JPH06225707A - Device for continuously treating liquid under high pressure - Google Patents

Device for continuously treating liquid under high pressure

Info

Publication number
JPH06225707A
JPH06225707A JP5037310A JP3731093A JPH06225707A JP H06225707 A JPH06225707 A JP H06225707A JP 5037310 A JP5037310 A JP 5037310A JP 3731093 A JP3731093 A JP 3731093A JP H06225707 A JPH06225707 A JP H06225707A
Authority
JP
Japan
Prior art keywords
pressure
liquid
pump
container
orifice
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.)
Withdrawn
Application number
JP5037310A
Other languages
Japanese (ja)
Inventor
Keiichi Hori
恵一 堀
Yoshio Sugimoto
喜雄 杉本
Yukio Manabe
幸男 真鍋
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5037310A priority Critical patent/JPH06225707A/en
Publication of JPH06225707A publication Critical patent/JPH06225707A/en
Withdrawn legal-status Critical Current

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Landscapes

  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Non-Alcoholic Beverages (AREA)

Abstract

PURPOSE:To enable stable pressure reduction and discharge of a highpressure fluid by a compact and inexpensive device for continuously treating a liquid under high pressure by adopting a pressure reducing device of simple structure. CONSTITUTION:A device for continuously treating a liquid such as drink under high pressure consists of a pressure pump 25 connected to an inlet side of a pressure chamber 23 in a high-pressure container barrel 20 and an orifice nozzle linked to an outlet side of the pressure chamber. The pressure chamber 23 is pressurized by supply of a liquid by the pressure pump 25 and the liquid is treated under pressure for a given time. When a high-pressure sluice valve 3 is opened, the pressurized liquid is properly decompressed by the orifice nozzle 1 and discharged. The amount of the pressure pump 25 delivered is increased and reduced in order to maintain pressure moderately by detecting pressure in the pressure chamber 23.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は天然果汁、牛乳等の液状
食品或いは薬液等の液状を高圧加圧して殺菌或いは物性
変化を行なう高圧液体連続処理装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-pressure liquid continuous treatment apparatus for sterilizing or changing the physical properties of a liquid food such as natural fruit juice or milk or a liquid such as a liquid medicine under high pressure.

【0002】[0002]

【従来の技術】従来天然果汁等の飲料の殺菌は加熱処理
により行なってきたが、加熱に伴う風味の劣化、栄養素
の損失或いは加熱臭の生成など好ましくない面が多く、
新しい殺菌技術の開発が望まれていた。これに対し近年
食品を数千気圧の高い静水圧下で高圧処理することによ
り、殺菌或いは有用な物性変化が生じることが分かり、
加熱に代わる食品の加工方法として実用化の研究が盛ん
である。
Background Art Conventionally, beverages such as natural fruit juice have been sterilized by heat treatment, but there are many unfavorable aspects such as deterioration of flavor due to heating, loss of nutrients or generation of heating odor,
Development of new sterilization technology was desired. On the other hand, in recent years, by high-pressure treatment of food under a high hydrostatic pressure of several thousand atmospheric pressure, it was found that sterilization or useful physical property changes occur,
Practical research is being actively conducted as a food processing method instead of heating.

【0003】図4に従来使用されている液状食品の高圧
処理装置の概要を示す(特願平3−11697号)。図
4において、高圧容器胴20内の加圧室23は、下蓋2
1、上蓋22と加圧時の軸力を支持するヨークフレーム
24とで構成される。この高圧容器の外部に液体被処理
物を連続で加圧、注入する加圧ポンプ25と高圧処理物
を減圧、排出する減圧ポンプ26が設けられている。ま
た各ポンプに取付けられた油圧ユニット27及び28
は、付属する切替弁操作コントロールにより、ピストン
29,30を油圧シリンダ31,32内で左右にスライ
ドさせる。各ポンプの両側には、油圧シリンダ31,3
2と隔離されたシリンダ33a,33b,34a,34
bを持ち、油圧ピストン29,30と同軸に連結したピ
ストン35a,35b,36a,36bを設ける。また
各ポンプの両端に処理液の出入を司る弁機構37a,3
7b、38a,38bを設ける。弁機構37a,37
b,38a,38b群はチェック弁37a,37b及び
自動弁(自動開閉弁)38a,38bからなり、制御装
置50の設定に従って作動する。なお、制御装置50に
は高圧容器内圧を検出する圧力センサー51、被処理物
流量センサー52、油圧ピストン29,30の作動をコ
ントロールする油圧切替弁操作ユニット53,54等の
検出及び制御機構が内蔵されており、高圧容器内圧の保
持と被処理物の一定流量注入及び加圧作動をコントロー
ルさせる。更に補機として原料供給ポンプ60、供給タ
ンク61等が設けられている。
FIG. 4 shows an outline of a conventional high-pressure processing apparatus for liquid foods (Japanese Patent Application No. 3-11697). In FIG. 4, the pressurizing chamber 23 in the high-pressure container barrel 20 is a lower lid 2
1. The upper lid 22 and the yoke frame 24 that supports the axial force at the time of pressurization. A pressure pump 25 that continuously pressurizes and injects the liquid processing object and a decompression pump 26 that depressurizes and discharges the high pressure processing object are provided outside the high pressure container. Also, hydraulic units 27 and 28 attached to each pump
Slides the pistons 29 and 30 left and right in the hydraulic cylinders 31 and 32 by an attached switching valve operation control. On each side of each pump, hydraulic cylinders 31, 3
Cylinders 33a, 33b, 34a, 34 separated from 2
pistons 35a, 35b, 36a, 36b which have b and are coaxially connected to the hydraulic pistons 29, 30 are provided. In addition, valve mechanisms 37a, 3 that control the inflow and outflow of the processing liquid at both ends of each pump.
7b, 38a, 38b are provided. Valve mechanism 37a, 37
The groups b, 38a, 38b are composed of check valves 37a, 37b and automatic valves (automatic opening / closing valves) 38a, 38b, and operate according to the setting of the control device 50. The control device 50 has a built-in detection and control mechanism such as a pressure sensor 51 for detecting the internal pressure of the high-pressure container, an object flow rate sensor 52, and hydraulic switching valve operation units 53, 54 for controlling the operation of the hydraulic pistons 29, 30. The internal pressure of the high-pressure container is maintained, and a constant flow rate injection and pressurization operation of the object to be processed are controlled. Further, a raw material supply pump 60, a supply tank 61 and the like are provided as auxiliary machines.

【0004】以下この従来の高圧処理装置における連続
処理工程について述べる。原料供給ポンプ60及び加圧
ポンプ25用油圧ユニット27を作動させると、ピスト
ン29が左右に往復運動し、例えば右側にスライドする
時は左側の原料シリンダ33a内に原料がチェック弁3
7aを通って吸引される。同時にシリンダ33bの原料
は、チェック弁37bを経て矢印の流れ方向で、連絡管
41を経て高圧容器加圧室23内へ供給される。加圧室
23内が充満されると、次いで昇圧が始まる。次いで加
圧室23が制御装置50に設定された高圧値になると、
減圧ポンプ26が作動する。また高圧処理液が、例えば
自動弁38bを通してシリンダ部34aへ流入すると、
ピストン36aには高圧がかかって、急激に右側に移動
することにより高圧容器室23内が急激に減圧する。従
ってこれを防ぐために、ピストン30の右側シリンダに
油圧で背圧をかけると、高圧容器内圧力の変動を抑える
ようにピストン30は徐々に右へスライドする。
The continuous processing steps in this conventional high-pressure processing apparatus will be described below. When the raw material supply pump 60 and the hydraulic unit 27 for the pressurizing pump 25 are operated, the piston 29 reciprocates left and right, and for example, when the piston 29 slides to the right side, the raw material is placed in the left side raw material cylinder 33a and the raw material is checked in the check valve 3a.
It is sucked through 7a. At the same time, the raw material of the cylinder 33b is supplied into the high pressure vessel pressurizing chamber 23 through the check valve 37b and in the flow direction of the arrow through the connecting pipe 41. When the inside of the pressurizing chamber 23 is filled, pressurization starts next. Next, when the pressure chamber 23 reaches the high pressure value set in the control device 50,
The decompression pump 26 operates. Further, when the high-pressure treatment liquid flows into the cylinder portion 34a through the automatic valve 38b, for example,
High pressure is applied to the piston 36a, and the piston 36a is rapidly moved to the right side, so that the inside of the high-pressure container chamber 23 is rapidly depressurized. Therefore, in order to prevent this, when a back pressure is hydraulically applied to the right cylinder of the piston 30, the piston 30 gradually slides to the right so as to suppress the fluctuation of the pressure in the high-pressure container.

【0005】高圧液体が大気圧まで減圧する際の膨張代
として必要なシリンダ容積の或る割合を残す位置までピ
ストンが移動すると、左側自動弁38bが閉じ、同時に
背圧をかけている油圧を抜くことによってピストンはそ
のまま右端までスライドしてシリンダの内圧力を大気圧
近くまで減圧する。この時点で右側自動弁38bが開
き、高圧処理液が流入すると、油圧は左シリンダ部に切
替えられて背圧をかけ、同時に左自動弁38aが開き、
ピストン36aの左スライドにつれて、高圧処理液が排
出され、これが繰り返される。また原料ポンプ60は連
続的に駆動して、流量センサー52の設定値により加圧
ポンプ用油圧ユニット、油圧切替操作ユニット53が作
動し、高圧容器内へ連続して一定流量の供給が行なわれ
る。以上の操作により被処理液は高圧加圧状態で加圧室
23内を図4において下から上へ流動し、一定時間高圧
下に保持され、この間に殺菌或いは物性変化がなされ
る。加圧ポンプの注入量と減圧ポンプの排出量を同一に
コントロールすることにより、加圧室23内は一定圧力
に保たれることになる。
When the piston moves to a position where a certain proportion of the cylinder volume required as an expansion allowance when the high-pressure liquid is depressurized to atmospheric pressure, the left-side automatic valve 38b closes, and at the same time the hydraulic pressure applying back pressure is released. As a result, the piston slides to the right end as it is, and the internal pressure of the cylinder is reduced to near atmospheric pressure. At this point, the right-side automatic valve 38b opens, and when the high-pressure processing liquid flows in, the hydraulic pressure is switched to the left cylinder section to apply back pressure, and at the same time, the left automatic valve 38a opens.
The high-pressure processing liquid is discharged as the piston 36a slides to the left, and this is repeated. Further, the raw material pump 60 is continuously driven, and the pressurizing pump hydraulic unit and the hydraulic pressure switching operation unit 53 are operated according to the set value of the flow rate sensor 52, so that a constant flow rate is continuously supplied into the high-pressure container. By the above operation, the liquid to be treated flows in the pressurizing chamber 23 from the bottom to the top in FIG. 4 under high pressure and is kept under high pressure for a certain period of time, during which sterilization or physical property change is performed. By controlling the injection amount of the pressurizing pump and the discharge amount of the depressurizing pump to be the same, the inside of the pressurizing chamber 23 is maintained at a constant pressure.

【0006】[0006]

【発明が解決しようとする課題】前記したような従来の
高圧処理装置では、急激な減圧を回避するために背圧を
かけたり、減圧を得るための油圧切替操作ユニットや制
御機構、更には自動開閉弁を必要とし、減圧ポンプが大
型化して設備の設置面積に占める割合も大きくなる。従
って設備価格も高くなり、更に減圧ポンプの運転制御が
複雑になりがちであり、操作の安定性を確保することも
難しいなどの問題があった。本発明はこのような従来の
高圧処理装置における減圧ポンプが有する課題を解決し
ようとするもので、簡単な構造の減圧装置を採用するこ
とによってコンパクトで安価な高圧液体連続処理装置を
提供せんとするものである。
SUMMARY OF THE INVENTION In the conventional high-pressure processing apparatus as described above, a back pressure is applied to avoid a sudden pressure reduction, and a hydraulic pressure switching operation unit and a control mechanism for obtaining the pressure reduction, and further, an automatic pressure change operation unit. An on-off valve is required, and the decompression pump becomes larger and the proportion of the installation area of the equipment becomes larger. Therefore, the equipment price becomes high, the operation control of the decompression pump tends to be complicated, and it is difficult to secure the operation stability. The present invention is intended to solve the problem of the decompression pump in such a conventional high-pressure processing apparatus, and intends to provide a compact and inexpensive high-pressure liquid continuous processing apparatus by adopting a decompression apparatus having a simple structure. It is a thing.

【0007】[0007]

【課題を解決するための手段】このため本発明は、飲料
等の液体食品を高圧処理する高圧処理装置において、被
処理液が供給口から流入して高圧下で内部を流動通過し
た後、別の排出口から排出される高圧容器と、同容器の
入口側に接続された加圧ポンプと、同容器の出口側に接
続されたオリフィスノズルで構成され、同加圧ポンプで
連続的に被処理液を高圧容器内に加圧、供給すると共
に、高圧容器からオリフィスノズルを通って被処理液が
連続的に減圧、排出されるようにしてなるもので、これ
を課題解決のための手段とするものである。また本発明
は、高圧容器内の圧力に相応して加圧ポンプからの供給
量を増加、減少させてなるものであり、更にオリフィス
ノズルの出口に噴流を受止めるキャッチャーを設けると
共に、同キャッチャー及びキャッチャーからの排出配管
に冷却装置を設けてなるもので、これを課題解決のため
の手段とするものである。
For this reason, the present invention provides a high-pressure processing apparatus for high-pressure processing of liquid foods such as beverages, in which the liquid to be processed flows from the supply port, flows through the inside under high pressure, and then separates. It consists of a high-pressure container discharged from the discharge port, a pressure pump connected to the inlet side of the container, and an orifice nozzle connected to the outlet side of the container. The liquid is pressurized and supplied into the high-pressure container, and the liquid to be treated is continuously depressurized and discharged from the high-pressure container through the orifice nozzle. This is a means for solving the problem. It is a thing. Further, the present invention is such that the supply amount from the pressurizing pump is increased or decreased according to the pressure in the high-pressure container, and further, a catcher for receiving the jet flow is provided at the outlet of the orifice nozzle, and the catcher and The exhaust pipe from the catcher is provided with a cooling device, which serves as a means for solving the problem.

【0008】[0008]

【作用】本発明はオリフィスの有する減圧作用を利用す
るもので、流体の粘度、圧力が一定であれば噴出流量は
オリフィスの孔径に依存して決定されることから、加圧
ポンプの供給量(吐出量)に相応してオリフィスノズル
の孔径を選定してオリフィスノズルを高圧の被処理液が
通過する際の圧損によって高圧容器の加圧室内の圧力を
保持しつつ、連続的に被処理液を減圧、排出する。また
温度変化により流体の粘度が変化してオリフィスの噴出
流量が変化する場合には、加圧室内の圧力変化に応じて
加圧ポンプの吐出量を変化させることで安定した圧力保
持が可能となる。更にオリフィスノズル出口側に冷却装
置を設けることにより、オリフィス通過後の高速噴流の
衝突による被処理液の温度上昇を抑え、品質への悪影響
を最小限とする。このようにオリフィスの有する減圧作
用と加圧ポンプの制御とを組合せることにより、常に最
適な流量と圧力を維持して高圧で液体を連続処理でき
る。
The present invention utilizes the depressurizing action of the orifice. If the viscosity and pressure of the fluid are constant, the jet flow rate is determined depending on the hole diameter of the orifice. The diameter of the orifice nozzle is selected in accordance with the discharge amount), and the pressure in the high-pressure processing liquid passes through the orifice nozzle. Decompress and discharge. Further, when the viscosity of the fluid changes due to the temperature change and the ejection flow rate of the orifice changes, it is possible to maintain stable pressure by changing the discharge rate of the pressure pump according to the pressure change in the pressure chamber. . Further, by providing a cooling device on the outlet side of the orifice nozzle, the temperature rise of the liquid to be treated due to the collision of the high-speed jet after passing the orifice is suppressed, and the adverse effect on the quality is minimized. By combining the depressurizing action of the orifice and the control of the pressurizing pump in this manner, the liquid can be continuously processed at a high pressure while always maintaining the optimum flow rate and pressure.

【0009】[0009]

【実施例】以下本発明を図面の実施例について説明する
と、図1に本発明の高圧液体連続処理装置の第1実施例
を示す。被処理液が流動し、高圧下で所定時間保持され
る加圧室23は、高圧容器胴20と下蓋21、上蓋22
で形成されている。下蓋21、上蓋22はヨークフレー
ム24で支持され、内圧により生じる軸力を支えてい
る。また下蓋21に連結した供給管である連絡管41の
前流に加圧ポンプ25が設けられており、同加圧ポンプ
25は油圧シリンダ31、高圧シリンダ33a,33b
を持ち、油圧シリンダ31内の油圧ピストン29と同軸
に高圧ピストン35a,35bが連結されている。油圧
ピストン29は油圧ユニット27の作動油により左右に
往復作動する。また高圧シリンダ33a,33bには高
圧逆止弁37a,37bが連結され、被処理液が供給タ
ンク61から供給ポンプ60を介し、逆止弁37aを通
って加圧ポンプ25へ供給される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the embodiments of the drawings. FIG. 1 shows a first embodiment of the high-pressure liquid continuous processing apparatus of the present invention. The pressurizing chamber 23 in which the liquid to be treated flows and is maintained under high pressure for a predetermined time includes a high-pressure container barrel 20, a lower lid 21, and an upper lid 22.
Is formed by. The lower lid 21 and the upper lid 22 are supported by the yoke frame 24 and support the axial force generated by the internal pressure. A pressurizing pump 25 is provided in the upstream of the connecting pipe 41, which is a supply pipe connected to the lower lid 21, and the pressurizing pump 25 includes a hydraulic cylinder 31, high-pressure cylinders 33a and 33b.
The high pressure pistons 35a and 35b are coaxially connected to the hydraulic piston 29 in the hydraulic cylinder 31. The hydraulic piston 29 reciprocates left and right by the hydraulic oil of the hydraulic unit 27. The high-pressure check valves 37a and 37b are connected to the high-pressure cylinders 33a and 33b, and the liquid to be treated is supplied from the supply tank 61 to the pressurizing pump 25 through the supply pump 60 and the check valve 37a.

【0010】一方高圧容器の上蓋22に連結した連絡管
42には圧力センサー51が接続され、更に後流側に高
圧仕切弁3及びオリフィスノズル1が接続されている。
オリフィスノズル1の出口にはキャッチャー2を介して
排出管4が連結されており、同キャッチャー2は、例え
ば一端を封止した円筒管であり、同排出管4は同円筒管
の側面に連結される。機器の動作は制御装置50によっ
て制御される。図3にオリフィスノズル1の詳細構造を
示す。オリフィスホルダー13に嵌着されたオリフィス
14は、ダイヤモンド或いはサファイア等の硬質材料に
より製作され、中央部に通過流量に応じて0.1〜1.
0mm程度の微小な孔が加工されている。オリフィスホ
ルダー13はオリフィス押え12によってボディ11に
固定されており、同ボディ11とオリフィス14との間
には外部へ流体が逃げないようにOリング15が組込ま
れている。またボディ11側には連絡管42がカラー1
7、グランドナット18によって接続され、オリフィス
押え12にはキャッチャー2が接続されている。
On the other hand, a pressure sensor 51 is connected to the connecting pipe 42 connected to the upper lid 22 of the high pressure container, and a high pressure sluice valve 3 and an orifice nozzle 1 are further connected to the downstream side.
A discharge pipe 4 is connected to the outlet of the orifice nozzle 1 via a catcher 2. The catcher 2 is, for example, a cylindrical pipe having one end sealed, and the discharge pipe 4 is connected to a side surface of the cylindrical pipe. It The operation of the device is controlled by the control device 50. FIG. 3 shows a detailed structure of the orifice nozzle 1. The orifice 14 fitted in the orifice holder 13 is made of a hard material such as diamond or sapphire, and has a central portion of 0.1-1.
A small hole of about 0 mm is processed. The orifice holder 13 is fixed to the body 11 by an orifice retainer 12, and an O-ring 15 is incorporated between the body 11 and the orifice 14 so that the fluid does not escape to the outside. On the body 11 side, the connecting pipe 42 has a collar 1
7, the gland nut 18 is connected, and the orifice presser 12 is connected to the catcher 2.

【0011】次に以上のように構成された本発明の実施
例について作用を説明すると、被処理液は供給タンク6
1から供給ポンプ60により加圧ポンプ25に供給され
る。次いで油圧ユニット27を作動させてピストン29
が左右に往復運動し、例えば右側へ高圧ピストン35a
が移動すると、高圧シリンダ33a内に被処理液がチェ
ック弁37aを通って吸引される。同時にシリンダ33
b内の被処理液はチェック弁37b及び連絡管41を通
って加圧室23に供給される。なお、初めは高圧仕切弁
3は閉じられており、加圧室23内の圧力は上昇する。
圧力が所定値に達したら油圧ユニット27を一時停止し
て加圧ポンプ25からの供給を停止し、加圧室23内の
被処理液を所定時間高圧下で保持する。所定時間が経過
したら再び油圧ユニット27を起動し、加圧ポンプ25
を作動させて被処理液を加圧、供給すると同時に、高圧
仕切弁3を開放し、加圧室23内の被処理液をオリフィ
スノズル1を通して排出する。オリフィス1に加工した
孔は小径であり、流体が通過する際に大きな圧力損失を
伴う。従って加圧ポンプ25の吐出量に等しい量だけ噴
出させるための差圧が、所定加圧保持圧力に等しくなる
ようにオリフィス孔径を選定しておけば、加圧室23内
の圧力を保持しながら連続的に被処理液を排出させるこ
とが可能となる。
Next, the operation of the embodiment of the present invention configured as described above will be explained.
It is supplied to the pressurizing pump 25 from 1 by the supply pump 60. Next, the hydraulic unit 27 is operated to operate the piston 29.
Reciprocate left and right, for example, to the right side of the high pressure piston 35a
When is moved, the liquid to be treated is sucked into the high-pressure cylinder 33a through the check valve 37a. Cylinder 33 at the same time
The liquid to be treated in b is supplied to the pressurizing chamber 23 through the check valve 37b and the connecting pipe 41. The high-pressure sluice valve 3 is initially closed, and the pressure in the pressurizing chamber 23 rises.
When the pressure reaches a predetermined value, the hydraulic unit 27 is temporarily stopped to stop the supply from the pressurizing pump 25, and the liquid to be treated in the pressurizing chamber 23 is kept under high pressure for a predetermined time. When the predetermined time has elapsed, the hydraulic unit 27 is activated again and the pressurizing pump 25
Is operated to pressurize and supply the liquid to be treated, and at the same time, the high-pressure sluice valve 3 is opened to discharge the liquid to be treated in the pressurizing chamber 23 through the orifice nozzle 1. The hole processed in the orifice 1 has a small diameter, and a large pressure loss occurs when the fluid passes through. Therefore, if the orifice hole diameter is selected so that the differential pressure for ejecting the same amount as the discharge amount of the pressurizing pump 25 becomes equal to the predetermined pressurizing and holding pressure, the pressure in the pressurizing chamber 23 is maintained. It becomes possible to continuously discharge the liquid to be treated.

【0012】この時被処理液は加圧室23内を流動する
間高圧下で保持され、殺菌、物性変化がなされる。また
オリフィス1を通過した流体は高速ジェット噴流となる
ので、キャッチャー2で噴流を受け止めた(例えば封止
端に噴流を衝突させる)後、排出管4から排出し、次工
程(バッファタンク等)へ送液される。処理装置を停止
する場合は仕切弁3を閉じると同時に加圧ポンプ25に
よる供給を停止し、一度加圧室23内の被処理液をすべ
て所定時間高圧下で保持する。その後仕切弁3を開放し
て減圧排出し、更に供給ポンプ60で、例えば無菌水を
加圧室に供給して加圧室内の処理済液を全量排出する。
被処理液の温度が変化すると、粘度が変化してオリフィ
スの噴出量が変化する場合があるので、圧力センサー5
1の測定値を制御装置50で読み取り、圧力が低下する
場合は油圧ユニット27の吐出量を増大して加圧ポンプ
25による供給量を増大させ、反対に圧力が上昇する場
合には同様に加圧ポンプ25による供給量を減少させる
制御を行なう。
At this time, the liquid to be treated is kept under high pressure while flowing in the pressure chamber 23, and is sterilized and its physical properties are changed. Further, the fluid that has passed through the orifice 1 becomes a high-speed jet jet, so after catching the jet with the catcher 2 (for example, the jet collides with the sealing end), it is discharged from the discharge pipe 4 and then to the next step (buffer tank etc.). Liquid is sent. When the processing apparatus is stopped, the sluice valve 3 is closed and at the same time the supply by the pressurizing pump 25 is stopped, and all the liquid to be processed in the pressurizing chamber 23 is once kept under high pressure for a predetermined time. After that, the sluice valve 3 is opened to discharge under reduced pressure, and then, for example, aseptic water is supplied to the pressurizing chamber by the supply pump 60 to discharge the entire amount of the treated liquid in the pressurizing chamber.
When the temperature of the liquid to be treated changes, the viscosity may change and the ejection amount of the orifice may change, so the pressure sensor 5
The measured value of 1 is read by the control device 50, and when the pressure decreases, the discharge amount of the hydraulic unit 27 is increased to increase the supply amount by the pressurizing pump 25. Conversely, when the pressure rises, the same is applied. Control for reducing the supply amount by the pressure pump 25 is performed.

【0013】次に図2により本発明の高圧液体連続処理
装置の第2実施例を説明すると、図2ではオリフィス1
の出口のキャッチャー2及び排出管4にそれぞれ熱交換
器5,6を取付け、冷却装置7からの冷媒を循環配管8
を通じて循環させるようにしている。またオリフィスノ
ズル1を通過した高速噴流がキャッチャー2で受け止め
られる際被処理液の温度が上昇するが、前記の冷却機構
により速やかに冷却して被処理液の品質への影響を最小
限に抑えることができる。またこの第2実施例では被処
理液が高圧に保持される加圧室23が高圧円筒胴及び上
下蓋で構成されているが、これは耐圧強度を有する高圧
配管の長い管路であってもよい。
Next, a second embodiment of the high pressure liquid continuous processing apparatus of the present invention will be described with reference to FIG.
The heat exchangers 5 and 6 are attached to the catcher 2 and the discharge pipe 4 at the outlet of the cooling pipe 7 to circulate the refrigerant from the cooling device 7, respectively.
I am trying to circulate through. Further, the temperature of the liquid to be treated rises when the high-speed jet flow passing through the orifice nozzle 1 is received by the catcher 2, but the cooling mechanism promptly cools it to minimize the influence on the quality of the liquid to be treated. You can Further, in the second embodiment, the pressurizing chamber 23 in which the liquid to be treated is kept at high pressure is composed of the high-pressure cylinder and the upper and lower lids, but this is even if the high-pressure pipe having a high pressure resistance is long. Good.

【0014】[0014]

【発明の効果】以上詳細に説明した如く本発明による
と、簡単なオリフィスノズルと加圧ポンプとを組合せて
使用することにより、高圧加圧保持した液状食品を連続
的に減圧、排出することができ、コンパクトで安価な高
圧液体連続処理装置を提供しすることができる。またオ
リフィス出口に続くキャッチャー部及び排出配管に冷却
装置を設けることにより、オリフィス通過後の被処理液
の温度上昇を有効に抑え、食品品質への悪影響を最小限
にすることができる。
As described in detail above, according to the present invention, by using a simple orifice nozzle and a pressure pump in combination, it is possible to continuously depressurize and discharge the liquid food under high pressure and pressure. It is possible to provide a compact and inexpensive high-pressure liquid continuous treatment device. Further, by providing a cooling device in the catcher section and the discharge pipe that follow the orifice outlet, it is possible to effectively suppress the temperature rise of the liquid to be treated after passing through the orifice, and to minimize the adverse effect on the food quality.

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

【図1】本発明の第1実施例に係る高圧液体連続処理装
置のフロー図である。
FIG. 1 is a flowchart of a high pressure liquid continuous processing apparatus according to a first embodiment of the present invention.

【図2】本発明の第2実施例に係る高圧液体連続処理装
置のフロー図である。
FIG. 2 is a flow chart of a high pressure liquid continuous processing apparatus according to a second embodiment of the present invention.

【図3】本発明の実施例を示すオリフィスノズルの断面
図である。
FIG. 3 is a sectional view of an orifice nozzle showing an embodiment of the present invention.

【図4】従来の高圧液体連続処理装置を示すフロー図で
ある。
FIG. 4 is a flow chart showing a conventional high-pressure liquid continuous processing apparatus.

【符号の説明】[Explanation of symbols]

1 オリフィスノズル 2 キャッチャー 3 高圧仕切弁 4 排出管 5,6 熱交換器 7 冷却装置 20 高圧容器胴 21 下蓋 22 上蓋 23 加圧室 24 ヨークフレーム 25 加圧ポンプ 27 油圧ユニット 31 油圧シリンダ 41,42 連絡管 1 Orifice Nozzle 2 Catcher 3 High Pressure Gate Valve 4 Discharge Pipe 5, 6 Heat Exchanger 7 Cooling Device 20 High Pressure Vessel Body 21 Lower Lid 22 Upper Lid 23 Pressurizing Chamber 24 Yoke Frame 25 Pressurizing Pump 27 Hydraulic Unit 31 Hydraulic Cylinder 41, 42 Connecting pipe

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 飲料等の液体食品を高圧処理する高圧処
理装置において、被処理液が供給口から流入して高圧下
で内部を流動通過した後、別の排出口から排出される高
圧容器と、同容器の入口側に接続された加圧ポンプと、
同容器の出口側に接続されたオリフィスノズルで構成さ
れ、同加圧ポンプで連続的に被処理液を高圧容器内に加
圧、供給すると共に、高圧容器からオリフィスノズルを
通って被処理液が連続的に減圧、排出されることを特徴
とする高圧液体連続処理装置。
1. A high-pressure processing apparatus for high-pressure processing of liquid foods such as beverages, wherein a liquid to be processed flows in through a supply port, flows through the inside under high pressure, and is then discharged through another discharge port. , A pressure pump connected to the inlet side of the container,
It is composed of an orifice nozzle connected to the outlet side of the container, and continuously pressurizes and supplies the liquid to be processed into the high-pressure container with the same pressure pump. A high-pressure liquid continuous treatment device characterized by being continuously decompressed and discharged.
【請求項2】 高圧容器内の圧力に相応して加圧ポンプ
からの供給量を増加、減少させることを特徴とする請求
項1記載の高圧液体連続処理装置。
2. The high-pressure liquid continuous processing apparatus according to claim 1, wherein the supply amount from the pressurizing pump is increased or decreased in accordance with the pressure in the high-pressure container.
【請求項3】 オリフィスノズルの出口に噴流を受止め
るキャッチャーを設けると共に、同キャッチャー及びキ
ャッチャーからの排出配管に冷却装置を設けたことを特
徴とする請求項1記載の高圧液体連続処理装置。
3. The high-pressure liquid continuous treatment apparatus according to claim 1, wherein a catcher for receiving the jet flow is provided at the outlet of the orifice nozzle, and a cooling device is provided for the catcher and a discharge pipe from the catcher.
JP5037310A 1993-02-03 1993-02-03 Device for continuously treating liquid under high pressure Withdrawn JPH06225707A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5037310A JPH06225707A (en) 1993-02-03 1993-02-03 Device for continuously treating liquid under high pressure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5037310A JPH06225707A (en) 1993-02-03 1993-02-03 Device for continuously treating liquid under high pressure

Publications (1)

Publication Number Publication Date
JPH06225707A true JPH06225707A (en) 1994-08-16

Family

ID=12494126

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5037310A Withdrawn JPH06225707A (en) 1993-02-03 1993-02-03 Device for continuously treating liquid under high pressure

Country Status (1)

Country Link
JP (1) JPH06225707A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000236857A (en) * 1999-02-22 2000-09-05 Ebara Corp Inactivation of pathogenic cyst-forming microorganism in liquid
WO2001060508A1 (en) * 2000-02-17 2001-08-23 The Japan Steel Works, Ltd. Device and method for continuous high-pressure treatment
JP2001300291A (en) * 2000-02-17 2001-10-30 Japan Steel Works Ltd:The Method and apparatus for continuous high pressure treatment
JP2002219352A (en) * 2001-01-29 2002-08-06 Japan Steel Works Ltd:The Continuous high-pressure treatment method and apparatus
WO2019004277A1 (en) * 2017-06-27 2019-01-03 国立大学法人九州大学 Method for manufacturing liquid product and device for manufacturing liquid product

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000236857A (en) * 1999-02-22 2000-09-05 Ebara Corp Inactivation of pathogenic cyst-forming microorganism in liquid
WO2001060508A1 (en) * 2000-02-17 2001-08-23 The Japan Steel Works, Ltd. Device and method for continuous high-pressure treatment
JP2001300291A (en) * 2000-02-17 2001-10-30 Japan Steel Works Ltd:The Method and apparatus for continuous high pressure treatment
JP2002219352A (en) * 2001-01-29 2002-08-06 Japan Steel Works Ltd:The Continuous high-pressure treatment method and apparatus
JP4580564B2 (en) * 2001-01-29 2010-11-17 株式会社日本製鋼所 Continuous high-pressure processing method and apparatus
WO2019004277A1 (en) * 2017-06-27 2019-01-03 国立大学法人九州大学 Method for manufacturing liquid product and device for manufacturing liquid product

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