JP6397796B2 - Food liquid heat sterilization method and apparatus - Google Patents

Food liquid heat sterilization method and apparatus Download PDF

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JP6397796B2
JP6397796B2 JP2015101824A JP2015101824A JP6397796B2 JP 6397796 B2 JP6397796 B2 JP 6397796B2 JP 2015101824 A JP2015101824 A JP 2015101824A JP 2015101824 A JP2015101824 A JP 2015101824A JP 6397796 B2 JP6397796 B2 JP 6397796B2
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木原 均
均 木原
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本発明は、食品液の加熱殺菌方法及び装置に係り、例えばドレッシング、調味液等の低温殺菌を連続的に行うのに適した食品液加熱殺菌方法及び装置に関する。 The present invention relates to a food liquid heat sterilization method and apparatus, and more particularly to a food liquid heat sterilization method and apparatus suitable for continuously performing pasteurization such as dressing and seasoning liquid.

従来、特許文献1に記載のように、食品液はビンや缶等の容器に充填される前に加熱殺菌が行われている。そして、特許文献2には、殺菌機の入口側に真空蒸気制御弁を設け、出口側に吸引手段を設けて、真空蒸気制御弁で殺菌機に供給する蒸気を大気圧以下の真空蒸気とすると共に、吸引手段で殺菌機内を所定の減圧状態に維持して、大気圧以下の蒸気、即ち100℃以下の低温蒸気を殺菌機内に安定に供給して、食品を100℃以下の品質劣化を来すことのない蒸気温度で殺菌することが行われている。
また、特許文献2には、吸引手段として、循環ポンプとエジェクターを組み合わせたエジェクター式の真空ポンプを使用することも開示されている。
Conventionally, as described in Patent Document 1, food sterilization is performed by heat sterilization before filling a container such as a bottle or a can. And in patent document 2, a vacuum steam control valve is provided in the inlet side of a sterilizer, a suction means is provided in an outlet side, and the vapor | steam supplied to a sterilizer with a vacuum steam control valve is made into the vacuum steam below atmospheric pressure. At the same time, the inside of the sterilizer is maintained at a predetermined reduced pressure by the suction means, and the steam below the atmospheric pressure, that is, the low-temperature steam at 100 ° C. or lower is stably supplied to the sterilizer, resulting in the quality deterioration of the food at 100 ° C. or lower. Sterilization is performed at a steam temperature that does not occur.
Patent Document 2 also discloses the use of an ejector-type vacuum pump in which a circulation pump and an ejector are combined as suction means.

特開平6−98734号公報JP-A-6-98734 特開平11−332532号公報JP 11-332532 A

しかしながら、特許文献2記載の技術は、殺菌機が密封タンクであるので、食品を連続的に低温殺菌できるものではない。
また、エジェクターへの水は循環使用しているが、殺菌機によって使用された高温蒸気も混入するので、徐々に温度上昇する。勿論途中で温度上昇した水を廃棄し、タンクに水を入れることも可能であるが水及び熱の有効利用がなされていない。
更には、殺菌機内に搬送される食品は、前もって予熱されているわけではないので、加熱殺菌に時間がかかるという問題がある。
However, since the sterilizer is a sealed tank, the technique described in Patent Document 2 cannot continuously pasteurize food.
In addition, although the water to the ejector is circulated, the high temperature steam used by the sterilizer is also mixed, so the temperature gradually rises. Of course, it is possible to discard the water whose temperature has risen in the middle and put water in the tank, but water and heat are not effectively used.
Furthermore, since the food conveyed in a sterilizer is not preheated beforehand, there exists a problem that heat sterilization takes time.

また、図3に示すように、熱交換器を用いその加熱源に温水を用いて食品液を加熱する方法も行われている。この食品液加熱殺菌装置60は、内管61、外管62、及びフランジ63〜66を有する熱交換器を用い、内管61内に食品液を流し、外管62内に温水を流して食品液の適正温度の加熱殺菌を行っている。ここで、68は循環ポンプを、69は温水の加熱装置を示す。 Moreover, as shown in FIG. 3, the method of heating a food liquid using a heat exchanger using the warm water for the heating source is also performed. The food liquid heat sterilization apparatus 60 uses a heat exchanger having an inner tube 61, an outer tube 62, and flanges 63 to 66. The food liquid flows through the inner tube 61, and hot water flows through the outer tube 62 to produce food. Heat sterilization at the proper temperature of the liquid. Here, 68 indicates a circulation pump and 69 indicates a heating device for hot water.

ところが、この装置60においては、下流側に設けられている食品液の充填装置にトラブル等が発生した場合、熱交換器から温水を抜くのに時間がかかり、必要以上に食品液が加熱されてしまうという問題があった。また、温水を用いるので、その装置60及び温水の温度上昇に時間がかかるという問題があった。
更に、特許文献1記載の技術においても、同様な問題があった。
However, in this apparatus 60, when trouble occurs in the food liquid filling apparatus provided on the downstream side, it takes time to drain the hot water from the heat exchanger, and the food liquid is heated more than necessary. There was a problem that. In addition, since warm water is used, there is a problem that it takes time to increase the temperature of the apparatus 60 and the warm water.
Further, the technique described in Patent Document 1 has the same problem.

本発明はかかる事情に鑑みてなされたもので、装置全体の応答性を高めて、全体の熱効率を向上させた食品液加熱殺菌方法及び装置を提供することを目的とする。 This invention is made | formed in view of this situation, and it aims at providing the responsiveness of the whole apparatus, and providing the food liquid heat sterilization method and apparatus which improved the whole thermal efficiency.

前記目的に沿う第1の発明に係る食品液加熱殺菌方法は、屈曲形成された内管と、該内管を囲む外管とを有する加熱器を用い、前記内管に食品液を流し、前記外管の入口側に高温蒸気を供給すると共に前記外管の出口側から、高圧流水によってその周囲に負圧を発生させるエジェクターを用いて真空吸引(減圧吸引)を行い、前記加熱器の温度を制御する食品液加熱殺菌方法において、
前記エジェクターで、吸引された蒸気と前記高圧流水が一体化して加温された水と、前記加熱器に供給される前の前記食品液との熱交換を行い、前記エジェクターから排出された前記水の冷却と、前記食品液の加熱を同時に行う。
The food liquid heat sterilization method according to the first aspect of the present invention uses a heater having a bent inner tube and an outer tube surrounding the inner tube, and flows the food liquid through the inner tube, the inlet side of the outer tube supplies high-temperature steam, from the outlet side of the outer tube, and vacuum suction (vacuum suction) with an ejector for generating a negative pressure in its surroundings by high-pressure water flow, the temperature of the heater In the food liquid heat sterilization method for controlling
The water discharged from the ejector by exchanging heat between the water heated by integrating the sucked steam and the high-pressure flowing water with the food liquid before being supplied to the heater. And the heating of the food liquid are performed simultaneously.

前記目的に沿う第2の発明に係る食品液加熱殺菌装置は、加熱殺菌しようとする食品液を流す内管、及び該内管を囲む外管を有する加熱器と、前記外管の入口側に高温蒸気を供給する高温蒸気発生源と、前記外管の出口側に接続されて、高圧流水によってその周囲に負圧を発生させ、真空吸引により前記外管内の圧力を制御するエジェクターとを備えた食品液加熱殺菌装置において、
前記エジェクターで、吸引された蒸気と前記高圧流水が一体化して加温された水と、前記加熱器に供給される前の前記食品液との熱交換を行う加熱用熱交換器を設け、前記水の温度上昇を防止し、かつ前記食品液の加熱を行う。
The food liquid heat sterilization apparatus according to the second aspect of the present invention is directed to a heater having an inner pipe through which a food liquid to be sterilized by heating, an outer pipe surrounding the inner pipe, and an inlet side of the outer pipe. A high-temperature steam generating source that supplies high-temperature steam, and an ejector that is connected to the outlet side of the outer pipe, generates negative pressure around the high-pressure running water, and controls the pressure in the outer pipe by vacuum suction . In the food liquid heat sterilizer,
In the ejector, provided is a heat exchanger for heating that performs heat exchange between water sucked and water heated by integrating the high-pressure flowing water and the food liquid before being supplied to the heater, The temperature of water is prevented from rising and the food liquid is heated.

第1の発明に係る食品液加熱殺菌方法、及び第2の発明に係る食品液加熱殺菌装置においては、加熱器の加熱源に高温蒸気を用い、しかも、加熱器の出口側にはエジェクターを接続しているので、加熱器内の圧力を制御し、加熱温度を調整できる。
この場合、加熱源は蒸気であって、温水に比較して残存する熱量が小さく、食品液加熱殺菌装置の事故対応をする場合の応答性が速い。
なお、前記加熱器は直列又は並列に配置された複数の加熱器から構成することもできる。
In the food liquid heat sterilization method according to the first invention and the food liquid heat sterilization apparatus according to the second invention, high temperature steam is used as a heating source of the heater, and an ejector is connected to the outlet side of the heater. Therefore, the pressure in the heater can be controlled to adjust the heating temperature.
In this case, the heating source is steam, the amount of heat remaining is smaller than that of hot water, and the responsiveness when responding to an accident in the food liquid heat sterilizer is fast.
In addition, the said heater can also be comprised from the some heater arrange | positioned in series or in parallel.

本発明の一実施の形態に係る食品液加熱殺菌装置のブロック図である。1 is a block diagram of a food liquid heat sterilization apparatus according to an embodiment of the present invention. 同食品液加熱殺菌装置の部分説明図である。It is a partial explanatory view of the food liquid heat sterilizer. 比較する従来例に係る食品液加熱殺菌装置の部分説明図である。It is a partial explanatory view of a food liquid heat sterilizer according to a conventional example to be compared.

続いて、添付した図面を参照しながら、本発明を具体化した実施の形態について説明する。
図1、図2に示すように、本発明の一実施の形態に係る食品液加熱殺菌装置10は、食品液(例えば、調味液)を加熱殺菌する加熱器11を有している。この加熱器11は、内管12とその主要部の外側を囲む外管13とを有する熱交換器11aからなっている。
Next, embodiments of the present invention will be described with reference to the accompanying drawings.
As shown in FIGS. 1 and 2, a food liquid heat sterilization apparatus 10 according to an embodiment of the present invention has a heater 11 that heats and sterilizes food liquid (for example, seasoning liquid). The heater 11 includes a heat exchanger 11a having an inner tube 12 and an outer tube 13 surrounding the outside of the main part.

加熱器11の外管13は筒状となって、図2に示すように、両端部にフランジ(端板)14、15を有し、このフランジ14、15にはフランジ14、15を挿通する内管12の直管部に連接するUベンド17、18が複数設けられ、接続フランジ19、20が連結されて、熱交換器11a内にジグザグ状に折り返し配置(屈曲形成)された内管12を形成している。なお、この熱交換器11aの構造については、例えば、特許第5358660号公報に開示されている。また、複数の熱交換器11aを直列又は並列に接続して、一つの加熱器とすることもできる。 As shown in FIG. 2, the outer tube 13 of the heater 11 has a cylindrical shape and has flanges (end plates) 14 and 15 at both ends, and the flanges 14 and 15 are inserted into the flanges 14 and 15. A plurality of U-bends 17 and 18 connected to the straight pipe portion of the inner pipe 12 are provided, the connecting flanges 19 and 20 are connected, and the inner pipe 12 is arranged in a zigzag manner (bently formed) in the heat exchanger 11a. Is forming. In addition, about the structure of this heat exchanger 11a, it is disclosed by patent 5358660, for example. In addition, a plurality of heat exchangers 11a can be connected in series or in parallel to form a single heater.

外管13の一側端部(入口側)の上位置には、高温蒸気を入れる蒸気入口21が設けられ、外管13の他側端部(出口側)の下位置には、高温蒸気(及び水)を排出する蒸気出口22が設けられている。 A steam inlet 21 for introducing high-temperature steam is provided at a position above one side end (inlet side) of the outer pipe 13, and a high-temperature steam (at a position below the other end (outlet side) of the outer pipe 13 is provided. And a steam outlet 22 for discharging water).

加熱器11の蒸気出口22には図示しない逆止弁を介してエジェクター24が接続されている。エジェクター24は、高圧流水の周囲に負圧を発生させ、蒸気出口22からの蒸気を真空吸引するもので、真空ポンプと同様な働きをする。なお、吸引された蒸気は高圧流水と一体化し水となる。吸引される蒸気は高温蒸気であるから、高圧流水を加温することになる。このエジェクター24によって、外管13内の圧力を制御(加熱)して、加熱器11の蒸気温度を例えば90℃より低い70〜80℃に制御している。 An ejector 24 is connected to the steam outlet 22 of the heater 11 via a check valve (not shown). The ejector 24 generates a negative pressure around the high-pressure flowing water and vacuums the steam from the steam outlet 22 and functions in the same manner as a vacuum pump. The sucked steam is integrated with the high-pressure flowing water to become water. Since the sucked steam is high-temperature steam, the high-pressure running water is heated. The ejector 24 controls (heats) the pressure in the outer tube 13 to control the vapor temperature of the heater 11 to, for example, 70 to 80 ° C. lower than 90 ° C.

エジェクター24からの水は、タンク25に送られ、ポンプ26を介して、直列接続された食品液の加熱用熱交換器27に送られ、加熱用熱交換器27で冷却されてエジェクター24に供給される。 The water from the ejector 24 is sent to the tank 25, sent to the food liquid heating heat exchanger 27 connected in series via the pump 26, cooled by the heating heat exchanger 27, and supplied to the ejector 24. Is done.

一方、加熱器11を構成する熱交換器11aに供給する高温蒸気は、高温蒸気を発生する蒸気源(高温蒸気発生源)29(0.02MPa)から供給を受けて、ストレーナーを通って、バルブ、減圧弁、止めバルブ、流量調整弁(蒸気バルブ38)、バルブ、逆止弁を備えた蒸気機器を経て、蒸気入口21に供給される。蒸気入口21の蒸気温度は70〜80℃になるように蒸気機器及びエジェクター24の吸引圧力を調整している。 On the other hand, the high temperature steam supplied to the heat exchanger 11a constituting the heater 11 is supplied from a steam source (high temperature steam generation source) 29 (0.02 MPa) that generates high temperature steam, passes through a strainer, Then, the steam is supplied to the steam inlet 21 through a steam device including a pressure reducing valve, a stop valve, a flow rate adjusting valve (steam valve 38), a valve, and a check valve. The suction pressure of the steam device and the ejector 24 is adjusted so that the steam temperature at the steam inlet 21 is 70 to 80 ° C.

食品液は最初食品液タンク31に貯留され、ポンプ32を介して加熱用熱交換器27に供給され、タンク25(エジェクター24からの水)の水と熱交換される。この加熱用熱交換器27によって、食品液は加熱され、タンク25の水は冷やされ、温度上昇を防止している。 The food liquid is first stored in the food liquid tank 31, supplied to the heat exchanger 27 for heating via the pump 32, and heat-exchanged with water in the tank 25 (water from the ejector 24). By this heat exchanger 27 for heating, the food liquid is heated, the water in the tank 25 is cooled, and temperature rise is prevented.

加熱用熱交換器27で予備加熱された食品液は熱交換器11aの内管12内を流れて加熱殺菌される。熱交換器11aを出た食品液は、必要な場合、図示しない保温ユニットに供給される。保温ユニットの出口には切り換えバルブ33があり、必要でない食品液を食品液タンク31に戻す場合と、食品液を外部に流す場合の選択ができる。 The food liquid preheated by the heating heat exchanger 27 flows through the inner tube 12 of the heat exchanger 11a and is sterilized by heating. When necessary, the food liquid leaving the heat exchanger 11a is supplied to a heat retaining unit (not shown). A switching valve 33 is provided at the outlet of the heat retaining unit, and a selection can be made between returning unnecessary food liquid to the food liquid tank 31 and flowing food liquid to the outside.

従って、この実施の形態に係る食品液加熱殺菌方法及びその装置においては、熱交換器11a内に屈曲形成された内管12に食品液を流し、内管12を囲む外管13によって所定温度の蒸気加熱を行い、加熱殺菌された食品液を図示しない充填装置に搬送する。
この場合、エジェクター24を通過する圧力流水(高圧流水)は、高温蒸気によって加熱されるので、加熱用熱交換器27で熱回収して、食品液を加熱している。
Therefore, in the food liquid heating sterilization method and apparatus according to this embodiment, the food liquid is caused to flow through the inner tube 12 bent in the heat exchanger 11a, and the outer tube 13 surrounding the inner tube 12 has a predetermined temperature. Steam heating is performed, and the heat-sterilized food liquid is conveyed to a filling device (not shown).
In this case, since the pressure flowing water (high pressure flowing water) passing through the ejector 24 is heated by the high-temperature steam, the heat is recovered by the heating heat exchanger 27 to heat the food liquid.

また、下流側に配置された食品液の充填装置が止まると、食品液の加熱も急停止する必要があり、蒸気機器の蒸気バルブ38を閉にして、熱交換器11aに冷水を注水することによって、食品液加熱殺菌装置10の急速停止を行うことができる。食品液加熱殺菌装置10が加熱を停止するまでに要した時間は、従来の1/3程度となることが確認されている。
更には、熱交換器11aに温水を使用しないで、蒸気を使用するので、熱交換器11aの応答性が速くなって、熱交換器11aの目標加熱温度を直ぐに達成できる。
Moreover, when the food liquid filling device disposed on the downstream side stops, the heating of the food liquid needs to be stopped suddenly, and the steam valve 38 of the steam device is closed to inject cold water into the heat exchanger 11a. Thus, the food liquid heat sterilization apparatus 10 can be rapidly stopped. It has been confirmed that the time required for the food liquid heat sterilizer 10 to stop heating is about 1/3 of the conventional time.
Furthermore, since steam is used without using hot water in the heat exchanger 11a, the responsiveness of the heat exchanger 11a is increased, and the target heating temperature of the heat exchanger 11a can be achieved immediately.

そして、本発明においては、蒸気を直接使用するので、エネルギーロスが減少する。また、蒸気は境膜伝熱係数が高いので、伝熱効率が向上する。
本実施の形態に係る食品液加熱殺菌装置10においては、外管13内を負圧にしているので、熱交換器11aの漏れを常時監視できる。食品液の急速加熱停止も行える。なお、図1において、35は水源、36はバルブである。また、37は圧力コントローラであって蒸気バルブ38を制御し、二次側の蒸気圧力を一定に保持している。39、40は温度センサーで常時食品液、エジェクター24の水の温度を管理している。
In the present invention, since steam is used directly, energy loss is reduced. Moreover, since the steam has a high film heat transfer coefficient, the heat transfer efficiency is improved.
In the food liquid heat sterilization apparatus 10 according to the present embodiment, since the inside of the outer tube 13 is set to a negative pressure, leakage of the heat exchanger 11a can always be monitored. You can also stop the rapid heating of the food liquid. In FIG. 1, 35 is a water source and 36 is a valve. Reference numeral 37 denotes a pressure controller that controls the steam valve 38 to keep the secondary side steam pressure constant. Reference numerals 39 and 40 are temperature sensors that always manage the temperature of the food liquid and the water in the ejector 24.

本発明は前記した実施の形態に限定されるものではなく、本発明の要旨を変更しない範囲でその構成を変更することもできる。 The present invention is not limited to the above-described embodiment, and the configuration thereof can be changed without changing the gist of the present invention.

10:食品液加熱殺菌装置、11:加熱器、11a:熱交換器、12:内管、13:外管、14、15:フランジ、17、18:Uベント、19、20:接続フランジ、21:蒸気入口、22:蒸気出口、24:エジェクター、25:タンク、26:ポンプ、27:加熱用熱交換器、29:蒸気源、31:食品液タンク、32:ポンプ、33:切り換えバルブ、35:水源、36:バルブ、37:圧力コントローラ、38:蒸気バルブ、39、40:温度センサー 10: Food liquid heat sterilizer, 11: Heater, 11a: Heat exchanger, 12: Inner pipe, 13: Outer pipe, 14, 15: Flange, 17, 18: U vent, 19, 20: Connection flange, 21 : Steam inlet, 22: Steam outlet, 24: Ejector, 25: Tank, 26: Pump, 27: Heat exchanger for heating, 29: Steam source, 31: Food liquid tank, 32: Pump, 33: Switching valve, 35 : Water source, 36: Valve, 37: Pressure controller, 38: Steam valve, 39, 40: Temperature sensor

Claims (2)

屈曲形成された内管と、該内管を囲む外管とを有する加熱器を用い、前記内管に食品液を流し、前記外管の入口側に高温蒸気を供給すると共に前記外管の出口側から、高圧流水によってその周囲に負圧を発生させるエジェクターを用いて真空吸引を行い、前記加熱器の温度を制御する食品液加熱殺菌方法において、
前記エジェクターで、吸引された蒸気と前記高圧流水が一体化して加温された水と、前記加熱器に供給される前の前記食品液との熱交換を行い、前記エジェクターから排出された前記水の冷却と、前記食品液の加熱を同時に行うことを特徴とする食品液加熱殺菌方法。
An inner tube which is bent, with a heating device having an outer tube surrounding the inner tube, flushed with food liquid into said tube, to supply hot steam to the inlet side of the outer tube, the outer tube In the food liquid heating and sterilization method for controlling the temperature of the heater by performing vacuum suction using an ejector that generates a negative pressure around the outlet by high-pressure running water from the outlet side,
The water discharged from the ejector by exchanging heat between the water heated by integrating the sucked steam and the high-pressure flowing water with the food liquid before being supplied to the heater. The food liquid heat sterilization method characterized by simultaneously cooling the food liquid and heating the food liquid.
加熱殺菌しようとする食品液を流す内管、及び該内管を囲む外管を有する加熱器と、前記外管の入口側に高温蒸気を供給する高温蒸気発生源と、前記外管の出口側に接続されて、高圧流水によってその周囲に負圧を発生させ、真空吸引により前記外管内の圧力を制御するエジェクターとを備えた食品液加熱殺菌装置において、
前記エジェクターで、吸引された蒸気と前記高圧流水が一体化して加温された水と、前記加熱器に供給される前の前記食品液との熱交換を行う加熱用熱交換器を設け、前記水の温度上昇を防止し、かつ前記食品液の加熱を行うことを特徴とする食品液加熱殺菌装置。
An inner pipe through which a food liquid to be heat-sterilized flows, a heater having an outer pipe surrounding the inner pipe, a high-temperature steam generating source for supplying high-temperature steam to the inlet side of the outer pipe, and an outlet side of the outer pipe In the food liquid heating and sterilization apparatus comprising an ejector that generates a negative pressure around the high pressure flowing water and controls the pressure in the outer pipe by vacuum suction ,
In the ejector, provided is a heat exchanger for heating that performs heat exchange between water sucked and water heated by integrating the high-pressure flowing water and the food liquid before being supplied to the heater, A food liquid heating and sterilizing apparatus for preventing temperature rise of water and heating the food liquid.
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