JP4951769B2 - Full container heat treatment apparatus and method - Google Patents

Full container heat treatment apparatus and method Download PDF

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JP4951769B2
JP4951769B2 JP2007182649A JP2007182649A JP4951769B2 JP 4951769 B2 JP4951769 B2 JP 4951769B2 JP 2007182649 A JP2007182649 A JP 2007182649A JP 2007182649 A JP2007182649 A JP 2007182649A JP 4951769 B2 JP4951769 B2 JP 4951769B2
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hot water
temperature
pipe
water tank
water
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JP2009018836A (en
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健良 原田
健二 西田
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Mitsubishi Heavy Industries Machinery Systems Co Ltd
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Mitsubishi Heavy Industries Food and Packaging Machinery Co Ltd
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Description

本発明は、容器に飲料等を充填済みの実入り容器を搬送中に容器と容器内の液体を加熱又は冷却処理する温度処理装置に関し、特に実入り容器を順次高温に加熱し容器温度が設定温度に達した後,順次常温まで冷却させる殺菌処理(パストライザー処理)と低温の実入り容器を30℃付近まで加熱する加温処理(ウォーマー処理)に切換えることができる実入り容器熱処理装置及び方法に関する。   The present invention relates to a temperature processing apparatus that heats or cools a container and a liquid in the container while the container is filled with a beverage or the like, and in particular, heats the container and sequentially heats the container to a set temperature. The present invention relates to an actual container heat treatment apparatus and method that can be switched to a sterilization process (path trizer process) for cooling to room temperature after the temperature has reached, and a heating process (warmer process) for heating a low temperature actual container to around 30 ° C.

パストライザー(高温殺菌処理装置)は、実入り容器を順次高温に加熱し、その後順次冷却できるように、容器が通過する各シャワー槽の水温と容器の通過時間を設定してある殺菌処理装置であり、特許文献1(図1)で示す従来例のパストライザーは、熱エネルギーの消費を節約するために、装置の入口から搬入される容器の緩い加熱を行う第1の散水ノズルの散水を集める第1の貯水タンクの水を後段の第6の冷却用散水ノズルへ回流し、この冷却用散水を集めた第6の貯水タンクの水を第1の散水ノズルへ回流するようにしたもので、第1の貯水タンクの水を送り出すポンプは可変流量ポンプとし、このポンプから第6の散水ノズルへの配管に水温を調整する熱交換機と水量比を調整できる開度可変の三方弁が設置されている。   Pastorizer (high-temperature sterilization treatment device) is a sterilization treatment device that sets the water temperature of each shower tank through which the container passes and the passage time of the container so that the actual container can be heated to high temperature sequentially and then cooled sequentially. The conventional path riser shown in Patent Document 1 (FIG. 1) collects water from the first watering nozzle that loosely heats a container carried in from the inlet of the apparatus in order to save heat energy consumption. The water in the first water storage tank is circulated to the sixth cooling water spray nozzle, and the water in the sixth water storage tank that collects the water spray for cooling is circulated to the first water spray nozzle. The pump that pumps out the water in one storage tank is a variable flow pump, and a heat exchanger that adjusts the water temperature and a three-way valve that can adjust the water amount ratio are installed in the pipe from this pump to the sixth watering nozzle. .

このパストライザーの加熱工程を切換えて、低温の実入り容器を30℃付近まで加熱する容器ウォーマーとしての加温処理をするには、高温水の散水を止め、1部の貯水タンクの水温をウォーマー用に設定しその温度を保持しながら温水を回流させて運転すればよい。   To change the heating process of this paste riser and heat the container as a warmer that heats low temperature containers up to around 30 ° C, stop the watering of hot water and use the water temperature of one part of the water storage tank for the warmer. It is only necessary to operate by circulating hot water while maintaining the temperature.

また、特許文献2(図2)で示す従来例のウォーマーは、単数、または、複数の散水ノズルと貯水タンクの組み合わせたもので、温水を温度調整しながら回流させる専用の容器温度処理装置である。   The conventional warmer shown in Patent Document 2 (FIG. 2) is a single or a combination of a plurality of watering nozzles and a water storage tank, and is a dedicated container temperature processing device that circulates hot water while adjusting the temperature. .

特許文献3(第2図、第3図)は、パストライザーの温水循環系統の模式図(図10)と、パストライザーの各水槽内の水温と容器の温度を示す線図(図11)を説明している。図10によりパストライザー1の温水、高温水の循環系統の説明をする。
本体上2と本体下3で囲われた筺体の中に、入口側の前段の本体上2にノズル群6A、6B、6C、6D、6E、6Fが設置され、本体下3の前段にノズル群6A、6Bからの温水の散水を受けて集める温水槽4A、4B、中段にノズル群6C、6Dからの高温水の散水を受けて集める高温水槽4C、4D、後段にノズル群6E、6Fからの冷却水の散水を受けて集める冷却用温水槽4E、4Fを配置し、実入り容器7を連続搬送する容器コンベア5を備えた構成である。
Patent Document 3 (FIGS. 2 and 3) shows a schematic diagram (FIG. 10) of a hot water circulation system of a path riser, and a diagram (FIG. 11) showing a water temperature and a container temperature in each water tank of the path riser. Explains. The circulation system of the hot water and high temperature water of the path riser 1 will be described with reference to FIG.
Nozzle groups 6A, 6B, 6C, 6D, 6E, and 6F are installed in the front upper body 2 on the inlet side in the casing surrounded by the upper body 2 and the lower body 3. The hot water tanks 4A and 4B that receive and collect hot water sprinkling from 6A and 6B, the high temperature water tanks 4C and 4D that receive and collect hot water sprinkling from the nozzle groups 6C and 6D in the middle stage, and the nozzle groups 6E and 6F in the rear stage. It is the structure provided with the container conveyor 5 which arrange | positions the hot water tank 4E and 4F for cooling which receives and collects the sprinkling of cooling water, and conveys the container 7 with a fruit continuously.

各水槽4A〜4Fの温度処理水は、それぞれ配管12A〜12Fでポンプ11A〜11Fへ送られ、ポンプ11A〜11Fの出口配管13A〜13Fにはそれぞれの配管内の水温(それぞれの配管が繋がる温水槽の水温)を検出する温度センサT1、T2、T3、T4、T5、T6を備えている。ポンプ11Aの出口配管13Aはノズル群6Fへ繋がり、ポンプ11Bの出口配管13Bはノズル群6Eへ繋がり、ポンプ11Eの出口配管13Eはノズル群6Bへ繋がり、ポンプ11Fの出口配管13Fはノズル群6Aへ繋がっている。ポンプ11Cの出口配管13Cはノズル群6Cへ繋がり、ポンプ11Dの出口配管13Dはノズル群6Dへ繋がっている。また、高温の加熱用スチーム供給配管16からスチームを各水槽4A〜4Fへ取り込むスチーム供給弁15A、15B、15C、15D、15E、15Fを備えている。   The temperature-treated water in each of the water tanks 4A to 4F is sent to the pumps 11A to 11F through the pipes 12A to 12F, respectively, and the outlet pipes 13A to 13F of the pumps 11A to 11F are supplied with water temperatures (temperatures connected to the respective pipes). Temperature sensors T1, T2, T3, T4, T5, and T6 for detecting the water temperature of the water tank are provided. The outlet pipe 13A of the pump 11A is connected to the nozzle group 6F, the outlet pipe 13B of the pump 11B is connected to the nozzle group 6E, the outlet pipe 13E of the pump 11E is connected to the nozzle group 6B, and the outlet pipe 13F of the pump 11F is connected to the nozzle group 6A. It is connected. The outlet piping 13C of the pump 11C is connected to the nozzle group 6C, and the outlet piping 13D of the pump 11D is connected to the nozzle group 6D. Moreover, the steam supply valve 15A, 15B, 15C, 15D, 15E, 15F which takes in steam into each water tank 4A-4F from the high temperature heating steam supply piping 16 is provided.

制御装置25には各水槽4A〜4Fの水温の設定値が記憶されている。制御装置25に内蔵するCPU(中央処理ユニット)において、各温度センサT1、T2、T3、T4、T5、T6の検出信号を各水槽4A〜4Fの水温の設定値と比較してその設定値になるようにスチーム供給弁15A〜15Fの開閉を指示し、スチームで処理水を直接、又は間接加熱する。   The control device 25 stores a set value of the water temperature of each of the water tanks 4A to 4F. In the CPU (central processing unit) built in the control device 25, the detection signal of each temperature sensor T1, T2, T3, T4, T5, T6 is compared with the set value of the water temperature of each of the water tanks 4A to 4F to the set value. The steam supply valves 15A to 15F are instructed to open and close, and the treated water is directly or indirectly heated with steam.

パストライザー1による実入り容器7のパストライザー処理について説明する(図10、図11参照)。容器コンベア5により連続搬送された実入り容器7は、温水槽4Aと4Bの上部の予熱ゾーンに入り、ノズル群6Aの約30℃のシャワーとノズル群6Bよりの約40℃のシャワーを浴びて緩加熱され実入り容器7の温度は約30℃まで温められる。次いで、実入り容器7は高温水槽4C、4Dの加熱ゾーンに入り、ノズル群6Cの約65℃のシャワー、ノズル群6Dの約60℃のシャワーを浴びて60℃に加熱され30〜40分間その温度を維持し、次の冷却用温水槽4E、4Fが置かれた冷却ゾーンへ送られ、ノズル群6Eの約40℃の温水シャワーとノズル群6Fの約25℃のシャワーを浴びて約30℃に冷却され、機外に送り出される。   A description will be given of the path trizer processing of the actual container 7 by the path trizer 1 (see FIGS. 10 and 11). The actual container 7 continuously conveyed by the container conveyor 5 enters the preheating zone at the upper part of the hot water tanks 4A and 4B and takes a shower of about 30 ° C. from the nozzle group 6A and a shower of about 40 ° C. from the nozzle group 6B. The temperature of the actual container 7 is heated to about 30 ° C. Next, the actual container 7 enters the heating zone of the high temperature water tanks 4C, 4D, and is heated to 60 ° C. by taking a shower of about 65 ° C. of the nozzle group 6C and a shower of about 60 ° C. of the nozzle group 6D, and the temperature is kept for 30-40 minutes. And is sent to a cooling zone in which the next cooling hot water tanks 4E and 4F are placed, and takes about 40 ° C. hot water shower of the nozzle group 6E and about 25 ° C. shower of the nozzle group 6F to about 30 ° C. It is cooled and sent out of the machine.

温水槽4Aに回収された温水は温度調整されてノズル群6Fに回流し、冷却用温水槽4Fに回収された温水は温度調整されてノズル群6Aに回流される。また、温水槽4Bに回収された温水は温度調整されてノズル群6Eに回流し、冷却用温水槽4Eに回収された温水は温度調整されてノズル群6Bに回流される。高温水槽4Cに回収された高温水は温度調整されてノズル群6Cに循環し、高温水槽4Dに回収された高温水は温度調整されてノズル群6Dに循環する。   The temperature of the hot water collected in the hot water tank 4A is adjusted and circulated to the nozzle group 6F, and the temperature of the hot water collected in the hot water tank 4F for cooling is adjusted and circulated to the nozzle group 6A. The temperature of the hot water collected in the hot water tank 4B is adjusted and circulated to the nozzle group 6E, and the temperature of the hot water collected in the cooling hot water tank 4E is adjusted and circulated to the nozzle group 6B. The temperature of the high temperature water collected in the high temperature water tank 4C is adjusted and circulated to the nozzle group 6C, and the temperature of the high temperature water collected in the high temperature water tank 4D is adjusted and circulated to the nozzle group 6D.

炭酸ガス飲料のように、0℃近い温度で容器に充填したものは直ぐに容器周囲の空気に含まれる水蒸気がコンデンスして容器周囲に付着するので、ラインの流れのまま早急に箱詰めすることは不適当であり、実入り容器を早く常温まで温めるために、工場設備の一つであるパストライザーのウォーマーへの転用が求められる。   As in the case of a carbon dioxide beverage, when the container is filled at a temperature close to 0 ° C, water vapor contained in the air around the container immediately condenses and adheres to the container. It is appropriate, and in order to quickly warm the actual container to room temperature, it is required to divert the Pastoriser, which is one of the factory equipment, to a warmer.

特開2006−145139号公報(図1)JP 2006-145139 A (FIG. 1) 特開2002−12208号公報(図1)Japanese Patent Laid-Open No. 2002-12208 (FIG. 1) 実公平4−9289(第2図、第3図)4-9289 (Figures 2 and 3)

従来のパストライザーの約60℃まで高温加熱する処理を、低温の実入り容器を30℃付近まで加熱する容器ウォーマーとしての加温処理に切換えるときには、高温処理槽の高温水を排水し、常温の水を供給し、加熱用蒸気を供給する等の作業が必要であり、相当な人工コストと時間がかかる。また、高温水の排水により高温水の保持する大量の熱エネルギーのロスを生じるという問題がある。
本発明は、パストライザーの加熱工程の運転後に、同設備をウォーマーとしての加温処理に切換えるときに、多くの手間を掛けることなく、熱エネルギーのロスが少なくなるような加温装置と、切換運転の方法を提供することを目的とする。
When switching the conventional high temperature heating process to about 60 ° C to a warming process as a container warmer that heats low temperature containers up to about 30 ° C, drain the high temperature water from the high temperature processing tank, Work, such as supplying steam for heating and supplying steam for heating, and requires considerable artificial cost and time. In addition, there is a problem that a large amount of heat energy retained by the high temperature water is lost due to the drainage of the high temperature water.
The present invention provides a heating device that reduces the loss of heat energy without much trouble when switching to the warming treatment as a warmer after the operation of the heating process of the path riser, and switching. The purpose is to provide a method of driving.

上記の問題点に対し、本発明は以下の各手段により課題の解決を図る。
(1)第1の手段の実入り容器熱処理装置は、
前段に温水槽、中段に高温水槽、後段に冷却用温水槽を配置し、実入り容器を連続搬送中に容器毎中身の液体を加熱又は冷却処理するパストライザー装置であって、各槽の水温を温度調整する温度センサとスチーム供給弁を備え、前段の温水槽の温水を温度調整して温水ポンプにより後段の温水ノズル配管へ送り出し、後段の温水槽の温水を温度調整して温水ポンプにより前段の温水ノズル配管へ回流する循環系と、中段槽高温水循環系に高温水ポンプと高温水循環配管と高温水ノズル循環配管を備えたパストライザー処理装置において、前段の温水槽の温水を同じ温水槽上の温水ノズル配管へ回流バイパスするバイパス配管と、該配管に設置されたバイパス開閉弁と、同配管から後段の温水ノズルへの循環配管を遮断する開閉弁と、前記前段のノズル配管へ温水を送り出す後段の温水ポンプの配管上に該ポンプへ向う流れを阻止する逆止弁を備えることによりパストライザーと容器ウォーマーを兼用できるようにしたことを特徴とする。
With respect to the above problems, the present invention aims to solve the problems by the following means.
(1) The actual container heat treatment apparatus of the first means is:
A hot water tank in the front stage, a hot water tank in the middle stage, and a hot water tank for cooling in the rear stage, which is a pastoriser device that heats or cools the liquid in each container while continuously transporting the actual containers, It is equipped with a temperature sensor for adjusting the temperature and a steam supply valve, adjusts the temperature of the hot water in the preceding hot water tank, sends it to the hot water nozzle pipe by the hot water pump, adjusts the temperature of the hot water in the latter hot water tank, In a path riser treatment device equipped with a circulation system that circulates to the hot water nozzle pipe and a high temperature water pump, high temperature water circulation pipe, and high temperature water nozzle circulation pipe in the middle tank high temperature water circulation system, the warm water in the previous stage water tank is on the same hot water tank. A bypass pipe for circulating bypass to the hot water nozzle pipe, a bypass on-off valve installed in the pipe, an on-off valve for shutting off the circulation pipe from the pipe to the subsequent hot water nozzle, Characterized in that to allow shared with pasteurizer and the container Warmer by on the pipe downstream of the hot water pump for feeding hot water into the nozzle pipe comprising a check valve which prevents the flow towards the said pump.

(2)第2の手段の実入り容器熱処理装置は、上記(1)の実入り容器熱処理装置において、中段の高温水ポンプをインバータ制御モータにより駆動される可変吐出量ポンプとし、該可変吐出量ポンプの出口配管から前段の温水槽へ通じるバイパス配管と、該バイパス配管上に設置した開閉弁と、前記バイパス配管の分岐点より先の温水配管に設置した開閉弁とを追加してなることを特徴とする。   (2) The actual container heat treatment apparatus of the second means is the actual container heat treatment apparatus of (1) described above, wherein the middle-stage high-temperature water pump is a variable discharge pump driven by an inverter control motor, and the variable discharge pump A bypass pipe that leads from the outlet pipe to the preceding hot water tank, an on-off valve installed on the bypass pipe, and an on-off valve installed on the hot water pipe beyond the branch point of the bypass pipe To do.

(3)第3の手段の実入り容器熱処理方法は、上記(1)の実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、中段、後段の高温水以降の処理水の加熱及び循環を止め、処理装置入口側の温水槽のノズル配管に前記バイパス配管より同じ温水槽の温水を回流し、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記温水槽内の加熱用スチームの流量を制御することを特徴とする。   (3) The third means of the actual container heat treatment method uses the actual container heat treatment apparatus of (1) above to switch the low temperature actual container from the warmer process to the warmer process after the middle stage and the latter stage of the high temperature water. Stop the heating and circulation of the treated water, circulate the warm water in the same hot water tank from the bypass pipe to the nozzle pipe of the hot water tank on the treatment equipment inlet side, and the temperature detected by the temperature sensor installed in the hot water circulation pipe becomes the set value Thus, the flow rate of the steam for heating in the hot water tank is controlled.

(4)第4の手段の実入り容器熱処理方法は、上記(2)の実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、前段、中段、後段の処理水の加熱スチームを止め、後段の温水ポンプを停止し、前記バイパス配管の分岐点より先の温水配管の開閉弁を閉じ、前記バイパス配管上の開閉弁を開き、前記可変吐出量ポンプより吐出する高温水を前段の温水槽に送り込み、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御し、高温水槽の水温が加温槽内の水温まで下がったときバイパス配管の高温水流入を閉じ、前段の温水槽用のスチームを通にして温水槽の循環と温水温度調整に移行することを特徴とする。   (4) The fourth means of the actual container heat treatment method uses the above-described actual container heat treatment apparatus (2) to switch the low temperature actual container from the warmer process to the warmer process when the first stage, middle stage and rear stage treatment water is used. The heating steam is stopped, the subsequent hot water pump is stopped, the open / close valve of the hot water pipe before the branch point of the bypass pipe is closed, the open / close valve on the bypass pipe is opened, and the high temperature discharged from the variable discharge pump The amount of water discharged from the variable discharge pump is controlled so that the temperature detected by the temperature sensor installed in the hot water circulation piping is set to the preset temperature, and the water temperature in the high-temperature water tank is kept in the warming tank. When the water temperature drops to the water temperature, the high-temperature water inflow of the bypass pipe is closed, and the process moves to the circulation of the hot water tank and the hot water temperature adjustment through the steam for the hot water tank in the previous stage.

(5)第5の手段の実入り容器熱処理方法は、上記(4)の実入り容器熱処理方法において、中段の高温水槽の高温水を加熱するスチームの供給弁を開閉して高温水の温度がパストライザー稼動時の温度を維持するように制御し、前段の温水槽の温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御して、加温処理からパストライザー処理へ切換られるようにしたことを特徴とする。   (5) The fifth means of the actual container heat treatment method is the same as the above-mentioned (4) actual container heat treatment method, wherein the steam supply valve for heating the high temperature water in the middle high temperature water tank is opened and closed so that the temperature of the high temperature water Control to maintain the temperature at the time of operation, and control the discharge amount of the variable discharge pump so that the temperature detected by the temperature sensor installed in the hot water circulation pipe of the preceding stage hot water tank becomes the set value, It is characterized in that the heating process can be switched to the path riser process.

(6)第6の手段の実入り容器熱処理装置は、前段に温水槽、中段に高温水槽、後段に冷却用温水槽を配置し、実入り容器を連続搬送中に容器毎中身の液体を加熱又は冷却処理するパストライザー装置であって、各槽の水温を温度調整する温度センサとスチーム供給弁を備え、前段の温水槽の温水を温度調整して温水ポンプにより後段の温水ノズル配管へ送り出し、後段の温水槽の温水を温度調整して温水ポンプにより前段の温水ノズル配管へ回流する循環系と、中段槽高温水循環系に高温水ポンプと高温水循環配管と高温水ノズル循環配管を備えたパストライザー処理装置において、後段の温水槽の温水を同じ温水槽上の温水ノズル配管へ回流バイパスするバイパス配管と、該配管に設置されたバイパス開閉弁と、同配管から前段の温水ノズルへの循環配管を遮断する開閉弁と、前記後段のノズル配管へ温水を送り出す前段の温水ポンプの配管上に該ポンプへ向う流れを阻止する逆止弁を備えることによりパストライザーと容器ウォーマーを兼用できるようにしたことを特徴とする。   (6) The sixth means of the actual container heat treatment apparatus has a warm water tank in the front stage, a high temperature water tank in the middle stage, and a warm water tank for cooling in the latter stage, and heats or cools the liquid in each container while the actual container is continuously transported. This is a path riser device for processing, which is equipped with a temperature sensor for adjusting the water temperature of each tank and a steam supply valve, adjusts the temperature of the hot water tank in the previous stage, and sends it to the subsequent hot water nozzle pipe by the hot water pump. A path system that adjusts the temperature of hot water in the hot water tank and circulates it through the hot water pump to the preceding hot water nozzle pipe, and a high-temperature water pump, high-temperature water circulation pipe, and high-temperature water nozzle circulation pipe in the middle-stage high-temperature water circulation system , A bypass pipe that circulates and bypasses the hot water in the subsequent hot water tank to the hot water nozzle pipe on the same hot water tank, a bypass on-off valve installed in the pipe, The on-off valve for shutting off the circulation pipe to the pipe and the check valve for preventing the flow toward the pump on the pipe of the preceding stage hot water pump for sending the hot water to the latter nozzle pipe It is characterized by the fact that it can be used for both purposes.

(7)第7の手段の実入り容器熱処理装置は、上記(6)の実入り容器熱処理装置において、中段の高温水ポンプをインバータ制御モータにより駆動される可変吐出量ポンプとし、該可変吐出量ポンプの出口配管から後段の温水槽へ通じるバイパス配管と、該バイパス配管上に設置した開閉弁と、前記バイパス配管の分岐点より先の温水配管に設置した開閉弁とを追加してなることを特徴とする。   (7) The actual container heat treatment apparatus according to the seventh means is the actual container heat treatment apparatus according to (6), wherein the middle-stage high-temperature water pump is a variable discharge pump driven by an inverter control motor, and the variable discharge pump A bypass pipe that leads from the outlet pipe to the subsequent hot water tank, an on-off valve installed on the bypass pipe, and an on-off valve installed on the hot water pipe beyond the branch point of the bypass pipe To do.

(8)第8の手段の実入り容器熱処理方法は、上記(6)の実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、前段、中段の高温水以降の処理水の加熱及び循環を止め、後段の温水槽のノズル配管に前記バイパス配管より同じ温水槽の温水を回流し、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記温水槽内の加熱用スチームの流量を制御することを特徴とする。   (8) The actual container heat treatment method of the eighth means uses the actual container heat treatment apparatus of (6) above, and when the low temperature actual container is switched from the warmer process to the warmer process, Stop the heating and circulation of the treated water, circulate the hot water of the same hot water tank from the bypass pipe to the nozzle pipe of the subsequent hot water tank, and the temperature detected by the temperature sensor installed in the hot water circulation pipe becomes the set value, The flow rate of the steam for heating in the hot water tank is controlled.

(9)第9の手段の実入り容器熱処理方法は、上記(7)の実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、前段、中段、後段の処理水の加熱スチームを止め、前段の温水ポンプを停止し、前記バイパス配管の分岐点より先の温水配管の開閉弁を閉じ、前記バイパス配管上の開閉弁を開き、前記可変吐出量ポンプより吐出する高温水を後段の温水槽に送り込み、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御し、高温水槽の水温が加温槽内の水温まで下がったときバイパス配管の高温水流入を閉じ、後段の温水槽用のスチームを通にして温水槽の循環と温水温度調整に移行することを特徴とする。   (9) The ninth means of the actual container heat treatment method uses the actual container heat treatment apparatus described in (7) above, and when the low temperature actual container is switched from the pasterizer process to the warmer process, the pre-stage, middle-stage, and post-stage treated water. The heating steam is stopped, the preceding hot water pump is stopped, the open / close valve of the hot water pipe before the branch point of the bypass pipe is closed, the open / close valve on the bypass pipe is opened, and the high temperature discharged from the variable discharge pump Water is sent to the subsequent hot water tank, and the discharge amount of the variable discharge pump is controlled so that the temperature detected by the temperature sensor installed in the hot water circulation pipe becomes the set value. When the water temperature drops to the water temperature, the high-temperature water inflow of the bypass pipe is closed, and the process moves to the circulation of the hot water tank and the hot water temperature adjustment through the steam for the hot water tank in the subsequent stage.

(10)第10の手段の実入り容器熱処理方法は、上記(9)に記載する実入り容器熱処理方法において、中段の高温水槽の高温水を加熱するスチーム供給弁を開閉して高温水の温度がパストライザー稼動時の温度を維持するように制御し、後段の温水槽の温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御して、加温処理からパストライザー処理へ切換られるようにしたことを特徴とする。   (10) The actual container heat treatment method according to the tenth means is the actual container heat treatment method described in (9) above, wherein the steam supply valve for heating the high-temperature water in the middle high-temperature water tank is opened and closed so that the temperature of the high-temperature water is past. Control to maintain the temperature when the riser is operating, and control the discharge rate of the variable discharge pump so that the temperature detected by the temperature sensor installed in the hot water circulation pipe of the subsequent hot water tank becomes the set value Further, the present invention is characterized in that the heating process can be switched to the path trizer process.

請求項1に係わる発明は上記第1の手段の実入り容器熱処理装置であり、この容器熱処理装置を用いて請求項3に係わる発明の上記第3の手段の実入り容器熱処理方法を行えば、実入り容器を高温に加熱し冷却させるパストライザー処理と、低温の実入り容器を30℃近辺まで加温するウォーマー処理とを手間をとらず、容易に切換えることができる。   The invention according to claim 1 is an actual container heat treatment apparatus according to the first means. If the container heat treatment method according to the third means according to the invention according to claim 3 is performed using the container heat treatment apparatus, the actual container is treated. It is possible to easily switch between a pasterizer process that heats and cools the container to a high temperature and a warmer process that heats a low-temperature actual container up to about 30 ° C. without taking time and effort.

請求項2に係わる発明は上記第2の手段の容器熱処理装置であり、この容器処理装置を用いた請求項4に係る発明の上記第4の手段の実入り容器熱処理方法を行うことにより、パストライザー処理からウォーマー処理に切換えるとき、容器に散布する温水温の調整に中段の高温槽よりバイパス配管で高温水を混入するようにしているので、処理水の熱エネルギーの有効利用ができる。   The invention according to claim 2 is the container heat treatment apparatus according to the second means, and by performing the actual container heat treatment method according to the fourth means according to the invention according to claim 4 using this container treatment apparatus, When switching from the treatment to the warmer treatment, high temperature water is mixed in the bypass pipe from the middle high temperature tank to adjust the temperature of the warm water sprayed on the container, so that the thermal energy of the treated water can be effectively used.

請求項5に係わる発明は、上記第5の手段の実入り容器熱処理方法であり、上記第4の手段と同じ効果を有すると同時に、ウォーマー処理からパストライザー処理に容易に切換えて戻すことができる。   The invention according to claim 5 is the actual container heat treatment method of the fifth means, and has the same effect as the fourth means, and at the same time can be easily switched back from the warmer process to the pasterizer process.

請求項6に係わる発明は上記第6の手段の実入り容器熱処理装置であり、この容器処理装置を用いた請求項8に係わる発明の上記第8の手段の実入り容器熱処理方法を行うことにより、第1の手段、第3の手段と同じ効果に加え、前段の温水槽と中段の高温水槽の雰囲気を通過することにより予熱されるので、より高い加温効率が得られる。   The invention according to claim 6 is the actual container heat treatment apparatus according to the sixth means, and by performing the actual container heat treatment method according to the eighth means of the invention according to claim 8 using this container processing apparatus, In addition to the same effects as the first means and the third means, preheating is performed by passing through the atmosphere of the preceding stage hot water tank and the middle stage high temperature water tank, so that higher heating efficiency can be obtained.

請求項7に係わる発明は上記第7の手段の容器熱処理装置であり、この容器処理装置を用いた請求項9に係わる発明の上記第9の手段の実入り容器熱処理方法により、上記第2、第4の手段と同様に、パストライザー処理からウォーマー処理に切換えるとき、処理水の熱エネルギーの有効利用ができる。   The invention according to claim 7 is the container heat treatment apparatus of the seventh means, and the second, second, and second container heat treatment methods of the ninth means of the invention according to claim 9 using this container treatment apparatus. Similar to the means 4, when switching from the pasterizer process to the warmer process, the thermal energy of the treated water can be effectively used.

請求項10に係わる発明は上記第10の手段の容器熱処理方法であり、上記第9の手段と同様に処理水の熱エネルギーの有効利用ができ、また、第5の手段と同様ウォーマー処理からパストライザー処理に容易に切換えて戻すことができる。   The invention according to claim 10 is the container heat treatment method according to the tenth means, wherein the thermal energy of the treated water can be effectively used as in the ninth means, and the warmer treatment is passed from the warmer treatment as in the fifth means. It can be easily switched back to the riser process.

以下、図面を参照して本発明の好適な実施例を例示的に詳しく説明する。但しこの実施例に記載されている構成部品の寸法、材質、形状、その相対的配置等は特に特定的な記載がない限りは、この発明の範囲をそれに限定する趣旨ではなく、単なる説明例に過ぎない。   Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, but are merely illustrative examples. Not too much.

この発明は、標準的なパストライザーにおいて、温水の配管系統の適宜位置にバイパス配管と開閉弁、流量可変ポンプ(可変吐出量ポンプ)を設けることにより、以下のごとく、数種類の加温設備と方法を提案するものである。
(第1の実施の形態)
According to the present invention, in a standard path riser, by providing a bypass pipe, an on-off valve, and a variable flow rate pump (variable discharge pump) at an appropriate position of a hot water piping system, several types of heating equipment and methods are provided as follows. This is a proposal.
(First embodiment)

第1の実施の形態を図に基づいて説明する。図1は本発明の第1の形態に係わる実入り容器ウォーマー(熱処理装置)の温水循環系統の模式図、図7は図1の実入り容器ウォーマーの前段の水槽内の水温と容器の温度を示す線図である。   A first embodiment will be described with reference to the drawings. FIG. 1 is a schematic diagram of a hot water circulation system of the actual container warmer (heat treatment apparatus) according to the first embodiment of the present invention, and FIG. 7 is a line showing the water temperature and the temperature of the container in the preceding stage of the actual container warmer of FIG. FIG.

図1に示した、第1の実施の形態のパストライザー装置兼用のウォーマー20は最も簡単な方式である。即ち、図10のパストライザー1の入り口側の温水槽4Aの温水はポンプ11Aより出口配管13Aに送り出されるが、この出口配管13Aから出口配管13Fへバイパスするバイパス配管21Aを設置し、バイパス配管21Aにバイパス開閉弁22A、バイパス配管21Aの分岐点から先の出口配管13Aに循環配管を遮断する開閉弁23Aが設置される。同様に、温水槽4Bの温水はポンプ11Bより出口配管13Bに送り出されるが、この出口配管13Bから出口配管13Eへバイパスするバイパス配管21Bが設置され、バイパス配管21Bにバイパス開閉弁22B、バイパス配管21Bの分岐点から先の出口配管13Bに循環配管を遮断する開閉弁23Bが設置される。また、ポンプ11E、11Fの吐出口に近い出口配管13E、13Fには回流水の逆流を防止する逆止弁24,24を設けている。   The warmer 20 that also serves as the path riser device of the first embodiment shown in FIG. 1 is the simplest method. That is, the hot water in the hot water tank 4A on the inlet side of the path riser 1 in FIG. 10 is sent from the pump 11A to the outlet pipe 13A, but a bypass pipe 21A is installed to bypass the outlet pipe 13A to the outlet pipe 13F. An on-off valve 23A for shutting off the circulation pipe from the branch point of the bypass on-off valve 22A and the bypass pipe 21A to the outlet pipe 13A is installed. Similarly, the hot water in the hot water tank 4B is sent from the pump 11B to the outlet pipe 13B, and a bypass pipe 21B that bypasses the outlet pipe 13B to the outlet pipe 13E is installed, and the bypass pipe 21B has a bypass on-off valve 22B and a bypass pipe 21B. An on-off valve 23B that shuts off the circulation pipe is installed at the outlet pipe 13B from the branch point. In addition, check valves 24 and 24 for preventing the backflow of the circulating water are provided in the outlet pipes 13E and 13F close to the discharge ports of the pumps 11E and 11F.

実入り容器7を、例えば30〜40℃まで過熱するウォーマー処理に切換えて、ウォーマーの機能を持たせるときは、ポンプ11C、11D、11E、11Fを停止し、スチーム供給弁15C、15D、15E、5Fを閉じ、出口配管13A上の開閉弁23Aを閉じ、バイパス開閉弁22Aを開き、温水槽4Aの温水をポンプ11Aによりノズル群6Aに循環させる。温水槽4Aの温水は温度センサT6が検出した検出値を制御装置25に内蔵した設定値に合わせるようにスチーム供給弁15Aを適宜オン、オフして加熱する。同様に、出口配管13B上の開閉弁23Bを閉じ、バイパス配管21B上のバイパス開閉弁22Bを開き、温水槽4Bの温水をポンプ11Bによりノズル群6Bに循環させる。温水槽4Bの温水は温度センサT5が検出した検出値を制御装置25に内蔵した設定値に合わせるようにスチーム供給弁15Bを適宜オン、オフして加熱する。図7に示すように、温水槽4Aとノズル群6A、温水槽4Bとノズル群6Bの循環水温をtwとしたとき実入り容器7の経過温度はTbで示すような曲線となる。   For example, when the actual container 7 is switched to warmer processing that heats up to 30 to 40 ° C. and has the function of warmer, the pumps 11C, 11D, 11E, and 11F are stopped, and the steam supply valves 15C, 15D, 15E, and 5F are stopped. Is closed, the on-off valve 23A on the outlet pipe 13A is closed, the bypass on-off valve 22A is opened, and the hot water in the hot water tank 4A is circulated to the nozzle group 6A by the pump 11A. The hot water in the hot water tank 4A is heated by appropriately turning on and off the steam supply valve 15A so that the detected value detected by the temperature sensor T6 matches the set value built in the control device 25. Similarly, the on-off valve 23B on the outlet pipe 13B is closed, the bypass on-off valve 22B on the bypass pipe 21B is opened, and the hot water in the hot water tank 4B is circulated to the nozzle group 6B by the pump 11B. The hot water in the hot water tank 4B is heated by appropriately turning on and off the steam supply valve 15B so that the detected value detected by the temperature sensor T5 matches the set value built in the control device 25. As shown in FIG. 7, when the circulating water temperature of the hot water tank 4A and the nozzle group 6A, and the hot water tank 4B and the nozzle group 6B is tw, the elapsed temperature of the actual container 7 is a curve as indicated by Tb.

以上の第1の実施の形態のようにパストライザー装置の入り口側の温水槽4A、4Bを用いて容易にパストライザー処理から低温の実入り容器を30℃近辺まで加熱するウォーマー処理へと切換えることができる。
(第2の実施の形態)
As in the first embodiment described above, the hot water tanks 4A and 4B on the entrance side of the path riser device can be used to easily switch from the path riser process to the warmer process in which the low temperature container is heated to around 30 ° C. it can.
(Second Embodiment)

図2に示す第2の実施の形態のパストライザー装置兼用のウォーマー30は、図10のパストライザー1を稼動したときに高温水槽4C、4Dに貯水してある高温水を、ウォーマー処理の温度調整に利用し、熱エネルギーの回収を図ったものである。第1の実施の形態のウォーマー20(図1)に、配管周りの要素部品を追加し流路を変更する部品構成と、ウォーマー作用と、図9のウォーマー30の節減熱量を示す図を用いて省エネルギーの計算例を示す。   The warmer 30 that also serves as the path riser device according to the second embodiment shown in FIG. 2 adjusts the temperature of warmer water stored in the high temperature water tanks 4C and 4D when the path riser 1 of FIG. 10 is operated. It is used to recover heat energy. The figure which shows the component structure which adds the element components around piping, changes a flow path to the warmer 20 (FIG. 1) of 1st Embodiment, a warmer effect | action, and the heat-saving amount of the warmer 30 of FIG. An example of energy saving calculation is shown.

図2に示すように、高温水槽4Cの高温水を送り出すポンプ11Cをインバータ制御モータで駆動する可変吐出量ポンプ35Cに置換え、同様に、高温水槽4Dのポンプ11Dを可変吐出量ポンプ35Dに置換える。可変吐出量ポンプ35C、35Dの出口配管13C、13Dから温水槽4A、4Bへ通じる高温水バイパス配管31A、31Bを配設し、同配管31Aには開閉弁33C、同配管31Bには開閉弁33Dを設ける。また、高温水バイパス配管31Aが結合される分岐点より先の出口配管13Cに開閉弁34C、高温水バイパス配管31Bが結合される分岐点より先の出口配管13Dに開閉弁34Dが設置されている。   As shown in FIG. 2, the pump 11C for feeding the high-temperature water in the high-temperature water tank 4C is replaced with a variable discharge pump 35C driven by an inverter control motor, and similarly, the pump 11D in the high-temperature water tank 4D is replaced with a variable discharge pump 35D. . High-temperature water bypass pipes 31A and 31B leading from the outlet pipes 13C and 13D of the variable discharge pumps 35C and 35D to the hot water tanks 4A and 4B are arranged. The pipe 31A has an on-off valve 33C, and the pipe 31B has an on-off valve 33D. Is provided. Further, an on-off valve 34C is installed at the outlet pipe 13C ahead of the branch point where the high temperature water bypass pipe 31A is coupled, and an on-off valve 34D is installed at the outlet pipe 13D ahead of the branch point where the high temperature water bypass pipe 31B is joined. .

温水槽4Aの水温を温度センサT6で測り、温度センサT6が検出した水温検出値を制御装置25に送り、制御装置は同装置に内蔵した水温設定値に合わせるように、可変吐出量ポンプ35Cの吐出量を指示制御する。同様に、温水槽4Bの水温を温度センサT5で測り、温度センサT5が検出した検出値を制御装置25に送り、制御装置25は同装置に内蔵した設定値に合わせるように、可変吐出量ポンプ35Cの吐出量を指示制御する。パストライザー処理のときの温水槽4Bの水温はウォーマー処理水温より高いので、配管31Bに冷水供給配管32Bを繋ぎ、開閉弁33Bを設けて、水温調整のために冷水を投入するようにしている。   The water temperature in the hot water tank 4A is measured by the temperature sensor T6, the detected water temperature value detected by the temperature sensor T6 is sent to the control device 25, and the control device adjusts the water discharge temperature of the variable discharge pump 35C so as to match the water temperature set value built in the device. The discharge amount is commanded and controlled. Similarly, the water temperature in the hot water tank 4B is measured by the temperature sensor T5, and the detected value detected by the temperature sensor T5 is sent to the control device 25. The control device 25 adjusts to the set value built in the same device. Instruct and control the discharge amount of 35C. Since the water temperature of the hot water tank 4B at the time of the path riser process is higher than the warmer process water temperature, the cold water supply pipe 32B is connected to the pipe 31B, and the open / close valve 33B is provided so that the cold water is supplied to adjust the water temperature.

ウォーマー30のウォーマー処理作用は、パストライザー1のパストライザー処理から低温の実入り容器7を30〜40℃まで加熱するウォーマー処理に切換えるとき、スチーム供給弁15A、15B、15C、15D、15E、15Fを閉じて水槽全部のスチーム加熱を止め、ポンプ11E、11Fを停止し、開閉弁23A、23Bを閉じ、開閉弁22A、22Bを開にすることにより、温水槽4Aの温水をポンプ11A、バイパス配管21A、出口配管13Fを経てノズル群6Aに回流させ、同様に、温水槽4Bの温水をポンプ11B、バイパス配管21B、出口配管13Eを経てノズル群6Bに回流させる。   When the warmer treatment operation of the warmer 30 is switched from the pasterizer treatment of the pasterizer 1 to the warmer treatment in which the low temperature container 7 is heated to 30 to 40 ° C., the steam supply valves 15A, 15B, 15C, 15D, 15E, and 15F are turned on. Close the steam tank to stop steam heating, stop the pumps 11E and 11F, close the on-off valves 23A and 23B, and open the on-off valves 22A and 22B, thereby supplying hot water from the hot water tank 4A to the pump 11A and the bypass piping 21A. Then, the water is circulated to the nozzle group 6A through the outlet pipe 13F, and similarly, the hot water in the hot water tank 4B is circulated to the nozzle group 6B through the pump 11B, the bypass pipe 21B, and the outlet pipe 13E.

温水槽4Aの水温の調整は、開閉弁33Cを開にして高温水バイパス配管31Aより可変吐出量ポンプ35Cより吐出する高温水槽4Cの高温水を温水槽4Aに送り込み、温度センサT6が検出した温度が制御装置25に記憶してある設定値になるように、可変吐出量ポンプ35Cの吐出量を制御する。また、温水槽4Bの水温の調整は、この水温が設定値より高いときは、高温水バイパス配管31Bに繋いだ冷水供給配管32B上の開閉弁33Bを開にして、温水槽4Bに冷水を投入し温度センサT5を介して水温調整する。温水槽4Bの水温が設定値になったとき開閉弁33Bを閉じる。これ以降の水温調整は、開閉弁33Dを開にして、高温水バイパス配管31Bを経由して可変吐出量ポンプ35Dより吐出する高温水槽4Dの高温水を温水槽4Bに送り込み、温度センサT5が検出した温度が制御装置25に記憶してある設定値になるように、可変吐出量ポンプ35Dの吐出量を制御する。   The temperature of the hot water tank 4A is adjusted by opening the on-off valve 33C and feeding the high temperature water in the high temperature water tank 4C discharged from the variable discharge pump 35C from the high temperature water bypass pipe 31A to the hot water tank 4A and detecting the temperature detected by the temperature sensor T6. The discharge amount of the variable discharge amount pump 35C is controlled so that becomes the set value stored in the control device 25. Also, when adjusting the water temperature of the hot water tank 4B, when this water temperature is higher than the set value, the on-off valve 33B on the cold water supply pipe 32B connected to the high temperature water bypass pipe 31B is opened, and cold water is poured into the hot water tank 4B. The water temperature is adjusted via the temperature sensor T5. When the water temperature in the hot water tank 4B reaches the set value, the on-off valve 33B is closed. In the subsequent water temperature adjustment, the on-off valve 33D is opened and the high temperature water in the high temperature water tank 4D discharged from the variable discharge pump 35D is sent to the hot water tank 4B via the high temperature water bypass pipe 31B and detected by the temperature sensor T5. The discharge amount of the variable discharge amount pump 35D is controlled so that the set temperature becomes the set value stored in the control device 25.

温水槽4Cの水温(温度センサT3の検出温度)が温水槽4A内の設定水温まで下がったとき、可変吐出量ポンプ35Cの送水を0(ゼロ)にし、開閉弁33Cを閉じて高温水バイパス配管31Aからの水流入を止め、温水槽4Aからノズル群6Aへの循環はポンプ11Aにより行い、スチーム供給弁15Aを開可能にして温水槽4A内の水温調整は温度センサT6とスチームのオン、オフ制御に移行する。同様に、高温水槽4Dの水温(温度センサT4の検出温度)が温水槽4B内の設定水温まで下がったとき、可変吐出量ポンプ35Dの送水を0(ゼロ)にし、開閉弁33Dを閉じて高温水バイパス配管31Bからの水流入を止め、温水槽4Bからノズル群6Bへの循環はポンプ11Bにより行い、スチーム供給弁15Bを開可能にして温水槽4B内の水温調整は温度センサT5とスチームのオン、オフ制御に移行する。   When the water temperature of the hot water tank 4C (detected temperature of the temperature sensor T3) falls to the set water temperature in the hot water tank 4A, the water supply of the variable discharge pump 35C is set to 0 (zero), the on-off valve 33C is closed, and the hot water bypass pipe Water inflow from 31A is stopped, circulation from the hot water tank 4A to the nozzle group 6A is performed by the pump 11A, the steam supply valve 15A can be opened, and the water temperature in the hot water tank 4A is adjusted by turning on and off the temperature sensor T6 and steam. Transition to control. Similarly, when the water temperature of the high temperature water tank 4D (detected temperature of the temperature sensor T4) falls to the set water temperature in the hot water tank 4B, the water supply of the variable discharge pump 35D is set to 0 (zero), the on-off valve 33D is closed and the temperature is high. Water inflow from the water bypass pipe 31B is stopped, circulation from the hot water tank 4B to the nozzle group 6B is performed by the pump 11B, the steam supply valve 15B can be opened, and the water temperature in the hot water tank 4B is adjusted by the temperature sensor T5 and the steam. Transition to on / off control.

図9によりウォーマー30の熱量エネルギー節減について説明する。図に示すta、tb、tc、td、te、tfは各水槽4A、4B、4C、4D、4E、4Fのパストライザー処理時のそれぞれの循環水温を示しTbは実入り容器7の経過温度を示す。また、twはウォーマー処理時の水槽4A及び4Bの循環水温を示す。図にハッチングした温度差と高温水槽4A、4Bの水量の積が、温水槽4A、4Bの温度調整に利用可能な熱量となる。ウォーマー30において、高温水槽4C、4Dの高温水を使用するときの使用可能な熱量は、図の温度差Ac、Adと高温水槽4C、4Dの水量の積である熱量となる。   The heat energy saving of the warmer 30 will be described with reference to FIG. In the figure, ta, tb, tc, td, te, and tf indicate the circulating water temperatures during the pasterizer treatment of each of the water tanks 4A, 4B, 4C, 4D, 4E, and 4F, and Tb indicates the elapsed temperature of the actual container 7. . Moreover, tw shows the circulating water temperature of water tank 4A and 4B at the time of a warmer process. The product of the temperature difference hatched in the figure and the amount of water in the high temperature water tanks 4A, 4B is the amount of heat available for temperature adjustment of the hot water tanks 4A, 4B. In the warmer 30, the amount of heat that can be used when using the high-temperature water in the high-temperature water tanks 4C and 4D is the heat quantity that is the product of the temperature differences Ac and Ad in the figure and the amount of water in the high-temperature water tanks 4C and 4D.

節減熱量の試算例を次に示す。
容器:500ml缶(冷却充填時の生産能力は1600缶/分である)
容器温度:2℃
500ml缶を2℃から30℃にする熱量Qb:0.505kcal/℃×(30−2)℃=14.1kcal
温水槽4Aと4Bの貯水量合計:22m
温水槽4Aと4Bの循環水温:60℃
とすると(0.505kcal/℃は、飲料と缶の合算値)、パストライザーからウォーマーに切換えるときに余る熱量(節減熱量)Qaは、
Qa:22m(22×1,000kg)×1kcal/kg・℃×(60℃−30℃)=66×10,000kcal
となる。このQaで2℃の500ml缶を30℃まで温めることができる缶数は:Qa÷Qb=46,808缶となる。
また、1600缶/分の生産能力のとき、加温を継続できる分数は:46,808缶÷1600缶=29分となる。
さらに、Qa(66×10,000kcal)に相当するスチームは132.4kgであり、約4,000円に相当する。
A trial calculation example of energy saving is shown below.
Container: 500 ml can (Production capacity at the time of cooling filling is 1600 cans / minute)
Container temperature: 2 ° C
Calorie Qb for making a 500 ml can from 2 ° C. to 30 ° C .: 0.505 kcal / ° C. × (30-2) ° C. = 14.1 kcal
Total amount of water stored in hot water tanks 4A and 4B: 22m 3
Circulating water temperature of hot water tanks 4A and 4B: 60 ° C
Then (0.505 kcal / ° C is the total value of beverage and can), the amount of heat (amount of heat saved) Qa remaining when switching from the path riser to the warmer is:
Qa: 22 m 3 (22 × 1,000 kg) × 1 kcal / kg · ° C. × (60 ° C.-30 ° C.) = 66 × 10,000 kcal
It becomes. The number of cans which can heat a 500 ml can at 2 ° C. to 30 ° C. with this Qa is: Qa ÷ Qb = 46,808 cans.
In addition, when the production capacity is 1600 cans / minute, the fraction in which heating can be continued is: 46,808 cans / 1600 cans = 29 minutes.
Furthermore, the steam corresponding to Qa (66 × 10,000 kcal) is 132.4 kg, which corresponds to about 4,000 yen.

以上のように、第2の実施の形態によれば、高温水槽4C、4Dの高温水を用いて、パストライザー処理から低温の実入り容器を30℃近辺まで加熱するウォーマー処理へと容易に切換えることができる。また、大きな節減熱量を得ることができる。
(第3の実施の形態)
As described above, according to the second embodiment, the hot water in the high temperature water tanks 4C and 4D is used to easily switch from the pasterizer process to the warmer process in which the low temperature container is heated to around 30 ° C. Can do. Also, a large amount of heat saving can be obtained.
(Third embodiment)

図3に示す第3の実施の形態のパストライザー装置兼用のウォーマー40はパストライザー1を稼動するときに貯蔵している高温水をそのままパストライザー1の状態に温度調整し、ウォーマー40の温度調整に転用する熱エネルギー回収方式であると同時に、ウォーマー40からパストライザー1へ容易に切換え、戻すことができる方式である。この実施の形態の部品構成は図2に示した第2の実施の形態と全く同じであるので、構成の説明は省略し、以下にウォーマー作用を説明する。   The warmer 40 that also functions as a path riser device according to the third embodiment shown in FIG. 3 adjusts the temperature of the high-temperature water stored when operating the path riser 1 to the state of the path riser 1 as it is. In addition to the thermal energy recovery system that is diverted to the above, it is a system that can be easily switched from the warmer 40 to the path riser 1 and returned. Since the component configuration of this embodiment is exactly the same as that of the second embodiment shown in FIG. 2, the description of the configuration is omitted, and the warmer action will be described below.

第3の実施の形態のウォーマー40の作用が、上記第2の実施の形態のウォーマー30の作用と異なるところは、高温水槽4Cの高温水を加熱するスチーム供給弁15Cと高温水槽4Dの高温水を加熱するスチーム供給弁15Dを制御装置25からの制御指令で開閉させて、高温水槽4C、4Dの内の高温水の温度がパストライザー1が稼動時の温度を維持するように制御し、ウォーマー処理からパストライザー処理へ容易に切換られるようにしてあることで、そのため、高温水槽4C、4Dの水温(温度センサT3、T4の検出温度)は下がること無く、可変吐出量ポンプ35C、35Dの送水を続け、高温水バイパス配管31A、31Bからの水流入を続ける。ウォーマー40からパストライザー1へ容易に切換え、戻すことができるので、高温水と温水の熱量エネルギーの交流に損得は生じない。
(第4の実施の形態)
The action of the warmer 40 of the third embodiment differs from the action of the warmer 30 of the second embodiment described above in that the steam supply valve 15C for heating the high temperature water in the high temperature water tank 4C and the high temperature water in the high temperature water tank 4D. The steam supply valve 15D that heats the steam is opened and closed by a control command from the control device 25, and the temperature of the high-temperature water in the high-temperature water tanks 4C and 4D is controlled so as to maintain the temperature at which the pastoriser 1 is in operation. Since the process can be easily switched from the process to the path riser process, the water temperature of the high-temperature water tanks 4C, 4D (the temperature detected by the temperature sensors T3, T4) does not drop, and the water supply of the variable discharge pumps 35C, 35D The water inflow from the high temperature water bypass piping 31A, 31B is continued. Since the warmer 40 can be easily switched to and returned from the path riser 1, there is no loss in the alternating current between the high-temperature water and the heat energy of the hot water.
(Fourth embodiment)

図4に示した、第4の実施の形態のパストライザー装置兼用のウォーマー50は、温水ノズル群と回収水槽を、実入り容器の出口側に設けた最も簡単な方式である。   The warmer 50 also serving as a path riser device according to the fourth embodiment shown in FIG. 4 is the simplest system in which a hot water nozzle group and a recovery water tank are provided on the outlet side of the actual container.

図4は、第1の実施の形態で説明した同じパストライザー1をウォーマー装置に兼用するもので、パストライザー1の出口側の冷却用温水槽4Eの温水はポンプ11Eより出口配管13Eに送り出されるが、この出口配管13Eから出口配管13Bへバイパスするバイパス配管21Eが設置され、バイパス配管21Eにバイパス開閉弁22E、バイパス配管21Eの分岐点から先の出口配管13Eを遮断する開閉弁23Eが設置される。同様に、冷却用温水槽4Fの温水はポンプ11Fより出口配管13Fに送り出されるが、この出口配管13Fから出口配管13Aへバイパスするバイパス配管21Fが設置され、同配管21Fにバイパス開閉弁22F、バイパス配管21Fの分岐点から先の出口配管13Fに循環配管を遮断する開閉弁23Fが設置される。また、ポンプ11A、11Bの吐出口に近い配管13A、13Bには回流水の逆流を防止する逆止弁24,24を設けている。   In FIG. 4, the same path riser 1 described in the first embodiment is also used as a warmer device, and the hot water in the cooling hot water tank 4E on the outlet side of the path riser 1 is sent from the pump 11E to the outlet pipe 13E. However, a bypass pipe 21E that bypasses the outlet pipe 13E to the outlet pipe 13B is installed, and a bypass on-off valve 22E is installed in the bypass pipe 21E, and an on-off valve 23E that shuts off the previous outlet pipe 13E from the branch point of the bypass pipe 21E is installed. The Similarly, the hot water in the cooling hot water tank 4F is sent out from the pump 11F to the outlet pipe 13F. A bypass pipe 21F is installed to bypass the outlet pipe 13F to the outlet pipe 13A. An open / close valve 23F that shuts off the circulation pipe is installed from the branch point of the pipe 21F to the outlet pipe 13F. Further, check valves 24 and 24 for preventing the backflow of the circulating water are provided in the pipes 13A and 13B close to the discharge ports of the pumps 11A and 11B.

ウォーマーの機能を持たせるときは、ポンプ11A、11B、11C、11Dを停止し、スチーム供給弁15A、15B、15C、5Dを閉じ、出口配管13E上の開閉弁23Eを閉じ、バイパス開閉弁22Eを開き、冷却用温水槽4Eの温水をポンプ11Eにより循環させる。冷却用温水槽4Eの温水は温度センサT2が検出した検出値を制御装置25に内蔵した設定値に合わせるようにスチーム供給弁15Eを適宜オン、オフして加熱する。同様に、出口配管13F上の開閉弁23Fを閉じ、バイパス開閉弁22Fを開き、冷却用温水槽4Fの温水をポンプ11Fにより循環させる。   When the warmer function is provided, the pumps 11A, 11B, 11C, and 11D are stopped, the steam supply valves 15A, 15B, 15C, and 5D are closed, the on-off valve 23E on the outlet pipe 13E is closed, and the bypass on-off valve 22E is closed. The hot water in the cooling hot water tank 4E is circulated by the pump 11E. The hot water in the cooling hot water tank 4E is heated by appropriately turning on and off the steam supply valve 15E so that the detected value detected by the temperature sensor T2 matches the set value built in the control device 25. Similarly, the on-off valve 23F on the outlet pipe 13F is closed, the bypass on-off valve 22F is opened, and the hot water in the cooling hot water tank 4F is circulated by the pump 11F.

冷却用温水槽4Fの温水は温度センサT6が検出した検出値を制御装置25に内蔵した設定値に合わせるようにスチーム供給弁15Fを適宜オン、オフして加熱する。図8に示すように、冷却用温水槽4Eとノズル群6E、冷却用温水槽4Fとノズル群6Fの循環水温をtwとしたとき、実入り容器7はウォーマー50内の雰囲気に触れて徐々に温まり、冷却用温水槽4E、4Fの上部からのノズル群6E、6Fからの散水により急上昇し、実入り容器7の経過温度はTbで示すような曲線となる。   The hot water in the cooling hot water tank 4F is heated by appropriately turning on and off the steam supply valve 15F so that the detected value detected by the temperature sensor T6 matches the set value built in the control device 25. As shown in FIG. 8, when the circulating water temperature of the cooling hot water tank 4E and the nozzle group 6E and the cooling hot water tank 4F and the nozzle group 6F is tw, the actual container 7 is gradually warmed by touching the atmosphere in the warmer 50. The temperature rises rapidly due to water spraying from the nozzle groups 6E and 6F from above the cooling hot water tanks 4E and 4F, and the elapsed temperature of the actual container 7 becomes a curve as indicated by Tb.

以上のように、第4の実施の形態によれば、パストライザー装置の出口側の冷却用温水槽4E、4Fを用いて容易にウォーマー処理へと切換えることができる。
(第5の実施の形態)
As described above, according to the fourth embodiment, it is possible to easily switch to the warmer process using the cooling hot water tanks 4E and 4F on the outlet side of the path riser device.
(Fifth embodiment)

図5に示す第5の実施の形態のパストライザー装置兼用のウォーマー60はパストライザー1を稼動したときに貯蔵した高温水を、ウォーマー60の容器の出口側に設けた温水ノズル群と回収水槽の循環水の温度調整に転用する熱エネルギー回収方式である。以下に追加変更する部品構成と、ウォーマー作用とを説明する。   The warmer 60 also serving as a path riser device according to the fifth embodiment shown in FIG. 5 is a combination of a hot water nozzle group provided on the outlet side of the container of the warmer 60 and a recovered water tank. This is a thermal energy recovery system that is diverted to adjust the temperature of circulating water. The component configuration to be added and changed and the warmer action will be described below.

高温水槽4Cの高温水を送り出すポンプ11Cをインバータ制御モータで駆動して可変吐出量ポンプ35Cに置換え、同様に、高温水槽4Dのポンプ11Dを可変吐出量ポンプ35Dに置換える。可変吐出量ポンプ35C、35Dの出口配管13C、13Dから冷却用温水槽4E、4Fへ通じる高温水バイパス配管31E、31Fを配設し、高温水バイパス配管31Eには開閉弁33E、高温水バイパス配管31Fには開閉弁33Fを設ける。また、高温水バイパス配管31Eが結合される分岐点より先の出口配管13Cに開閉弁34E、高温水バイパス配管31Fが結合される分岐点より先の出口配管13Dに開閉弁34Fが設置されている。   The pump 11C that feeds the high-temperature water in the high-temperature water tank 4C is driven by an inverter control motor and replaced with the variable discharge pump 35C. Similarly, the pump 11D of the high-temperature water tank 4D is replaced with the variable discharge pump 35D. High temperature water bypass pipes 31E and 31F leading from the outlet pipes 13C and 13D of the variable discharge pumps 35C and 35D to the hot water tanks 4E and 4F for cooling are arranged. The high temperature water bypass pipe 31E has an on-off valve 33E and a high temperature water bypass pipe. An opening / closing valve 33F is provided at 31F. Further, an on-off valve 34E is installed at the outlet pipe 13C ahead of the branch point where the high temperature water bypass pipe 31E is coupled, and an on-off valve 34F is installed at the outlet pipe 13D ahead of the branch point where the high temperature water bypass pipe 31F is joined. .

冷却用温水槽4Eの水温を温度センサT2で測り、温度センサT2が検出した水温検出値を制御装置25に送り、制御装置25は同装置に内蔵した水温設定値に合わせるように、可変吐出量ポンプ35Cの吐出量を指示制御する。同様に、冷却用温水槽4Fの水温を温度センサT1で測り、温度センサT1が検出した検出値を制御装置25に送り、制御装置25は同装置に内蔵した設定値に合わせるように、可変吐出量ポンプ35Dの吐出量を指示制御する。パストライザー処理のときの冷却用温水槽4Eの水温はウォーマー処理水温より高いので、高温水バイパス配管31Eに冷水供給配管35Eを繋ぎ、開閉弁36Eを設けて、水温調整のために冷水を投入するようにしている。   The water temperature in the cooling hot water tank 4E is measured by the temperature sensor T2, and the detected water temperature value detected by the temperature sensor T2 is sent to the control device 25. The control device 25 is adjusted so as to match the water temperature setting value built in the same device. The discharge amount of the pump 35C is instructed and controlled. Similarly, the temperature of the cooling hot water tank 4F is measured by the temperature sensor T1, and the detected value detected by the temperature sensor T1 is sent to the control device 25, and the control device 25 performs variable discharge so as to match the set value built in the device. The discharge amount of the quantity pump 35D is instructed and controlled. Since the water temperature of the cooling hot water tank 4E at the time of the path riser treatment is higher than the warmer treatment water temperature, the cold water supply pipe 35E is connected to the high temperature water bypass pipe 31E, and an on-off valve 36E is provided to supply cold water for water temperature adjustment. I am doing so.

ウォーマー60のウォーマー処理作用は、パストライザー1のパストライザー処理から低温の実入り容器7を30〜40℃まで加熱するウォーマー処理に切換えるとき、スチーム供給弁15A、15B、15C、15D、15E、15Fを閉じて水槽全部のスチーム加熱を止め、ポンプ11A、11Bを停止し、開閉弁23E、23Fを閉じ、バイパス開閉弁22E、22Fを開にすることにより、冷却用温水槽4Eの温水をポンプ11E、バイパス配管21E、出口配管13Eを経てノズル群6Eに回流させ、同様に、冷却用温水槽4Fの温水をポンプ11F、バイパス配管21F、出口配管13Fを経てノズル群6Fに回流させる。   When the warmer processing operation of the warmer 60 is switched from the pastorizer processing of the pastoriser 1 to the warmer processing in which the low temperature container 7 is heated to 30 to 40 ° C., the steam supply valves 15A, 15B, 15C, 15D, 15E, and 15F are turned on. Close the steam heating of all the water tanks, stop the pumps 11A and 11B, close the on-off valves 23E and 23F, and open the bypass on-off valves 22E and 22F, so that the hot water in the cooling hot water tank 4E is pumped 11E, Similarly, the hot water in the cooling hot water tank 4F is circulated to the nozzle group 6F via the pump 11F, the bypass pipe 21F, and the outlet pipe 13F via the bypass pipe 21E and the outlet pipe 13E.

冷却用温水槽4Eの水温の調整は、この水温が設定値より高いときは、高温水バイパス配管31Eに繋いだ冷水供給配管35E上の開閉弁36Eを開にして、冷却用温水槽4Eに冷水を投入し温度センサT2を介して水温調整する。冷却用温水槽4Eの水温が設定値になったとき開閉弁36Eを閉じる。これ以降の水温調整は、バイパス開閉弁22Eを開にして高温水バイパス配管31Eより可変吐出量ポンプ35Cより吐出する高温水槽4Cの高温水を冷却用温水槽4Eに送り込み、温度センサT2が検出した温度が制御装置25に記憶してある設定値になるように、可変吐出量ポンプ35Cの吐出量を制御する。また、冷却用温水槽4Fの水温の調整は、開閉弁33Fを開にして高温水バイパス配管31Fより可変吐出量ポンプ35Dより吐出する高温水槽4Dの高温水を冷却用温水槽4Fに送り込み、温度センサT1が検出した温度が制御装置25に記憶してある設定値になるように、可変吐出量ポンプ35Dの吐出量を制御する。   When the water temperature is higher than the set value, the on-off valve 36E on the cold water supply pipe 35E connected to the high temperature water bypass pipe 31E is opened to adjust the water temperature of the cooling hot water tank 4E, and the cooling hot water tank 4E has cold water. And the water temperature is adjusted via the temperature sensor T2. When the water temperature in the cooling hot water tank 4E reaches the set value, the on-off valve 36E is closed. In the subsequent water temperature adjustment, the bypass on-off valve 22E is opened and the high-temperature water in the high-temperature water tank 4C discharged from the variable discharge pump 35C from the high-temperature water bypass pipe 31E is sent to the cooling hot water tank 4E and detected by the temperature sensor T2. The discharge amount of the variable discharge amount pump 35C is controlled so that the temperature becomes a set value stored in the control device 25. Further, the water temperature of the cooling hot water tank 4F is adjusted by opening the on-off valve 33F and sending the high temperature water in the high temperature water tank 4D discharged from the variable discharge pump 35D from the high temperature water bypass pipe 31F to the cooling hot water tank 4F. The discharge amount of the variable discharge amount pump 35D is controlled so that the temperature detected by the sensor T1 becomes the set value stored in the control device 25.

高温水槽4Cの水温(温度センサT3の検出温度)が冷却用温水槽4E内の設定水温まで下がったとき、可変吐出量ポンプ35Cの送水を0(ゼロ)にし、開閉弁33Eを閉じて高温水バイパス配管31Eからの水流入を止め、冷却用温水槽4Eからノズル群6Eへの循環はポンプ11Eにより行い、スチーム供給弁15Eを開閉可能にして冷却用温水槽4E内の水温調整は温度センサT2とスチーム供給弁15Eのオン、オフ制御に移行する。同様に、高温水槽4Dの水温(温度センサT4の検出温度)が冷却用温水槽4F内の設定水温まで下がったとき、可変吐出量ポンプ35Dの送水を0(ゼロ)にし、開閉弁33Fを閉じて高温水バイパス配管31Fからの水流入を止め、冷却用温水槽4Fからノズル群6Fへの循環はポンプ11Fにより行い、スチーム供給弁15Fを開閉可能にして冷却用温水槽4F内の水温調整は温度センサT1とスチーム供給弁15Fのオン、オフ制御に移行する。   When the water temperature of the high temperature water tank 4C (detected temperature of the temperature sensor T3) falls to the set water temperature in the cooling water tank 4E, the water supply of the variable discharge pump 35C is set to 0 (zero), the on-off valve 33E is closed, and high temperature water is supplied. Water inflow from the bypass pipe 31E is stopped, circulation from the cooling hot water tank 4E to the nozzle group 6E is performed by the pump 11E, and the steam supply valve 15E can be opened and closed to adjust the water temperature in the cooling hot water tank 4E. And the steam supply valve 15E shifts to ON / OFF control. Similarly, when the water temperature of the high temperature water tank 4D (detected temperature of the temperature sensor T4) falls to the set water temperature in the cooling water tank 4F, the water supply of the variable discharge pump 35D is set to 0 (zero), and the open / close valve 33F is closed. The water flow from the hot water bypass pipe 31F is stopped, the circulation from the cooling hot water tank 4F to the nozzle group 6F is performed by the pump 11F, and the steam supply valve 15F can be opened and closed to adjust the water temperature in the cooling hot water tank 4F. The process proceeds to on / off control of the temperature sensor T1 and the steam supply valve 15F.

ウォーマー60の熱量エネルギー節減は、第2の実施の形態のウォーマー30の場合と同じである。即ち、パストライザー処理時の高温水槽4C、4Dの循環水温とウォーマー処理時の冷却用温水槽4E及び4Fの循環水温との温度差は、図9にハッチングしたAcとAdであり、この温度差と高温水槽4C、4Dの水量の積が冷却用温水槽4E、4Fの温度調整に利用できる可能な熱量となる。冷却用温水槽4E、4Fを合わせた水量が温水槽4A、4Bを合わせた水量と同じであれば、第2の実施の形態のウォーマー30の場合の計算例がそのまま適用できる。
(第6の実施の形態)
The heat energy saving of the warmer 60 is the same as that of the warmer 30 of the second embodiment. That is, the temperature difference between the circulating water temperature of the high-temperature water tanks 4C and 4D during the path riser treatment and the circulating water temperature of the cooling hot water tanks 4E and 4F during the warmer treatment is Ac and Ad hatched in FIG. And the amount of water in the high-temperature water tanks 4C and 4D is an amount of heat that can be used for temperature adjustment of the cooling water tanks 4E and 4F. If the amount of water combined with the hot water tanks 4E and 4F for cooling is the same as the amount of water combined with the hot water tanks 4A and 4B, the calculation example in the case of the warmer 30 of the second embodiment can be applied as it is.
(Sixth embodiment)

図6に示す第6の実施の形態のパストライザー装置兼用のウォーマー70は、パストライザー1を稼動するときに貯蔵している高温水をそのままパストライザー1の状態に温度調整し、ウォーマー70の容器の出口側に設けた温水ノズル群と回収水槽の循環水の温度調整に転用する熱エネルギー回収方式であると同時に、ウォーマー70からパストライザー1へ容易に切換え、戻すことができる方式である。以下に追加変更する部品構成と、ウォーマー作用を説明する。この実施の形態の部品構成は第5の実施の形態と全く同じであるので、構成の説明は省略し、以下にウォーマー作用を説明する。   A warmer 70 that also serves as a path riser device according to the sixth embodiment shown in FIG. 6 adjusts the temperature of high-temperature water stored when the path riser 1 is operated to the state of the path riser 1 as it is. This is a thermal energy recovery method that is diverted to adjust the temperature of the circulating water in the recovery water tank and the group of hot water nozzles provided on the outlet side, and at the same time, it is a method that can be easily switched from the warmer 70 to the path riser 1. The component structure to be added and changed and the warmer action will be described below. Since the component configuration of this embodiment is exactly the same as that of the fifth embodiment, the description of the configuration is omitted, and the warmer action will be described below.

第6の実施の形態のウォーマー70の作用が、上記第5の実施の形態のウォーマー60の作用と異なるところは、高温水槽4Cの高温水を加熱するスチーム供給弁15Cと高温水槽4Dの高温水を加熱するスチーム供給弁15Dを制御装置25からの制御指令で開閉させて、高温水槽4C、4Dの内の高温水の温度がパストライザー1の稼動時の温度を維持するように制御し、ウォーマー処理からパストライザー処理へ容易に切換られるようにしてあることで、そのため、高温水槽4C、4Dの水温(温度センサT3、T4の検出温度)が下がること無く、可変吐出量ポンプ35C、35Dの送水を続け、高温水バイパス配管31E、31Fからの水流入を続ける。ウォーマー70からパストライザー1へ容易に切換え、戻すことができるので、高温水と温水の熱量エネルギーの交流に損得は生じない。   The action of the warmer 70 of the sixth embodiment differs from the action of the warmer 60 of the fifth embodiment in that the steam supply valve 15C for heating the high temperature water in the high temperature water tank 4C and the high temperature water in the high temperature water tank 4D. The steam supply valve 15D that heats the steam is opened and closed by a control command from the control device 25, and the temperature of the hot water in the hot water tanks 4C and 4D is controlled so as to maintain the temperature at the time of operation of the path riser 1. Since the process can be easily switched from the process to the path riser process, the water temperature of the high-temperature water tanks 4C and 4D (the temperature detected by the temperature sensors T3 and T4) does not drop, and the water supply of the variable discharge pumps 35C and 35D The water inflow from the high temperature water bypass pipes 31E and 31F is continued. Since the warmer 70 can be easily switched to and returned from the path riser 1, there is no loss in the exchange of heat energy between the high-temperature water and the hot water.

本発明の第1の形態に係わる実入り容器熱処理装置の温水循環系統の模式図である。It is a schematic diagram of the hot water circulation system of the actual container heat treatment apparatus concerning the 1st form of this invention. 本発明の第2の形態に係わる実入り容器熱処理装置の温水循環系統の模式図である。It is a schematic diagram of the hot water circulation system of the actual container heat treatment apparatus concerning the 2nd form of this invention. 本発明の第3の形態に係わる実入り容器熱処理装置の温水循環系統の模式図である。It is a schematic diagram of the hot water circulation system of the actual container heat treatment apparatus concerning the 3rd form of this invention. 本発明の第4の形態に係わる実入り容器熱処理装置の温水循環系統の模式図であるIt is a schematic diagram of the hot water circulation system of the actual container heat processing apparatus concerning the 4th form of this invention. 本発明の第5の形態に係わる実入り容器熱処理装置の温水循環系統の模式図である。It is a schematic diagram of the hot water circulation system of the actual container heat treatment apparatus concerning the 5th form of this invention. 本発明の第6の形態に係わる実入り容器熱処理装置の温水循環系統の模式図である。It is a schematic diagram of the hot water circulation system of the actual container heat treatment apparatus concerning the 6th form of this invention. 図1〜図3の実入り容器処理装置の前段の槽内の水温と容器の温度を示す線図である。It is a diagram which shows the water temperature in the tank of the front | former stage of the actual container processing apparatus of FIGS. 1-3, and the temperature of a container. 図4〜図6の実入り容器処理装置の後段の槽内の水温と容器の温度を示す線図である。It is a diagram which shows the water temperature in the tank of the back | latter stage of the real container processing apparatus of FIGS. 4-6, and the temperature of a container. 図2、図3、図5、図6の実入り容器処理装置の節減熱量を示す図である。It is a figure which shows the amount of heat saving of the actual container processing apparatus of FIG.2, FIG.3, FIG.5, FIG.6. 従来のパストライザーの温水循環系統の模式図である。It is a schematic diagram of the hot water circulation system of the conventional path riser. 図10のパストライザーの各槽内の水温と容器の温度を示す線図である。It is a diagram which shows the water temperature in each tank of the path riser of FIG. 10, and the temperature of a container.

符号の説明Explanation of symbols

1 パストライザー
4A、4B 温水層
4C、4D 高温水槽
4E、4F 冷却用温水槽
5 容器コンベア
6A、6B、6C、6D、6E、6F ノズル群
7 実入り容器
11A、11B、11C、11D、11E、11F ポンプ
13A、13B、13C、13D、13E、13F 出口配管(循環配管)
15A、15B、15C、15D、15E、15F スチーム供給弁
20、30、40、50、60、70 ウォーマー
21A、21B、21E、21F バイパス配管
22A、22B、22E、22F バイパス開閉弁
23A、23B、23E、23F 開閉弁
24 逆止弁
25 制御装置
31A、31B、31E、31F 高温水バイパス配管
33C、33D、33E、33F、34C、34D、34E、34F、36E 開閉弁
35C、35D 可変吐出量ポンプ
35E 冷水供給配管
T1、T2、T3、T4、T5、T6 温度センサ
1 Pastorizer 4A, 4B Hot water layer 4C, 4D Hot water tank 4E, 4F Cooling hot water tank 5 Container conveyor 6A, 6B, 6C, 6D, 6E, 6F Nozzle group 7 Actual containers 11A, 11B, 11C, 11D, 11E, 11F Pump 13A, 13B, 13C, 13D, 13E, 13F Outlet piping (circulation piping)
15A, 15B, 15C, 15D, 15E, 15F Steam supply valves 20, 30, 40, 50, 60, 70 Warmers 21A, 21B, 21E, 21F Bypass piping 22A, 22B, 22E, 22F Bypass opening / closing valves 23A, 23B, 23E , 23F On-off valve 24 Check valve 25 Controllers 31A, 31B, 31E, 31F High-temperature water bypass piping 33C, 33D, 33E, 33F, 34C, 34D, 34E, 34F, 36E On-off valve 35C, 35D Variable discharge pump 35E Cold water Supply piping T1, T2, T3, T4, T5, T6 Temperature sensor

Claims (10)

前段に温水槽、中段に高温水槽、後段に冷却用温水槽を配置し、実入り容器を連続搬送中に容器毎中身の液体を加熱又は冷却処理するパストライザー装置であって、各槽の水温を温度調整する温度センサとスチーム供給弁を備え、前段の温水槽の温水を温度調整して温水ポンプにより後段の温水ノズル配管へ送り出し、後段の温水槽の温水を温度調整して温水ポンプにより前段の温水ノズル配管へ回流する循環系と、中段槽高温水循環系に高温水ポンプと高温水循環配管と高温水ノズル循環配管を備えたパストライザー処理装置において、前段の温水槽の温水を同じ温水槽上の温水ノズル配管へ回流バイパスするバイパス配管と、該配管に設置されたバイパス開閉弁と、同配管から後段の温水ノズルへの循環配管を遮断する開閉弁と、前記前段のノズル配管へ温水を送り出す後段の温水ポンプの配管上に該ポンプへ向う流れを阻止する逆止弁を備えることによりパストライザーと容器ウォーマーを兼用できるようにしたことを特徴とする実入り容器熱処理装置。   A hot water tank in the front stage, a hot water tank in the middle stage, and a hot water tank for cooling in the rear stage, which is a pastoriser device that heats or cools the liquid in each container while continuously transporting the actual containers, It is equipped with a temperature sensor for adjusting the temperature and a steam supply valve, adjusts the temperature of the hot water in the preceding hot water tank, sends it to the hot water nozzle pipe by the hot water pump, adjusts the temperature of the hot water in the latter hot water tank, In a path riser treatment device equipped with a circulation system that circulates to the hot water nozzle pipe and a high temperature water pump, high temperature water circulation pipe, and high temperature water nozzle circulation pipe in the middle tank high temperature water circulation system, the warm water in the previous stage water tank is on the same hot water tank. A bypass pipe for circulating bypass to the hot water nozzle pipe, a bypass on-off valve installed in the pipe, an on-off valve for shutting off the circulation pipe from the pipe to the subsequent hot water nozzle, An actual container heat treatment apparatus characterized by having a check valve for preventing the flow toward the pump on the pipe of the subsequent stage hot water pump for sending the hot water to the nozzle pipe of the nozzle so that it can be used as a past riser and a container warmer. . 中段の高温水ポンプをインバータ制御モータにより駆動される可変吐出量ポンプとし、該可変吐出量ポンプの出口配管から前段の温水槽へ通じるバイパス配管と、該バイパス配管上に設置した開閉弁と、前記バイパス配管の分岐点より先の温水配管に設置した開閉弁とを追加してなることを特徴とする請求項1記載の実入り容器熱処理装置。   The middle high-temperature water pump is a variable discharge pump driven by an inverter control motor, a bypass pipe leading from the outlet pipe of the variable discharge pump to the preceding hot water tank, an on-off valve installed on the bypass pipe, 2. An actual container heat treatment apparatus according to claim 1, further comprising an on-off valve installed in the hot water pipe ahead of the branch point of the bypass pipe. 請求項1に記載する実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、中段、後段の高温水以降の処理水の加熱及び循環を止め、処理装置入口側の温水槽のノズル配管に前記バイパス配管より同じ温水槽の温水を回流し、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記温水槽内の加熱用スチームの流量を制御することを特徴とする実入り容器熱処理方法。   When switching from a pasteurizer process to a warmer process using the actual container heat treatment apparatus according to claim 1, the heating and circulation of the process water after the middle stage and the latter stage of the high temperature water are stopped, and the process apparatus inlet side The hot water in the same hot water tank is circulated from the bypass pipe to the nozzle pipe of the hot water tank, and the flow rate of the heating steam in the hot water tank is set so that the temperature detected by the temperature sensor installed in the hot water circulation pipe becomes the set value. An actual container heat treatment method characterized by controlling the temperature. 請求項2に記載する実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、前段、中段、後段の処理水の加熱スチームを止め、後段の温水ポンプを停止し、前記バイパス配管の分岐点より先の温水配管の開閉弁を閉じ、前記バイパス配管上の開閉弁を開き、前記可変吐出量ポンプより吐出する高温水を前段の温水槽に送り込み、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御し、高温水槽の水温が加温槽内の水温まで下がったときバイパス配管の高温水流入を閉じ、前段の温水槽用のスチームを通にして温水槽の循環と温水温度調整に移行することを特徴とする実入り容器熱処理方法。   When switching from a pasteurizer treatment to a warmer treatment using a filled container heat treatment apparatus according to claim 2, the heating steam of the first, middle, and second stages of treated water is stopped, and the second stage hot water pump is stopped. Close the on-off valve of the hot water pipe ahead of the branch point of the bypass pipe, open the on-off valve on the bypass pipe, and send the high-temperature water discharged from the variable discharge pump to the preceding hot water tank to the hot water circulation pipe The discharge amount of the variable discharge pump is controlled so that the temperature detected by the installed temperature sensor becomes the set value.When the water temperature in the high-temperature water tank falls to the water temperature in the heating tank, An actual container heat treatment method characterized in that the process proceeds to the circulation of the hot water tank and the adjustment of the hot water temperature through the steam for the hot water tank in the preceding stage. 中段の高温水槽の高温水を加熱するスチームの供給弁を開閉して高温水の温度がパストライザー稼動時の温度を維持するように制御し、前段の温水槽の温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御して、加温処理からパストライザー処理へ切換られるようにしたことを特徴とする請求項4記載の実入り容器熱処理方法。   A temperature sensor installed in the hot water circulation piping of the preceding hot water tank, controlling the temperature of the hot water to maintain the temperature at the time of pastrizer operation by opening and closing the steam supply valve that heats the hot water in the middle hot water tank The actual container according to claim 4, wherein the discharge amount of the variable discharge pump is controlled so as to switch from the warming process to the path riser process so that the detected temperature becomes a set value. Heat treatment method. 前段に温水槽、中段に高温水槽、後段に冷却用温水槽を配置し、実入り容器を連続搬送中に容器毎中身の液体を加熱又は冷却処理するパストライザー装置であって、各槽の水温を温度調整する温度センサとスチーム供給弁を備え、前段の温水槽の温水を温度調整して温水ポンプにより後段の温水ノズル配管へ送り出し、後段の温水槽の温水を温度調整して温水ポンプにより前段の温水ノズル配管へ回流する循環系と、中段槽高温水循環系に高温水ポンプと高温水循環配管と高温水ノズル循環配管を備えたパストライザー処理装置において、後段の温水槽の温水を同じ温水槽上の温水ノズル配管へ回流バイパスするバイパス配管と、該配管に設置されたバイパス開閉弁と、同配管から前段の温水ノズルへの循環配管を遮断する開閉弁と、前記後段のノズル配管へ温水を送り出す前段の温水ポンプの配管上に該ポンプへ向う流れを阻止する逆止弁を備えることによりパストライザーと容器ウォーマーを兼用できるようにしたことを特徴とする実入り容器熱処理装置。   A hot water tank in the front stage, a hot water tank in the middle stage, and a hot water tank for cooling in the rear stage, which is a pastoriser device that heats or cools the liquid in each container while continuously transporting the actual containers, It is equipped with a temperature sensor for adjusting the temperature and a steam supply valve, adjusts the temperature of the hot water in the preceding hot water tank, sends it to the hot water nozzle pipe by the hot water pump, adjusts the temperature of the hot water in the latter hot water tank, In a path riser treatment device equipped with a circulation system that circulates to the hot water nozzle pipe and a high-temperature water pump, high-temperature water circulation pipe, and high-temperature water nozzle circulation pipe in the middle tank high-temperature water circulation system, the hot water in the latter-stage hot water tank is placed on the same hot water tank. A bypass pipe for circulating bypass to the hot water nozzle pipe, a bypass on-off valve installed in the pipe, an on-off valve for shutting off the circulation pipe from the pipe to the preceding stage hot water nozzle, An actual container heat treatment apparatus characterized by having a check valve for preventing the flow toward the pump on the pipe of the preceding stage hot water pump for sending the hot water to the nozzle pipe of the container so that it can be used as a past riser and a container warmer. . 中段の高温水ポンプをインバータ制御モータにより駆動される可変吐出量ポンプとし、該可変吐出量ポンプの出口配管から後段の温水槽へ通じるバイパス配管と、該バイパス配管上に設置した開閉弁と、前記バイパス配管の分岐点より先の温水配管に設置した開閉弁とを追加してなることを特徴とする請求項6記載の実入り容器熱処理装置。   The middle high-temperature water pump is a variable discharge pump driven by an inverter control motor, a bypass pipe leading from the outlet pipe of the variable discharge pump to the subsequent hot water tank, an on-off valve installed on the bypass pipe, The actual container heat treatment apparatus according to claim 6, further comprising an on-off valve installed in the hot water pipe ahead of the branch point of the bypass pipe. 請求項6に記載する実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、前段、中段の高温水以降の処理水の加熱及び循環を止め、後段の温水槽のノズル配管に前記バイパス配管より同じ温水槽の温水を回流し、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記温水槽内の加熱用スチームの流量を制御することを特徴とする実入り容器熱処理方法。   When switching from a pasteurizer process to a warmer process using the actual container heat treatment apparatus according to claim 6, the heating and circulation of the treated water after the first stage and middle stage high temperature water are stopped, and the subsequent stage hot water tank The hot water in the same hot water tank is circulated from the bypass pipe to the nozzle pipe, and the flow rate of the heating steam in the hot water tank is controlled so that the temperature detected by the temperature sensor installed in the hot water circulation pipe becomes the set value. An actual container heat treatment method characterized by that. 請求項7に記載する実入り容器熱処理装置を用いて、パストライザー処理から低温の実入り容器をウォーマー処理に切換えるとき、前段、中段、後段の処理水の加熱スチームを止め、前段の温水ポンプを停止し、前記バイパス配管の分岐点より先の温水配管の開閉弁を閉じ、前記バイパス配管上の開閉弁を開き、前記可変吐出量ポンプより吐出する高温水を後段の温水槽に送り込み、温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御し、高温水槽の水温が加温槽内の水温まで下がったときバイパス配管の高温水流入を閉じ、後段の温水槽用のスチームを通にして温水槽の循環と温水温度調整に移行することを特徴とする実入り容器熱処理方法。   When switching from a pasteurizer process to a warmer process using the actual container heat treatment apparatus according to claim 7, the heating steam of the first, middle, and subsequent stages is stopped, and the warm water pump is stopped. Close the on-off valve of the hot water pipe ahead of the branch point of the bypass pipe, open the on-off valve on the bypass pipe, and send the high-temperature water discharged from the variable discharge pump to the hot water tank in the subsequent stage to the hot water circulation pipe The discharge amount of the variable discharge pump is controlled so that the temperature detected by the installed temperature sensor becomes the set value.When the water temperature in the high-temperature water tank falls to the water temperature in the heating tank, An actual container heat treatment method characterized in that the process proceeds to the circulation of the hot water tank and the adjustment of the hot water temperature through the steam for the hot water tank in the subsequent stage. 中段の高温水槽の高温水を加熱するスチーム供給弁を開閉して高温水の温度がパストライザー稼動時の温度を維持するように制御し、後段の温水槽の温水循環配管に設置した温度センサが検出した温度が設定値になるように、前記可変吐出量ポンプの吐出量を制御して、加温処理からパストライザー処理へ切換られるようにしたことを特徴とする請求項9記載の実入り容器熱処理方法。   The steam supply valve that heats the high-temperature water in the middle high-temperature water tank is opened and closed to control the temperature of the high-temperature water so that it maintains the temperature when the path riser is operating, and a temperature sensor installed in the hot-water circulation piping of the latter-stage hot water tank The actual container heat treatment according to claim 9, wherein the discharge amount of the variable discharge pump is controlled so that the detected temperature becomes a set value, and the heating process is switched to the path riser process. Method.
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