JP4730251B2 - Fluid heat sterilizer - Google Patents

Fluid heat sterilizer Download PDF

Info

Publication number
JP4730251B2
JP4730251B2 JP2006225104A JP2006225104A JP4730251B2 JP 4730251 B2 JP4730251 B2 JP 4730251B2 JP 2006225104 A JP2006225104 A JP 2006225104A JP 2006225104 A JP2006225104 A JP 2006225104A JP 4730251 B2 JP4730251 B2 JP 4730251B2
Authority
JP
Japan
Prior art keywords
fluid
storage tank
transfer pipe
pig
pipe
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
Application number
JP2006225104A
Other languages
Japanese (ja)
Other versions
JP2008048616A (en
Inventor
徳子 古宮
重治 鈴木
志記 山元
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.)
Dai Nippon Printing Co Ltd
Original Assignee
Dai Nippon Printing Co 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 Dai Nippon Printing Co Ltd filed Critical Dai Nippon Printing Co Ltd
Priority to JP2006225104A priority Critical patent/JP4730251B2/en
Publication of JP2008048616A publication Critical patent/JP2008048616A/en
Application granted granted Critical
Publication of JP4730251B2 publication Critical patent/JP4730251B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Description

本発明は、飲食品等の流動体を加熱殺菌するための装置に関する。   The present invention relates to an apparatus for heat sterilizing a fluid such as a food or drink.

スープ、ソース、ジュース等の流動体を長期保存するには予め加熱して滅菌する必要があり、その殺菌方法としてはレトルト殺菌法、UHT(Ultra High Temperature)殺菌法等がある。   In order to preserve fluids such as soups, sauces and juices for a long period of time, they must be preliminarily heated and sterilized. Examples of sterilization methods include retort sterilization and UHT (Ultra High Temperature) sterilization.

レトルト殺菌法は、スープ等の流動体を缶、パウチ等の気密性容器に入れて密封し、レトルト釜内で高温・高圧の下、容器ごと滅菌する方法である。この殺菌方法はバッチ処理となるので、小容量の流動体であっても比較的容易に処理可能である。   The retort sterilization method is a method in which a fluid such as soup is put in an airtight container such as a can or pouch and sealed, and the whole container is sterilized in a retort kettle under high temperature and high pressure. Since this sterilization method is a batch process, even a small volume fluid can be processed relatively easily.

また、UHT殺菌法は、流動体をポンプによりタンクから移送管内に送り出しながら殺菌する方法である(例えば、特許文献1、2参照。)。この殺菌方法は連続的な処理となるので、殺菌に必要な熱量だけ流動体に加えることができ、したがって流動体を高品質で殺菌することができる。   The UHT sterilization method is a method of sterilizing a fluid while sending it from a tank into a transfer pipe by a pump (see, for example, Patent Documents 1 and 2). Since this sterilization method is a continuous process, the amount of heat necessary for sterilization can be added to the fluid, and thus the fluid can be sterilized with high quality.

このUHT殺菌方法によれば、流動体を移送管で送るので、移送終了後に流動体が移送管内に残留するという問題があるが、従来、そのような残留物を回収するためピグが使用されている(例えば、特許文献3参照。)。   According to this UHT sterilization method, since the fluid is sent by the transfer pipe, there is a problem that the fluid remains in the transfer pipe after the transfer is finished. Conventionally, a pig is used to collect such a residue. (For example, refer to Patent Document 3).

特開平8−322463号公報JP-A-8-322463 特開平11−239469号公報JP 11-239469 A 特開平9−192620号公報Japanese Patent Laid-Open No. 9-192620

レトルト殺菌法は、缶、パウチ等の気密性容器内に封入された流動体の中心部が所定の温度に達するまで長時間加熱しなければならないことから、一般にUHT殺菌方法に比べて過加熱となりやすく、風味、テクスチャー、栄養素が低下したり、褐色等に変色したりし、流動体の品質が低下しやすいという傾向がある。   The retort sterilization method is generally overheated compared to the UHT sterilization method because the center of the fluid sealed in an airtight container such as a can or pouch must be heated for a long time until it reaches a predetermined temperature. There is a tendency that the quality of the fluid tends to be lowered because the flavor, texture, and nutrients are lowered or the color is changed to brown or the like.

一方、UHT殺菌法は、ポンプ等により流動体を移送管内に連続的に送りながら加熱殺菌と冷却を行うので、移送管の全体積以上の流動体を常時流す必要があり、従って容量が少ない流動体には適さない。また、UHT殺菌法は流動体を移送管で送るので、移送が終了した際に流動体が移送管の内面に付着し残留しやすいという問題がある。   On the other hand, the UHT sterilization method performs heat sterilization and cooling while continuously feeding the fluid into the transfer pipe by a pump or the like, so it is necessary to constantly flow the fluid over the entire volume of the transfer pipe, and therefore the flow with a small capacity. Not suitable for the body. In addition, since the UHT sterilization method sends the fluid through the transfer pipe, there is a problem that the fluid tends to adhere to the inner surface of the transfer pipe when the transfer is completed.

本発明はこのような問題点を解消する流動体加熱殺菌装置を提供することを目的とする。   It is an object of the present invention to provide a fluid heating sterilizer that eliminates such problems.

上記課題を解決するため、本発明は次のような構成を採用する。   In order to solve the above problems, the present invention employs the following configuration.

すなわち、請求項1に係る発明は、第一の貯留タンク(1)から第二の貯留タンク(2)へ移送管(3)を通して流動体(A)を送り、上流側の所定箇所で加熱殺菌手段(9)により流動体(A)を加熱殺菌処理し、下流側の所定箇所で冷却手段(19)により流動体(A)を冷却するようにした流動体加熱殺菌装置において、上記第一の貯留タンク(1)に上記加熱殺菌手段(9)を設け、上記移送管における上記第一の貯留タンクに通じる上流側と上記第二の貯留タンクに通じる下流側に各々開閉弁を設け、上記移送管(3)の上記両開閉弁で挟まれた中間部に上記冷却手段(19)を設け、流動体(A)を上記第一の貯留タンク(1)内で上記加熱殺菌手段(9)により所定の温度まで加熱しつつ、かつ、圧空供給手段(18)から上記第一の貯留タンク(1)に供給される無菌の圧空により加圧しつつ殺菌した後、上記上流側の開閉弁を開けて、圧空供給手段(18)から上記第一の貯留タンク(1)に供給される無菌の圧空により、上記第一の貯留タンク内の流動体を上記下流側の閉じた開閉弁側へと送って上記移送管(3)の中間部内に溜め、この中間部内の流動体を上記冷却手段(19)により冷却し、しかる後上記下流側の開閉弁を開けて冷却された流動体を上記第二の貯留タンク(2)に送るようにしたことを特徴とする。 That is, the invention according to claim 1 sends the fluid (A) through the transfer pipe (3) from the first storage tank (1) to the second storage tank (2), and heat sterilization at a predetermined location on the upstream side. In the fluid heat sterilization apparatus in which the fluid (A) is heat sterilized by the means (9) and the fluid (A) is cooled by the cooling means (19) at a predetermined downstream position. The storage tank (1) is provided with the heat sterilization means (9), and an on-off valve is provided on the upstream side of the transfer pipe leading to the first storage tank and on the downstream side of the second storage tank. The cooling means (19) is provided at an intermediate portion of the pipe (3) sandwiched between the on-off valves, and the fluid (A) is placed in the first storage tank (1) by the heat sterilization means (9). while heating to a predetermined temperature, and, above the pneumatic supply means (18) Was sterilized while pressing the pressure sterile supplied to the first storage tank (1), by opening the on-off valve of the upstream side, the pressure supply means (18) to said first storage tank (1) With the supplied aseptic compressed air , the fluid in the first storage tank is sent to the closed on-off valve side on the downstream side and stored in the intermediate portion of the transfer pipe (3), and the fluid in the intermediate portion Is cooled by the cooling means (19), and then the downstream on-off valve is opened to send the cooled fluid to the second storage tank (2).

また、請求項2に係る発明は、請求項1に記載の流動体加熱殺菌装置において、移送管(3)の下流側を開閉弁(10)で遮蔽し、上流側から圧空供給手段(18)により無菌の圧空を供給して、流動体(A)を移送管(3)の冷却手段(19)の位置に保持しつつ冷却するようにしたことを特徴とする。 The invention according to claim 2 is the fluid heat sterilizer according to claim 1 , wherein the downstream side of the transfer pipe (3) is shielded by the on-off valve (10), and the compressed air supply means (18) from the upstream side. Aseptic pressure air is supplied to the fluid (A), and the fluid (A) is cooled while being held at the position of the cooling means (19) of the transfer pipe (3).

また、請求項3に係る発明は、請求項1に記載の流動体加熱殺菌装置において、移送管(3)内に移動可能に挿入されたピグ(4)と、移送管(3)における冷却手段(19)よりも上流側に設けられたピグ(4)の待機室(5)と、移送管(3)における冷却手段(19)よりも下流側に設けられたピグ(4)の行止室(6)とを備えたことを特徴とする。 The invention according to claim 3 is the fluid heat sterilization apparatus according to claim 1, wherein the pig (4) movably inserted into the transfer pipe (3) and the cooling means in the transfer pipe (3) are provided. The waiting chamber (5) of the pig (4) provided upstream from (19) and the closing chamber (5) of the pig (4) provided downstream from the cooling means (19) in the transfer pipe (3) 6).

本発明によれば、流動体(A)の過加熱を防止し、風味、テクスチャー、栄養素等の品質低下や変色を来たすことなく流動体(A)を殺菌することができ、また、流動体(A)を移送管(3)内で連続的に流しながら加熱殺菌等を行う必要はないので、移送管(3)の体積程度の量であれば殺菌処理可能であり、従って容量が少ない流動体(A)であっても殺菌可能である。 According to the present invention, to prevent overheating of the flow body (A), flavor, texture, it is possible to sterilize the fluid (A) without causing the degradation or discoloration of the nutrient, also, the fluid ( Since it is not necessary to carry out heat sterilization while continuously flowing A) through the transfer pipe (3), it can be sterilized as long as the volume of the transfer pipe (3), and therefore has a small capacity. Even (A) can be sterilized.

また、本発明によれば、移送管(3)内に移動可能に挿入されたピグ(4)と、移送管(3)における冷却手段(19)よりも上流側に設けられたピグ(4)の待機室(5)と、移送管(3)における冷却手段(19)よりも下流側に設けられたピグ(4)の行止室(6)とを備えたことから、流動体(A)を移送管(3)で冷却することにより流動体(A)が移送管(3)の内面に多く付着し残留したとしても、その残留した流動体(A)を適正に回収することができる。   Moreover, according to this invention, the pig (4) movably inserted in the transfer pipe (3) and the pig (4) provided on the upstream side of the cooling means (19) in the transfer pipe (3). The waiting chamber (5) and the closing chamber (6) of the pig (4) provided downstream of the cooling means (19) in the transfer pipe (3) are provided. Even if the fluid (A) adheres and remains on the inner surface of the transfer tube (3) by cooling with the transfer tube (3), the remaining fluid (A) can be properly recovered.

次に、本発明の実施の形態について図面を参照して説明する。   Next, embodiments of the present invention will be described with reference to the drawings.

図1に示すように、この流動体加熱殺菌装置は、第一の貯留タンク1から第二の貯留タンク2へ移送管3を通して流動体を送り、上流側の所定箇所で加熱殺菌手段により流動体を加熱殺菌処理し、下流側の所定箇所で冷却手段により流動体を冷却するように構成される。   As shown in FIG. 1, this fluid heat sterilizer sends a fluid through a transfer pipe 3 from a first storage tank 1 to a second storage tank 2, and the fluid is sterilized by a heat sterilization means at a predetermined location on the upstream side. The fluid is sterilized by heating, and the fluid is cooled by cooling means at a predetermined location on the downstream side.

第一の貯留タンク1から第二の貯留タンク2へと移送管3を介して送られる流動体は、スープ、ソース、ジュース等であるが、飲食物に限られるものではない。   Although the fluid sent from the 1st storage tank 1 to the 2nd storage tank 2 via the transfer pipe 3 is soup, a sauce, juice, etc., it is not restricted to food and drink.

第一の貯留タンク1は、流動体を溜めておくための容積の大きい密封容器である。図5に示すように、第一の貯留タンク1は開閉可能な蓋1aを有し、この蓋1aを開けて流動体Aをタンク本体内に流し込むようになっている。   The first storage tank 1 is a large-capacity sealed container for storing a fluid. As shown in FIG. 5, the first storage tank 1 has a lid 1a that can be opened and closed. The lid 1a is opened to allow the fluid A to flow into the tank body.

第二の貯留タンク2は、第一の貯留タンク1と同様な大きさを有し、第一の貯留タンク1に貯留された流動体のすべてが移送管3を通して流入可能である。第二の貯留タンク2には、図示しないが袋、容器等に流動体を充填して包装する無菌充填機に流動体を送るための導管が接続される。   The second storage tank 2 has the same size as the first storage tank 1, and all of the fluid stored in the first storage tank 1 can flow in through the transfer pipe 3. Although not shown, the second storage tank 2 is connected to a conduit for sending the fluid to an aseptic filling machine that fills and packs the fluid in bags, containers, and the like.

移送管3は、第一の貯留タンク1から第二の貯留タンク2へと伸び、第一の貯留タンク1側すなわち上流側の送出部3aと、第二の貯留タンク2側すなわち下流側の流入部3cと、送出部3aと流入部3cとの間の中間部3bとで構成される。   The transfer pipe 3 extends from the first storage tank 1 to the second storage tank 2, and the first storage tank 1 side, that is, the upstream delivery section 3a, and the second storage tank 2 side, that is, the downstream side inflow. It is comprised by the part 3c and the intermediate part 3b between the sending part 3a and the inflow part 3c.

移送管3の送出部3aには、第一の貯留タンク1寄りの箇所と、中間部3b寄りの箇所とにそれぞれ電磁弁である開閉弁7,8が設けられる。また、流入部3cにも電磁弁である開閉弁10が設けられる。   The delivery part 3a of the transfer pipe 3 is provided with on-off valves 7 and 8 which are electromagnetic valves, respectively, near the first storage tank 1 and near the intermediate part 3b. The inflow portion 3c is also provided with an on-off valve 10 that is an electromagnetic valve.

この流動体加熱殺菌装置には、流動体Aを供給する前に予めこの装置内を殺菌する蒸気殺菌手段が設けられる。すなわち、図1に示すように、第一の貯留タンク1には、殺菌用蒸気の供給管9が連結される。移送管3の中間部3bの上流側にも殺菌用蒸気の供給管14が連結される。第二の貯留タンク2には、上記殺菌用蒸気の供給管9から第一の貯留タンク1内と移送管3とに注入された蒸気を排出するための排気管11が接続される。移送管3の中間部3bの上流側にも蒸気の排気管16が接続される。   This fluid heating sterilization apparatus is provided with steam sterilization means for sterilizing the inside of the apparatus before supplying the fluid A. That is, as shown in FIG. 1, a sterilization steam supply pipe 9 is connected to the first storage tank 1. A sterilizing steam supply pipe 14 is also connected to the upstream side of the intermediate portion 3 b of the transfer pipe 3. The second storage tank 2 is connected to an exhaust pipe 11 for discharging steam injected into the first storage tank 1 and the transfer pipe 3 from the sterilizing steam supply pipe 9. A steam exhaust pipe 16 is also connected to the upstream side of the intermediate portion 3 b of the transfer pipe 3.

当初第一及び第二の貯留タンク1,2内は空の状態とされ、殺菌用蒸気の供給管9から第一の貯留タンク1内に蒸気が注入されると、蒸気は第一の貯留タンク1、移送管3、第二の貯留タンク2等の内部を殺菌した後、排気管11から排出される。この殺菌用の蒸気は注入時に例えば130℃程度であり、約30分間注入される。   Initially, the first and second storage tanks 1 and 2 are empty, and when steam is injected into the first storage tank 1 from the sterilizing steam supply pipe 9, the steam is stored in the first storage tank. 1, the inside of the transfer pipe 3, the second storage tank 2 and the like is sterilized and then discharged from the exhaust pipe 11. The sterilizing vapor is, for example, about 130 ° C. at the time of injection, and is injected for about 30 minutes.

この流動体加熱殺菌装置には、第一の貯留タンク1から第二の貯留タンク2へと流動体Aを供給するため、後述するピグ4を駆動するため、流動体加熱殺菌装置内を陽圧に保つために、圧空供給手段が設けられる。すなわち、図1に示すように、第一の貯留タンク1と第二の貯留タンク2には、それぞれ圧空供給管18,20が連結される。移送管3の中間部3bの上流側にも圧空供給管15が連結される。圧空供給管15,18,20の上流側には図示しないコンプレッサ、フィルタ等が設けられ、そこから無菌化された圧空が各圧空供給管15,18を通してこの流動体加熱殺菌装置内に供給される。   In order to supply the fluid A from the first storage tank 1 to the second storage tank 2 in this fluid heating sterilization device, a positive pressure is generated in the fluid heating sterilization device in order to drive a pig 4 described later. In order to maintain the pressure, a compressed air supply means is provided. That is, as shown in FIG. 1, the compressed air supply pipes 18 and 20 are connected to the first storage tank 1 and the second storage tank 2, respectively. A compressed air supply pipe 15 is also connected to the upstream side of the intermediate portion 3 b of the transfer pipe 3. A compressor, a filter, etc. (not shown) are provided on the upstream side of the compressed air supply pipes 15, 18, 20, and sterilized compressed air is supplied from the compressed air supply pipes 15, 18 into the fluid heating sterilizer. .

図7に示すように、圧空供給管18から第一の貯留タンク1内に供給される無菌の加圧された空気により、第一の貯留タンク1内の流動体Aは移送管3内に送り出される。また、図10に示すように、圧空供給管15から移送管3の中間部3b内に供給される無菌の加圧された空気により、ピグ4が中間部3b内を下流側へと移動し、中間部3b内に残留した流動体Aを掻き落として第二の貯留タンク2へと送り出す。また、圧空供給管18,15,20からこの流動体加熱殺菌装置内に供給されることにより、この装置内が陽圧に保持される。   As shown in FIG. 7, the fluid A in the first storage tank 1 is sent into the transfer pipe 3 by aseptic pressurized air supplied from the compressed air supply pipe 18 into the first storage tank 1. It is. Further, as shown in FIG. 10, the pig 4 is moved downstream in the intermediate part 3 b by the sterile pressurized air supplied from the compressed air supply pipe 15 into the intermediate part 3 b of the transfer pipe 3. The fluid A remaining in the intermediate part 3b is scraped off and sent to the second storage tank 2. Further, by supplying the fluid heating sterilizer from the compressed air supply pipes 18, 15 and 20, the inside of the apparatus is maintained at a positive pressure.

上記第一の貯留タンク1には、流動体Aの加熱殺菌手段が設けられる。この加熱殺菌手段としては、図1に示した第一の貯留タンク1に接続された殺菌用蒸気の供給管9と圧空供給管18とを用いることができる。圧空供給管18から圧空を第一の貯留タンク1内に供給して流動体Aを加圧しつつ殺菌用蒸気の供給管9から蒸気を第一の貯留タンク1内に注入することにより、第一の貯留タンク1に貯留された流動体Aを高温・高圧のもとで加熱殺菌することができる。   The first storage tank 1 is provided with heat sterilization means for the fluid A. As the heat sterilization means, the sterilization steam supply pipe 9 and the compressed air supply pipe 18 connected to the first storage tank 1 shown in FIG. 1 can be used. By supplying pressurized air from the compressed air supply pipe 18 into the first storage tank 1 and injecting steam into the first storage tank 1 from the supply pipe 9 for the sterilizing steam while pressurizing the fluid A, The fluid A stored in the storage tank 1 can be sterilized by heating under high temperature and high pressure.

流動体Aの加熱殺菌は、蒸気を直接流動体A内に吹き込むことによるほか、第一の貯留タンク1の壁をジャケットで覆い、このジャケット内に蒸気を供給し、伝熱により流動体Aを加熱することによっても行うことができる。また、流動体Aに電気を直接流すことにより流動体A自体の電気抵抗により発生するジュール熱で流動体Aを加熱することもできる。これらの手段を用いる場合も圧空供給管18から圧空を送って加圧状態の下で加熱することができる。   The heat sterilization of the fluid A is not only by blowing steam directly into the fluid A, but also covering the wall of the first storage tank 1 with a jacket, supplying the steam into the jacket, and transferring the fluid A by heat transfer. It can also be performed by heating. In addition, by directly flowing electricity through the fluid A, the fluid A can be heated by Joule heat generated by the electrical resistance of the fluid A itself. Even when these means are used, the compressed air can be sent from the compressed air supply pipe 18 and heated under a pressurized condition.

上記移送管3には、加熱殺菌された流動体Aを冷却するための冷却手段が設けられる。図1に示すように、冷却手段は、移送管3の中間部3bに被せられた冷却用ジャケット19を備える。冷却用ジャケット19には、冷却水の給水管19aと排水管19bが接続される。図8に示すように、冷却水が給水管19aから冷却用ジャケット19内に供給され、排水管19bから排出されることにより、移送管3の中間部3b内に導入された流動体Aが例えば後の包装に支障を生じない程度の温度である30℃〜40℃まで冷却される。また、図8に示すように、この冷却手段による流動体Aの冷却の際は、望ましくは移送管3の下流側が開閉弁10で遮蔽され、上流側から圧空供給管18により無菌の圧空が供給されることで、流動体Aが移送管3の中間部3b内に静止状態で保持される。このように加熱部分から冷却部分が分けられていることにより、流動体Aは速やかに上記適正温度まで冷却される。   The transfer pipe 3 is provided with a cooling means for cooling the heat-sterilized fluid A. As shown in FIG. 1, the cooling means includes a cooling jacket 19 that covers the intermediate portion 3 b of the transfer pipe 3. A cooling water supply pipe 19 a and a drain pipe 19 b are connected to the cooling jacket 19. As shown in FIG. 8, the cooling water is supplied from the water supply pipe 19 a into the cooling jacket 19 and discharged from the drain pipe 19 b, so that the fluid A introduced into the intermediate portion 3 b of the transfer pipe 3 is, for example, It is cooled to 30 ° C. to 40 ° C., which is a temperature that does not hinder subsequent packaging. Further, as shown in FIG. 8, when the fluid A is cooled by the cooling means, the downstream side of the transfer pipe 3 is preferably shielded by the on-off valve 10, and sterile compressed air is supplied from the upstream side by the compressed air supply pipe 18. As a result, the fluid A is held in a stationary state in the intermediate portion 3 b of the transfer pipe 3. Thus, by dividing the cooling part from the heating part, the fluid A is quickly cooled to the appropriate temperature.

図9に示すように、移送管3の中間部3b内で冷却された流動体Aは第二の貯留タンク2へと送られるが、流動体Aは冷却される結果粘度が高くなり移送管3の中間部3bの内面に厚い層となって付着し残留しやすくなる。この残留した流動体Aを回収するため、図1及び図2に示すように、移送管3の中間部3b内にピグ4が移動可能に設けられる。また、移送管3の中間部3bにおける冷却用ジャケット19よりも上流側にはピグ4の待機室5が設けられ、冷却用ジャケット19よりも下流側にはピグ4の行止室6が設けられる。   As shown in FIG. 9, the fluid A cooled in the intermediate portion 3 b of the transfer pipe 3 is sent to the second storage tank 2, but as a result of cooling the fluid A, the viscosity increases and the transfer pipe 3 It becomes easy to adhere and remain as a thick layer on the inner surface of the intermediate portion 3b. In order to collect the remaining fluid A, the pig 4 is movably provided in the intermediate portion 3b of the transfer pipe 3, as shown in FIGS. Further, the waiting chamber 5 of the pig 4 is provided upstream of the cooling jacket 19 in the intermediate portion 3 b of the transfer pipe 3, and the closing chamber 6 of the pig 4 is provided downstream of the cooling jacket 19.

移送管3の中間部3bは、その上流側から下流側へと所望の箇所で屈曲して伸びるものであってもよいが、望ましくは図1に示すように待機室5と行止室6との間において直管すなわち真っ直ぐに伸びる管として構成される。これにより、この流動体加熱殺菌装置の構造が簡素化され、省スペース化も可能になる。   The intermediate portion 3b of the transfer pipe 3 may be bent and extended at a desired location from the upstream side to the downstream side. Preferably, as shown in FIG. It is configured as a straight pipe, that is, a pipe extending straight in between. Thereby, the structure of this fluid heating sterilization apparatus is simplified and space saving is also attained.

ピグ4は、軟質材であり弾性材である樹脂、ゴム等により、図3に示すごとく、略円柱体として形成される。ピグ4は、移送管3内を移動しつつ移送管3の内面に付着し残留した流動体Aを掻き落とすことができるように、その外径が移送管3の内径よりもやや小さくなるように形成される。ピグ4の前部すなわち移送管3内で流動体Aの流れる方向に向く前部分の回りには、必要に応じてOリング12が嵌め込まれる。Oリング12により移送管3の中間部3bの内面に付着した流動体Aはより効果的に掻き落とされる。   As shown in FIG. 3, the pig 4 is formed as a substantially cylindrical body by using a soft material and an elastic material such as resin, rubber, and the like. The outer diameter of the pig 4 is slightly smaller than the inner diameter of the transfer pipe 3 so that the fluid A remaining on the inner surface of the transfer pipe 3 can be scraped off while moving in the transfer pipe 3. It is formed. An O-ring 12 is fitted around the front part of the pig 4, that is, around the front part of the transfer pipe 3 that faces the direction in which the fluid A flows. The fluid A attached to the inner surface of the intermediate portion 3b of the transfer pipe 3 by the O-ring 12 is scraped off more effectively.

また、ピグ4の中央部には、後述する拘束具13が係脱自在に入り込む環状溝4aが設けられる。拘束具13がこの環状溝4a内に入り込むとピグ4は待機室5内の定位置から移動しないように拘束され、環状溝4a外に出るとピグ4は解放され移送管3内を移動可能となる。   In addition, an annular groove 4 a into which a later-described restraining tool 13 enters and disengages is provided at the center of the pig 4. When the restraining tool 13 enters the annular groove 4a, the pig 4 is restrained from moving from a fixed position in the standby chamber 5, and when it moves out of the annular groove 4a, the pig 4 is released and can move within the transfer pipe 3. Become.

図2に示すように、待機室5は、ピグ4の前部が挿入される移送管3の中間部3bと略同じ太さの延長管5aと、ピグ4の後部が挿入される移送管3より太い拡張管5bとで構成される。延長管5aは移送管3の中間部3bと送出部3aとの境界近傍から中間部3bの延長方向に突出するごとく分岐する。拡張管5bはピグ4の径よりも大きい内径を有し、ピグ4の外周面との間に空室を形成する。拡張管5bと延長管5aとの間には内径を徐々に変化させるための円錐管5cが必要に応じて設けられる。   As shown in FIG. 2, the waiting room 5 includes an extension pipe 5 a having substantially the same thickness as the intermediate part 3 b of the transfer pipe 3 into which the front part of the pig 4 is inserted, and a transfer pipe 3 into which the rear part of the pig 4 is inserted. It is comprised with the thicker expansion tube 5b. The extension pipe 5a branches off from the vicinity of the boundary between the intermediate part 3b of the transfer pipe 3 and the delivery part 3a so as to protrude in the extension direction of the intermediate part 3b. The expansion pipe 5 b has an inner diameter larger than the diameter of the pig 4, and forms an empty space between the expansion pipe 5 b and the outer peripheral surface of the pig 4. A conical tube 5c for gradually changing the inner diameter is provided between the expansion tube 5b and the extension tube 5a as necessary.

拡張管5bには、上述した蒸気供給管14と、圧空供給管15とが接続される。また、蒸気排気管16も接続される。図4に示すように、蒸気供給管14から殺菌用の蒸気が拡張管5b内に注入されると、この蒸気がピグ4の表面を加熱殺菌する。この蒸気は例えば130℃程度であり、約30分間注入される。ピグ4は待機室5内で待機中その前部が延長管5a内に嵌り込むことから拡張管5b内で宙吊り状に保持され、その略全表面に蒸気が接触する。従って、ピグ4の表面が適正に殺菌処理される。蒸気はピグ4の殺菌後、拡張管5bに接続された排気管16から外部に排出される。また、殺菌用蒸気の供給を停止し、図10に示すように、圧空をその供給管15から拡張管5b内に注入すると、その圧力によりピグ4が待機室5から移送管3内に出て移送管3内を下流側に移動し、図11に示すように、行止室6内に到達して停止する。ピグ4を移動させるための圧空の圧力は例えば0.3〜0.4MPa程度である。   The steam supply pipe 14 and the compressed air supply pipe 15 described above are connected to the expansion pipe 5b. A steam exhaust pipe 16 is also connected. As shown in FIG. 4, when sterilization steam is injected into the expansion pipe 5 b from the steam supply pipe 14, the steam heat-sterilizes the surface of the pig 4. This vapor is, for example, about 130 ° C. and is injected for about 30 minutes. Since the front portion of the pig 4 is fitted in the extension pipe 5a during standby in the standby chamber 5, the pig 4 is held suspended in the extension pipe 5b, and the vapor contacts the substantially entire surface. Therefore, the surface of the pig 4 is appropriately sterilized. After the sterilization of the pig 4, the steam is discharged to the outside from the exhaust pipe 16 connected to the expansion pipe 5 b. Further, when the supply of the sterilizing steam is stopped and the compressed air is injected into the expansion pipe 5b from the supply pipe 15 as shown in FIG. 10, the pig 4 comes out of the standby chamber 5 into the transfer pipe 3 by the pressure. The inside of the transfer pipe 3 moves downstream, and reaches the stop chamber 6 and stops as shown in FIG. The pressure of the compressed air for moving the pig 4 is, for example, about 0.3 to 0.4 MPa.

図2に示すように、待機室5には、拡張管5bの管壁に形成された貫通孔17を管内へ貫通する拘束具13が設けられる。拘束具13は具体的には丸棒であり、作業者が貫通孔17から待機室5内に拘束具13を挿入した際にその先端部がピグ4の環状溝4a内に食い込むことで、ピグ4を待機室5中に拘束する。これにより、殺菌用蒸気供給管14から殺菌用蒸気を供給する際に、ピグ4は蒸気圧に抗して待機室5中の定位置に留まることになる。また、作業者が拘束具13を拡張管5bの外側へと引いて拘束具13の先端部をピグ4の環状溝4aから離脱させると、ピグ4は待機室5中での拘束を解かれる。これにより、圧空供給管15から圧空が供給されると、ピグ4は待機室5から移送管3内に押し出されることとなる。   As shown in FIG. 2, the waiting chamber 5 is provided with a restraining tool 13 that penetrates the through hole 17 formed in the pipe wall of the expansion pipe 5 b into the pipe. Specifically, the restraining tool 13 is a round bar, and when the operator inserts the restraining tool 13 into the standby chamber 5 from the through-hole 17, the tip of the restraining tool 13 bites into the annular groove 4 a of the pig 4. 4 is restrained in the waiting room 5. Accordingly, when supplying the sterilizing steam from the sterilizing steam supply pipe 14, the pig 4 stays at a fixed position in the standby chamber 5 against the steam pressure. Further, when the operator pulls the restraining tool 13 to the outside of the expansion tube 5 b to disengage the tip of the restraining tool 13 from the annular groove 4 a of the pig 4, the pig 4 is released from the restraint in the standby chamber 5. Thus, when pressurized air is supplied from the compressed air supply pipe 15, the pig 4 is pushed out from the standby chamber 5 into the transfer pipe 3.

行止室6は、移送管3の中間部3bと流入部3cとの境界近傍から中間部3bが分岐することにより形成される。この分岐部の末端は端板6aで閉じられ、ピグ4はこの端板6aに当たって停止する。この行止室6の上流端から上記第二の貯留タンク2に向かって流入部3cが伸びている。ピグ4が上記待機室5から行止室6へと移動することにより、移送管3の内壁面に付着し残留した流動体Aがピグ4により掻き落とされ、流入部3cから第二の貯留タンク2内に流れ込むことで回収される。   The closing chamber 6 is formed by branching the intermediate portion 3b from the vicinity of the boundary between the intermediate portion 3b of the transfer pipe 3 and the inflow portion 3c. The end of this branching portion is closed by an end plate 6a, and the pig 4 hits the end plate 6a and stops. An inflow portion 3 c extends from the upstream end of the closing chamber 6 toward the second storage tank 2. When the pig 4 moves from the standby chamber 5 to the closing chamber 6, the fluid A attached to and remaining on the inner wall surface of the transfer pipe 3 is scraped off by the pig 4, and the second storage tank 2 from the inflow portion 3 c. It collects by flowing in.

次に、上記流動体加熱殺菌装置の作用について説明する。   Next, the operation of the fluid heat sterilizer will be described.

(1)当初、図4に示すように、第一及び第二の貯留タンク1,2内は空の状態とされる。また、図2に示すように、作業者により拘束具13が拡張管5bの貫通孔17から待機室5内に挿入され、拘束具13の先端がピグ4の環状溝4aに差し込まれる。これにより、ピグ4は待機室5内に拘束される。   (1) Initially, the first and second storage tanks 1 and 2 are emptied as shown in FIG. As shown in FIG. 2, the restraint 13 is inserted into the standby chamber 5 from the through hole 17 of the expansion pipe 5 b by the operator, and the tip of the restraint 13 is inserted into the annular groove 4 a of the pig 4. Thereby, the pig 4 is restrained in the waiting room 5.

(2)図4に示すように、移送管3上の開閉弁7,8,10が開けられ、殺菌用の蒸気が殺菌用蒸気の供給管9から第一の貯留タンク1内に注入される。この蒸気は第一の貯留タンク1から、移送管3内に流入し、その送出部3a、中間部3b及び流入部3cを通って第二の貯留タンク2へと流れつつ、これらの内部を殺菌した後、排気管11から第二の貯留タンク2外へ排出される。
また、図2に示すように、殺菌用の蒸気は、待機室5内すなわち拡張管5b、延長管5aの内部にも殺菌用蒸気供給管14から注入される。ピグ4は待機室5内においてその前部が延長管5a内に嵌り込み拡張管5b内で宙吊り状に保持される。これにより、拡張管5b内に注入された蒸気はピグ4の略全表面を殺菌する。蒸気はピグ4の殺菌後、拡張管5bに接続された排気管16から外部に排出される。
かくて流動体加熱殺菌装置の内部が殺菌処理されると、殺菌用蒸気供給管9,14、排気管11,16等の各種配管に設けられた図示しないバルブが閉じられ、系内が密閉される。
(2) As shown in FIG. 4, the on-off valves 7, 8, 10 on the transfer pipe 3 are opened, and sterilizing steam is injected into the first storage tank 1 from the sterilizing steam supply pipe 9. . This steam flows from the first storage tank 1 into the transfer pipe 3 and flows into the second storage tank 2 through the delivery part 3a, the intermediate part 3b and the inflow part 3c, and sterilizes the inside thereof. After that, the exhaust pipe 11 is discharged out of the second storage tank 2.
As shown in FIG. 2, the sterilizing vapor is also injected from the sterilizing vapor supply pipe 14 into the standby chamber 5, that is, inside the extension pipe 5b and the extension pipe 5a. The front part of the pig 4 is fitted in the extension pipe 5a in the standby chamber 5, and is held suspended in the extension pipe 5b. Thereby, the vapor | steam inject | poured in the expansion pipe | tube 5b sterilizes the substantially whole surface of the pig 4. FIG. After the sterilization of the pig 4, the steam is discharged to the outside from the exhaust pipe 16 connected to the expansion pipe 5 b.
Thus, when the inside of the fluid heating sterilizer is sterilized, valves (not shown) provided in various pipes such as the sterilizing steam supply pipes 9 and 14 and the exhaust pipes 11 and 16 are closed, and the system is sealed. The

(3)図5に示すように、移送管3の最上流側の開閉弁7が閉じられ、各種圧空供給管15,20から移送管3内に無菌の圧空が供給される。これにより、流動体加熱殺菌装置の内部が第一の貯留タンク1を除き陽圧に保たれ、菌類の流動体加熱殺菌装置内への侵入が阻止される。
そこで、図5に示すように、第一の貯留タンク1の蓋1aが開けられ、第一の貯留タンク1内にスープ、ソース、ジュース等所望の流動体Aが無菌的に一定量充填され、図6に示すように、再び蓋1aが被せられ第一の貯留タンク1が密閉される。
(3) As shown in FIG. 5, the on-off valve 7 on the most upstream side of the transfer pipe 3 is closed, and aseptic compressed air is supplied into the transfer pipe 3 from various compressed air supply pipes 15 and 20. Thereby, the inside of the fluid heating sterilizer is kept at a positive pressure except for the first storage tank 1, and fungi are prevented from entering the fluid heating sterilizer.
Therefore, as shown in FIG. 5, the lid 1a of the first storage tank 1 is opened, and a desired amount of fluid A such as soup, sauce and juice is aseptically filled in the first storage tank 1, As shown in FIG. 6, the lid 1a is put on again and the first storage tank 1 is sealed.

(4)図6に示すように、第一の貯留タンク1内に圧空供給管18から圧空が供給され、殺菌用蒸気供給管9から殺菌用の蒸気が注入される。これにより、第一の貯留タンク1内の流動体Aは高温・高圧のもとで加熱殺菌される。このように流動体Aは一定容積の貯留タンク内に貯留された状態で、しかもレトルト殺菌のような袋等の包装体を介することなく加熱されるので、速やかに加熱され、過加熱による品質の劣化が防止される。   (4) As shown in FIG. 6, pressurized air is supplied from the compressed air supply pipe 18 into the first storage tank 1, and sterilizing steam is injected from the sterilizing steam supply pipe 9. Thereby, the fluid A in the 1st storage tank 1 is heat-sterilized under high temperature and a high pressure. Thus, the fluid A is heated in a state where it is stored in a storage tank of a constant volume and without passing through a packaging body such as a bag such as retort sterilization. Deterioration is prevented.

(5)第一の貯留タンク1内の流動体Aが所定の温度まで加熱され殺菌されると、図7に示すように、第一の貯留タンク1内への蒸気の供給が停止され、直ちに移送管3の最上流側の開閉弁7が開けられ、最下流側の開閉弁10が閉じられる。これにより、第一の貯留タンク1内の流動体Aは、圧空供給管18から供給される圧空により、速やかに移送管3内に流入し、移送管3の中間部3b内に溜まる。流動体Aはポンプによることなく圧空で送られるので、移送管3内を円滑に流れる。   (5) When the fluid A in the first storage tank 1 is heated to a predetermined temperature and sterilized, the supply of steam into the first storage tank 1 is stopped as shown in FIG. The on-off valve 7 on the most upstream side of the transfer pipe 3 is opened, and the on-off valve 10 on the most downstream side is closed. As a result, the fluid A in the first storage tank 1 quickly flows into the transfer pipe 3 by the pressurized air supplied from the compressed air supply pipe 18 and accumulates in the intermediate portion 3 b of the transfer pipe 3. Since the fluid A is sent by compressed air without using a pump, the fluid A flows smoothly in the transfer pipe 3.

(6)図8に示すように、冷却用ジャケット19内に冷却水が供給され、移送管3の中間部3b内に溜まった流動体Aの冷却が行われる。流動体Aは第一の貯留タンク1内から速やかに移送管3内に流入し、直ちに冷却されるので、過度に加熱されることがなく、風味、テクスチャー、栄養素等の品質が高度に保持され、変色等も来たすことがない。
この流動体Aの冷却時、圧空供給管18,15から無菌の圧空が移送管3側へ供給され、その圧力により流動体Aは移送管3の中間部3b内に適正に保持される。また、流動体Aのピグ待機室5内への流入が防止される。また、圧空供給管20から無菌の圧空が第二の貯留タンク2内へ供給され、第二の貯留タンク2内が陽圧に保持される。
(6) As shown in FIG. 8, cooling water is supplied into the cooling jacket 19, and the fluid A accumulated in the intermediate portion 3 b of the transfer pipe 3 is cooled. Since the fluid A quickly flows into the transfer pipe 3 from the first storage tank 1 and is immediately cooled, it is not heated excessively, and the quality of flavor, texture, nutrients, etc. is maintained at a high level. No discoloration will occur.
When the fluid A is cooled, aseptic compressed air is supplied from the compressed air supply pipes 18 and 15 to the transfer pipe 3 side, and the fluid A is properly held in the intermediate portion 3 b of the transfer pipe 3 by the pressure. Further, the inflow of the fluid A into the pig waiting chamber 5 is prevented. Further, aseptic compressed air is supplied from the compressed air supply pipe 20 into the second storage tank 2, and the second storage tank 2 is maintained at a positive pressure.

(7)図9に示すように、第二の貯留タンク2への圧空供給管20からの圧空の供給が遮断され、移送管3の最下流側の開閉弁10が開けられる。これにより、移送管3の中間部3b内で冷却された流動体Aが第二の貯留タンク2内に流入する。   (7) As shown in FIG. 9, the supply of pressurized air from the pressurized air supply pipe 20 to the second storage tank 2 is shut off, and the on-off valve 10 on the most downstream side of the transfer pipe 3 is opened. Thereby, the fluid A cooled in the intermediate part 3 b of the transfer pipe 3 flows into the second storage tank 2.

(8)冷却された流動体Aが第二の貯留タンク2内に流入すると、図10に示すように、作業者により拘束具13が拡張管5bの外側へと引かれる。拘束具13は拡張管5bの貫通孔17から抜き取ってもよいし、貫通孔17内に残してもよい。貫通孔17内に残すようにすると、圧空の漏れ出しを防止することができる。このように拘束具13を管外に引いて拘束具13の先端部をピグ4の環状溝4aから離脱させると、ピグ4は待機室5内での拘束を解かれる。   (8) When the cooled fluid A flows into the second storage tank 2, as shown in FIG. 10, the operator pulls the restraining tool 13 to the outside of the expansion pipe 5b. The restraining tool 13 may be extracted from the through hole 17 of the expansion pipe 5 b or may remain in the through hole 17. If it is left in the through hole 17, leakage of compressed air can be prevented. Thus, when the restraint 13 is pulled out of the pipe and the tip of the restraint 13 is detached from the annular groove 4 a of the pig 4, the pig 4 is released from the restraint in the standby chamber 5.

(9)図10に示すように、移送管3の流入部3aが中間部3bに合流する箇所に設けられた開閉弁8が閉じられると、待機室5内に供給される圧空によりピグ4は待機室5から移送管3の中間部3b内に押し出され、中間部3b内を下流側に移動する。
ピグ4は移送管3の中間部3b内を移動しつつ、移送管3の内壁面に付着し残留した流動体Aを掻き落とし、掻き落とした流動体Aを流入部3cから第二の貯留タンク2内に押し込む。
(9) As shown in FIG. 10, when the on-off valve 8 provided at the location where the inflow portion 3a of the transfer pipe 3 joins the intermediate portion 3b is closed, the pig 4 is moved by the pressurized air supplied into the standby chamber 5. It is pushed out from the waiting chamber 5 into the intermediate part 3b of the transfer pipe 3, and moves in the intermediate part 3b to the downstream side.
The pig 4 moves in the intermediate portion 3b of the transfer pipe 3, scrapes off the remaining fluid A attached to the inner wall surface of the transfer pipe 3, and removes the scraped fluid A from the inflow portion 3c to the second storage tank. Push into 2.

(10)やがてピグ4は、図11に示すように行止室6内に入り込み、端板6aに当たって停止する。これにより、移送管3の中間部3b内に残留したすべての流動体Aの回収が完了し、また第一の貯留タンク1から第二の貯留タンク2への流動体Aの移送が完了する。   (10) Eventually, the pig 4 enters the closing chamber 6 as shown in FIG. 11, and hits the end plate 6a and stops. Thereby, the recovery of all the fluid A remaining in the intermediate portion 3b of the transfer pipe 3 is completed, and the transfer of the fluid A from the first storage tank 1 to the second storage tank 2 is completed.

(11)第二の貯留タンク2には、図示しない導管が接続され、第二の貯留タンク2内の流動体Aはこの導管から図示しない無菌充填機に送られ、袋、容器等に充填され包装される。   (11) A conduit (not shown) is connected to the second storage tank 2, and the fluid A in the second storage tank 2 is sent from this conduit to an aseptic filling machine (not shown) and filled into bags, containers, and the like. Packaged.

(12)行止室6内に入ったピグ4は、例えば端板6aに予め穿設されプラグで閉じられた孔から作業者によって操作棒が挿入されることにより、待機室5内へ押し戻される。或いは端板6aの孔から圧縮空気を注入して押し戻すことも可能である。
待機室5内に復帰したピグ4は、図1及び図2に示すように、拘束具13により再び待機室5内に拘束される。
(12) The pig 4 that has entered the closing chamber 6 is pushed back into the waiting chamber 5 by inserting an operating rod by an operator through a hole that has been previously drilled in the end plate 6a and closed with a plug, for example. Alternatively, it is possible to inject compressed air from the hole of the end plate 6a and push it back.
As shown in FIGS. 1 and 2, the pig 4 that has returned to the waiting chamber 5 is again restrained in the waiting chamber 5 by the restraining tool 13.

本発明は以上説明したように構成されるが、上記実施の形態に限定されるものではなく、本発明の要旨の範囲内において種々変更可能である。   Although the present invention is configured as described above, the present invention is not limited to the above-described embodiment, and various modifications can be made within the scope of the gist of the present invention.

本発明に係る流動体加熱殺菌装置の概念図である。It is a conceptual diagram of the fluid heating sterilizer which concerns on this invention. 図1中、ピグが待機する箇所の拡大図である。FIG. 2 is an enlarged view of a place where a pig waits in FIG. 1. ピグの一例の斜視図である。It is a perspective view of an example of a pig. 流動体加熱殺菌装置の内部を殺菌する工程を示す説明図である。It is explanatory drawing which shows the process of disinfecting the inside of a fluid heating sterilizer. 流動体加熱殺菌装置内に流動体を供給する工程を示す説明図である。It is explanatory drawing which shows the process of supplying a fluid into a fluid heating sterilizer. 流動体加熱殺菌装置内で流動体を加熱殺菌する工程を示す説明図である。It is explanatory drawing which shows the process of heat-sterilizing a fluid within a fluid-heat-sterilization apparatus. 流動体加熱殺菌装置内で流動体を第一の貯留タンクから移送管内へと送り出す工程を示す説明図である。It is explanatory drawing which shows the process of sending out a fluid from a 1st storage tank in a transfer pipe | tube in a fluid heating sterilizer. 流動体加熱殺菌装置内で流動体を冷却する工程を示す説明図である。It is explanatory drawing which shows the process of cooling a fluid within a fluid heating sterilizer. 流動体加熱殺菌装置内で流動体を移送管内から第二の貯留タンクへと送り出す工程を示す説明図である。It is explanatory drawing which shows the process of sending out a fluid from the inside of a transfer pipe to a 2nd storage tank within a fluid heating sterilizer. 流動体加熱殺菌装置内でピグを移送管中下流側に移動させる工程を示す説明図である。It is explanatory drawing which shows the process of moving a pig to the downstream in a transfer pipe within a fluid heating sterilizer. 流動体加熱殺菌装置内でピグが行止室へ到達し流動体の回収が完了した状態を示す説明図である。It is explanatory drawing which shows the state which the pig | pig reached | attained a deadline chamber and the collection | recovery of the fluid was completed within the fluid heat sterilizer.

A…流動体
1…第一の貯留タンク
2…第二の貯留タンク
3…移送管
4…ピグ
5…待機室
6…行止室
9…蒸気供給管
10…開閉弁
18…圧空供給管
19…冷却用ジャケット
DESCRIPTION OF SYMBOLS A ... Fluid 1 ... 1st storage tank 2 ... 2nd storage tank 3 ... Transfer pipe 4 ... Pig 5 ... Standby chamber 6 ... Closure chamber 9 ... Steam supply pipe 10 ... On-off valve 18 ... Pressure air supply pipe 19 ... Cooling Jacket

Claims (3)

第一の貯留タンクから第二の貯留タンクへ移送管を通して流動体を送り、上流側の所定箇所で加熱殺菌手段により流動体を加熱殺菌処理し、下流側の所定箇所で冷却手段により流動体を冷却するようにした流動体加熱殺菌装置において、上記第一の貯留タンクに上記加熱殺菌手段を設け、上記移送管における上記第一の貯留タンクに通じる上流側と上記第二の貯留タンクに通じる下流側に各々開閉弁を設け、上記移送管の上記両開閉弁で挟まれた中間部に上記冷却手段を設け、流動体を上記第一の貯留タンク内で上記加熱殺菌手段により所定の温度まで加熱しつつ、かつ、圧空供給手段から上記第一の貯留タンクに供給される無菌の圧空により加圧しつつ殺菌した後、上記上流側の開閉弁を開けて、圧空供給手段から上記第一の貯留タンクに供給される無菌の圧空により、上記第一の貯留タンク内の流動体を上記下流側の閉じた開閉弁側へと送って上記移送管の中間部内に溜め、この中間部内の流動体を上記冷却手段により冷却し、しかる後上記下流側の開閉弁を開けて冷却された流動体を上記第二の貯留タンクに送るようにしたことを特徴とする流動体加熱殺菌装置。 The fluid is sent from the first storage tank to the second storage tank through the transfer pipe, the fluid is heat sterilized by the heat sterilization means at a predetermined location on the upstream side, and the fluid is cooled by the cooling means at a predetermined location on the downstream side. In the fluid heat sterilization apparatus to be cooled, the heat sterilization means is provided in the first storage tank, and the upstream side of the transfer pipe that leads to the first storage tank and the downstream that leads to the second storage tank. An opening / closing valve is provided on each side, the cooling means is provided in an intermediate portion sandwiched between the both opening / closing valves of the transfer pipe, and the fluid is heated to a predetermined temperature by the heating sterilization means in the first storage tank. In addition , after sterilization while being pressurized with aseptic compressed air supplied from the compressed air supply means to the first storage tank, the upstream opening / closing valve is opened, and the first storage tank is opened from the compressed air supply means. In The pressure of the sterile to be fed, the fluid of the first reservoir tank sent to off valve side is closed in the downstream reservoir into the middle portion of the transfer tube, the cooling fluid in the intermediate portion A fluid heating sterilizer characterized in that the fluid is cooled by means and then the downstream on-off valve is opened to send the cooled fluid to the second storage tank. 請求項1に記載の流動体加熱殺菌装置において、移送管の下流側を開閉弁で遮蔽し、上流側から圧空供給手段により無菌の圧空を供給して、流動体を移送管の冷却手段の位置に保持しつつ冷却するようにしたことを特徴とする流動体加熱殺菌装置。 The fluid heating sterilization apparatus according to claim 1 , wherein the downstream side of the transfer pipe is shielded by an on-off valve, and sterile compressed air is supplied from the upstream side by the compressed air supply means, so that the fluid is positioned at the cooling means of the transfer pipe. A fluid heating sterilizer characterized in that it is cooled while being held in place. 請求項1に記載の流動体加熱殺菌装置において、移送管内に移動可能に挿入されたピグと、移送管における冷却手段よりも上流側に設けられたピグの待機室と、移送管における冷却手段よりも下流側に設けられたピグの行止室とを備えたことを特徴とする流動体加熱殺菌装置。   In the fluid heat sterilization apparatus according to claim 1, a pig inserted movably in the transfer pipe, a waiting room for a pig provided upstream of the cooling means in the transfer pipe, and a cooling means in the transfer pipe A fluid heating sterilizer comprising a pig closing chamber provided on the downstream side.
JP2006225104A 2006-08-22 2006-08-22 Fluid heat sterilizer Expired - Fee Related JP4730251B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006225104A JP4730251B2 (en) 2006-08-22 2006-08-22 Fluid heat sterilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006225104A JP4730251B2 (en) 2006-08-22 2006-08-22 Fluid heat sterilizer

Publications (2)

Publication Number Publication Date
JP2008048616A JP2008048616A (en) 2008-03-06
JP4730251B2 true JP4730251B2 (en) 2011-07-20

Family

ID=39233248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006225104A Expired - Fee Related JP4730251B2 (en) 2006-08-22 2006-08-22 Fluid heat sterilizer

Country Status (1)

Country Link
JP (1) JP4730251B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5838720B2 (en) * 2011-10-25 2016-01-06 大日本印刷株式会社 Sterilization treatment line and purification method thereof
KR101420008B1 (en) 2012-08-21 2014-07-17 주식회사 한국가스기술공사 A cleaning apparatus for pipe
CA2933771C (en) * 2014-01-06 2020-07-07 Uresh Ag Aseptic pipeline pig with identification means
JP5659311B1 (en) * 2014-02-15 2015-01-28 大森機械工業株式会社 Pig cleaning device

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59216574A (en) * 1983-05-20 1984-12-06 Sanyo Electric Co Ltd Sterilization apparatus with microwave heating
JPH09126399A (en) * 1995-10-31 1997-05-13 Asia Kako Kk Recovery device for fluid in pipe of fluid transfer piping
JPH09192620A (en) * 1996-01-19 1997-07-29 Tsuuhen Haagen Japan:Kk Pig cleaning method and pig cleaner
JPH09198141A (en) * 1996-01-19 1997-07-31 Tsuuhen Haagen Japan:Kk Pig and pig position detection method and controller
JPH11155500A (en) * 1997-11-21 1999-06-15 Frontier Engineering:Kk Production of sealed processed food and device therefor
JP2001072189A (en) * 1999-09-03 2001-03-21 Shibuya Kogyo Co Ltd Beverage producing line
JP2005040742A (en) * 2003-07-24 2005-02-17 Sadakuni Daiku Automatic transportation pipe washing apparatus using pig
JP2005087822A (en) * 2003-09-16 2005-04-07 Maruho Co Ltd Washing method for pipe for transferring ointment, recovery method for ointment and continuous manufacturing method for ointment

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59216574A (en) * 1983-05-20 1984-12-06 Sanyo Electric Co Ltd Sterilization apparatus with microwave heating
JPH09126399A (en) * 1995-10-31 1997-05-13 Asia Kako Kk Recovery device for fluid in pipe of fluid transfer piping
JPH09192620A (en) * 1996-01-19 1997-07-29 Tsuuhen Haagen Japan:Kk Pig cleaning method and pig cleaner
JPH09198141A (en) * 1996-01-19 1997-07-31 Tsuuhen Haagen Japan:Kk Pig and pig position detection method and controller
JPH11155500A (en) * 1997-11-21 1999-06-15 Frontier Engineering:Kk Production of sealed processed food and device therefor
JP2001072189A (en) * 1999-09-03 2001-03-21 Shibuya Kogyo Co Ltd Beverage producing line
JP2005040742A (en) * 2003-07-24 2005-02-17 Sadakuni Daiku Automatic transportation pipe washing apparatus using pig
JP2005087822A (en) * 2003-09-16 2005-04-07 Maruho Co Ltd Washing method for pipe for transferring ointment, recovery method for ointment and continuous manufacturing method for ointment

Also Published As

Publication number Publication date
JP2008048616A (en) 2008-03-06

Similar Documents

Publication Publication Date Title
JP2528856B2 (en) Method and mechanism for sterilizing packaging machines
US4999978A (en) Aseptic filling apparatus
CN103917453B (en) Beverage fill method and device thereof
JP4730251B2 (en) Fluid heat sterilizer
CN101588781A (en) Fill and sealing contain medical use liquid container closure construction and fill and the method for closed container with medical use liquid
JP7434749B2 (en) Sterilization method and sterilization device in sterile water supply piping of aseptic filling machine
US20080152537A1 (en) Sterilization System
JPH06171618A (en) Method of processing and packing liquid food
MX2007009214A (en) An integrated fitment for aseptic packaging.
JP2009533659A (en) Fixed amount collection device
KR100818184B1 (en) vessel and packing structure of vinyl pack of apparatus for manufacturing bean curd
JP5153786B2 (en) Apparatus and method for refilling powders and solids while preventing contamination, and novel use of weldable and peelable tubular film
JP2003325645A (en) Sterilization method for pouch with spout and sterile filling apparatus
JP4830716B2 (en) Fluid transfer device
JPH0576328A (en) High-pressure sterilization apparatus having temperature-control function
JP6583398B2 (en) Aseptic filling machine and aseptic filling method
KR20150093074A (en) Production of beverage having high-temperature short time pasteurization apparatus for liquid
JP4091168B2 (en) Bag-in-box with heat-resistant valve
JPS59194745A (en) Sterilizing and filling system capable of continuously treating liouid
US20060210685A1 (en) Adiabatic and aseptic food packaging method and apparatus
JP3162032B2 (en) Sterilization method of food etc.
JP2005280717A (en) Manufacturing method for package and packaging apparatus
JP2006188251A (en) Method and device for filling product for bag container
JP2721217B2 (en) Aseptic packaging container and filling method
JP3676057B2 (en) Cooking equipment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20090604

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100917

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100928

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20101117

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20101207

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20110222

A911 Transfer of reconsideration by examiner before appeal (zenchi)

Free format text: JAPANESE INTERMEDIATE CODE: A911

Effective date: 20110302

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20110322

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20110404

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

Free format text: PAYMENT UNTIL: 20140428

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees