JPH0576328A - High-pressure sterilizer with temperature control function - Google Patents
High-pressure sterilizer with temperature control functionInfo
- Publication number
- JPH0576328A JPH0576328A JP23797091A JP23797091A JPH0576328A JP H0576328 A JPH0576328 A JP H0576328A JP 23797091 A JP23797091 A JP 23797091A JP 23797091 A JP23797091 A JP 23797091A JP H0576328 A JPH0576328 A JP H0576328A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- supply
- food
- valve
- pipeline
- 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.)
- Pending
Links
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Abstract
(57)【要約】
【構成】耐圧円筒(11)と耐圧上蓋(12)と耐圧底蓋(13)と
で構成した高圧処理室(10)と、高圧処理室(10)内を加圧
する加圧装置(20)と、高圧処理室(10)内に通じる食品類
供給管路(39)と食品類排出管路(49)と空気給排気管路(5
9)とから成る高圧殺菌処理装置であって、食品類供給管
路(39)と食品類排出管路(49)との、どちらか一方に又は
両方に加熱装置(30)を設けたことによって、また前記の
加熱装置(30)の下流側であって、前記の食品類供給管路
(39)と食品類排出管路(49)との、どちらか一方に又は両
方に冷却装置(40)を設けたことによって、
【効果】包装容器に充填する前の液状食品類などの、常
温又は加温での2000気圧以上の高圧殺菌処理の前工
程又は後工程で、100℃以下の加熱殺菌処理を連続し
て併用実施できる温度調節機能付の高圧殺菌処理装置で
ある。
(57) [Summary] [Structure] A high-pressure processing chamber (10) composed of a pressure-resistant cylinder (11), a pressure-resistant upper lid (12), and a pressure-resistant bottom lid (13), and a pressure-applying chamber. The pressure device (20), the food supply pipe (39), the food discharge pipe (49), and the air supply / exhaust pipe (5) that communicate with the high-pressure processing chamber (10).
A high-pressure sterilization apparatus comprising 9) and a food supply pipeline (39) and a food discharge pipeline (49), by providing a heating device (30) on either one or both. Further, the foodstuffs supply pipeline, which is downstream of the heating device (30),
By providing the cooling device (40) on either or both of the (39) and the food product discharge pipeline (49), [Effect] At room temperature, such as liquid food products before being filled in the packaging container. Alternatively, it is a high-pressure sterilization apparatus with a temperature control function that can continuously perform a combined heat sterilization treatment at 100 ° C. or lower in a pre-process or a post-process of a high-pressure sterilization process at a heating temperature of 2000 atm or higher.
Description
【0001】[0001]
【産業上の利用分野】本発明は、包装容器に充填する前
の液状食品類などを、連続的に2000気圧以上に加圧
して殺菌処理する温度調節機能付の高圧殺菌処理装置に
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 sterilization apparatus having a temperature control function for continuously sterilizing liquid foods or the like before they are filled in a packaging container by pressurizing them to 2000 atm or more. ..
【0002】[0002]
【従来の技術】ジュースやジャムや酒類などの液状食品
類などを2000気圧以上に加圧して殺菌処理する、栄
養成分を破壊し味覚を劣化させることがない高圧殺菌処
理技術が開発されている。また最近は、加熱や冷凍など
を併用して2000気圧以上に加圧して殺菌処理する、
高圧殺菌処理の効率を向上させた温度調節機能付の高圧
殺菌処理技術が開発されており、例えば特開平 2-89598
号公報では、高圧処理室内に加熱手段を設けて、加熱と
加圧とを併用できる高圧殺菌処理装置が開示されてい
て、また例えば特開平2-182157号公報では、循環させた
圧力媒体を加熱又は冷却することによって、加熱又は冷
凍と加圧とを併用できる高圧殺菌処理装置が開示されて
いる。2. Description of the Related Art A high-pressure sterilization technique has been developed in which liquid foods such as juices, jams and alcoholic beverages are sterilized by pressurizing them to 2000 atmospheric pressure or more, which does not destroy nutritional components and deteriorate taste. In addition, recently, sterilization treatment is carried out by pressurizing to 2000 atm or more by using heating and freezing together.
High-pressure sterilization technology with a temperature control function that improves the efficiency of high-pressure sterilization has been developed.
Japanese Patent Publication No. 2-182157 discloses a high-pressure sterilization treatment device in which heating means is provided in the high-pressure treatment chamber and heating and pressurization can be used in combination. Further, for example, in JP-A-2-182157, heating a circulated pressure medium is disclosed. Alternatively, a high-pressure sterilization treatment device is disclosed which can use both heating or freezing and pressurization by cooling.
【0003】また、本願出願人に係る特願平2-207073号
では、2000気圧以上の高圧殺菌処理の前工程又は後
工程で100℃以下の加熱殺菌処理を併用して、頑強な
細菌胞子などを殺菌処理する高圧殺菌処理技術を開発し
て出願したものである。Further, in Japanese Patent Application No. 2-207073 relating to the applicant of the present application, a robust bacterial spore, etc. is obtained by using a heat sterilization treatment at 100 ° C. or lower in a step before or after a high pressure sterilization treatment of 2000 atm or more. It was developed and applied for high-pressure sterilization technology for sterilizing
【0004】[0004]
【発明が解決しようとする課題】本発明は、前記の本願
出願人に係る特願平2-207073号の発明を実施するに当た
って、包装容器に充填する前の液状食品類などの、20
00気圧以上の高圧殺菌処理の前工程又は後工程で、1
00℃以下の加熱殺菌処理を連続して併用実施したいと
の要請があって、開発した温度調節機能付の高圧殺菌処
理装置である。すなわち、前記の特開平 2-89598号公報
や特開平2-182157号公報などの高圧殺菌処理装置におい
ては、加熱などを併用した高圧殺菌処理は出来るもの
の、前工程又は後工程での加熱殺菌処理を連続して併用
実施するには不向きであって、2倍の処理時間がかかる
ことや別に加熱殺菌処理装置が必要であることなどの問
題があった。さらに、前記の従来の高圧殺菌処理装置
は、原則として、包装容器に充填密封した液状食品類な
どを、間欠的に高圧殺菌処理するものであった。In carrying out the invention of Japanese Patent Application No. 2-207073 relating to the applicant of the present invention, the present invention provides a liquid food product, such as liquid foods, which is not filled in a packaging container.
In the pre-process or post-process of high-pressure sterilization treatment of at least 00 atm, 1
It is a high-pressure sterilization treatment device with a temperature control function that was developed in response to a request to continuously perform heat sterilization treatment at 00 ° C or less. That is, in the high-pressure sterilization apparatus such as the above-mentioned JP-A-2-89598 and JP-A-2-182157, it is possible to perform high-pressure sterilization treatment in combination with heating, but heat sterilization treatment in the pre-process or post-process. Is not suitable for continuous continuous use, and there are problems such as double processing time and the need for a separate heat sterilization processing device. Further, in principle, the above-mentioned conventional high-pressure sterilization treatment apparatus intermittently high-pressure sterilizes the liquid foods and the like filled and sealed in the packaging container.
【0005】[0005]
【課題を解決するための手段】本発明の温度調節機能付
の高圧殺菌処理装置は、図1に示すように、耐圧円筒(1
1)と耐圧上蓋(12)と耐圧底蓋(13)とで構成した高圧処理
室(10)と、高圧処理室(10)内を加圧する加圧装置(20)
と、高圧処理室(10)内に通じる食品類供給管路(39)と食
品類排出管路(49)と空気給排気管路(59)とから成る高圧
殺菌処理装置であって、食品類供給管路(39)と食品類排
出管路(49)との、どちらか一方に又は両方に加熱装置(3
0)を設けたことによって、また、前記の加熱装置(30)の
下流側であって、前記の食品類供給管路(39)と食品類排
出管路(49)との、どちらか一方に又は両方に冷却装置(4
0)を設けたことによって、包装容器に充填する前の液状
食品類などの、2000気圧以上の高圧殺菌処理の前工
程又は後工程で、100℃以下の加熱殺菌処理を連続し
て併用実施したいとの要請に応えたものである。As shown in FIG. 1, a high-pressure sterilization apparatus having a temperature control function according to the present invention has a pressure-resistant cylinder (1
1), a pressure resistant top lid (12) and a pressure resistant bottom lid (13), a high pressure processing chamber (10), and a pressure device (20) for pressurizing the inside of the high pressure processing chamber (10).
And a high-pressure sterilization apparatus comprising a food supply pipe (39), a food discharge pipe (49), and an air supply / exhaust pipe (59) that communicate with the high-pressure processing chamber (10). A heating device (3) is provided on either or both of the supply line (39) and the food discharge line (49).
By providing the (0), also on the downstream side of the heating device (30), in one of the food supply pipeline (39) and the food discharge pipeline (49), Or both with cooling devices (4
By providing (0), it is desired to continuously perform heat sterilization treatment at 100 ° C. or lower in a pre-process or a post-process of high-pressure sterilization treatment of 2000 atm or more for liquid foods or the like before being filled in a packaging container. In response to the request.
【0006】[0006]
【実施例】図1は、本発明の実施例における、温度調節
機能付の高圧殺菌処理装置の構成を示す説明図である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an explanatory view showing the construction of a high-pressure sterilization apparatus with a temperature adjusting function in an embodiment of the present invention.
【0007】本実施例の高圧処理室(10)については、厚
肉金属製の耐圧円筒(11)と耐圧上蓋(12)と耐圧底蓋(13)
とで構成したものであって、2000〜7000気圧の
加圧に耐える強度と液密封性を有しており、内容積は約
6.0L である。耐圧上蓋(12)には、後述するベローズ(2
1)と加圧水給排水管路(29)と空気給排気管路(59)とが、
耐圧底蓋(13)には、食品類供給管路(39)と食品類排出管
路(49)とが、それぞれ高圧処理室(10)内に通じるように
耐圧液密封性を有して設けてある。なお、図1には1個
の高圧処理室(10)を図示したが、高圧処理室(10)のみを
複数個設置して( 後述する加圧装置などは共用にして
)、順にタイミングをずらして加圧することによって、
包装容器に充填する前の液状食品類などを、連続的に高
圧殺菌処理することが出来るものである。In the high pressure processing chamber (10) of this embodiment, a pressure resistant cylinder (11), a pressure resistant upper lid (12) and a pressure resistant bottom lid (13) are made of thick metal.
It has the strength to withstand pressurization of 2000 to 7000 atm and the liquid tightness, and the internal volume is about 6.0 L. The pressure resistant lid (12) has a bellows (2
1) and the pressurized water supply / drainage line (29) and the air supply / exhaust line (59)
The pressure-resistant bottom cover (13) is provided with a pressure-resistant liquid-tight seal so that the food supply line (39) and the food discharge line (49) communicate with the high-pressure processing chamber (10). There is. In addition, although one high pressure processing chamber (10) is illustrated in FIG. 1, only a plurality of high pressure processing chambers (10) are installed (a pressurizing device described later is commonly used.
), By shifting the timing in order and applying pressure,
Liquid foods and the like before being filled in a packaging container can be continuously subjected to high-pressure sterilization treatment.
【0008】本実施例の加圧装置(20)については、高圧
処理室(10)内で上下方向に伸縮して高圧処理室(10)を加
圧するベローズ( 21, 蛇腹式加圧器, テフロン樹脂製 )
と、超多段タービンポンプなどの加圧ポンプ(22)と、給
水タンク(23)と加圧水給排水管路(29)と耐圧弁( 24,25,
26,27)とで構成したものであって、加圧水であるイオン
交換水を2000〜7000気圧に加圧する能力と耐圧
液密封性を有しており、加圧水の給水能力は約0.6L/分
である。The pressurizing device (20) of this embodiment is a bellows (21, bellows type pressurizer, Teflon resin) which vertically expands and contracts in the high pressure processing chamber (10) to pressurize the high pressure processing chamber (10). (Made)
A pressure pump (22) such as an ultra multi-stage turbine pump, a water tank (23), a pressurized water supply / drainage line (29), and a pressure resistant valve (24, 25,
26, 27), and has the ability to pressurize ion-exchanged water, which is pressurized water, to 2000 to 7000 atm and the pressure-resistant liquid sealing property, and the pressurized water supply capacity is about 0.6 L / min. Is.
【0009】また、本実施例のベロース(21)内への加圧
水の給水方法については、耐圧弁(24)を開放して加圧ポ
ンプ(22)を稼動させた状態で、耐圧弁(25)と耐圧弁(26)
とを開放して給水するものであって、耐圧弁(25)を閉止
して耐圧弁(27)を開放することによって、ベローズ(21)
内の加圧水を給水タンク(23)へ排水するものである。こ
の場合に、2000〜7000気圧に達する加圧水の安
全性と誤作動防止のために、図示していない適宜の圧調
弁や流量調節弁やインターロック機構などが設けてあ
る。なお、本実施例においては、4個の高圧処理室(10)
を設置したものであって、耐圧弁(24)と耐圧弁(25)との
間に分岐管路(28)を設けて、図示していない他の3個の
高圧処理室(10)についても、分岐管路(28)から給水タン
ク(23)までの加圧水給排水管路(29)及び耐圧弁(25,26,2
7)をそれぞれ設けたものである。Regarding the method of supplying pressurized water into the bellows (21) of this embodiment, the pressure resistant valve (25) is opened with the pressure resistant valve (24) open and the pressure pump (22) is operated. With pressure valve (26)
To open the pressure supply valve (25) and open the pressure resistance valve (27) to open the bellows (21).
The pressurized water inside is drained to the water supply tank (23). In this case, for the safety of the pressurized water reaching 2000 to 7000 atm and the prevention of malfunction, an appropriate pressure regulating valve, flow rate regulating valve, interlock mechanism, etc., which are not shown, are provided. In this embodiment, four high pressure processing chambers (10)
In addition, a branch pipe (28) is provided between the pressure resistant valve (24) and the pressure resistant valve (25), and the other three high pressure processing chambers (10) not shown are also provided. , The pressurized water supply / drainage line (29) from the branch line (28) to the water supply tank (23) and the pressure resistant valve (25, 26, 2)
7) are provided respectively.
【0010】本実施例の食品類供給管路(39)について
は、液状食品類などに含有する固形物の性状に適合した
プランジャーポンプなどの供給ポンプ(31)と、後述する
加熱装置(30)及び冷却装置(40)と、液状食品類などの供
給ホッパー(32)と食品類供給管路(39)と供給弁( 33,34)
と逆止弁(35)とで構成したものであって、供給弁(33)を
開放して供給ポンプ(31)を稼動させた状態で供給弁(34)
を開放して、高圧殺菌処理前の液状食品類などを逆止弁
(35)を経由して高圧処理室(10)内へ供給するものであっ
て、液状食品類などの供給能力は約6.0L/分である。Regarding the food supply pipe (39) of this embodiment, a supply pump (31) such as a plunger pump suitable for the properties of solids contained in liquid foods and a heating device (30) described later. ) And a cooling device (40), a supply hopper (32) for liquid foods, a food supply line (39), and a supply valve (33, 34)
And the check valve (35), the supply valve (34) with the supply valve (33) opened and the supply pump (31) operating.
To open the check valve for liquid foods, etc. before high pressure sterilization.
It is to be supplied into the high-pressure processing chamber (10) via (35), and the supply capacity for liquid foods is about 6.0 L / min.
【0011】本実施例の食品類排出管路(49)について
は、液状食品類などに含有する固形物の性状に適合した
プランジャーポンプなどの搬送ポンプ(41)と、後述する
加熱装置(30)及び冷却装置(40)と、圧調弁付の無菌空気
管(43)と殺菌清掃用の水蒸気管(44)とを有する液状食品
類などのサージタンク(42)と、食品類排出管路(49)と排
出弁( 45,46)と逆止弁(47)とで構成したものであって、
排出弁(45)を開放して後述する空気給排気管路(59)の空
気圧によって、高圧殺菌処理後の液状食品類などを逆止
弁(47)を経由してサージタンク(42)内へ排出した後に、
排出弁(46)を開放して搬送ポンプ(41)を稼動させて、次
工程の無菌包装充填機などへ搬送するものである。As for the food discharge pipe (49) of this embodiment, a transport pump (41) such as a plunger pump suitable for the properties of solids contained in liquid foods and a heating device (30) described later. ) And a cooling device (40), a sterile tank (42) for liquid foods and the like having a sterile air pipe (43) with a pressure regulating valve and a steam pipe (44) for sterilization cleaning, and a food product discharge pipeline. (49), a discharge valve (45, 46) and a check valve (47),
By opening the discharge valve (45) and using the air pressure in the air supply / exhaust pipe line (59), which will be described later, liquid foods, etc. after high-pressure sterilization are passed into the surge tank (42) via the check valve (47). After discharging
The discharge valve (46) is opened and the transfer pump (41) is operated to transfer to the aseptic packaging and filling machine in the next step.
【0012】本実施例の空気給排気管路(59)について
は、ペパフィルターなどの除菌フィルター(51)を有する
中圧の空気圧縮機(50)と、殺菌清掃用の水蒸気管(52)
と、空気給排気管路(59)と空気弁(53,54,55,56,57)と逆
止弁(58)とで構成したものであって、高圧殺菌処理前の
液状食品類などを高圧処理室(10)内へ供給する場合は、
空気弁(53)と空気弁(54)を開放して、高圧処理室(10)内
の無菌空気を逆止弁(58)を経由して排気するものであっ
て、高圧殺菌処理後の液状食品類などを高圧処理室(10)
内から排出する場合は、空気弁(56)を開放して空気圧縮
機(50)を稼動させた状態で空気弁(53)と空気弁(55)を開
放して、除菌フィルター(51)を経由した約1.0気圧の中
圧の無菌空気を高圧処理室(10)内に給気して、その空気
圧によって液状食品類などをサージタンク(42)内へ排出
して、同時にベローズ(21)内にわずかに残存した加圧水
を給水タンク(23)へ排水するものである。なお、この中
圧の無菌空気の一部を減圧( 図示せず )してサージタン
ク(42)の無菌空気管(43)に給気して、サージタンク(42)
内のヘッドスペースを常時無菌状態に保持しているもの
である。Regarding the air supply / exhaust pipe line (59) of the present embodiment, a medium pressure air compressor (50) having a sterilizing filter (51) such as a pepper filter, and a steam pipe (52) for sterilizing and cleaning.
And an air supply / exhaust pipe line (59), an air valve (53, 54, 55, 56, 57) and a check valve (58), which can be used for liquid foods before high pressure sterilization. When supplying into the high pressure processing chamber (10),
The air valve (53) and the air valve (54) are opened, and the sterile air in the high-pressure processing chamber (10) is exhausted via the check valve (58). High pressure processing room for food etc. (10)
When discharging from the inside, open the air valve (56) and operate the air compressor (50), open the air valve (53) and the air valve (55), and remove the sterilization filter (51). Aseptic air of about 1.0 atm under pressure is supplied into the high-pressure processing chamber (10) via the air, and the liquid pressure is discharged into the surge tank (42) by the air pressure, and at the same time, the bellows ( The pressurized water that slightly remains inside 21) is discharged to the water supply tank (23). In addition, a part of this medium-pressure sterile air is depressurized (not shown) to supply the sterile air pipe (43) of the surge tank (42) to the surge tank (42).
The inner headspace is always kept sterile.
【0013】また、本実施例の殺菌清掃用の水蒸気管(5
2)については、高圧殺菌処理作業の開始前又は終了時
に、高圧処理室(10)内とその下流側の全ての装置及び管
路を殺菌又は清掃するものであって、空気弁(53)と空気
弁(55)と空気弁(57)を開放して、水蒸気管(52)から約
2.0気圧の飽和水蒸気を供給して、高圧処理室(10)内な
どを加熱殺菌して、同様に水蒸気管(52)から約2.0気圧
の無菌水を供給して、わずかに残存する液状食品類など
を水洗清掃するものである。なお、同様の目的で、サー
ジタンク(42)に殺菌清掃用の水蒸気管(44)を設けたもの
である。Further, the steam pipe (5
Regarding 2), before or at the end of the high-pressure sterilization process, the inside of the high-pressure process chamber (10) and all downstream devices and pipes are sterilized or cleaned, and the air valve (53) and Open the air valve (55) and the air valve (57), supply saturated steam of about 2.0 atm from the steam pipe (52), heat sterilize the inside of the high pressure processing chamber (10), etc. Sterile water of about 2.0 atm is supplied from the steam pipe (52) to the liquid foods and the like, which are slightly left behind, for cleaning. For the same purpose, the surge tank (42) is provided with a steam pipe (44) for sterilizing and cleaning.
【0014】なお、本実施例においては、前述した4個
の高圧処理室(10)に対応するために、前述の加圧装置(2
0)の場合と同様に、食品類供給管路(39)と食品類排出管
路(49)と空気給排気管路(59)とのそれぞれに、図1に示
す分岐管路(28)を設けたものであって、図示していない
他の3個の高圧処理室(10)についても、分岐管路(28)か
ら下流側の食品類供給管路(39)と供給弁(34)と逆止弁(3
5)とを、また分岐管路(28)から上流側の食品類排出管路
(49)と排出弁(45)と逆止弁(47)とを、さらに分岐管路(2
8)から下流側の空気給排気管路(59)と空気弁(53,54,55)
と逆止弁(58)とを、それぞれの高圧処理室(10)に対応さ
せて設けたものである。In this embodiment, in order to correspond to the above-mentioned four high pressure processing chambers (10), the above-mentioned pressurizing device (2
As in the case of (0), the branch pipeline (28) shown in FIG. 1 is provided to each of the food supply pipeline (39), the food discharge pipeline (49), and the air supply / exhaust pipeline (59). The other three high-pressure processing chambers (10), which are not shown, are provided with the foods supply pipeline (39) and the supply valve (34) downstream of the branch pipeline (28). Check valve (3
5) and the food discharge line upstream from the branch line (28)
(49), the discharge valve (45) and the check valve (47), and the branch pipe (2
8) Air supply / exhaust line (59) and air valves (53, 54, 55) downstream from
A check valve (58) and a check valve (58) are provided corresponding to each high-pressure processing chamber (10).
【0015】ここで、本実施例の高圧殺菌処理装置にお
ける、高圧殺菌処理作業の手順をまとめると下記のとお
りである。なお、手順終了後の弁類の閉止とポンプなど
の停止とについては記述を省略してある。 空気弁(53,55,57)と排出弁(45,46又は75) とを開放
して、水蒸気管(52)から飽和水蒸気を供給して、高圧処
理室(10)内とその下流側の全ての装置及び管路を加熱殺
菌する、この殺菌手順は約30分で終了する。 空気弁(53,55,56)と排出弁(45,46又は75) とを開放
して、空気圧縮機(50)を稼動させて無菌空気を給気し
て、高圧処理室(10)内とその下流側の全ての装置及び管
路を無菌空気で置換する、次に耐圧弁( 26,27)を開放し
て排出弁(45)を閉止して、高圧処理室(10)内の無菌空気
圧によって、ベローズ(21)内に残存した加圧水を排水す
る、この置換排水手順は約10分で終了する。 供給弁( 33,34)と空気弁( 53,54)とを開放して、供
給ポンプ(31)を稼動させて高圧殺菌処理前の液状食品類
などを高圧処理室(10)内へ供給して、同時に高圧処理室
(10)内の無菌空気を完全に排気する、この供給排気手順
は約2分で終了する。 供給弁(34)と排出弁(45)と空気弁(53)とを閉止して
耐圧弁(24,25,26)を開放して、加圧ポンプ(22)を稼動さ
せてベローズ(21)内へ加圧水を給水して、ベローズ(21)
を伸長させて高圧処理室(10)内を加圧する、この高圧殺
菌処理は約10〜20分で終了する。 排出弁(45)と耐圧弁( 26,27)と空気弁(53,55,56)と
を開放して、空気圧縮機(50)を稼動させて無菌空気を給
気して、高圧処理室(10)内の無菌空気圧によって、高圧
殺菌処理後の液状食品類などをサージタンク(42)内へ排
出して、同時にベローズ(21)内に残存した加圧水を排水
する、この排出排水手順は約3分で終了する。 からの、供給排気手順と高圧殺菌処理と排出排
水手順とを繰返す、この高圧殺菌処理作業の1サイクル
は約15〜25分で終了する。したがって、高圧処理室
(10)のみを複雑個設置して、例えば5分ずつタイミング
をずらしてからの手順を繰返すことによって、液状
食品類などを連続的に高圧殺菌処理することが出来る。 空気弁(53,55,57)と排出弁(45,46又は75) とを開放
して、水蒸気管(52)から無菌水を供給して、高圧処理室
(10)とその下流側の全ての装置及び管路にわずかに残存
する液状食品類などを水洗清掃する、この清掃手順は約
10分で終了する。Here, the procedure of the high-pressure sterilization operation in the high-pressure sterilization apparatus of this embodiment is summarized as follows. It should be noted that the description of closing the valves and stopping the pump etc. after the procedure is omitted. Open the air valve (53, 55, 57) and the exhaust valve (45, 46 or 75), supply saturated steam from the steam pipe (52), and supply the saturated steam to the high pressure processing chamber (10) and its downstream side. Heat sterilize all equipment and lines, the sterilization procedure is completed in about 30 minutes. Open the air valve (53, 55, 56) and the discharge valve (45, 46 or 75) and operate the air compressor (50) to supply aseptic air to the high pressure processing chamber (10). And replace all equipment and pipes on the downstream side with sterile air, then open the pressure resistant valves (26, 27) and close the discharge valve (45) to ensure that the high pressure processing chamber (10) is sterile. This displacement drainage procedure, which drains the pressurized water remaining in the bellows (21) by air pressure, is completed in about 10 minutes. Open the supply valves (33, 34) and air valves (53, 54) and operate the supply pump (31) to supply liquid foods, etc. before high-pressure sterilization into the high-pressure treatment chamber (10). At the same time, high pressure processing room
Completely evacuate the sterile air in (10). This supply / evacuation procedure is completed in about 2 minutes. The supply valve (34), the discharge valve (45), and the air valve (53) are closed, the pressure resistant valves (24, 25, 26) are opened, and the pressurizing pump (22) is operated to operate the bellows (21). Supply pressurized water into the bellows (21)
Is extended to pressurize the inside of the high-pressure treatment chamber (10), and this high-pressure sterilization treatment is completed in about 10 to 20 minutes. Open the exhaust valve (45), pressure resistant valve (26, 27) and air valve (53, 55, 56), operate the air compressor (50) and supply sterile air to the high pressure processing chamber. By aseptic air pressure in (10), liquid foods etc. after high-pressure sterilization are discharged into the surge tank (42), and at the same time, the pressurized water remaining in the bellows (21) is drained. It will be finished in 3 minutes. The cycle of the high-pressure sterilization operation, which is the repetition of the supply / exhaust procedure, the high-pressure sterilization procedure, and the discharge / drainage procedure, is completed in about 15 to 25 minutes. Therefore, the high pressure processing chamber
Liquid foods and the like can be continuously subjected to high-pressure sterilization treatment by arranging only (10) in a complicated manner and repeating the procedure after shifting the timing by 5 minutes, for example. Open the air valve (53, 55, 57) and the discharge valve (45, 46 or 75) and supply sterile water from the steam pipe (52) to the high pressure processing chamber.
(10) and all the downstream equipment and liquid foods slightly remaining in the pipelines are washed and cleaned, and this cleaning procedure is completed in about 10 minutes.
【0016】図2は、本発明の実施例の温度調節機能付
の高圧殺菌処理装置における、加熱装置(30)及び冷却装
置(40)の構成を示す説明図である。FIG. 2 is an explanatory view showing the constitution of the heating device (30) and the cooling device (40) in the high-pressure sterilization apparatus with temperature control function of the embodiment of the present invention.
【0017】本発明の食品類供給管路(39)と食品類排出
管路(49)との、どちらか一方に又は両方に加熱装置(30)
を設けたことについては、前記の本願出願人に係る特願
平2-207073号の発明を実施するために設けたものであっ
て、包装容器に充填する前の液状食品類などの、200
0気圧以上の高圧殺菌処理の前工程で100℃以下の加
熱殺菌処理を併用実施する場合は食品類供給管路(39)
に、また2000気圧以上の高圧殺菌処理の後工程で1
00℃以下の加熱殺菌処理を併用実施する場合は食品類
排出管路(49)に、さらに70℃以下の加温を併用した2
000気圧以上の高圧殺菌処理の後工程で100℃以下
の加熱殺菌処理を併用実施する場合は食品類供給管路(3
9)と食品類排出管路(49)の両方に、それぞれ必要に応じ
て設けるものである。A heating device (30) is provided in either or both of the food supply line (39) and the food discharge line (49) of the present invention.
Regarding the provision of the above, it is provided in order to carry out the invention of Japanese Patent Application No. 2-207073 relating to the applicant of the present application.
When performing a heat sterilization treatment at 100 ° C or less in the previous step of the high pressure sterilization treatment of 0 atm or more, the food supply pipeline (39)
In addition, in the post process of high pressure sterilization treatment of 2000 atm or more, 1
When heat sterilization treatment at a temperature of 00 ° C or less is also used, the foods discharge pipeline (49) is further heated at a temperature of 70 ° C or less.
When heat sterilization treatment at 100 ° C or less is also performed in the post-process of high-pressure sterilization treatment of 000 atm or more, the food supply pipeline (3
Both the 9) and the food discharge pipeline (49) are provided as needed.
【0018】また本発明の加熱装置(30)の下流側であっ
て、前記の食品類供給管路(39)と食品類排出管路(49)と
の、どちらか一方に又は両方に冷却装置(40)を設けたこ
とについては、常温での又は加温での2000気圧以上
の高圧殺菌処理の前工程で、100℃以下の加熱殺菌処
理を併用実施する場合は食品類供給管路(39)に、また後
工程が100℃以下の加熱殺菌処理又は70℃以下の加
温を併用した2000気圧以上の高圧殺菌処理であっ
て、次工程の無菌包装充填機などで冷却が必要な場合は
食品類排出管路(49)に、それぞれ必要に応じて設けるも
のである。Further, on the downstream side of the heating device (30) of the present invention, a cooling device is provided in either one or both of the food supply pipeline (39) and the food discharge pipeline (49). As for the provision of (40), in the case where heat sterilization treatment at 100 ° C or lower is also performed in the pre-process of high-pressure sterilization treatment at room temperature or at a temperature of 2000 atm or higher, the food supply pipeline (39 ), And if the subsequent step is a heat sterilization treatment of 100 ° C. or lower or a high pressure sterilization treatment of 2000 atm or higher in combination with heating of 70 ° C. or lower, and cooling is required in the aseptic packaging and filling machine in the next step, etc. The food discharge pipes (49) are provided as needed.
【0019】本実施例の加熱装置(30)及び冷却装置(40)
については、食品類供給管路(39)と食品類排出管路(49)
の両方に設けたものであって、図2に示すように、液状
食品類などに含有する固形物の性状に適合した2重多管
式熱交換器などの同一形状の予熱器(61)と加熱器(62)と
冷却器(63)と、内容積約18L の屈曲円筒式のホールデ
ィングパイプ(64)と、水蒸気管(65)と冷却水管(66)と加
熱冷却管路(67)と加熱冷却弁( 68,69,70,71,72,73,74,7
5,76,77)とで構成したものであって、前記のプランジャ
ーポンプなどの供給ポンプ(31)又は搬送ポンプ(41)を稼
動させて、高圧殺菌処理前又は高圧殺菌処理後の液状食
品類などを、加熱殺菌処理及び冷却処理するものであ
る。この場合に、加熱殺菌処理の温度や時間又は冷却処
理の温度などを制御するために、図示していない適宜の
温度検出器や流量調節弁やその制御機構などが設けてあ
る。なお、本実施例においては、2重多管式熱交換器を
予熱器(61)と加熱器(62)と冷却器(63)に用いたが、液状
食品類などの性状と液状食品類などに含有する固形物の
性状に適合した機器であれば、プレート式熱交換器や円
筒型掻面式熱交換器や電熱式又は電磁式加熱器などを、
制約なく用いることが出来るものである。The heating device (30) and cooling device (40) of this embodiment
For food supply pipelines (39) and food discharge pipelines (49)
As shown in FIG. 2, a preheater (61) having the same shape, such as a double multi-tube heat exchanger, which is suitable for the properties of solids contained in liquid foods, etc. Heater (62), cooler (63), bent cylindrical holding pipe (64) with internal volume of about 18L, steam pipe (65), cooling water pipe (66), heating cooling pipe line (67) and heating Cooling valve (68,69,70,71,72,73,74,7
5,76,77), which is operated by the feed pump (31) such as the plunger pump or the transport pump (41), and is a liquid food product before or after high-pressure sterilization treatment. It is a material for which heat sterilization treatment and cooling treatment are performed on the kind and the like. In this case, in order to control the temperature and time of the heat sterilization process or the temperature of the cooling process, an appropriate temperature detector (not shown), a flow rate control valve, its control mechanism, etc. are provided. In addition, in the present embodiment, the double shell and tube heat exchanger was used for the preheater (61), the heater (62) and the cooler (63), but the properties such as liquid foods and liquid foods, etc. If the equipment is suitable for the properties of the solid matter contained in, plate type heat exchangers and cylindrical scraping surface heat exchangers and electrothermal or electromagnetic heaters,
It can be used without restriction.
【0020】ここで、本実施例の加熱装置(30)及び冷却
装置(40)における、30℃( 常温 )での又は60℃( 加
温 )での高圧殺菌処理と、例えば90℃での加熱殺菌処
理と、30℃( 常温)での無菌包装充填とを組合せた場
合の、温度調節機能付の高圧殺菌処理作業の手順をまと
めると下記のとおりである。なお、高圧殺菌処理及び加
熱殺菌処理の時間と、手順中の弁類の閉止とポンプなど
の停止とについては記述を省略してある。 加熱冷却弁( 68,69,71,73)を開放して供給ポンプ(3
1)を稼動させることによって、90℃での加熱殺菌処理
後の常温での高圧殺菌処理が可能である。すなわち、3
0℃供給→60℃予熱→90℃加熱殺菌→60℃予冷→
30℃冷却→30℃高圧殺菌→30℃充填である。 加熱冷却弁( 68,69,71,74,75,77)を開放して、供給
ポンプ(31)と搬送ポンプ(41)とを稼動させることによっ
て、90℃での加熱殺菌処理後の加温での高圧殺菌処理
と常温での無菌包装充填が可能である。すなわち、30
℃供給→60℃予熱→90℃加熱殺菌→60℃予冷→6
0℃高圧殺菌→30℃冷却→30℃充填である。 加熱冷却弁( 75,76)を開放して搬送ポンプ(41)を稼
動させることによって、常温での高圧殺菌処理後の90
℃での加熱殺菌処理と常温での無菌包装充填が可能であ
る。すなわち、30℃供給→30℃高圧殺菌→60℃予
熱→90℃加熱殺菌→60℃予冷→30℃冷却→30℃
充填である。 加熱冷却弁( 68,70,72,74,75,76)を開放して、供給
ポンプ(31)と搬送ポンプ(41)とを稼動させることによっ
て、加温での高圧殺菌処理後の90℃での加熱殺菌処理
と常温での無菌包装充填が可能である。すなわち、30
℃供給→60℃加温→60℃高圧殺菌→75℃予熱→9
0℃加熱殺菌→75℃予冷→30℃冷却→30℃充填で
ある。 加熱冷却弁( 68,70,72,74,75,77)を開放して、供給
ポンプ(31)と搬送ポンプ(41)とを稼動させることによっ
て、加温での高圧殺菌処理と常温での無菌包装充填が可
能である。すなわち、30℃供給→60℃加温→60℃
高圧殺菌→30℃冷却→30℃充填である。Here, in the heating device (30) and the cooling device (40) of the present embodiment, high-pressure sterilization treatment at 30 ° C. (normal temperature) or 60 ° C. (heating) and heating at 90 ° C., for example. The procedure of the high-pressure sterilization work with temperature control function when the sterilization treatment and the aseptic packaging and filling at 30 ° C (normal temperature) are combined is summarized as follows. It should be noted that the description of the time for the high pressure sterilization treatment and the heat sterilization treatment, the closing of the valves and the stop of the pump during the procedure are omitted. Open the heating / cooling valve (68,69,71,73) and supply pump (3
By operating 1), high-pressure sterilization at room temperature is possible after heat sterilization at 90 ° C. That is, 3
0 ℃ supply → 60 ℃ preheat → 90 ℃ heat sterilization → 60 ℃ precool →
Cooling at 30 ° C → high pressure sterilization at 30 ° C → filling at 30 ° C. Heating and cooling valves (68,69,71,74,75,77) are opened, and the supply pump (31) and the transfer pump (41) are operated to heat the sterilization treatment at 90 ° C. It is possible to perform high-pressure sterilization treatment at room temperature and aseptic packaging and filling at room temperature. That is, 30
℃ supply → 60 ℃ preheat → 90 ℃ heat sterilization → 60 ℃ precool → 6
0 ° C. high pressure sterilization → 30 ° C. cooling → 30 ° C. filling. By opening the heating and cooling valves (75, 76) and operating the transfer pump (41), 90
Heat sterilization at ℃ and aseptic packaging and filling at room temperature are possible. That is, 30 ° C. supply → 30 ° C. high pressure sterilization → 60 ° C. preheating → 90 ° C. heat sterilization → 60 ° C. pre-cooling → 30 ° C. cooling → 30 ° C.
Filling. By opening the heating and cooling valves (68, 70, 72, 74, 75, 76) and operating the supply pump (31) and the transfer pump (41), 90 ° C after high-pressure sterilization treatment by heating. It is possible to sterilize by heat treatment and aseptic packaging and filling at room temperature. That is, 30
℃ supply → 60 ℃ heating → 60 ℃ high pressure sterilization → 75 ℃ preheating → 9
Heat sterilization at 0 ° C → precooling at 75 ° C → cooling at 30 ° C → filling at 30 ° C. By opening the heating / cooling valves (68, 70, 72, 74, 75, 77) and operating the supply pump (31) and the transfer pump (41), high-pressure sterilization treatment by heating and normal temperature Aseptic packaging and filling is possible. That is, 30 ° C supply → 60 ° C heating → 60 ° C
High-pressure sterilization → 30 ° C. cooling → 30 ° C. filling.
【0021】[0021]
【作用】以上本実施例の温度調節機能付の高圧殺菌処理
作業の手順に示すとおり、本実施例の加熱装置(30)及び
冷却装置(40)によれば、包装容器に充填する前の液状食
品類などの、2000気圧以上の高圧殺菌処理の前工程
又は後工程で、100℃以下の加熱殺菌処理を連続して
併用実施することが出来る。すなわち、常温( 30℃ )
の液状食品類などを、予熱器(61)を経由し予熱( 60℃
)して、加熱器(62)で約2.0気圧の飽和水蒸気を供給し
て例えば90℃に加熱して、ホールディングパイプ(64)
内で一定時間保持して加熱殺菌処理した後に、予熱器(6
1)を経由し予冷( 60℃ )して、冷却器(63)で約5℃の
冷却水を供給して例えば30℃に冷却するものである。
この場合に、加熱温度及び冷却温度の設定には、供給ポ
ンプ(31)又は搬送ポンプ(41)の供給量又は搬送量( 各々
約6.0L/分 )に見合った、飽和水蒸気又は冷却水の供給
量を調節して自由に設定できるものである。なお、2重
多管式熱交換器である加熱器(62)内又は冷却器(63)内に
残留する液状食品類などの、過剰加熱や過剰冷却などに
よる悪影響を防止するために、供給ポンプ(31)又は搬送
ポンプ(41)の稼動と同時に飽和水蒸気又は冷却水の供給
を開始して、供給ポンプ(31)又は搬送ポンプ(41)の停止
の数秒前に、飽和水蒸気又は冷却水の供給を停止するこ
とが好ましい。[Function] As described above in the procedure of the high-pressure sterilization work with temperature control function of the present embodiment, according to the heating device (30) and the cooling device (40) of the present embodiment, the liquid before filling the packaging container The heat sterilization treatment at 100 ° C. or lower can be continuously performed in combination in the pre-process or the post-process of the high-pressure sterilization treatment of 2000 atm or more for foods and the like. That is, room temperature (30 ° C)
Preheat (60 ℃) liquid foods, etc. from the preheater (61).
), And supply saturated steam of about 2.0 atm with the heater (62) to heat it to, for example, 90 ° C., and hold pipe (64)
After heating and sterilizing by holding for a certain time in the preheater (6
It is precooled (60 ° C.) via 1) and supplied with cooling water of about 5 ° C. by a cooler (63) to cool it to, for example, 30 ° C.
In this case, the heating temperature and cooling temperature should be set to saturated steam or cooling water that is commensurate with the feed rate or feed rate of the feed pump (31) or the feed pump (41) (about 6.0 L / min each). It can be set freely by adjusting the supply amount. In addition, in order to prevent adverse effects due to overheating or overcooling of liquid foods or the like remaining in the heater (62) or the cooler (63) that is a double-pipe heat exchanger, a supply pump Supply of saturated steam or cooling water is started at the same time as the operation of (31) or the transfer pump (41), and saturated steam or cooling water is supplied a few seconds before the supply pump (31) or transfer pump (41) is stopped. Is preferably stopped.
【0022】また本実施例の場合には、高圧処理室(10)
の内容積約6.0L の3倍に相当する、内容積約18L の
屈曲円筒式のホールディングパイプ(64)を用いたもので
あって、前記の高圧殺菌処理作業の手順に示すとお
り、例えば4個の高圧処理室(10)を設置して、5分ずつ
タイミングをずらして、液状食品類などの供給排気手順
と高圧殺菌処理と排出排水手順を繰返す連続的な高圧殺
菌処理の場合に、15分の加熱殺菌処理時間を保持した
100℃以下の加熱殺菌処理を、連続して併用実施する
ことが出来るものである。なお、前記の温度調節機能付
の高圧殺菌処理作業の手順及び手順に示す、70℃
以下の加温を併用した2000気圧以上の高圧殺菌処理
の場合には、加熱冷却弁(72)を開放して、液状食品類な
どをホールディングパイプ(64)を経由させないで高圧処
理室(10)に供給するものである。In the case of this embodiment, the high pressure processing chamber (10)
Using a bent cylindrical holding pipe (64) with an internal volume of about 18 L, which is three times the internal volume of about 6.0 L, as shown in the procedure of the high-pressure sterilization process described above, for example, 4 In the case of continuous high-pressure sterilization treatment in which individual high-pressure treatment chambers (10) are installed and timings are shifted by 5 minutes and the supply / exhaust procedure of liquid foods, high-pressure sterilization procedure and discharge / drainage procedure are repeated, The heat sterilization treatment at 100 ° C. or less while maintaining the heat sterilization treatment time for one minute can be continuously performed in combination. It should be noted that 70 ° C, which is shown in the procedure and procedure of the high-pressure sterilization work with the temperature control function,
In the case of high pressure sterilization treatment of 2000 atm or more using the following heating together, the heating and cooling valve (72) is opened, and liquid foods etc. are not passed through the holding pipe (64) but the high pressure treatment chamber (10). To supply.
【0023】[0023]
【発明の効果】以上実施例及び作用に示すとおり、本発
明の温度調節機能付の高圧殺菌処理装置については、包
装容器に充填する前の液状食品類などの、常温又は加温
での2000気圧以上の高圧殺菌処理の前工程又は後工
程で、100℃以下の加熱殺菌処理を連続して併用実施
できるものであって、本願出願人に係る特願平2-207073
号の発明に示すとおり、10000気圧以上の高圧殺菌
処理に対しても耐性が強く、栄養成分を破壊し味覚を劣
化させる100℃以上の加熱殺菌処理を必要とした、中
性食品類の保存において問題であった頑強な細菌胞子な
どを、連続的に効率良く殺菌処理する温度調節機能付の
高圧殺菌処理装置を提供するものである。As shown in the above examples and operations, the high-pressure sterilization apparatus with temperature control function of the present invention has a pressure of 2000 atm at room temperature or heating such as liquid foods before being filled in a packaging container. In the pre-process or post-process of the above high-pressure sterilization treatment, heat sterilization treatment at 100 ° C. or less can be continuously carried out in combination, and Japanese Patent Application No. 2-207073 of the present applicant
In the preservation of neutral foods, which has strong resistance to high-pressure sterilization treatment of 10000 atm or higher and requires heat sterilization treatment of 100 ° C or higher that destroys nutritional components and deteriorates taste, as shown in the invention of No. It is intended to provide a high-pressure sterilization apparatus having a temperature control function for continuously and efficiently sterilizing a robust bacterial spore, which has been a problem.
【0024】また実施例に示すとおり、本発明の温度調
節機能付の高圧殺菌処理装置については、複数個の高圧
処理室(10)を設置することによって、液状食品類などの
供給及び排出のタイミングをずらして連続的に高圧殺菌
処理することが可能であって、また高圧殺菌処理作業の
開始前又は終了時に、水蒸気管(52)から飽和水蒸気又は
無菌水を供給することによって、高圧処理室(10)内とそ
の下流側の全ての装置及び管路を簡単に殺菌又は清掃で
きるものであって、殺菌又は清掃後は、空気給排気管路
(59)から無菌空気を供給することによって、高圧処理室
(10)内とその下流側の全ての装置及び管路を常時無菌状
態に保持できるものであって、さらに液状食品類などに
含有する固形物の性状に適合したプランジャーポンプ(
31,41)や2重多管式熱交換器(61,62,63)などを用いたた
めに、高圧殺菌処理中の管路閉塞などの障害を防止でき
るものである。Further, as shown in the examples, in the high-pressure sterilization apparatus with temperature control function of the present invention, by installing a plurality of high-pressure processing chambers (10), the timing of supply and discharge of liquid foods, etc. It is possible to perform high-pressure sterilization treatment continuously by shifting, and before starting or at the end of high-pressure sterilization treatment work, by supplying saturated steam or sterile water from the steam pipe (52), the high-pressure treatment chamber ( 10) All devices and pipelines inside and downstream of them can be easily sterilized or cleaned, and after sterilization or cleaning, air supply and exhaust pipelines
By supplying sterile air from (59),
(10) Plunger pump that can keep all devices and pipelines inside and downstream in a sterile state at all times, and that is suitable for the properties of solids contained in liquid foods (
(31, 41) and double multitubular heat exchangers (61, 62, 63) are used, so that obstacles such as blockage of the pipeline during high-pressure sterilization can be prevented.
【図1】本発明の実施例における、温度調節機能付の高
圧殺菌処理装置の構成を示す説明図である。FIG. 1 is an explanatory diagram showing a configuration of a high-pressure sterilization apparatus with a temperature adjusting function in an embodiment of the present invention.
【図2】本発明の実施例の温度調節機能付の高圧殺菌処
理装置における、加熱装置(30)及び冷却装置(40)の構成
を示す説明図である。FIG. 2 is an explanatory diagram showing the configurations of a heating device (30) and a cooling device (40) in the high-pressure sterilization apparatus with a temperature adjusting function according to the embodiment of the present invention.
10 …高圧処理室 11 …耐圧円筒 12 …耐圧上蓋 13 …耐圧底蓋 20 …加圧装置 21 …ベローズ 22 …加圧ポンプ 23 …給水タンク 24, 25, 26, 27 …耐圧弁 28 …分岐管路 29 …加圧水給排水管路 30 …加熱装置 31 …供給ポンプ 32 …供給ホッパー 33, 34 …供給弁 35, 47, 58 …逆止弁 39 …食品類供給管路 40 …冷却装置 41 …搬送ポンプ 42 …サージタンク 43 …無菌空気管 44 …水蒸気管 45, 46 …排出弁 49 …食品類排出管路 50 …空気圧縮機 51 …除菌フィルター 52, 65 …水蒸気管 53, 54, 55, 56, 57 …空気弁 59 …空気給排気管路 61 …予熱器 62 …加熱器 63 …冷却器 64 …ホールディングパイプ 66 …冷却水管 67 …加熱冷却管路 68, 69, 70, 71, 72 …加熱冷却弁 73, 74, 75, 76, 77 …加熱冷却弁 10 ... High-pressure processing chamber 11 ... Pressure-resistant cylinder 12 ... Pressure-resistant upper lid 13 ... Pressure-resistant bottom lid 20 ... Pressurizing device 21 ... Bellows 22 ... Pressurizing pump 23 ... Water supply tank 24, 25, 26, 27 ... Pressure-resistant valve 28 ... Branch pipe line 29 ... Pressurized water supply / drainage line 30 ... Heating device 31 ... Supply pump 32 ... Supply hopper 33, 34 ... Supply valve 35, 47, 58 ... Check valve 39 ... Food product supply line 40 ... Cooling device 41 ... Conveyance pump 42 ... Surge tank 43 ... Aseptic air pipe 44 ... Steam pipe 45, 46 ... Discharge valve 49 ... Food discharge pipe 50 ... Air compressor 51 ... Sterilization filter 52, 65 ... Steam pipe 53, 54, 55, 56, 57 ... Air valve 59 ... Air supply / exhaust pipeline 61 ... Preheater 62 ... Heater 63 ... Cooler 64 ... Holding pipe 66 ... Cooling water pipe 67 ... Heating / cooling pipeline 68, 69, 0, 71, 72 ... heating and cooling valve 73, 74, 75, 76, 77 ... heating and cooling valves
Claims (2)
た高圧処理室と、高圧処理室内を加圧する加圧装置と、
高圧処理室内に通じる食品類供給管路と食品類排出管路
と空気給排気管路とから成る高圧殺菌処理装置であっ
て、食品類供給管路と食品類排出管路との、どちらか一
方に又は両方に加熱装置を設けたことを特徴とする温度
調節機能付の高圧殺菌処理装置。1. A high-pressure processing chamber composed of a pressure-resistant cylinder, a pressure-resistant upper lid, and a pressure-resistant bottom lid, and a pressure device for pressurizing the high-pressure processing chamber.
A high-pressure sterilization treatment device comprising a food supply pipeline, a food discharge pipeline, and an air supply / exhaust pipeline that communicate with the high-pressure processing chamber, and either one of the food supply pipeline and the food discharge pipeline A high-pressure sterilization treatment device with a temperature control function, characterized in that a heating device is provided in either or both.
食品類供給管路と食品類排出管路との、どちらか一方に
又は両方に冷却装置を設けたことを特徴とする、請求項
1に記載の温度調節機能付の高圧殺菌処理装置。2. A cooling device is provided on the downstream side of the heating device and on either or both of the food product supply pipe and the food product discharge pipe. The high-pressure sterilization apparatus with a temperature control function according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23797091A JPH0576328A (en) | 1991-09-18 | 1991-09-18 | High-pressure sterilizer with temperature control function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23797091A JPH0576328A (en) | 1991-09-18 | 1991-09-18 | High-pressure sterilizer with temperature control function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0576328A true JPH0576328A (en) | 1993-03-30 |
Family
ID=17023170
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23797091A Pending JPH0576328A (en) | 1991-09-18 | 1991-09-18 | High-pressure sterilizer with temperature control function |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0576328A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999029187A1 (en) * | 1997-12-05 | 1999-06-17 | Meyer Richard S | Ultra high pressure, low temperature food preservation process |
| US6017572A (en) * | 1998-09-17 | 2000-01-25 | Meyer; Richard S. | Ultra high pressure, high temperature food preservation process |
| JP2004154007A (en) * | 2002-11-01 | 2004-06-03 | Puraseramu:Kk | Apparatus for impregnation treatment and method for impregnation treatment for material to be treated |
| JP2009193756A (en) * | 2008-02-13 | 2009-08-27 | Izumi Food Machinery Co Ltd | Fluid heating device |
| JP2014514522A (en) * | 2011-03-17 | 2014-06-19 | ネステク ソシエテ アノニム | System and method for heat exchange |
| US11154080B2 (en) | 2007-06-27 | 2021-10-26 | Jcr Technologies Llc | High pressure frozen sterilization process |
-
1991
- 1991-09-18 JP JP23797091A patent/JPH0576328A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1999029187A1 (en) * | 1997-12-05 | 1999-06-17 | Meyer Richard S | Ultra high pressure, low temperature food preservation process |
| US6017572A (en) * | 1998-09-17 | 2000-01-25 | Meyer; Richard S. | Ultra high pressure, high temperature food preservation process |
| US6177115B1 (en) | 1998-09-17 | 2001-01-23 | Richard S. Meyer | Ultra high pressure, high temperature food preservation process |
| JP2004154007A (en) * | 2002-11-01 | 2004-06-03 | Puraseramu:Kk | Apparatus for impregnation treatment and method for impregnation treatment for material to be treated |
| US11154080B2 (en) | 2007-06-27 | 2021-10-26 | Jcr Technologies Llc | High pressure frozen sterilization process |
| JP2009193756A (en) * | 2008-02-13 | 2009-08-27 | Izumi Food Machinery Co Ltd | Fluid heating device |
| JP2014514522A (en) * | 2011-03-17 | 2014-06-19 | ネステク ソシエテ アノニム | System and method for heat exchange |
| JP2016040514A (en) * | 2011-03-17 | 2016-03-24 | ネステク ソシエテ アノニム | System and method for heat exchange |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4257686B2 (en) | High pressure sterilization method and equipment | |
| US4830865A (en) | Method for aseptically processing a food product | |
| US7186430B2 (en) | UHT pasteurizer with regeneration | |
| JP3342872B2 (en) | Pneumatic cooking system | |
| EP0692198B1 (en) | Method and apparatus for heating and sterilizing food | |
| CN110213969A (en) | The method of Equipment for Heating Processing and operation Equipment for Heating Processing | |
| US3835762A (en) | Device for the sterilization of food products in flexible packages | |
| JP2636242B2 (en) | Food heating packaging equipment | |
| US11608892B2 (en) | Plug, machine and processing method under high pressure | |
| US4597945A (en) | Sterilization apparatus | |
| WO1996013278A1 (en) | Solution sterilization system and method of operation | |
| CN114642247A (en) | Food cooking sterilization and aseptic packaging integrated equipment and processing method | |
| AU769174B2 (en) | Method and apparatus for pressure processing a pumpable substance | |
| JP3263609B2 (en) | Operating method of continuous high-pressure sterilizer | |
| US20010041206A1 (en) | Method and apparatus for pressure processing a pumpable substance | |
| JP3297319B2 (en) | Continuous high pressure sterilizer | |
| US1491092A (en) | Heat-treating substance packed in sealed receptacles | |
| EP1187766B1 (en) | Apparatus and method for heat-treatment of food products in plastic bags | |
| JP3162032B2 (en) | Sterilization method of food etc. | |
| RU48143U1 (en) | INSTALLATION FOR STERILIZING PACKAGES WITH FOOD | |
| JPS60135055A (en) | Continuous heating pasturization apparatus | |
| JPS585174A (en) | Heat sterilization for food and its device | |
| RU2001134615A (en) | APPARATUS AND METHOD OF HEAT PROCESSING OF FOOD PRODUCTS IN PLASTIC BAGS | |
| EP1620318A1 (en) | Method and apparatus for packaging products | |
| JP2006271296A (en) | Sterilization method and apparatus |