 (10 to 2)
It is disclosed that a melt can be obtained by applying heat treatment at 10°C for 1 to 5 minutes, and it is noteworthy that unprecedented effects are brought out, especially in the presence of pressure. This is a worthy point.

(発明が解決しようとする課題) 上記した従来技術の内、魚肉等から成る動物性蛋白を主
成分とする食品素材に対し、加熱、加圧処理を施すこと
により溶融状態を得る方法において、本発明は、これを
実験室的乃至は工業的量産規模のもとに実現する具体的
装置として、加圧下で安定的にかつ効率的に溶融させる
ことが可能であるとともに、その圧力条件を従来の数1
0 kg f / c+aのレベルに止まることなく、
数1(101(10O/c4のレベルまで引上げても、
尚安定的に動作させることのできる加圧上溶融装置を提
供し、また併せてその温度と圧力との相乗効果を利用し
た食品加工に好適な処理装置の提供をも意図したもので
ある。
(Problems to be Solved by the Invention) Among the above-mentioned conventional techniques, the present invention is a method for obtaining a molten state by heating and pressurizing a food material whose main component is animal protein, such as fish meat. The present invention is a concrete device that realizes this on a laboratory or industrial mass production scale, which is capable of stably and efficiently melting under pressure, and which also improves the pressure conditions from conventional ones. Number 1
without stopping at the level of 0 kg f/c+a,
Even if it is raised to the level of number 1 (101 (10O/c4),
The present invention is intended to provide a pressurized melting device that can operate stably, and also to provide a processing device suitable for food processing that utilizes the synergistic effect of temperature and pressure.

(課題を解決するための手段) 本発明は上記した目的を達成するために、フリーピスト
ンによって2室に分割される圧力容器の一方の室に被処
理物を供給するとともに、他方の室に圧媒を供給して加
圧するとともに、同時に被処理物に対して熱作用を及ぼ
すことができるようにしたものである。具体的には、圧
力容器と、該圧力容器内に充填されたフリーピストンと
から成り、圧力容器の前記ピストンにより距てられた一
方の室には圧媒の供給並びに圧力調整装置が接続される
とともに、他方の室には被処理物が供給可能とされ、か
つ圧力容器内の被処理物に対する熱処理手段が設けられ
ている点に特徴がある。
(Means for Solving the Problems) In order to achieve the above-mentioned object, the present invention supplies a workpiece to one chamber of a pressure vessel divided into two chambers by a free piston, and pressurizes the other chamber. It is designed so that a medium can be supplied and pressurized, and at the same time, a thermal effect can be exerted on the object to be treated. Specifically, it consists of a pressure vessel and a free piston filled in the pressure vessel, and a pressure medium supply and pressure adjustment device is connected to one chamber separated by the piston of the pressure vessel. In addition, the other chamber is characterized in that the object to be processed can be supplied thereto, and a heat treatment means for the object to be processed in the pressure vessel is provided.

また、複数個の圧力容器は、共通の圧媒並びに圧力調整
装置に接続することができ、前記熱処理手段として、圧
力容器を被包するジャケットを備えた加熱および/また
は冷却液循環手段を用いることができる。
Furthermore, the plurality of pressure vessels can be connected to a common pressure medium and pressure regulating device, and the heat treatment means may include a heating and/or cooling liquid circulation means provided with a jacket enclosing the pressure vessels. I can do it.

そして、前記フリーピストンは、その少くとも1つを増
圧型とすることができる。
At least one of the free pistons may be of a pressure increasing type.

さらに、前記被処理物が流動状である場合は、被処理物
を圧力容器の他の室に、ポンプにより供給するのが好ま
しく、その供給系路に設けられる開閉弁は、その開閉位
置を前記他の室内に近い部分に配するのが望ましい。
Further, when the object to be processed is in a fluid state, it is preferable to supply the object to be processed into another chamber of the pressure vessel by a pump, and the on-off valve provided in the supply line is set to the above-mentioned opening/closing position. It is preferable to place it near the rest of the room.

また圧媒の供給並びに圧力調整装置から、圧力容器の一
方の室への供給圧媒は水とすることができ、さらにまた
圧媒の供給並びに圧力調整装置から、圧力容器の一方の
室への供給圧媒により、フリーピストンを移動させ、他
方の室内の処理済み被処理物を取出し可能とすることが
できる。
Furthermore, the pressure medium supplied from the pressure medium supply and pressure regulating device to one chamber of the pressure vessel can be water, and furthermore, the pressure medium supplied from the pressure medium supply and pressure regulating device to one chamber of the pressure vessel The free piston can be moved by the supplied pressure medium, and the processed material in the other chamber can be taken out.

(作 用) 本発明の上記した技術的手段によれば、フリーピストン
によって距てられた圧力容器の他方の室に被処理物を供
給するとともに、これと対応する一方の室に圧媒供給並
びに圧力調整装置によって、所要の圧力値に調整した圧
媒を供給することにより、フリーピストンの加圧移動に
よって被処理物は加圧処理され、このさい被処理物を熱
処理手段により加熱および/または冷却処理することに
よって、被処理物は加圧と併行して熱作用を同時に受け
、加圧上溶融等の処理結果を任意に実現することができ
る。従って、この圧力容器内への被処理物の供給を自動
化し、圧媒供給並びに圧力調整装置および熱処理手段に
おける圧力コントロールと加熱および/ま、たは冷却温
度のコントロールを自動化することにより、安定した均
質の圧力・温度加工条件下に、かつ実験室的乃至は工業
的量産規模下に食品素材等の処理が可能である。加熱、
加圧処理によって魚肉等から成る動物性蛋白を主成分と
する食品素材を、溶融状態の製品とする場合、特にその
加熱温度が1(10″Cを越える場合には、常圧下では
食品中に含有する水分が沸騰するので、これを抑制する
という観点から、適切な加圧下に加熱並びに冷却に行な
うことが必要であるが、このような操作を確実かつ容易
に行なうことができる。
(Function) According to the above-mentioned technical means of the present invention, the material to be treated is supplied to the other chamber of the pressure vessel separated by the free piston, and the pressure medium is supplied to the corresponding one chamber. By supplying the pressure medium adjusted to the required pressure value by the pressure regulating device, the workpiece is subjected to pressure treatment by pressurizing movement of the free piston, and at this time, the workpiece is heated and/or cooled by the heat treatment means. By processing, the object to be processed is simultaneously subjected to pressure and heat action, and it is possible to arbitrarily achieve processing results such as melting under pressure. Therefore, by automating the supply of the material to be treated into the pressure vessel, automating the supply of pressure medium, the pressure control in the pressure adjustment device and the heat treatment means, and the control of the heating and/or cooling temperature, stable It is possible to process food materials, etc. under homogeneous pressure and temperature processing conditions and on a laboratory or industrial mass production scale. heating,
When pressure-processing a food material whose main component is animal protein, such as fish meat, into a molten product, especially if the heating temperature exceeds 1 (10"C), there may be Since the contained water boils, it is necessary to heat and cool it under appropriate pressure in order to suppress this boiling, but such operations can be carried out reliably and easily.

また、フリーピストンを距てて2室を形成したので、圧
媒と被処理物との混合、接触がなく安全性、清浄性を確
保されることも有利である。
Further, since the two chambers are formed with the free piston apart, there is no mixing or contact between the pressure medium and the object to be treated, which is advantageous in that safety and cleanliness are ensured.

そして、複数個の圧力容器が、共通の、即ち一基の圧媒
供給並びに圧力調整装置に連帯して接続されているので
、複数個の各圧力容器内の被処理物の均一同時加圧処理
が容易で、量産目的を達成し易く、従ってまた個々の圧
力容器は小型、薄肉化でき、熱伝達性も良好化して熱処
理手段による加熱および/または冷却も効率よく行なう
ことができるのである。
Since the plurality of pressure vessels are jointly connected to a common pressure medium supply and pressure adjustment device, uniform and simultaneous pressurization of the objects to be treated in each of the plurality of pressure vessels is possible. Therefore, individual pressure vessels can be made smaller and thinner, heat transfer properties are improved, and heating and/or cooling by heat treatment means can be performed efficiently.

また本発明では熱処理手段として、加熱および/または
冷却可能であるとともに、圧力容器を被包するジャケッ
トを備えた加熱液、冷却液の液循環装置を用いたので、
先ずその熱処理が単に加熱のみでなく、温間から熱間域
に亘る加熱と、マイナス温度域に亘る冷却の何れもが可
能で、これによって加熱後の冷却、冷却後の加熱という
ように加熱・冷却の広汎な操作ができ、被処理物に対す
る適切な熱処理操作が任意のパターンで得られ、また加
熱液または冷却液を循環させる型式としたので、必要な
熱処理を確実かつ容易に行ない得るし、温度コントロー
ルも容易である。
In addition, in the present invention, as a heat treatment means, a liquid circulation device for heating liquid and cooling liquid is used, which is capable of heating and/or cooling and is equipped with a jacket that covers the pressure vessel.
First of all, the heat treatment is not just heating, but also heating ranging from warm to hot range, and cooling ranging from negative temperature range. A wide range of cooling operations can be performed, appropriate heat treatment operations can be performed on the object to be treated in any pattern, and since the heating liquid or cooling liquid is circulated, the necessary heat treatment can be carried out reliably and easily. Temperature control is also easy.

なお、被処理物が流動状のときは、圧力容器の他方の室
に、ポンプにより送給可能としたので、多数の圧力容器
に対して、例えばスラリー状の被処理物を円滑かつ自動
化して供給でき、量産目的の達成を容易とするし、迅速
に処理可能である。
In addition, when the material to be processed is in a fluid state, it can be fed to the other chamber of the pressure vessel using a pump, so that the material to be processed, for example in the form of slurry, can be smoothly and automatically transferred to a large number of pressure vessels. It is easy to supply, easy to achieve mass production objectives, and can be processed quickly.

さらに、本発明では、被処理物の他方の室への供給を開
閉弁によって規制し、その開閉弁の開閉位置が、他方の
室における室内に近い部分に設けることによって、同室
に収容した被処理物に対して、熱処理手段を働かせるさ
い、その熱作用の均質性を確保すること、ができる。
Furthermore, in the present invention, the supply of the workpieces to the other chamber is regulated by the on-off valve, and the opening/closing position of the on-off valve is provided in a part of the other chamber close to the room, whereby the workpieces housed in the same chamber are When applying a heat treatment means to an object, it is possible to ensure the homogeneity of the heat action.

また、圧媒の供給並びに圧力調整装置から、圧力容器の
一方の室への供給圧媒が水とされることによって、フリ
ーピストンの移動に伴い、圧媒が圧力容器内面に付着し
、他方の室に収容した被処理物と接触する可能性がある
ので、これを防止し、被処理物の清浄性を守る意味にお
いて有益である。
In addition, since the pressure medium supplied from the pressure medium supply and pressure adjustment device to one chamber of the pressure vessel is water, the pressure medium adheres to the inner surface of the pressure vessel as the free piston moves, and the other chamber Since there is a possibility of contact with the objects to be processed stored in the chamber, this is useful in terms of preventing this and protecting the cleanliness of the objects to be processed.

なお、圧媒の供給並びに圧力調整装置から、圧力容器の
一方の室への供給圧媒によって、他方の室内に存在して
いる処理済みの被処理物を、前記圧媒によって移動する
フリーピストンを介して圧力容器外に押出して、被処理
物の取出しが高圧の圧力容器の開閉を伴うことな(、簡
単かつ容易に圧力容器外に取出せるため、一連の処理作
業の自動化に寄与し、作業性を良好とすることができる
In addition, by supplying pressure medium to one chamber of the pressure vessel from the pressure medium supply and pressure regulating device, a free piston is moved by the pressure medium to move the processed material existing in the other chamber. The material to be processed can be easily and easily removed from the pressure vessel without having to open and close the high-pressure pressure vessel, contributing to the automation of a series of processing operations and reducing the properties can be improved.

そして、前記フリーピストンの少くとも1つが、増圧型
とされているので、圧媒の圧力よりも大きな圧力によっ
て、被処理物の加圧処理ができる。
Since at least one of the free pistons is of a pressure increasing type, the object to be treated can be subjected to pressure treatment using a pressure greater than the pressure of the pressure medium.

さらに、各圧力容器を被包するジャケットに加熱手段を
設けることによって、必らずしも熱媒を循環させること
なく、効率的に加熱制御することができる。
Furthermore, by providing a heating means in the jacket enclosing each pressure vessel, heating can be efficiently controlled without necessarily circulating a heat medium.

(実施例) 本発明装置の適切な実施例を図について説示する。第1
図は本発明の第1実施例で、複数個の圧力容器例として
3個のものを示したが、その数はもとより自由であり、
各圧力容器1a、 lbおよびICは、何れも軸方向両
端が開口され、これら両開口にはそれぞれ閉塞部材2a
、2bおよび2C1閉塞部材3a、3bおよび3cがそ
れぞれ着脱可能に嵌設され、かつシール構造等を介し密
封される。これら閉塞部材2a〜2cおよび3a〜3c
には、圧媒による加圧施工時に軸力が働くので、これら
軸力を支承するため、図示のように圧力容器開口に対し
てネジ嵌合構造とするか、また被処理物出入の簡便性を
考慮して、例えば段隔式のネジ嵌合構造、あるいは再閉
塞部材2a〜2cおよび3a〜3Cに亘ってプレスフレ
ームで挟持する支承構造とすることができる。各圧力容
器1 a = 1 c内には、シール部材5a、5bお
よび5cをそれぞれ具備したフリーピストン4a、4b
および4cが摺動可能に装填される。該ピストン4a〜
4Cによって2室に分割された各圧力容器18〜ICに
おける一方の室(圧媒室)6a、6bおよび6Cには、
圧媒供給並びに圧力調整装置7が共通に接続される。
(Example) A suitable example of the device of the present invention will be described with reference to the drawings. 1st
The figure shows the first embodiment of the present invention, and three pressure vessels are shown as an example of a plurality of pressure vessels, but the number can be freely selected.
Each of the pressure vessels 1a, lb and IC is opened at both ends in the axial direction, and a closing member 2a is attached to each of these openings.
, 2b and 2C1 closing members 3a, 3b and 3c are respectively removably fitted and sealed via a seal structure or the like. These closing members 2a to 2c and 3a to 3c
In order to support these axial forces, it is necessary to use a screw-fitting structure for the pressure vessel opening as shown in the figure, or to make it easier to take in and out the objects to be treated. In consideration of this, for example, a stepped screw fitting structure or a support structure in which the reclosure members 2a to 2c and 3a to 3C are sandwiched between press frames can be used. Inside each pressure vessel 1a = 1c, free pistons 4a, 4b are provided with seal members 5a, 5b and 5c, respectively.
and 4c are slidably loaded. The piston 4a~
One chamber (pressure medium chamber) 6a, 6b and 6C in each pressure vessel 18 to IC divided into two chambers by 4C,
A pressure medium supply and a pressure regulating device 7 are connected in common.

該装置7は圧媒タンク12と各閉塞部材3a〜3Cに設
けた各通孔31a、31bおよび31cをつなぐ回路3
2に、加圧ポンプ8、開閉弁9,10、圧力調整弁11
、減圧弁11°を配設し、圧媒タンク12内の圧媒を加
圧ポンプ8および圧力調整弁11を介して所要圧力に加
圧し、これを開閉弁9を介し各通孔31a、31bおよ
び31cを経て室6a 、 6bおよび6C内に供給可
能とするのであり、また所定圧の維持、更には減圧、回
収を開閉弁10を介して可能とするのである。このさい
圧媒の加圧供給に関しては、比較的低圧の場合には図示
例のように電動式のポンプを利用できるが、高圧の場合
には例えば油圧駆動の増圧機タイプのもの等を用いるこ
とが好適であるが、勿論制限されない。更に第1実施例
では、各圧力容器la、 lbおよびlcを共通に被包
するジャケット13を設け、該ジャケラ目3に、加熱お
よび/または冷却可能な熱処理手段としての液循環装置
16を接続する。該装置16は、液タンク18とジャケ
ット13とをつなぐ循環管路14.Isに、循環ポンプ
17、開閉弁33.34および35を配設するとともに
、液タンク18には加熱器19および冷却器20を設け
たものである。そして、加熱器19によって加熱した熱
媒液および/または冷却器20によって冷却した冷媒を
、循環ポンプ17および管路14.15によりジャケッ
ト13内と液タンク18を循環させて、各圧力容器1a
+1bおよびlc内の各被処理物の加熱および/または
冷却を行なう。このさいジャケット13は、各圧力容器
1a〜1cを共通に被包する代わりに、各容器1a〜l
c毎にジャケットを設けてもよく、あるいはその熱処理
が加熱のみでよい場合には、各圧力容器1a=1cの外
周に通電バンドヒータ等を付設する構造のものとするこ
ともできる。尚、第1図において36は圧媒供給並びに
圧力調整装置7における圧力計、37は液循環装置16
における圧力計を示している。
The device 7 includes a circuit 3 that connects the pressure medium tank 12 and each of the through holes 31a, 31b, and 31c provided in each of the closing members 3a to 3C.
2, pressure pump 8, on-off valves 9, 10, pressure regulating valve 11
, a pressure reducing valve 11° is provided, the pressure medium in the pressure medium tank 12 is pressurized to a required pressure via the pressure pump 8 and the pressure regulating valve 11, and the pressure medium is transferred to the respective through holes 31a, 31b via the on-off valve 9. and 31c into the chambers 6a, 6b, and 6C, and it is also possible to maintain a predetermined pressure, further reduce the pressure, and recover it through the on-off valve 10. Regarding pressurized supply of the pressure medium at this time, if the pressure is relatively low, an electric pump can be used as shown in the example shown, but if the pressure is high, for example, a hydraulically driven pressure intensifier type pump may be used. is preferable, but is of course not limited. Furthermore, in the first embodiment, a jacket 13 is provided that commonly covers the pressure vessels la, lb, and lc, and a liquid circulation device 16 as a heat treatment means capable of heating and/or cooling is connected to the jacket 3. . The device 16 includes a circulation pipe 14. which connects the liquid tank 18 and the jacket 13. Is is provided with a circulation pump 17 and on-off valves 33, 34 and 35, and the liquid tank 18 is provided with a heater 19 and a cooler 20. Then, the heat medium liquid heated by the heater 19 and/or the refrigerant cooled by the cooler 20 are circulated within the jacket 13 and the liquid tank 18 by the circulation pump 17 and the pipe line 14.15, so that each pressure vessel 1a
+1b and lc are heated and/or cooled. In this case, the jacket 13 covers each of the pressure vessels 1a to 1c in common, and instead of encasing the pressure vessels 1a to 1c in common,
A jacket may be provided for each pressure vessel 1a, or if the heat treatment requires only heating, a structure may be adopted in which a current-carrying band heater or the like is attached to the outer periphery of each pressure vessel 1a=1c. In FIG. 1, 36 is a pressure gauge in the pressure medium supply and pressure adjustment device 7, and 37 is a pressure gauge in the liquid circulation device 16.
The pressure gauge is shown.

また第1実施例では、圧力容器1a〜IC内の各フリー
ピストン4a〜4cによって距てられた他方の室(被処
理物収容室)21a、 21bおよび21c内に被処理
物を供給する構造として、脱泡用(エア抜き)真空ポン
プ30を開閉弁38とともに具備した被処理物供給タン
ク22と供給ポンプ23、開閉弁24間に供給管路39
を設け、前記開閉弁24と各圧力容器1a〜ICの各閉
塞部材2a〜2Cにそれぞれ設けた通孔40a、40b
および40cとの間に出入管路41を共通に接続連通さ
せである。したがって、タンク22内にストックした食
品素材等の被処理物は、前記供給管路39から供給ポン
プ23により、開閉弁24、出入管路41を介して各通
孔40a〜40c側に供給され、該通孔40a〜40c
にそれぞれ開閉可能に封止された開閉弁25a。
In addition, in the first embodiment, the structure is such that the material to be processed is supplied into the other chambers (material storage chambers) 21a, 21b, and 21c separated by the free pistons 4a to 4c in the pressure vessels 1a to IC. A supply pipe line 39 is provided between the workpiece supply tank 22, which is equipped with a defoaming (air bleed) vacuum pump 30 together with an on-off valve 38, the supply pump 23, and the on-off valve 24.
and through holes 40a and 40b provided in the on-off valve 24 and each of the closing members 2a to 2C of the pressure vessels 1a to IC, respectively.
and 40c, an inlet/outlet pipe 41 is commonly connected and communicated therewith. Therefore, the objects to be processed such as food materials stocked in the tank 22 are supplied from the supply pipe line 39 by the supply pump 23 to the respective through holes 40a to 40c via the on-off valve 24 and the inlet/outlet pipe line 41, The through holes 40a to 40c
On-off valves 25a each are sealed so as to be openable and closable.

25bおよび25cの開放によって、被処理物は各圧力
容器1a〜1cの各室21a、 21bおよび21c内
に供給される。このさい前記した開閉弁25a〜25c
においては、通孔40a〜40cの各閉止部26a 、
 26bおよび26cの設置位置(閉止時)は、室21
a〜21cの各室端に近い位置に位置するように設置す
る。これは収容された被処理物に対する被処理手段にお
ける熱作用の均質性を確保する点において適切である。
By opening 25b and 25c, the object to be processed is supplied into each chamber 21a, 21b and 21c of each pressure vessel 1a to 1c. At this time, the above-mentioned on-off valves 25a to 25c
In, each closing portion 26a of the through holes 40a to 40c,
The installation positions of 26b and 26c (when closed) are in the chamber 21.
It is installed so as to be located close to the end of each chamber a to 21c. This is appropriate in ensuring the homogeneity of the heat action in the processing means on the accommodated processing objects.

また第1実施例においては、開閉弁24と各閉塞部材2
a〜2cの各通孔40a〜40cとをつなぐ出入管路4
1の一端を延長して回収管路42を設け、同管路42を
開閉弁28を介して処理済み被処理物の回収タンク27
に接続してあり、前記開閉弁28の直前に分岐開閉弁2
9を配設しである。従ってこの回収タンク27および回
収管路42を介して、各圧力容器1a〜1cの各室21
a〜21c内に収容し、かつ目的の加圧および加熱また
は冷却加工して処理済みの被処理物を、各圧力容器外に
取出し回収するに当っては、被処理物の前記処理完了後
、開閉弁25a〜25cを何れも開放姿勢として、閉止
部26a〜26cによる各通孔40a〜40cの閉止を
解放し、圧力容器1a〜1cの室6a〜6c内に、圧媒
供給並びに圧力調整装置7から、所要圧力の圧媒を圧送
し、これによる各フリーピストン4a〜4cの移動によ
り、室21a〜21c内に存在している被処理物(処理
済み)を、通孔40a〜40c、出入管路41(このさ
い開閉弁24は閉とする)、から回収管路42および開
閉弁28を介し、回収タンク27内に自動的に取出し、
回収することができる。この処理済み製品の取出しに当
たっては、それ程の大圧力は必要としないので、圧媒供
給並びに圧力調整装置7における加圧ポンプ8を、別箇
の例えば大容量の低圧ポンプとすることも可能である。
Further, in the first embodiment, the on-off valve 24 and each closing member 2
Inlet/outlet pipe 4 connecting each through hole 40a to 40c of a to 2c
A collection pipe 42 is provided by extending one end of 1, and the pipe 42 is connected to a collection tank 27 for the processed material via an on-off valve 28.
A branch on-off valve 2 is connected to the on-off valve 2 immediately before the on-off valve 28.
9 is arranged. Therefore, each chamber 21 of each pressure vessel 1a to 1c is
When taking out and recovering the processed objects stored in a to 21c and subjected to the desired pressurization and heating or cooling processing to the outside of each pressure vessel, after the completion of the processing of the processed objects, All of the on-off valves 25a to 25c are set in the open position, and the respective through holes 40a to 40c are released from the closure by the closing parts 26a to 26c, and the pressure medium is supplied and the pressure adjustment device is supplied into the chambers 6a to 6c of the pressure vessels 1a to 1c. 7, the pressure medium at the required pressure is fed, and by the movement of each free piston 4a to 4c, the objects to be processed (processed) existing in the chambers 21a to 21c are moved through the through holes 40a to 40c, in and out. It is automatically taken out from the pipe 41 (the on-off valve 24 is closed at this time) into the recovery tank 27 via the recovery pipe 42 and the on-off valve 28,
It can be recovered. Since such a large pressure is not required to take out the processed product, the pressurizing pump 8 in the pressure medium supply and pressure regulating device 7 can be replaced with a separate large-capacity, low-pressure pump, for example. .

また第1実施例においては、圧力容器18〜1cの各閉
塞部材28〜2cに設ける開閉弁25a〜25cとして
、閉塞部材28〜2C一端に設けたシリンダ機構のピス
トンロンドを利用し、加圧昇降自在として閉塞部材28
〜2c、通孔40a〜40cに亘って貫挿したものを示
したが、この取出し用の開閉弁を、閉止部26a〜26
cとは別個に設けることも、収容される被処理物との混
合を防止する上から適当である。
Further, in the first embodiment, as the on-off valves 25a to 25c provided in each of the closing members 28 to 2c of the pressure vessels 18 to 1c, a piston rond of a cylinder mechanism provided at one end of the closing members 28 to 2C is used to pressurize the lift up and down. Closing member 28 as a free
2c and 40a through 40c are shown;
It is also appropriate to provide it separately from c to prevent mixing with the processed material to be accommodated.

本発明装置において用いる圧媒としては、フリーピスト
ン48〜4cの移動に伴い、圧力容器内面に付着して被
処理物と接する可能性があるため、食品素材の清浄性確
保の点から、また経済性の点からも水が最適なものとし
て推奨されるが、もとよりこれに限定されるものでない
As the pressure medium used in the apparatus of the present invention may adhere to the inner surface of the pressure vessel and come into contact with the object to be processed as the free pistons 48 to 4c move, it is important to use the Although water is recommended as the most suitable water from the viewpoint of properties, it is not limited to this.

上記第1実施例によれば、例えば魚肉等から成る動物性
蛋白を主成分とする食品素材を、被処理物として加圧、
熱処理によって溶融状態の製品とするに当たっては、各
圧力容器18〜1cにおける他方の室21a〜21c内
に被処理物を投入、供給するのである。このさい被処理
物を凍結、固化して、閉塞部材28〜2cを開放して室
21a〜21c内に投入したり、またスラリー状にする
ことが可能な場合には、第1図の状態で供給タンク22
から供給ポンプ23を用い、開閉弁24および開閉弁2
5a〜25cを経て、各閉塞部材2a〜2cの各通孔4
0a〜40cから各室21a、21b、21c内に所要
定量を供給充填する。
According to the first embodiment, a food material whose main component is animal protein, such as fish meat, is pressurized and processed as an object to be processed.
In order to produce a molten product by heat treatment, the material to be treated is introduced into the other chambers 21a to 21c of each pressure vessel 18 to 1c. At this time, if it is possible to freeze and solidify the material to be treated and introduce it into the chambers 21a to 21c by opening the closing members 28 to 2c, or to make it into a slurry, the material is in the state shown in FIG. Supply tank 22
Using the supply pump 23 from the on-off valve 24 and the on-off valve 2
5a to 25c, each through hole 4 of each closing member 2a to 2c
A required amount is supplied and filled into each chamber 21a, 21b, 21c from 0a to 40c.

次いで、圧媒供給並びに圧力調整装置7より、加圧ポン
プ8を用いて圧媒タンク12内の圧媒を、圧力調整弁1
1および開閉弁9を介して、各閉塞部材3a〜3cの各
通孔31a〜31cから圧力容器1a〜1cの各室6a
〜6c内に、所要の圧力下に供給する。すると、フリー
ピストン48〜4cが圧媒により加圧移動されて、室2
1a〜21c内の各被処理物に対し圧力作用を及ぼすと
ともに、熱媒および/または冷却液循環装置16におい
て、例えば加熱器19により所定温度に加熱した加熱液
を循環回路14.15および循環ポンプ17によりジャ
ケット13内に循環させることにより、各圧力容器1a
の室21a〜21c内における被処理物は、前記圧力作
用と並行して加熱作用を受ける。したがって、被処理物
の加圧下溶融が、数1(101(10O/c1iの高圧
域内において、安定かつ効率的に工業的量産規模のもと
に容易に実施できる。かくして処理を終了した溶融状態
の製品は、圧媒供給並びに圧力調整装置7か、ら、加圧
ポンプ8による圧媒を室6a〜6cに供給することによ
り、フリーピストン48〜4cの加圧移動を介し、閉塞
部材28〜2c側の通孔40a〜40c、出入回路41
、回収回路42、開閉弁28を介して、回収タンク27
内に取出し回収される。
Next, the pressure medium in the pressure medium tank 12 is supplied from the pressure medium supply and pressure adjustment device 7 to the pressure adjustment valve 1 using the pressure pump 8.
1 and the opening/closing valve 9, from each through hole 31a to 31c of each closing member 3a to 3c to each chamber 6a of pressure vessel 1a to 1c.
~6c under the required pressure. Then, the free pistons 48 to 4c are pressurized and moved by the pressure medium, and the chamber 2
A pressure action is exerted on each of the objects to be processed in 1a to 21c, and in the heating medium and/or cooling liquid circulation device 16, the heated liquid heated to a predetermined temperature by, for example, a heater 19 is passed through the circulation circuit 14.15 and the circulation pump. 17 into the jacket 13, each pressure vessel 1a
The objects to be processed in the chambers 21a to 21c are subjected to a heating action in parallel with the pressure action. Therefore, the material to be treated can be melted under pressure stably and efficiently in the high pressure range of several 1 (10 O/c1i) on an industrial mass production scale. The product is manufactured by supplying the pressure medium from the pressure medium supply and pressure adjustment device 7 to the chambers 6a to 6c by the pressurizing pump 8, thereby moving the free pistons 48 to 4c under pressure to close the closing members 28 to 2c. Side through holes 40a to 40c, in/out circuit 41
, the recovery tank 27 via the recovery circuit 42 and the on-off valve 28.
It is taken out and collected inside.

前記した操業に当り、本発明の第1実施例ではその加熱
および/または冷却液循環装置16により、単に加熱の
みに止まることなく、マイナス温度域に亘る冷却処理と
圧力処理を被処理物に施すことができるので、被処理物
に対するきわめてバラエティに富んだ加工内容と結果と
を与えることが可能である。例えば、食品素材等の水分
を含有する被処理物においては、1(10″C以上の温
度域で、加圧、加熱処理して、被処理物を取出すに当り
、高い温度のままで大気圧まで減圧すると、水分が沸騰
して物性に変化を来すおそれがあるが、このような場合
第1実施例によれば、圧媒供給並びに圧力調整装置7お
よび加熱および/または冷却液循環装置16の存在によ
り、含有水分が沸騰しない程度までの減圧コントロール
、また冷媒による被処理物の冷却による温度低下コント
ロール等が自在に行える。また、目的温度以上に昇温し
た場合の温度下降コントロール、目的温度以上に降温し
た場合の温度上昇コントロール等、その圧力と温度との
組合わせ変化に即応した熱処理を容易に施行できるので
あり、かつ複数の圧力容器に対して均一かつ安定した圧
力と温度パターンによる加圧上溶融状態を実現できるの
である。
In the above-mentioned operation, in the first embodiment of the present invention, the heating and/or cooling liquid circulation device 16 not only performs heating, but also performs cooling treatment and pressure treatment over a negative temperature range on the object to be treated. Therefore, it is possible to provide an extremely wide variety of processing contents and results to the workpiece. For example, when processing objects containing moisture such as food materials, pressure and heat treatment is performed in a temperature range of 1 (10"C or higher), and when taking out the processing object, the temperature remains high and atmospheric pressure is applied. If the pressure is reduced to 100%, there is a risk that the water will boil and the physical properties will change. Due to the existence of It is possible to easily perform heat treatment that responds to changes in the combination of pressure and temperature, such as temperature rise control when the temperature drops above a certain amount, and it also allows for uniform and stable pressure and temperature patterns to be applied to multiple pressure vessels. This makes it possible to achieve a pressurized molten state.

第2図は本発明の第2実施例を示し、特に実験室的規模
に適するもので、第1実施例と異なるところは、各圧力
容器1a、 lb、 lcが、独立したジャケラ目3a
、 13b、 13cでそれ被包され、該ジャケット1
3a=13cの外周部にそれぞれ加熱用ヒーター(好ま
しくは電気加熱式バンドヒーター) 19a、 19b
FIG. 2 shows a second embodiment of the present invention, which is particularly suitable for a laboratory scale, and differs from the first embodiment in that each pressure vessel 1a, lb, lc has an independent jacquarite 3a.
, 13b, 13c, and the jacket 1
Heating heaters (preferably electric band heaters) 19a, 19b are provided on the outer periphery of 3a=13c, respectively.
.

19cが設けられた点と、上部閉塞部材2a、2b、2
cに被処理物供給通孔を備えていない点および1つのフ
リーピストン4Cが増圧型とされている点であり、その
他は第1実施例と同一である。したがって、第1実施例
と同一構成部分については、第1図と同じ符号を付し、
特徴部分について詳述する。
19c and the upper closing members 2a, 2b, 2
The second embodiment is the same as the first embodiment except that it does not have a through hole for supplying the material to be processed and one free piston 4C is of a pressure increasing type. Therefore, the same components as in the first embodiment are given the same reference numerals as in FIG.
The characteristic parts will be explained in detail.

前記ジャケット13a、 13b、 13cには、加熱
および/または冷却可能な熱処理手段としての液循環装
置16が接続されている。この液循環装置16は、液タ
ンク18と各ジャケット13a、 13b、 13cと
を接続する循環管路14.14a、 14b、 14c
および15.15a、 15b、 15cに、循環ポン
プ17、開閉弁33.34a、34b、34cを配設す
ると共に、液タンク18には冷却器20を設けたもので
ある。そして、被処理物の加熱時には、開閉弁34a、
34b、34cを閉じ、ジャケット13a、 13b、
 13c内に閉じ込められた冷却用媒体を前記ヒーター
19a〜19cにより加熱し、該媒体の薄層を通して圧
力容器1a〜1cの間接的加熱を個別に行なうように構
成されている。
A liquid circulation device 16 as a heat treatment means capable of heating and/or cooling is connected to the jackets 13a, 13b, and 13c. This liquid circulation device 16 includes circulation pipes 14.14a, 14b, and 14c that connect the liquid tank 18 and each jacket 13a, 13b, and 13c.
A circulation pump 17 and on-off valves 33.34a, 34b, and 34c are provided at 15.15a, 15b, and 15c, and a cooler 20 is provided at the liquid tank 18. When heating the object to be processed, the on-off valve 34a,
34b, 34c are closed, jackets 13a, 13b,
The cooling medium confined within 13c is heated by the heaters 19a-19c, and the pressure vessels 1a-1c are individually heated indirectly through the thin layer of the medium.

また、前記圧力容器1cは、一方の圧媒室6cの断面積
が他方の被処理収容室21cの断面積よりも大きくせら
れ、一方が大径で他方が小径の増圧型フリーピストン4
0が所定範囲内において移動可能に嵌入されており、前
記ジャケラ) 13cは他方の被処理物収容室21cの
外周部にのみ配設されている。
Further, in the pressure vessel 1c, the cross-sectional area of one pressure medium chamber 6c is made larger than the cross-sectional area of the other to-be-processed storage chamber 21c, and the pressure-increasing free piston 4 has one large diameter and the other small diameter.
0 is fitted so as to be movable within a predetermined range, and the jacket 13c is disposed only on the outer periphery of the other processing object storage chamber 21c.

この第2*施例によれば、まず、閉塞部材28〜2cを
開いて、前記室21a〜21cに被処理物を投入した後
、閉塞部材2a〜2cにより前記室21a〜21cを封
止し、圧媒室6a〜6cに圧媒供給並びに圧力調整装置
7により圧媒を供給して、フリーピストン48〜4cを
移動させ、被処理物を加圧する。そして、開閉弁34a
〜34cを閉じ、冷却用媒体ジャケット13a〜13c
内に閉じ込め、被処理物をその加圧下において、前記ヒ
ーター19a〜19cにより前記媒体を介して所定温度
に加熱し処理する。
According to the second *embodiment, first, the closing members 28 to 2c are opened and the objects to be processed are introduced into the chambers 21a to 21c, and then the chambers 21a to 21c are sealed by the closing members 2a to 2c. , the pressure medium is supplied to the pressure medium chambers 6a to 6c by the pressure medium supply and pressure adjustment device 7, the free pistons 48 to 4c are moved, and the object to be processed is pressurized. And the on-off valve 34a
~34c are closed and the cooling medium jackets 13a~13c are closed.
The object to be processed is heated to a predetermined temperature via the medium by the heaters 19a to 19c under pressure and processed.

なお、かかる処理操作は、魚肉等からなる動物性蛋白を
主成分とする食品素材を溶融状態の製品とする場合、特
に加熱温度が1(10’Cを越えるときは、常圧下では
熱変性が先行するので、これを抑制するという観点から
、加圧の先行下において加熱を行なうのである。
In addition, this processing operation is particularly important when the food material mainly composed of animal protein such as fish meat is made into a molten product, especially when the heating temperature exceeds 1 (10'C), as thermal denaturation may occur under normal pressure. Therefore, from the viewpoint of suppressing this, heating is performed prior to pressurization.

そして、被処理物を所定の圧力・温度の下に保持した後
、ヒーター19a〜19cによる加熱を停止し、開閉弁
34a〜34cを開いて循環ポンプ17を運転させ、ジ
ャケット13a〜13c内に冷却用媒体を循環させて、
被処理物を加圧下において冷却し、少なくとも1(10
°C以下の温度になると(常圧下での水分の沸騰蒸発が
起らない温度条件になると)、大気圧に減圧して被処理
物の取出しを行なう。
After the object to be processed is maintained at a predetermined pressure and temperature, the heating by the heaters 19a to 19c is stopped, the on-off valves 34a to 34c are opened, the circulation pump 17 is operated, and the cooling is carried out inside the jackets 13a to 13c. Circulating the medium for
The object to be treated is cooled under pressure and cooled to a temperature of at least 1 (10
When the temperature is below .degree. C. (when the temperature conditions do not cause boiling and evaporation of water under normal pressure), the pressure is reduced to atmospheric pressure and the material to be processed is taken out.

なお、前記室6a〜6c内に供給される圧媒としては、
フリーピストン48〜4cの移動に伴なって高圧容器1
a〜1c内壁に付着し、食品素材と接する可能性のある
ことから、水が最も好適である。
Note that the pressure medium supplied into the chambers 6a to 6c is as follows:
As the free pistons 48 to 4c move, the high pressure container 1
Water is most suitable because it may adhere to the inner walls of a to 1c and come into contact with food materials.

また、ジャケット13a〜13cに循環される冷却用媒
体としては、耐熱性が要求されるところから、シリコン
オイルなどを使用するのが好ましい。
Further, as the cooling medium circulated in the jackets 13a to 13c, it is preferable to use silicone oil or the like since heat resistance is required.

そして、圧媒の圧力調整、供給等については、第1実施
例と同様にして行なわれる。
The pressure adjustment, supply, etc. of the pressure medium are performed in the same manner as in the first embodiment.

さらに、第2実施例では、各圧力容器1a〜1cを個別
のヒーター19a〜19cによって、自在にかつ迅速に
温度制御できると共に、個別に温度変数を設定しかつ変
更して処理できるうえ、増圧型フリーピストン4cによ
って圧力変数をも任意に変えることができ、一定の実験
で多数のデータを得ることができ、実験を効率的に行な
うことが可能である。
Furthermore, in the second embodiment, the temperature of each pressure vessel 1a to 1c can be freely and quickly controlled by the individual heaters 19a to 19c, temperature variables can be individually set and changed, and the pressure increasing type The free piston 4c allows pressure variables to be changed arbitrarily, and a large amount of data can be obtained in a given experiment, making it possible to conduct experiments efficiently.

なお、上記第2実施例において、冷却用媒体として例え
ば電気絶縁性のオイル等を用いる場合、ヒーター19a
〜19cをジャケット13a〜13c内に配設すること
ができ、この場合、被処理物の加熱時はジャケット13
8〜13c内の冷却用媒体を排出することが好ましい。
In the second embodiment, if electrically insulating oil or the like is used as the cooling medium, the heater 19a
~19c can be disposed within the jackets 13a~13c. In this case, when heating the object, the jacket 13
It is preferable to discharge the cooling medium within 8 to 13c.

また、第2実施例は、食品素材への高圧処理適用に関し
ての探索・実験用装置を念頭に構成したものであるから
、被処理物の高圧容器1a=1cへの投入ならびに取出
しについて、特に手段を講じていないが、第1実施例の
ように、流動状被処理物の自動供給手段を設け、さらに
は、フリーピストン4a、4bの移動を利用して被処理
物の自動排出を行なうことも可能である。
In addition, since the second embodiment is constructed with an apparatus in mind for exploration and experimentation regarding the application of high-pressure processing to food materials, particular methods are required for loading and unloading the processed materials into and out of the high-pressure container 1a = 1c. However, as in the first embodiment, an automatic supply means for the fluid to be processed may be provided, and furthermore, the movement of the free pistons 4a and 4b may be used to automatically discharge the to be processed. It is possible.

第3図は本発明の第3実施例を示し、第2実施例と異な
るところは、埋込型の加熱用ヒーター19a。
FIG. 3 shows a third embodiment of the present invention, which differs from the second embodiment in an embedded heater 19a.

19b、 19cを、圧力容器1a〜ICの外周壁に装
着し、該ヒーター19a〜19cの外周部にジャケラ目
38〜13cを設けた点であり、その他の構成は第2実
施例と同一である。したがって、第3実施例においても
、第2実施例と同様の作用効果を期待することができる
。この第3実施例において、被処理物の加熱時には、ジ
ャケット13a〜13c内の冷却用媒体を排出するのが
好ましい。
19b and 19c are attached to the outer circumferential walls of the pressure vessels 1a to IC, and jacket holes 38 to 13c are provided on the outer circumferential portions of the heaters 19a to 19c, and the other configurations are the same as in the second embodiment. . Therefore, the same effects as in the second embodiment can be expected in the third embodiment as well. In this third embodiment, it is preferable to discharge the cooling medium inside the jackets 13a to 13c when heating the object to be processed.

なお、本発明は、上記各実施例に限定されるものではな
く、また、加熱、加圧処理により可能な全ゆる食品加工
に適用しうろこと勿論である。
It should be noted that the present invention is not limited to the above embodiments, and can of course be applied to all kinds of food processing that can be carried out by heating and pressure treatment.

(発明の効果) 本発明の加圧下処理装置によれば、魚肉等から成る動物
性蛋白を主成分とする固液混合相の食品素材の加圧下溶
融を、従来技術による圧力条件に止まることなく、これ
を数1(101(10O/cfflを越える高圧域内に
おいても、安定かつ効率的、更には実験室的規模は勿論
のこと工業的量産スケール下に実現できる点において、
優れた特徴と利点をもつものである。特に本発明におい
ては、複数個の圧力容器内をフリーピストンで2室に距
て、一方の室に圧媒供給並びに圧力調整装置が接続し、
他方の室に被処理物が供給可能とされ、かつ圧力容器内
の被処理物に対する熱処理手段を設けることにより、各
圧力容器において同時に同一条件下の加圧・熱処理が行
われ、個々の容器のコンパクト、小型薄肉化が図られ、
外部からの熱伝達性を良好として、加熱、冷却効率を向
上させられ、正確迅速な熱処理結果が得られる。圧力容
器内はフリーピストンによる分離のため、従来のシリン
ダピストンタンプより構造が簡単化され、ピストンロン
ドがないため、有効面積を拡大できるとともに、圧媒と
被処理物の混入のおそれなく、圧媒として水を用いるこ
とと相まって食品素材等の清浄性の確保も容易である。
(Effects of the Invention) According to the pressure processing apparatus of the present invention, a solid-liquid mixed phase food material mainly composed of animal protein, such as fish meat, can be melted under pressure without being limited to the pressure conditions of conventional technology. , in that it is stable and efficient even in a high pressure range exceeding 10 O/cffl, and can be realized not only on a laboratory scale but also on an industrial mass production scale.
It has excellent features and advantages. In particular, in the present invention, two chambers are separated by a free piston within a plurality of pressure vessels, and a pressure medium supply and pressure adjustment device is connected to one chamber,
By making it possible to supply the object to be treated to the other chamber and providing heat treatment means for the object to be treated in the pressure vessel, pressurization and heat treatment can be performed simultaneously under the same conditions in each pressure vessel. Compact, small and thin,
Improves heat transfer from the outside, improves heating and cooling efficiency, and provides accurate and quick heat treatment results. Since the inside of the pressure vessel is separated by a free piston, the structure is simpler than the conventional cylinder piston tamp.Since there is no piston rod, the effective area can be expanded, and there is no risk of mixing of the pressure medium and the processed material. In combination with using water as a liquid, it is easy to ensure the cleanliness of food materials, etc.

また熱処理として加熱と冷却両用の熱処理を可能と、こ
れによってその利用範囲を著しく拡大させることが可能
である。
Furthermore, it is possible to perform heat treatment for both heating and cooling, thereby significantly expanding its range of use.

さらに、増圧型フリーピストンを採用することによって
、圧力を変えすなわち圧力変数を任意に設定して実験を
効率的に実施することのできる探索・実験室的規模の装
置を得ることができる。
Furthermore, by employing a pressure-increasing free piston, it is possible to obtain an exploration/laboratory-scale device that can efficiently conduct experiments by changing the pressure, that is, setting pressure variables arbitrarily.

また、圧力容器は冷却用媒体循環ジャケットにより被包
され、かつジャケットに加熱手段が設けられることによ
って、自在でかつ迅速な温度制御が可能であり、特に、
探索・実験用として、加熱手段を個々の圧力容器に設け
ることにより、温度変数を任意に設定した実験を効率的
に実施することが可能である。
In addition, the pressure vessel is covered with a cooling medium circulation jacket, and the jacket is provided with a heating means, so that flexible and rapid temperature control is possible.
By providing heating means in each pressure vessel for exploration and experiment purposes, it is possible to efficiently conduct experiments with arbitrarily set temperature variables.

そして、本発明は、既知の魚肉等からなる動物性蛋白を
主成分とする食品素材に、新たな加工技術を提供できる
ばかりでなく、未知の食品加工製品を、加圧下でしかも
加熱および/または冷却により相乗作用によって探索す
るのに極めて有用な装置として、食品工業分野に寄与す
るところが甚大である。
The present invention not only provides a new processing technology for food materials whose main component is animal protein, such as fish meat, but also enables processing of unknown food processing products by heating and/or processing under pressure. As an extremely useful device for exploring the synergistic effects of cooling, it will greatly contribute to the food industry.

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

図面は本発明の実施例を示すもので、第1図は第1実施
例の縦断正面図、第2図は第2実施例の縦断正面図、第
3図は第3実施例の縦断正面図である。 18〜1c・・・圧力容器、2a〜2c、 3a〜3c
・−・−閉塞部材、4a〜4 c−・フリーピストン、
6a〜6c・・・室、7・・・圧媒供給並びに圧力調整
装置、8・・・加圧ポンプ、13゜13a、 13b、
 13cm・・冷却用媒体用循環ジャケット、16〜・
加熱および/または冷却液循環装置、17・・・循環ポ
ンプ、18−・液タンク、19−加熱器、19a〜19
c・−ヒーター、2〇−冷却器、21a 〜21cm室
、25a〜25c・−・開閉弁、26a〜26c −閉
止部、22・−・被処理物供給タンク、27・−回収タ
ンク。 第3
The drawings show embodiments of the present invention; FIG. 1 is a longitudinal sectional front view of the first embodiment, FIG. 2 is a longitudinal sectional front view of the second embodiment, and FIG. 3 is a longitudinal sectional front view of the third embodiment. It is. 18-1c...pressure vessel, 2a-2c, 3a-3c
・-・Closing member, 4a to 4 c-・Free piston,
6a to 6c... Chamber, 7... Pressure medium supply and pressure adjustment device, 8... Pressure pump, 13° 13a, 13b,
13cm... Circulation jacket for cooling medium, 16...
Heating and/or cooling liquid circulation device, 17--circulation pump, 18--liquid tank, 19-heater, 19a-19
c.--Heater, 20--Cooler, 21a-21cm chamber, 25a-25c--Opening/closing valve, 26a-26c--Closing section, 22--Process supply tank, 27--Recovery tank. Third

Claims (10)

【特許請求の範囲】[Claims] (1)圧力容器と、該容器内に充填されたフリーピスト
ンとから成り、圧力容器の前記ピストンにより距てられ
た一方の室には圧媒の供給並びに圧力調整装置が接続さ
れるとともに、他方の室には被処理物が供給可能とされ
、かつ圧力容器内の被処理物に対する熱処理手段が設け
られることを特徴とする食品素材の加圧下処理装置。
(1) Consisting of a pressure vessel and a free piston filled in the vessel, one chamber of the pressure vessel separated by the piston is connected to a pressure medium supply and pressure regulating device, and the other 1. An apparatus for processing food materials under pressure, characterized in that an object to be processed can be supplied to the chamber, and a heat treatment means for the object to be processed in the pressure vessel is provided.
(2)複数個の圧力容器が、共通の圧媒供給並びに圧力
調整装置に接続される請求項(1)記載の食品素材の加
圧下処理装置。
(2) The apparatus for processing food materials under pressure according to claim (1), wherein the plurality of pressure vessels are connected to a common pressure medium supply and pressure adjustment device.
(3)前記フリーピストンの少くとも1つが増圧型であ
る請求項(1)又は(2)記載の食品素材の加圧下処理
装置。
(3) The apparatus for processing food materials under pressure according to claim (1) or (2), wherein at least one of the free pistons is of a pressure increasing type.
(4)熱処理手段として、加熱および/または冷却液循
環手段を用いる請求項(1)、(2)又は(3)記載の
食品素材の加圧下処理装置。
(4) The apparatus for processing food materials under pressure according to claim (1), (2) or (3), wherein the heat treatment means includes heating and/or cooling liquid circulation means.
(5)被処理物が、圧力容器における他方の室にポンプ
により送給可能とされる請求項(1)〜(4)のうち1
つの項に記載の食品素材の加圧下処理装置。
(5) One of claims (1) to (4) in which the object to be treated can be fed to the other chamber in the pressure vessel by a pump.
Apparatus for processing food materials under pressure as described in paragraph 1.
(6)被処理物の他方の室への供給用開閉弁の開閉位置
が、該室内に近い部分に設けられる請求項(1)〜(5
)のうち1つの項に記載の食品素材の加圧下処理装置。
(6) Claims (1) to (5) in which the opening/closing position of the on-off valve for supplying the processed material to the other chamber is provided in a portion close to the chamber.
) The apparatus for processing food materials under pressure according to one of the items.
(7)圧媒の供給並びに圧力調整装置から、圧力容器の
一方の室への供給圧媒が水とされる請求項(1)〜(6
)のうち1つの項に記載の食品素材の加圧下処理装置。
(7) Claims (1) to (6) in which the pressure medium supplied from the pressure medium supply and pressure adjustment device to one chamber of the pressure vessel is water.
) The apparatus for processing food materials under pressure according to one of the items.
(8)圧媒の供給並びに圧力調整装置から、圧力容器の
一方の室への供給圧媒により、他方の室内における処理
済み被処理物が取出し可能とされる請求項(1)〜(7
)のうち1つの項に記載の食品素材の加圧下処理装置。
(8) Claims (1) to (7) wherein by supplying pressure medium to one chamber of the pressure vessel from the pressure medium supply and pressure adjustment device, the processed material in the other chamber can be taken out.
) The apparatus for processing food materials under pressure according to one of the items.
(9)圧力容器は冷却用媒体循環ジャケットにより被包
されている請求項(1)〜(8)のうち1つの項に記載
の食品素材の加圧下処理装置。
(9) The apparatus for processing food materials under pressure according to one of claims (1) to (8), wherein the pressure vessel is enclosed by a cooling medium circulation jacket.
(10)前記ジャケットに加熱手段が設けられている請
求項(9)に記載の食品素材の加圧下処理装置。
(10) The apparatus for processing food materials under pressure according to claim (9), wherein the jacket is provided with heating means.
JP1203539A 1989-03-18 1989-08-05 Apparatus and method for treating food material under pressure Expired - Fee Related JPH0757159B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1203539A JPH0757159B2 (en) 1989-03-18 1989-08-05 Apparatus and method for treating food material under pressure

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP6651689 1989-03-18
JP1-66516 1989-03-18
JP1203539A JPH0757159B2 (en) 1989-03-18 1989-08-05 Apparatus and method for treating food material under pressure

Publications (2)

Publication Number Publication Date
JPH037534A true JPH037534A (en) 1991-01-14
JPH0757159B2 JPH0757159B2 (en) 1995-06-21

Family

ID=26407702

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1203539A Expired - Fee Related JPH0757159B2 (en) 1989-03-18 1989-08-05 Apparatus and method for treating food material under pressure

Country Status (1)

Country Link
JP (1) JPH0757159B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009236584A (en) * 2008-03-26 2009-10-15 Yazaki Corp Column unit and gas chromatograph device
WO2019167547A1 (en) * 2018-02-28 2019-09-06 株式会社極洋 Fish powder and method for producing same, and formulation

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101059916B1 (en) * 2011-01-26 2011-08-29 옥광주 Dried fish sterilizer

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5945573A (en) * 1982-09-07 1984-03-14 Canon Inc Electronic equipment
JPH01171553A (en) * 1987-12-28 1989-07-06 Mitsubishi Heavy Ind Ltd Continuous pressurizing treating device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5945573A (en) * 1982-09-07 1984-03-14 Canon Inc Electronic equipment
JPH01171553A (en) * 1987-12-28 1989-07-06 Mitsubishi Heavy Ind Ltd Continuous pressurizing treating device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009236584A (en) * 2008-03-26 2009-10-15 Yazaki Corp Column unit and gas chromatograph device
WO2019167547A1 (en) * 2018-02-28 2019-09-06 株式会社極洋 Fish powder and method for producing same, and formulation
JP6578465B1 (en) * 2018-02-28 2019-09-18 株式会社極洋 Fish meal, method for producing the same, and preparation
JP2020031630A (en) * 2018-02-28 2020-03-05 株式会社極洋 Fish meal, method for producing the same, and preparation
CN111757676A (en) * 2018-02-28 2020-10-09 株式会社极洋 Fish meal and its manufacturing method, and preparation

Also Published As

Publication number Publication date
JPH0757159B2 (en) 1995-06-21

Similar Documents

Publication Publication Date Title
DE69613998T2 (en) METHOD AND DEVICE FOR HOT ISOSTATIC PRESSING OF PARTS
EP1399194B1 (en) Method and appartus for high pressure treatment of substances under controlled temperature conditions
JPH02182157A (en) High-pressure treating apparatus
EP0798369B1 (en) Process for dry fractionation of fats and oils
JPH037534A (en) Device for treating food raw material under pressure
CA2547273C (en) Isostat for processing materials and method for removing ceramic material from metallic articles by using said isostat
NO164331B (en) PROCEDURE FOR DRYING AND / OR FREEZING GRANULATES AND APPLIANCES FOR IMPLEMENTING THE PROCEDURE.
EP1115522B1 (en) Method and device for hot isostatic pressing
JPH01300841A (en) Melting device of food ingredient under pressure
AU2017200665A1 (en) Production process for stamped parts of high mechanical resistance, through controlled electric heating
JPH0335762A (en) Preparation of feed-fertilizer
JPH0740863B2 (en) Equipment for melting food materials under pressure
KR200337726Y1 (en) A temperature control apparatus
Owolarafe et al. The Effects of some processing conditions on oil point pressure of locust bean
US3601378A (en) Continuous hydrothermal apparatus and process
JPH02295473A (en) Apparatus for producing feed and fertilizer
JPH0771463B2 (en) High pressure processing equipment
JPH05161483A (en) Starting of high-pressure treatment
KR102232721B1 (en) How to treat articles and how to high-pressure articles
JP2553706B2 (en) Heat treatment apparatus for food material and twin-screw extruder used for this heat treatment apparatus
NO313222B1 (en) Process for preparing the feed pellet and plant for use in carrying out the process
US3497364A (en) Apparatus for making protein-meal
RU2850573C1 (en) Thermovacuum autoclave
JPH0330649A (en) Apparatus for melting food material under pressure
US3429710A (en) Pressure cooking process to produce fish cakes for animal use

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080621

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090621

Year of fee payment: 14

LAPS Cancellation because of no payment of annual fees