JPH0551088U - Heat sterilizer - Google Patents
Heat sterilizerInfo
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- JPH0551088U JPH0551088U JP10049291U JP10049291U JPH0551088U JP H0551088 U JPH0551088 U JP H0551088U JP 10049291 U JP10049291 U JP 10049291U JP 10049291 U JP10049291 U JP 10049291U JP H0551088 U JPH0551088 U JP H0551088U
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- heat
- hot water
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- cold water
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Abstract
(57)【要約】
【目的】 小電力用のヒートポンプで加熱殺菌すること
ができ、流体の加熱や冷却の制御が容易に行なえる加熱
殺菌装置を提供する。
【構成】 流体を加熱して殺菌する加熱部10と、加熱
した流体を冷却する冷却部13とを設け、その加熱と冷
却をヒートポンプ30で行なう加熱殺菌装置であって、
ヒートポンプの放熱部31と加熱部10とに温水を循環
させる温水循環路22と、放熱部で加熱された温水を温
水循環路内を循環させながら加熱部に送る温水ポンプ2
3と、ヒートポンプの吸熱部と冷却部とに冷水を循環さ
せる冷水循環路33と、吸熱部で冷却された冷水を冷水
循環路内を循環させながら冷却部に送る冷水ポンプ34
と、加熱部と冷却部との間の流路に、加熱部を通る前の
流体をその加熱部を通った流体とで熱交換させた後加熱
部に通す熱交換器12とを設けた。
(57) [Abstract] [Purpose] To provide a heat sterilizer capable of performing heat sterilization with a heat pump for low electric power and easily controlling heating and cooling of a fluid. A heating and sterilizing apparatus comprising a heating unit 10 for heating and sterilizing a fluid and a cooling unit 13 for cooling the heated fluid, the heating and cooling being performed by a heat pump 30.
A hot water circulation path 22 for circulating hot water between the heat radiating section 31 and the heating section 10 of the heat pump, and a hot water pump 2 for sending hot water heated by the heat radiating section to the heating section while circulating the hot water in the hot water circulating path.
3, a cold water circulation path 33 for circulating cold water between the heat absorption section and the cooling section of the heat pump, and a cold water pump 34 for sending the cold water cooled by the heat absorption section to the cooling section while circulating the cold water in the cold water circulation path.
In the flow path between the heating unit and the cooling unit, a heat exchanger 12 is provided, which causes the fluid before passing through the heating unit to exchange heat with the fluid passing through the heating unit and then passes through the heating unit.
Description
【0001】[0001]
この考案は、流体を加熱して殺菌する加熱部と、この加熱した流体を冷却する 冷却部とを備え、前記加熱部の加熱と冷却部の冷却をヒートポンプで行なう加熱 殺菌装置に関する。 The present invention relates to a heating and sterilizing apparatus including a heating unit for heating and sterilizing a fluid and a cooling unit for cooling the heated fluid, and performing heating of the heating unit and cooling of the cooling unit by a heat pump.
【0002】[0002]
従来、牛乳や果汁等の液状の食品は、所定の温度で一定時間加熱させて殺菌を 行なった後、その食品を高温のまま容器に充填していた。しかしながら、食品を 高温のまま容器に充填すると、味や風味が落ちてしまうという問題があった。そ こで、食品を加熱殺菌した後、直ちに冷却して食品の味や風味を落とさないよう にした加熱殺菌装置が提案されている。 Conventionally, liquid foods such as milk and fruit juice have been heated at a predetermined temperature for a certain period of time for sterilization and then filled in a container at a high temperature. However, there is a problem in that the taste and flavor are deteriorated when the food is filled in the container at a high temperature. Therefore, there has been proposed a heat sterilizer that heats and sterilizes food and then immediately cools it so as not to lose the taste and flavor of the food.
【0003】 かかる加熱殺菌装置として図5に示すものが知られている(特開昭60-182950 号公報参照)。As such a heat sterilizer, one shown in FIG. 5 is known (see Japanese Patent Laid-Open No. 60-182950).
【0004】 図5において、1は牛乳や果汁等の液状の食品である流体5aを加熱する加熱 部、2は加熱された流体5bを冷却する冷却部、3はヒートポンプである。4は ヒートポンプ3の放熱部で、この放熱部4の放熱によって加熱部1を通る流体5 aを加熱殺菌する。6はヒートポンプ3の吸熱部で、この吸熱部6の吸熱によっ て冷却部2を通る加熱された流体5bを冷却していくものである。7は膨張弁、 8は圧縮機である。In FIG. 5, 1 is a heating unit for heating a fluid 5a which is a liquid food such as milk or fruit juice, 2 is a cooling unit for cooling the heated fluid 5b, and 3 is a heat pump. A heat radiating portion 4 of the heat pump 3 heat-sterilizes the fluid 5 a passing through the heating portion 1 by the heat radiation of the heat radiating portion 4. Reference numeral 6 denotes a heat absorbing portion of the heat pump 3, which cools the heated fluid 5b passing through the cooling portion 2 by the heat absorption of the heat absorbing portion 6. Reference numeral 7 is an expansion valve, and 8 is a compressor.
【0005】[0005]
このような加熱殺菌装置にあっては、ヒートポンプ3が放熱する熱だけを用い て低い温度の流体5aを高い温度まで加熱させるので、大電力用のヒートポンプ が必要であり、さらに、ヒートポンプ3が放熱した熱は加熱部だけで利用されて いるだけなので、熱の有効利用が低い等の問題があった。 In such a heat sterilizer, since the heat of the heat pump 3 is used to heat the low temperature fluid 5a to a high temperature, a heat pump for high power is required. Since the generated heat is only used in the heating section, there were problems such as low effective use of heat.
【0006】 また、流体5aの温度が低いと、加熱部1で流体5aを殺菌できる温度まで上昇 しない場合があり、充分に殺菌を行なうことができなくなるという問題があった 。また、流体5aの温度が高いと流体5bの温度が高くなり過ぎてしまい、味や風 味を落としてしまう等の問題があった。Further, if the temperature of the fluid 5a is low, the temperature may not rise to a temperature at which the fluid 5a can be sterilized by the heating unit 1, and there is a problem that sterilization cannot be performed sufficiently. Further, if the temperature of the fluid 5a is high, the temperature of the fluid 5b becomes too high, and there is a problem that the taste and flavor are deteriorated.
【0007】 この問題を解消するために、流体5a,5bの温度に応じてヒートポンプ3を制 御すればよい。しかし、ヒートポンプ3を制御して放熱部4の放熱量を多くする と、吸熱部6の吸熱量が多くなるので、流体5cの温度を一定に保ったまま流体 5aの温度のみを上昇させたり、逆に、流体5bの温度を一定に保ったまま流体5 cの温度のみを下げたりすることができず、その温度制御が非常に難しいという 問題があった。In order to solve this problem, the heat pump 3 may be controlled according to the temperatures of the fluids 5a and 5b. However, when the heat pump 3 is controlled to increase the heat radiation amount of the heat radiation unit 4, the heat absorption amount of the heat absorption unit 6 increases, so that only the temperature of the fluid 5a is increased while keeping the temperature of the fluid 5c constant. On the contrary, there is a problem that it is difficult to control only the temperature of the fluid 5c while keeping the temperature of the fluid 5b constant, and it is very difficult to control the temperature.
【0008】 この考案は、上記問題点に鑑みてなされたもので、その目的は、小電力用のヒ ートポンプで加熱殺菌することができるとともに流体の加熱や冷却の制御が容易 に行なうことができ、また、熱の有効利用を図ることのできる加熱殺菌装置を提 供することにある。The present invention has been made in view of the above problems, and an object thereof is to be able to perform heat sterilization with a heat pump for small electric power and to easily control heating and cooling of a fluid. It is also to provide a heat sterilizer that can effectively utilize heat.
【0009】[0009]
この考案は、上記目的を達成するため、流体が流れる流路に、前記流体を加熱 して殺菌する加熱部と、この加熱した流体を冷却する冷却部とを設け、前記加熱 部の加熱と冷却部の冷却をヒートポンプで行なう加熱殺菌装置であって、 前記ヒートポンプの放熱部と前記加熱部とを循環し、前記放熱部で温水を加熱 させ、該温水で前記加熱部の流体を加熱させる温水循環路と、 前記放熱部で加熱された温水を前記温水循環路内を循環させながら加熱部に送 る温水ポンプと、 前記ヒートポンプの吸熱部と前記冷却部とを循環し、前記吸熱部で冷水を冷却 させ、該冷水で前記冷却部の流体を冷却させる冷水循環路と、 前記吸熱部で冷却された冷水を前記冷水循環路内を循環させながら冷却部に送 る冷水ポンプと、 前記加熱部と冷却部との間の流路に、前記加熱部を通る前の流体をその加熱部 を通った流体とで熱交換させた後前記加熱部に通す熱交換器とを設けたことを特 徴とする。 In order to achieve the above object, the present invention provides a heating section for heating and sterilizing the fluid and a cooling section for cooling the heated fluid in a flow path of the fluid, and heating and cooling the heating section. A heat sterilizer for cooling a part with a heat pump, which circulates between the heat radiating part and the heating part of the heat pump, heats hot water in the heat radiating part, and heats the fluid in the heating part with the hot water. And a hot water pump that sends hot water heated in the heat radiating section to the heating section while circulating the hot water in the hot water circulating path, circulates the heat absorbing section and the cooling section of the heat pump, and cools water in the heat absorbing section. A cooling water circulation passage for cooling and cooling the fluid of the cooling portion with the cooling water; a cooling water pump for sending the cooling water cooled by the heat absorbing portion to the cooling portion while circulating in the cooling water circulation passage; and the heating portion, Between the cooling unit The road, the feature in that a heat exchanger through the heating section after heat exchange with the fluid passing through the heating section in front of the fluid through the heating portion.
【0010】[0010]
この考案は、上記構成により、放熱部で加熱された温水は温水ポンプによって 加熱部に送られて温水循環路内を循環していき、該温水が加熱部に流れてきた流 体を加熱していく。また、熱交換器で加熱部を通る前の流体をその加熱部を通っ た流体とで熱交換させた後加熱部に通す。 With this configuration, the hot water heated by the heat radiating unit is sent to the heating unit by the hot water pump and circulates in the hot water circulation path, and the warm water flowing to the heating unit heats the fluid. Go In addition, the fluid before passing through the heating section in the heat exchanger is heat-exchanged with the fluid passing through the heating section and then passed through the heating section.
【0011】 他方、吸熱部で冷却された冷水は冷水ポンプによって冷却部に送られながら冷 水循環路内を循環していき、この冷水が冷却部に流れてきた加熱された流体を冷 却していく。On the other hand, the cold water cooled in the heat absorbing portion is circulated in the cold water circulation path while being sent to the cooling portion by the cold water pump, and the cold water cools the heated fluid flowing to the cooling portion. Go
【0012】[0012]
以下、この考案に係る加熱殺菌装置の実施例を図面に基づいて説明する。 An embodiment of the heat sterilization apparatus according to the present invention will be described below with reference to the drawings.
【0013】 図1において、10は流路11に設けられた加熱部で、この加熱部10に流入 してくる例えば清酒(流体)を60度まで加熱して殺菌を行なうものである。1 2は熱交換器で、これは、加熱された清酒と交換コイル12aに流入した加熱前 の清酒とを熱交換させ、加熱前の清酒の温度を上昇させ、加熱された清酒の温度 を下げるものである。In FIG. 1, 10 is a heating unit provided in the flow path 11, for example, sake (fluid) flowing into the heating unit 10 is heated to 60 degrees to sterilize it. A heat exchanger 12 heat-exchanges the heated sake with the unheated sake flowing into the exchange coil 12a to raise the temperature of the unheated sake and lower the temperature of the heated sake. It is a thing.
【0014】 そして、交換コイル12aで温度上昇した清酒は加熱部10に流入するように なっている。13は加熱された清酒を所定温度(20度)まで冷却する冷却部、 14は冷却された清酒を容器(図示せず)に充填する充填部である。Then, the sake whose temperature has risen in the exchange coil 12a flows into the heating unit 10. 13 is a cooling unit for cooling the heated sake to a predetermined temperature (20 degrees), and 14 is a filling unit for charging the cooled sake into a container (not shown).
【0015】 S1は加熱部10で加熱された清酒の温度を検出する温度センサ、S2は冷却部 13で冷却された清酒の温度を検出する温度センサである。S 1 is a temperature sensor that detects the temperature of the sake that has been heated by the heating unit 10, and S 2 is a temperature sensor that detects the temperature of the sake that has been cooled by the cooling unit 13.
【0016】 21は温水槽で、この温水槽21と加熱部10のヒータ10aとは温水循環路 22で連通されており、温水ポンプ23によって温水槽21の温水が温水循環路 22を循環しながら加熱部10のヒータ10aへ送られるようになっている。ま た温水槽21と前記容器を洗浄する洗浄部(副加熱部)24のヒータ24aとは 温水循環路(副温水循環路)25で連通され、温水ポンプ(副温水ポンプ)26 によって温水槽21の温水が温水循環路25を循環しながら洗浄部24のヒータ 24aへ送られるようになっている。Reference numeral 21 denotes a hot water tank, and the hot water tank 21 and the heater 10 a of the heating unit 10 are communicated with each other by a hot water circulation path 22, and hot water of the hot water tank 21 is circulated through the hot water circulation path 22 by a hot water pump 23. It is adapted to be sent to the heater 10a of the heating unit 10. In addition, the hot water tank 21 and the heater 24a of the cleaning unit (sub-heating unit) 24 for cleaning the container are communicated with each other by a hot water circulation passage (sub-hot water circulation passage) 25, and a hot water pump (sub-hot water pump) 26 is used for the warm water tank 21 The hot water is sent to the heater 24a of the cleaning section 24 while circulating in the hot water circulation path 25.
【0017】 洗浄部24のヒータ24aでは、洗浄水を70度に加熱し、この加熱した洗浄 水で前記容器を洗浄するものである。S5は洗浄水の温度を検出する温度センサ である。The heater 24a of the cleaning unit 24 heats the cleaning water to 70 degrees and cleans the container with the heated cleaning water. S5 is a temperature sensor that detects the temperature of the washing water.
【0018】 温水槽21は、図2に示すように、連通管27によってヒートポンプ30の放 熱部31に連通されている。この放熱部31にはヒートポンプ30の凝縮器31 aが設けられており、この凝縮器31aの放熱によって放熱部31に流入する温水 を加熱していく。28は温水槽21の温水を放熱部31へ循環させる温水ポンプ であり、この循環により放熱部31で加熱された温水が温水槽21に送られ、温 水槽21の温水が75度〜80度まで高められる。As shown in FIG. 2, the hot water tank 21 is connected to a heat releasing portion 31 of the heat pump 30 by a communication pipe 27. The radiator 31 is provided with a condenser 31a of the heat pump 30. The heat released from the condenser 31a heats the hot water flowing into the radiator 31. 28 is a hot water pump that circulates the hot water in the hot water tank 21 to the heat radiating section 31, and the hot water heated in the heat radiating section 31 is sent to the hot water tank 21 by this circulation, and the hot water in the hot water tank 21 is from 75 degrees to 80 degrees. To be enhanced.
【0019】 32は冷水槽で、図1に示すように、この冷水槽32と冷却部13の冷却コイ ル13aとは循環路33とで連通されており、冷水ポンプ34によって冷水槽3 2の冷水が循環路33を循環しながら冷却部13の冷却コイル13aに送られる ようになっている。Reference numeral 32 denotes a cold water tank. As shown in FIG. 1, the cold water tank 32 and the cooling coil 13 a of the cooling unit 13 are connected to each other by a circulation path 33, and a cold water pump 34 is provided to cool the cold water tank 32. Cold water is sent to the cooling coil 13a of the cooling unit 13 while circulating in the circulation path 33.
【0020】 冷水槽32は、図2に示すように、連通管35によってヒートポンプ30の吸 熱部36に連通されている。この吸熱部36にはヒートポンプ30の蒸発器36 aが設けられており、この蒸発器36aの吸熱によって吸熱部36に流入される冷 水を冷却していく。37は冷水槽32の冷水を吸熱部36へ循環させる冷水ポン プであり、この循環により吸熱部36で冷却された冷水が冷水槽32に送られ、 冷水槽32の冷水の温度が10度〜15度に保たれる。As shown in FIG. 2, the cold water tank 32 is connected to a heat absorbing portion 36 of the heat pump 30 by a communication pipe 35. The heat absorbing section 36 is provided with an evaporator 36a of the heat pump 30, and the cold water flowing into the heat absorbing section 36 is cooled by the heat absorption of the evaporator 36a. Reference numeral 37 is a cold water pump for circulating the cold water in the cold water tank 32 to the heat absorbing section 36. By this circulation, the cold water cooled in the heat absorbing section 36 is sent to the cold water tank 32, and the temperature of the cold water in the cold water tank 32 is 10 degrees Celsius or higher. It is kept at 15 degrees.
【0021】 36bは吸熱部36に並列接続された蒸発器で、電磁切換弁38の切り換えに よってヒートポンプ30の冷媒を蒸発器36aに流すことにより、外気から熱を 吸熱するものである。この場合、冷水の冷却は行なわれない。39は送風ファン である。Reference numeral 36b denotes an evaporator connected in parallel to the heat absorbing portion 36, which absorbs heat from the outside air by flowing the refrigerant of the heat pump 30 to the evaporator 36a by switching the electromagnetic switching valve 38. In this case, cooling of cold water is not performed. 39 is a blower fan.
【0022】 31bは、放熱部31に並列接続された凝縮器で、切換弁41の切り換えによ ってヒートポンプ30の冷媒を凝縮器31bに流すことにより、凝縮器31bが放 熱する熱を外気に放熱させるものである。この場合、温水は加熱されない。42 は送風ファン、43は減圧弁、44は受液器、45は圧縮器、S3は温水槽の温 水の温度を検出する温水センサ、S4は冷却水の温度を検出する冷水センサであ る。Reference numeral 31b denotes a condenser connected in parallel to the heat radiating unit 31. By switching the switching valve 41 to flow the refrigerant of the heat pump 30 to the condenser 31b, the heat released by the condenser 31b is released to the outside air. To dissipate heat. In this case, the warm water is not heated. 42 is a blower fan, 43 is a pressure reducing valve, 44 is a liquid receiver, 45 is a compressor, S3 is a hot water sensor for detecting the temperature of hot water in the hot water tank, and S4 is a cold water sensor for detecting the temperature of cooling water. ..
【0023】 図3は、各センサS1〜S5の検出する温度に基づいて、各ポンプ23,26,2 8,34,37や電磁切換弁38,41を制御する制御系の構成を示したブロック 図である。FIG. 3 is a block diagram showing a configuration of a control system for controlling the pumps 23, 26, 28, 34, 37 and the electromagnetic switching valves 38, 41 based on the temperatures detected by the sensors S1 to S5. It is a figure.
【0024】 図3において、50はマイクロコンピュータなどからなる制御装置で、これは 、センサS1,S2が検出する温度が60度,20度となるように温水ポンプ23, 冷水ポンプ34を制御して循環する温水量,冷水量を調整する。In FIG. 3, reference numeral 50 denotes a control device including a microcomputer, which controls the hot water pump 23 and the cold water pump 34 so that the temperatures detected by the sensors S1 and S2 are 60 degrees and 20 degrees, respectively. Adjust the circulating hot water volume and cold water volume.
【0025】 また、制御装置50は、センサS3,S4が検出する温度が75度〜80度,10 度〜15度となるように、電磁切換弁41,38の切換を行なうものである。Further, the control device 50 switches the electromagnetic switching valves 41 and 38 so that the temperatures detected by the sensors S3 and S4 are 75 degrees to 80 degrees and 10 degrees to 15 degrees.
【0026】 次に、上記のように構成される実施例の加熱殺菌装置の作用について説明する 。Next, the operation of the heat sterilization apparatus of the embodiment configured as described above will be described.
【0027】 先ず、ヒートポンプ30やポンプを作動させて、温水槽21の温水を75度〜 80度まで高め、冷水槽の冷水を10度〜15度まで冷却する。この後、温水ポ ンプ23や冷水ポンプ34を作動させて、温水槽21の温水を加熱部10のヒー タ10aに送りながら循環させ、冷水槽32の冷水を冷却コイル13aに送りなが ら循環させて、清酒を流路11aに流入させる。First, the heat pump 30 and the pump are operated to raise the hot water in the hot water tank 21 to 75 to 80 degrees and cool the cold water in the cold water tank to 10 to 15 degrees. After that, the hot water pump 23 and the cold water pump 34 are operated to circulate the hot water in the hot water tank 21 while sending it to the heater 10a of the heating unit 10, and the cold water in the cold water tank 32 to the cooling coil 13a. Then, sake is made to flow into the flow path 11a.
【0028】 流路11aに流入した清酒は、熱交換器12の交換コイル12aを介して加熱部 10へ流入していく。加熱部10では、ヒータ10aによってその清酒が加熱さ れていく。この加熱された清酒は熱交換器12へ流入して交換コイル12aを通 る清酒と熱交換される。The sake that has flowed into the flow path 11 a flows into the heating section 10 via the exchange coil 12 a of the heat exchanger 12. In the heating unit 10, the sake is heated by the heater 10a. The heated sake flows into the heat exchanger 12 and is heat-exchanged with the sake passing through the exchange coil 12a.
【0029】 交換コイル12aを通る清酒は20度〜50度に加温されて加熱部10へ流入 し、ヒータ10aによって60度まで加熱され、殺菌が行なわれる。殺菌が行な われた清酒は熱交換器12で熱交換されて温度が低下される。温度低下した清酒 は、冷却部13へ流入していき、冷却コイル13aによって20度まで冷却され る。The sake passing through the exchange coil 12a is heated to 20 to 50 degrees and flows into the heating section 10, where it is heated to 60 degrees by the heater 10a and sterilized. The sterilized sake is heat-exchanged in the heat exchanger 12 to lower its temperature. The temperature-decreased sake flows into the cooling unit 13 and is cooled to 20 degrees by the cooling coil 13a.
【0030】 冷却された清酒は充填部14へ流入して容器(図示せず)に充填されていく。容 器は洗浄部24によって予め殺菌洗浄される。The cooled sake flows into the filling section 14 and is filled in a container (not shown). The container is previously sterilized and cleaned by the cleaning unit 24.
【0031】 ところで、加熱部10のヒータ10aで加熱される清酒は、熱交換器12で2 0度〜50度に加温されているので、加熱殺菌を行なう温度60度までの加熱に 必要な熱量は小さくてよく、加熱するのに大電力を必要としない。また、冷却部 13で冷却される清酒は、熱交換器12で温度が低下されているので、20度ま で冷却するのに大きな電力を必要としない。したがって、ヒートポンプ30は小 型の小電力用のものでよいことになる。ちなみに、熱交換器12を設置しない場 合と比較して約1/3以下の小電力のヒートポンプでよい。By the way, since the sake to be heated by the heater 10a of the heating unit 10 is heated to 20 to 50 degrees by the heat exchanger 12, it is necessary to heat the sake to a temperature of 60 degrees to perform heat sterilization. The amount of heat can be small and does not require a large amount of electric power to heat. Also, since the temperature of the sake cooled in the cooling unit 13 is lowered in the heat exchanger 12, it does not require a large amount of electric power to cool it to 20 degrees. Therefore, the heat pump 30 may be a small one for small electric power. By the way, compared with the case where the heat exchanger 12 is not installed, a heat pump with a small electric power of about 1/3 or less may be used.
【0032】 また、例えば、冷却水の温度が10度から数度上昇し、この結果、冷却部13 で冷却される清酒が20度より高い温度になると、制御装置50は冷水ポンプ3 4の回転力を上げ、冷却コイル13aに流れる冷水の量を増加させて清酒を20 度に冷却させる。このとき、制御装置50は冷水ポンプ34の回転力を上げるだ けなので、加熱部10の加熱に対して何等影響を及ばさない。Further, for example, when the temperature of the cooling water rises from 10 degrees to several degrees and as a result, the temperature of the sake cooled in the cooling section 13 becomes higher than 20 degrees, the control device 50 causes the cooling water pump 34 to rotate. The power is increased to increase the amount of cold water flowing through the cooling coil 13a to cool the sake to 20 degrees. At this time, since the control device 50 only needs to increase the rotational force of the cold water pump 34, it has no effect on the heating of the heating unit 10.
【0033】 逆に、温水槽21の温水が例えば80度から数度下がり、この結果、加熱部1 0で加熱した清酒の温度が60度以下になると、制御装置50は温水ポンプ23 の回転力を上げ、ヒータ10aに流れる温水の量を増加させて清酒の加熱温度を 60度に維持させる。このときも、制御装置50は温水ポンプ23の回転力を上 げるだけなので、冷却部13の冷却に対して何等影響を及ばさない。On the contrary, when the temperature of the hot water in the hot water tank 21 drops from 80 degrees to several degrees, and as a result, the temperature of the sake heated in the heating section 10 becomes 60 degrees or less, the control device 50 causes the hot water pump 23 to rotate. To raise the amount of hot water flowing to the heater 10a to maintain the heating temperature of sake at 60 degrees. At this time as well, the control device 50 only increases the rotational force of the hot water pump 23, and therefore has no effect on the cooling of the cooling unit 13.
【0034】 このように、加熱部10の温度制御と冷却部13の温度制御とを互いに独立し て行えるので、その温度制御は容易に行うことができる。As described above, since the temperature control of the heating unit 10 and the temperature control of the cooling unit 13 can be performed independently of each other, the temperature control can be easily performed.
【0035】 冷水槽32の冷水の温度が10〜15度の範囲内で、温水槽21の温水の温度 が75度以下に下がった場合には、ヒートポンプ30は加熱単独運転を行なう。 すなわち、電磁切換弁41を切り換えて冷媒を凝縮器31aに流し、凝縮器31a で温水に放熱させることにより温水槽21の温水の温度を75度から上げる。こ のとき、凝縮器31aを通過し冷却された冷媒を減圧弁43を通過することによ って減圧膨張させた後、電磁切換弁38によって蒸発器36bに流すとともに送 風ファン39を駆動し、蒸発器36bにて外気へ吸熱させて冷媒を蒸発させる。 そして、この蒸発した冷媒を圧縮器45へ送る。When the temperature of the cold water in the cold water tank 32 falls within the range of 10 to 15 degrees and the temperature of the hot water in the hot water tank 21 drops to 75 degrees or lower, the heat pump 30 performs the independent heating operation. That is, the electromagnetic switching valve 41 is switched to flow the refrigerant into the condenser 31a, and the condenser 31a radiates heat to the hot water to raise the temperature of the hot water in the hot water tank 21 from 75 degrees. At this time, the refrigerant that has passed through the condenser 31a and has been cooled is decompressed and expanded by passing through the pressure reducing valve 43, and then is made to flow to the evaporator 36b by the electromagnetic switching valve 38 and the blower fan 39 is driven. The evaporator 36b absorbs heat into the outside air to evaporate the refrigerant. Then, the evaporated refrigerant is sent to the compressor 45.
【0036】 また、温水槽21の温水温度が80度を超えたときには、ヒートポンプ30の 運転は停止させる。これによって、冷水槽32の冷水温度を10〜15度に保持 させたまま温水槽21の温水温度を75〜80度に低下させることができる。When the hot water temperature of the hot water tank 21 exceeds 80 degrees, the operation of the heat pump 30 is stopped. Thereby, the hot water temperature of the hot water tank 21 can be lowered to 75 to 80 degrees while keeping the cold water temperature of the cold water tank 32 at 10 to 15 degrees.
【0037】 反対に、温水槽21の温水の温度が75〜80度の範囲内で、冷水槽32の冷 水の温度が15度以上に上がった場合には、ヒートポンプ30は冷却単独運転を 行なう。すなわち、電磁切換弁41を切り換えて冷媒を凝縮器31bに流すとと もに送風ファン42を駆動し、凝縮器31bの熱を外気に放熱させて温水槽21 の温水の温度上昇を防止する。このとき、凝縮器31bを通過し冷却された冷媒 を減圧弁43を通過することによって減圧膨張させた後、電磁切換弁38によっ て蒸発器36aに流し、蒸発器36aにて冷水から吸熱して冷媒を蒸発させる。そ して、この蒸発した冷媒を圧縮器45へ送る。これらにより、冷水槽32の冷水 が冷却されるだけとなる。On the other hand, when the temperature of the hot water in the hot water tank 21 is within the range of 75 to 80 degrees and the temperature of the cold water in the cold water tank 32 rises to 15 degrees or higher, the heat pump 30 performs the independent cooling operation. .. That is, the electromagnetic switching valve 41 is switched to flow the refrigerant to the condenser 31b, and at the same time, the blower fan 42 is driven to radiate the heat of the condenser 31b to the outside air to prevent the temperature rise of the hot water in the hot water tank 21. At this time, the refrigerant that has cooled by passing through the condenser 31b is decompressed and expanded by passing through the pressure reducing valve 43, and then is made to flow to the evaporator 36a by the electromagnetic switching valve 38, and heat is absorbed from the cold water by the evaporator 36a. To evaporate the refrigerant. Then, the evaporated refrigerant is sent to the compressor 45. As a result, the cold water in the cold water tank 32 is only cooled.
【0038】 また、冷水槽32の冷水温度が10度以下となったときには、ヒートポンプ3 0の運転は停止させる。これによって、温水槽21の温水温度を75〜80度に 保持させたまま、冷水槽21の冷水温度を10〜15度に上昇させることができ る。When the cold water temperature of the cold water tank 32 becomes 10 degrees or lower, the operation of the heat pump 30 is stopped. As a result, the cold water temperature of the cold water tank 21 can be raised to 10 to 15 degrees while keeping the hot water temperature of the hot water tank 21 at 75 to 80 degrees.
【0039】 温水槽21の温水の温度が75度以下に下がり、また、冷却槽32の冷水の温 度が15度以上に上がった場合には、ヒートポンプ30は加熱・冷却同時運転を 行なう。すなわち、電磁切換弁41を切り換えて冷媒を凝縮器31aに流し凝縮 器31aで温水に放熱させることにより温水槽21の温水の温度を75〜80度 まで上昇させる。When the temperature of the hot water in the hot water tank 21 is lowered to 75 degrees or lower and the temperature of the cold water in the cooling tank 32 is raised to 15 degrees or higher, the heat pump 30 performs the heating / cooling simultaneous operation. That is, the electromagnetic switching valve 41 is switched to cause the refrigerant to flow into the condenser 31a and radiate heat to the warm water in the condenser 31a, thereby raising the temperature of the warm water in the warm water tank 21 to 75 to 80 degrees.
【0040】 このとき、凝縮器31aを通過し冷却された冷媒を減圧弁43を通過させて減 圧・膨張させ、この冷媒を電磁弁38によって蒸発器36aに流す。そして、蒸 発器36aにて冷水から吸熱して冷媒を蒸発させる。これにより冷水槽32の冷 水を冷却し、冷水の温度を10〜15度まで冷却させる。蒸発した冷媒は圧縮器 45へ送る。At this time, the refrigerant cooled by passing through the condenser 31 a is passed through the pressure reducing valve 43 to be depressurized / expanded, and this refrigerant is caused to flow to the evaporator 36 a by the electromagnetic valve 38. Then, the evaporator 36a absorbs heat from the cold water to evaporate the refrigerant. Thereby, the cold water in the cold water tank 32 is cooled, and the temperature of the cold water is cooled to 10 to 15 degrees. The evaporated refrigerant is sent to the compressor 45.
【0041】 また、冷水槽32の冷水温度が10度を低下したときには、電磁切り換弁38 を切り換えて冷媒を蒸発器36bへ流し、ヒートポンプ30を加熱単独運転へ移 行させる。When the cold water temperature of the cold water tank 32 drops to 10 degrees, the electromagnetic switching valve 38 is switched to allow the refrigerant to flow to the evaporator 36b, and the heat pump 30 is moved to the independent heating operation.
【0042】 逆に、温水槽21の温水温度が80度を超えたときには、電磁切り換弁41を 切り換えて冷媒を凝縮器31bへ流し、ヒートポンプ30を冷却単独運転へ移行 させる。On the contrary, when the temperature of the hot water in the hot water tank 21 exceeds 80 degrees, the electromagnetic switching valve 41 is switched to allow the refrigerant to flow to the condenser 31b, and the heat pump 30 is shifted to the cooling independent operation.
【0043】 このように、一台のヒートポンプ30の運転によって加熱と冷却を同時に行な うことができるので、効率的な運転が可能であり、投入電力量の省エネルギー化 を図ることができる。As described above, since heating and cooling can be performed at the same time by operating one heat pump 30, efficient operation is possible and energy consumption of input power can be reduced.
【0044】 また、温水槽21の温水はポンプによって洗浄部に送られて、洗浄水の加熱に 利用されるので、ヒートポンプから放熱される熱の有効利用が図られることとな る。また、温水槽21からパイプを引くだけで他の箇所に温水を供給することが できるので、非常に便利である。Further, since the hot water in the hot water tank 21 is sent to the cleaning unit by the pump and used for heating the cleaning water, the heat radiated from the heat pump can be effectively used. In addition, it is very convenient because hot water can be supplied to other places simply by pulling a pipe from the hot water tank 21.
【0045】 なお、実施例では、一段圧縮式ヒートポンプの例を示したが、温水75〜80 度、冷水10〜15度程度に加熱・冷却させるためのヒートポンプは、蒸発器と 凝縮器側の温度差が大きくて、実際には一段圧縮式ヒートポンプでは対応できな い。これに対応させるためには、低段圧縮器と高段圧縮器との2段圧縮を行い、 凝縮温度を高める。Although the example of the one-stage compression heat pump is shown in the embodiment, the heat pump for heating / cooling the hot water to about 75 to 80 ° C. and the cold water to about 10 to 15 ° is used for the temperature of the evaporator and the condenser side. The difference is so large that a single-stage compression heat pump cannot actually handle it. In order to deal with this, two-stage compression of a low-stage compressor and a high-stage compressor is performed to raise the condensation temperature.
【0046】 具体的には、図4に示すように、低段側冷凍サイクルと高段側冷凍サイクルに 同一の冷媒を用いる2段圧縮式ヒートポンプ、又は、2つの異なる冷媒を用いる 2元圧縮ヒートポンプを用いて対応する。Specifically, as shown in FIG. 4, a two-stage compression heat pump that uses the same refrigerant for the low-stage refrigeration cycle and a high-stage refrigeration cycle, or a dual compression heat pump that uses two different refrigerants. To respond.
【0047】 また、温水が60度以下では一段圧縮式ヒートポンプの適用で十分可能である 。Further, when the hot water is 60 degrees or less, the application of the single-stage compression heat pump is sufficient.
【0048】 上記実施例は、食品を加熱殺菌する場合について説明したが、これに限らず、 例えば、栽培養液の殺菌等にも利用できることは勿論である。In the above-mentioned embodiment, the case where the food is sterilized by heating has been described. However, the present invention is not limited to this, and it is needless to say that it can be used for sterilization of the nutrient solution for cultivation.
【0049】[0049]
この発明は、以上説明したように、温水循環路と冷水循環路と熱交換器等とを 設けたものであるから、ヒートポンプは熱交換器を設置しない場合と比較して約 1/3以下の小電力用のものでよく、しかも、加熱部の温度制御と冷却部の温度制 御とを互いに独立して行えるので、その温度制御は容易に行うことができる。ま た、副加熱部に温水を循環させるようにしたものであるから、熱の有効利用を図 ることができる。 As described above, the present invention is provided with the hot water circulation path, the cold water circulation path, the heat exchanger, etc., so that the heat pump has about 1/3 or less of the heat pump compared to the case where the heat exchanger is not installed. It may be for a small electric power, and the temperature control of the heating part and the temperature control of the cooling part can be performed independently of each other, so that the temperature control can be easily performed. Moreover, since the hot water is circulated in the sub-heating section, the heat can be effectively used.
【図1】この発明にかかわる加熱殺菌装置の構成を概略
的に示したブロック図、FIG. 1 is a block diagram schematically showing the configuration of a heat sterilization apparatus according to the present invention,
【図2】ヒートポンプの構成を概略的に示したブロック
図、FIG. 2 is a block diagram schematically showing the configuration of a heat pump,
【図3】加熱殺菌装置の制御系の構成を示したブロック
図、FIG. 3 is a block diagram showing a configuration of a control system of the heat sterilizer.
【図4】他の実施例の構成を示した説明図、FIG. 4 is an explanatory diagram showing the configuration of another embodiment,
【図5】従来の加熱殺菌装置の構成を示した説明図であ
る。FIG. 5 is an explanatory diagram showing a configuration of a conventional heat sterilization device.
10 加熱部 11 流路 12 熱交換器 13 冷却部 22 温水循環路 23 温水ポンプ 30 ヒートポンプ 31 放熱部 33 冷水循環路 34 冷水ポンプ 10 Heating Section 11 Flow Path 12 Heat Exchanger 13 Cooling Section 22 Hot Water Circulation Path 23 Hot Water Pump 30 Heat Pump 31 Heat Dissipation Section 33 Cold Water Circulation Path 34 Cold Water Pump
───────────────────────────────────────────────────── フロントページの続き (72)考案者 網本 邦広 香川県香川郡香川町大野2086−4 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kunihiro Amimoto 2086-4 Ono, Kagawa-cho, Kagawa-gun, Kagawa Prefecture
Claims (3)
殺菌する加熱部と、この加熱した流体を冷却する冷却部
とを設け、前記加熱部の加熱と冷却部の冷却をヒートポ
ンプで行なう加熱殺菌装置であって、 前記ヒートポンプの放熱部と前記加熱部とを循環し、前
記放熱部で温水を加熱させ、該温水で前記加熱部の流体
を加熱させる温水循環路と、 前記放熱部で加熱された温水を前記温水循環路内を循環
させながら加熱部に送る温水ポンプと、 前記ヒートポンプの吸熱部と前記冷却部とを循環し、前
記吸熱部で冷水を冷却させ、該冷水で前記冷却部の流体
を冷却させる冷水循環路と、 前記吸熱部で冷却された冷水を前記冷水循環路内を循環
させながら冷却部に送る冷水ポンプと、 前記加熱部と冷却部との間の流路に、前記加熱部を通る
前の流体をその加熱部を通った流体とで熱交換させた後
前記加熱部に通す熱交換器とを設けたことを特徴とする
加熱殺菌装置。1. A heating section for heating and sterilizing the fluid and a cooling section for cooling the heated fluid are provided in a flow path of the fluid, and heating of the heating section and cooling of the cooling section are performed by a heat pump. A heat sterilization device for performing the heat radiating part of the heat pump and the heating part, heating the hot water in the heat radiating part, and heating the fluid of the heating part with the hot water, and the heat radiating part. A hot water pump that sends hot water heated in the heating section while circulating the hot water in the hot water circulation path, circulates the heat absorbing section and the cooling section of the heat pump, cools cold water in the heat absorbing section, and cools the cold water in the cold water. A cold water circulation path for cooling the fluid in the cooling section, a cold water pump for sending the cold water cooled by the heat absorption section to the cooling section while circulating the cold water in the cold water circulation path, and a flow path between the heating section and the cooling section. Before passing through the heating section Heat sterilization apparatus characterized in that a heat exchanger through the body to the heating section after heat exchange with the fluid passing through the heating section.
槽と、前記吸熱部で冷却された冷水を貯える冷水槽とを
備え、前記温水ポンプは温水槽の温水を循環させ、前記
冷水ポンプは冷水槽の冷水を循環させることを特徴とす
る請求項1の加熱殺菌装置。2. A hot water tank for storing hot water heated by the heat radiating section, and a cold water tank for storing cold water cooled by the heat absorbing section, wherein the hot water pump circulates the hot water in the hot water tank and the cold water pump. The heat sterilizer according to claim 1, wherein the cold water in the cold water tank is circulated.
と、 この副加熱部と前記ヒートポンプの放熱部とを循環する
副温水循環路と、 前記放熱部で加熱される温水を前記副温水循環路内を循
環させる副温水ポンプとを設けたことを特徴とする請求
項1の加熱殺菌装置。3. A sub-heating unit that heats something other than the fluid, a sub-hot water circulating path that circulates the sub-heating unit and the heat radiating unit of the heat pump, and hot water heated by the heat radiating unit. The heat sterilizer according to claim 1, further comprising a sub-hot water pump that circulates in the circulation path.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991100492U JPH0753519Y2 (en) | 1991-12-05 | 1991-12-05 | Heat sterilizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP1991100492U JPH0753519Y2 (en) | 1991-12-05 | 1991-12-05 | Heat sterilizer |
Publications (2)
Publication Number | Publication Date |
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JPH0551088U true JPH0551088U (en) | 1993-07-09 |
JPH0753519Y2 JPH0753519Y2 (en) | 1995-12-13 |
Family
ID=14275433
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JP1991100492U Expired - Lifetime JPH0753519Y2 (en) | 1991-12-05 | 1991-12-05 | Heat sterilizer |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007202446A (en) * | 2006-01-31 | 2007-08-16 | Kansai Electric Power Co Inc:The | Heating/cooling device for sterilization |
JP2011255952A (en) * | 2010-06-11 | 2011-12-22 | Suntory Holdings Ltd | Heating sterilization system |
JP2012503482A (en) * | 2008-09-25 | 2012-02-09 | リサーチ アンド デベロップメント システムズ リミテッド | Heat exchange and transport system for retort processing equipment |
JP2012073013A (en) * | 2010-02-23 | 2012-04-12 | Chubu Electric Power Co Inc | Heating and cooling device |
JP2012187037A (en) * | 2011-03-10 | 2012-10-04 | Tokyo Electric Power Co Inc:The | Sterilization system |
JP2012191910A (en) * | 2011-03-17 | 2012-10-11 | Tokyo Electric Power Co Inc:The | Sterilization system |
JP2016538040A (en) * | 2013-11-12 | 2016-12-08 | カーハーエス・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング | Method and equipment for pasteurizing products in containers |
CN118408336A (en) * | 2024-07-01 | 2024-07-30 | 珠海格力电器股份有限公司 | Disinfection storage process system and control method thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60182950A (en) * | 1984-03-02 | 1985-09-18 | 三菱電機株式会社 | Sterilization apparatus |
JPS62261872A (en) * | 1986-05-07 | 1987-11-14 | コニカ株式会社 | Manufacture of heating medium by heat pump system |
-
1991
- 1991-12-05 JP JP1991100492U patent/JPH0753519Y2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60182950A (en) * | 1984-03-02 | 1985-09-18 | 三菱電機株式会社 | Sterilization apparatus |
JPS62261872A (en) * | 1986-05-07 | 1987-11-14 | コニカ株式会社 | Manufacture of heating medium by heat pump system |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007202446A (en) * | 2006-01-31 | 2007-08-16 | Kansai Electric Power Co Inc:The | Heating/cooling device for sterilization |
JP4587964B2 (en) * | 2006-01-31 | 2010-11-24 | 関西電力株式会社 | Heating / cooling device for sterilization |
JP2012503482A (en) * | 2008-09-25 | 2012-02-09 | リサーチ アンド デベロップメント システムズ リミテッド | Heat exchange and transport system for retort processing equipment |
JP2012073013A (en) * | 2010-02-23 | 2012-04-12 | Chubu Electric Power Co Inc | Heating and cooling device |
JP2011255952A (en) * | 2010-06-11 | 2011-12-22 | Suntory Holdings Ltd | Heating sterilization system |
JP2012187037A (en) * | 2011-03-10 | 2012-10-04 | Tokyo Electric Power Co Inc:The | Sterilization system |
JP2012191910A (en) * | 2011-03-17 | 2012-10-11 | Tokyo Electric Power Co Inc:The | Sterilization system |
JP2016538040A (en) * | 2013-11-12 | 2016-12-08 | カーハーエス・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング | Method and equipment for pasteurizing products in containers |
CN118408336A (en) * | 2024-07-01 | 2024-07-30 | 珠海格力电器股份有限公司 | Disinfection storage process system and control method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH0753519Y2 (en) | 1995-12-13 |
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