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JP4012954B2 - Liquid heat treatment equipment - Google Patents

Liquid heat treatment equipment Download PDF

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Publication number
JP4012954B2
JP4012954B2 JP9758198A JP9758198A JP4012954B2 JP 4012954 B2 JP4012954 B2 JP 4012954B2 JP 9758198 A JP9758198 A JP 9758198A JP 9758198 A JP9758198 A JP 9758198A JP 4012954 B2 JP4012954 B2 JP 4012954B2
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JP
Japan
Prior art keywords
liquid
heating
cooling
vertical
tube
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
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JP9758198A
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Japanese (ja)
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JPH11290043A (en
Inventor
良郎 山中
茂夫 平井
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Okawara Mfg Co Ltd
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Okawara Mfg Co Ltd
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Priority to JP9758198A priority Critical patent/JP4012954B2/en
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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【0001】
【発明の属する技術分野】
本願発明は、特に具入りタレやレトルトカレーのように、比較的大きな固形物を含む生の低温液体或いは調理済みの高温液体を無菌状態で加熱・冷却し、または加熱殺菌後冷却する液体の熱処理装置に関する。
【0002】
【従来の技術】
本出願人は、先に液体を間接的に加熱殺菌する「間接加熱装置」(特公平7−26758)を出願し特許を得ている。本装置は、加熱管内に設置された固定攪拌機により液体を攪拌しながら加熱するため、効率的に均一な加熱ができる特徴を有するものである。
【0003】
【発明が解決しようとする課題】
しかし、肉片あるいは具等の固形物が混在している液体の場合、それらが固定攪拌機に引っかかり液路を閉鎖したり、また固定攪拌機部に液体が残留する等の問題点があった。そこで本願発明の目的は、上記した問題点を解消した液体の熱処理装置を提供することにある。
【0004】
【課題を解決するための手段】
【0005】
上記目的を達成するため請求項 1 、液体給送手段により給送される液体を貯留する密閉槽と、密閉槽内の液体を攪拌する攪拌手段と、密閉槽の下部に設けた多数の縦管を有する多管式熱交換器からなり該密閉槽に貯留された液体を縦管内で流下させその外周を通流する加熱流体で液体を加熱する液体加熱手段と、液体加熱手段の下部に設けた多数の縦管を有する多管式熱交換器からなり該液体加熱手段で加熱された液体を縦管内で流下させその外周を通流する冷却水で液体を冷却する液体冷却手段とを備え、液体加熱手 段の縦管と液体冷却手段の縦管はそれぞれ連通して設けられ、さらに、液体冷却手段の下部に設けた液体冷却手段の縦管内を流下する液体を集める密閉ホッパと、密閉ホッパに集められた液体を排出ポンプによって排出する液体排出手段とを備えてなることを特徴とする。
【0006】
請求項は、液体給送手段により給送される液体を貯留する密閉槽と、密閉槽内の液体を攪拌する攪拌手段と、密閉槽の下部に設けた多数の縦管を有する多管式熱交換器からなり該密閉槽に貯留された液体を縦管内で流下させその外周を通流する加熱流体で液体を加熱する液体加熱手段と、液体加熱手段の下部に設けた多数の縦管内に該液体加熱手段で加熱された液体を流下させ液体を加熱された液体の温度に保持する液体高温保持手段と、液体高温保持手段の下部に設けた多数の縦管を有する多管式熱交換器からなり縦管内で液体を流下させその外周を通流する冷却水で液体を冷却する液体冷却手段とを備え、液体加熱手段の縦管と液体高温保持手段の縦管と液体冷却手段の縦管とはそれぞれ連通して設けられ、さらに、液体冷却手段の下部に設けた液体冷却手段の縦管内を流下する液体を集める密閉ホッパと、密閉ホッパに集められた液体を排出ポンプによって排出する液体排出手段とを備えてなることを特徴とする。
【0007】
【発明の実施の形態】
本願発明においては、特に肉片あるいは野菜等の固形物を含む液体、または高粘度の液体を好適に処理できるが、通常の液体も処理可能である。以下、本願発明の実施の形態にかかる液体の熱処理装置を図1〜図3を参照して説明する。液体の熱処理装置は、液体給送手段Aと、これにより給送される液体を貯留する密閉槽4と、密閉層4に貯留される液体を攪拌する液体攪拌手段Bと、密閉層4の下部に設けた多数の垂直に設置された縦管8dを有する多管式熱交換器8Aからなり液体を加熱する液体加熱手段Cと、液体加熱手段Cの下部に設けた多数の垂直に設置された縦管12d内に液体を流下させる多管式熱交換器からなる液体高温保持手段Dと、液体高温保持手段Dの下部に設けた多数の垂直に設置された縦管14aを有する多管式熱交換器14A,14B,14C,14Dを積層状態に4段備えてなり液体を冷却する液体冷却手段Eと、液体冷却手段 E の下部に設けた液体冷却手段 E の縦管内を流下する液体を集める密閉ホッパ17と、密閉ホッパ17に集めた液体を排出ポンプによって排出する排出する液体排出手段Fと、コントローラGを備えてなる。
【0008】
本願発明は、液体を加熱し一定時間温度保持して殺菌しその後冷却する上記の実施の形態の装置に限定されない。本願発明は、液体を加熱しその後冷却を行う装置を含んでおり、そのときは、図1の装置から液体高温保持手段Dを取り除いた装置とする。なお、縦管8d,12d,14aは熱伝導比率が高い銅管が用いられることが好ましいが、耐久性や防錆上の問題からはステンレス管であることが好ましい。
0009
液体給送手段Aは、図示しない大釜で煮沸調理されたカレー、その他の固形物を有する液体をオープンホッパ1に投入し、外気を遮断できしかも液体内の固形物を噛み潰す惧れがないロータリーポンプ等の給送ポンプ2によって管3を介して液体攪拌手段Bの密閉槽4の上部に給送するように構成されている。給送ポンプ2は、予め設定された既定流量の液体を供給する。
0010
液体攪拌手段Bは、密閉槽4の大径筒4aの上下端にリングフランジ4b,4cを取り付け、上側のリングフランジ4bに鏡板4dを被せてボルト・ナット4eで締付固定し、下側のリングフランジ4cを液体加熱手段Cの密閉槽8を構成する上側の鏡板8bとボルト・ナット4fで締付固定して蜜閉空間を形成している。そして、鏡板4dの中央に上端が枢支された回転軸5の下端に攪拌翼6が固定され、さらに鏡板4dの上面に取付けられたモータ7の出力軸と回転軸5の上端が固定連結されている。この攪拌翼6は、通常一定回転数で駆動される。攪拌翼6は、密閉槽8内の液体を攪拌し隅部での液体の固化を防ぎ液体中の固形物等を均質に分布させ、固形物が鏡板8bの上に堆積するのを防止し、液体加熱手段Cの縦管8d内に均一に供給する役目を果たす。
0011
液体加熱手段Cは、多数の縦管8dを有する多管式熱交換器8Aを備えてなる。該多管式熱交換器8Aは、大径筒8aの上下端に鏡板8b,8cを備え、該板8b,8cに設けられた小孔に上下端が密閉槽4と後述の縦管12dに連通している多数の縦管8dが挿通設置されている。そして、該縦管8dの外周の空間を垂直方向に蛇行する蛇行空間8nを形成するために、大径筒8aの内壁に多段に仕切板8eが水平設置され、該多段の仕切板8eに設けた小孔に縦管8dが挿通されている。また、大径筒8aの、蛇行空間8nの最下部及びその空間8nの最上部の各々の端部に間接加熱媒体入口8fと間接加熱媒体出口8gが設置されており、さらに縦管8dの下流側に温度センサ9を取り付けてある。また、大径筒8aの下部にドレン8hを設置している。液体加熱手段Cに用いられる間接加熱媒体は、例えば、熱水や蒸気が用いられる。それらは、ライン10から制御弁11を介して間接加熱媒体入口8fより密閉槽8内に導入される。その加熱媒体は、大径筒8aの蛇行空間8nを流れ、間接加熱媒体出口8gから排出される。これにより、縦管8dを間接加熱媒体で加熱し、縦管8d内を流通する液体を間接的に加熱する。
0012
コントローラGは、縦管8dの下流部で液体の温度を検出する温度センサ9の信号を受けて目標値と比較演算し、制御弁11で間接加熱媒体の供給量を調節し、加熱温度の制御を行う。該液体加熱手段Cは、固形物を含む液体が多数の縦管8d内を通ることによって該管8d内に液体が溜まらず自重で流下させるとともに、縦管8dの外周を流通する加熱水が蛇行上昇する流れとなっていて、液体に対して対向流となり高い熱効率が得られる構造となっている。
0013
液体高温保持手段Dは、大径筒12aの上下端に鏡板12b,12cを取り付け、鏡板12b,12cに設けられた小孔に上下端が解放された多数の縦管12dが設けられ、大径筒12aにおける縦管12dの外周の空間が密閉され外気との間の熱交換が極小に抑えられてなる。液体高温保持手段Dの多数の縦管12dの上端は、前述の通り液体加熱手段Cの多数の縦管8dと各々対応して連通し、引続き液体が流下するように案内する。一方下端部は、後述の縦管14aと連通している。液体は、縦管12d内を流下するので該管12d内に溜まる惧れがない。前記温度センサ9は、縦管12dの下流側に設けてもよい。液体高温保持手段Dは、上側の鏡板12bと液体加熱手段Cの下側の鏡板8cと合わされボルト・ナット13により締付固定されることにより形成され、縦管12d内を流下する液体の温度を保つことにより殺菌を行う役目を果たす。
0014
液体冷却手段Eは、積層されボルト・ナット15a〜15cで連結された多数の縦管14aを備えた例えば4段の多管式熱交換器14A〜14Dを備えてなる。一番上の多管式熱交換器14Dは、前記液体高温保持手段Dの下側に積層されボルト・ナット15cで該手段D連結されている。4段の多管式熱交換器14A〜14Dの多数の縦管14aは各々対応して連通しており、かつ前述の通り液体高温保持手段Dの多数の縦管12dと各々対応して連通し、引続き液体が流下するように案内する。一方縦管14aの下端部は、後述の密閉ホッパ17に連通している。
0015
多管式熱交換器14A〜14Dは、液体加熱手段Cの多管式熱交換器8Aと実質的に同一の構造である。すなわち、仕切板14nにより蛇行空間14mが形成され、該空間14mを間接加熱媒体が流れ液体を間接的に加熱するのである。一番下に位置する第一の多管式熱交換器14Aの冷却水出口14cとその上の第二の多管式熱交換器14Bの冷却水入口14dとが、第一の三方弁16aを介して接続されている。そして、第二の多管式熱交換器14Bの冷却水出口14eとその上の第三の多管式熱交換器14Cの冷却水入口14fとが、第二の三方弁16bを介して接続されている。そしてさらに、第三の多管式熱交換器14Cの冷却水出口14gとその上の第四の多管式熱交換器14Dの冷却水入口14hとが第三の三方弁16cを介して接続されている。多管式熱交換器14A〜14Dはそれぞれドレン14jを有している。
0016
液体排出手段Fは、第一の多管式熱交換器14Aの縦管14aを流下する液体を密閉ホッパ17に集め、上流と下流を遮断できかつ液体内の固形物を噛み潰す惧れがないロータリーポンプ等の給送ポンプ18によって管19を介して図示しない充填包装機へ給送するように構成されている。密閉ホッパ17には、必要に応じ円錐面を覆う冷却ジャケット20が付設されている。該冷却ジャケット20には、下部に冷却水入口20aが、また反対側上部に冷却水出口20bが設けられている。コントローラHは、密閉ホッパ17内の圧力を検出する圧力センサ21の信号を受けて目標値圧力と比較演算し、高いときは給送ポンプ18の流量を大きくし、小さいときは給送ポンプ18の流量を小さくするように制御する。密閉ホッパ17のリングフランジ17aと多管式熱交換器14Aの鏡板14kが架台26に載置されボルト・ナット15eで連結され固定されている。
0017
冷却水出口20bは、管22により第一の多管式熱交換器14Aの冷却水入口14bと連通され、冷却水入口20aは、管22を介してポンプ23と冷却装置24と接続され、さらに、冷却装置24の入口は、戻り管25により前記の第一ないし第三の三方弁16a,16b,16cの帰還ポート16d,16e,16f、及び冷却水出口14iと接続されている。冷却装置24で例えば約10℃に冷やされた水は、ポンプ23により給送され、冷却ジャケット20内に流入して密閉ホッパ17内の液体を冷却した後、順に、第一ないし第四の多管式熱交換器14A〜14Dの縦管14aの外周を流通し、縦管14a内を流下する液体を冷却する。
0018
液体高温保持手段Dにおいて高温保持時間が短すぎるときは、第四の多管式熱交換器14Dを液体高温保持手段として使用することもできる。この場合には、第三の三方弁16cを操作しその帰還ポート16fと第三の多管式熱交換器14Cの冷却水出口14gとを連通させて、第一ないし第三の多管式熱交換器14A,14B,14Cを第一及び第二の三方弁16a,16bを介して連通状態とし、冷却水を第三の三方弁16cの帰還ポート16fより戻り管25に途中帰還させる。また、多管式熱交換器14Cも液体高温保持手段として使用するときは、第二の三方弁16bも、帰還側ポート16eと第二の多管式熱交換器14Bの冷却水出口14lとを連通し、冷却水を第二の三方弁16bの帰還ポート16eより戻り管25に途中帰還させる。さらに、多管式熱交換器14Bも液体高温保持手段として使用するときは、第一の三方弁16aも、帰還側ポートと第一の多管式熱交換器14Aの接続ポートとを連通し、冷却水を第一の三方弁16aの帰還ポートより循環経路に途中帰還させる。従って、この液体冷却手段Eは、多管式熱交換器を積層状態に4段備えて、下側から少なくとも1段を除く残りの熱交換器14B,14C,14Dを、前記液体高温保持手段として選択的に使用することも可能である。
【0019】
【作用】
肉片あるいは具のような固形物が混在している液体が、まずオープンホッパ1貯められ、次いで給液ポンプ2により密閉槽4に供給される。そこで液体は固形物と分離しないように攪拌されながら、液体加熱手段Cの縦管8d中を流下し、液体加熱手段Cで加熱殺菌される。以降液体は、縦管12d,14a中を流下しながら、液体高温保持手段Dで高温保持され、次いで液体冷却手段E冷却され、密閉ホッパ17に到達する。その後給液ポンプ18により次行程に送られる。なお、液体は液体加熱手段においては、温度コントローラGにより温度が制御され、また、コントローラHにより圧力が制御され、常に縦管8d,12d,14a中に液体が充満するよう調整されている。
【0020】
【発明の効果】
以上説明してきたように、本願における請求項によれば、液体を溜めて流下させ、流下中に、液体を加熱しその後冷却することができ、特に具入りタレやレトルトカレーのように、比較的大きな固形物を含む生の低温液体或いは調理済みの高温液体が重力作用により縦管内を流下するので、省エネルギーになり、液体が多量に管内に残る惧れがなく、従来装置に比べて経済的である。さらにまた、請求項によれば、液体を溜めて流下させ、流下中に、液体を加熱し一定時間温度保持して殺菌しその後冷却することができ、特に具入りタレやレトルトカレーのように、比較的大きな固形物を含む生の低温液体或いは調理済みの高温液体が重力作用により縦管内を流下するので、省エネルギーになり、液体が多量に管内に残る惧れがなく、従来装置に比べて経済的である。さらにまた、縦管中には何も設置していないので、作業終了後液体を全量排出でき、その後水を送るだけで縦管の掃除ができる。
【0021】
【図面の簡単な説明】
【図1】液体の熱処理装置の正面図。
【図2】液体の熱処理装置における液体加熱手段、液体加熱手段、及び液体高温保持手段部の拡大正面断面図
【図3】液体の熱処理装置における液体冷却手段、及び液体冷却手段部の拡大正面断面図
【符号の説明】
A 液体給送手段
B 液体攪拌手段
C 液体加熱手段
D 液体高温保持手段
E 液体冷却手段
F 液体排出手段
4 密閉槽
6 攪拌翼
8d 液体加熱手段の縦管
12d 液体高温保持手段の縦管
14a 液体冷却手段の縦管
17 密閉ホッパ
18 排出ポンプ
[0001]
BACKGROUND OF THE INVENTION
The present invention is a heat treatment of a liquid that heats or cools a raw low-temperature liquid containing a relatively large solid or a cooked high-temperature liquid in an aseptic condition, or cools after heat sterilization, such as a sauce or retort curry. Relates to the device.
[0002]
[Prior art]
The present applicant has previously applied for and obtained a patent for an “indirect heating device” (Japanese Patent Publication No. 7-267 58 ) for indirectly heating and sterilizing a liquid. Since this apparatus heats a liquid while stirring it with a fixed stirrer installed in a heating tube, it has a feature that enables uniform heating efficiently.
[0003]
[Problems to be solved by the invention]
However, in the case of liquids in which solids such as meat pieces or utensils are mixed, there are problems that they are caught by a fixed stirrer and the liquid path is closed, or the liquid remains in the fixed stirrer part. Accordingly, an object of the present invention is to provide a liquid heat treatment apparatus that solves the above-mentioned problems.
[0004]
[Means for Solving the Problems]
[0005]
In order to achieve the above object, claim 1 provides a sealed tank for storing the liquid fed by the liquid feeding means, a stirring means for stirring the liquid in the sealed tank, and a number of vertical pipes provided in the lower part of the sealed tank. A liquid heating means comprising a multi-tube heat exchanger having a tube, and a liquid heating means for heating the liquid with a heating fluid flowing down in the vertical pipe and flowing through the outer periphery of the liquid stored in the sealed tank; and provided below the liquid heating means Liquid cooling means comprising a multi-tubular heat exchanger having a number of vertical tubes and liquid cooled by the cooling water flowing down the outer periphery of the liquid heated by the liquid heating means and flowing through the outer periphery thereof , the vertical pipe of the vertical pipe and the liquid cooling unit in the liquid heating hand stage provided to communicate with each further comprises a sealed hopper for collecting the liquid flowing down the vertical tube of the liquid cooling means provided in the lower part of the liquid cooling means, closed hopper The liquid collected in the tank is discharged by the discharge pump And a liquid discharging means.
[0006]
Claim 2 is a multitubular type having a sealed tank for storing the liquid fed by the liquid feeding means, a stirring means for stirring the liquid in the sealed tank, and a number of vertical tubes provided at the lower part of the sealed tank. A liquid heating means that consists of a heat exchanger and flows down in the vertical tube and heats the liquid with a heating fluid flowing through the outer periphery of the liquid, and in a number of vertical tubes provided below the liquid heating means A liquid high temperature holding means for flowing down the liquid heated by the liquid heating means and holding the liquid at the temperature of the heated liquid, and a multi-tube heat exchanger having a number of vertical tubes provided below the liquid high temperature holding means Liquid cooling means for cooling the liquid with cooling water flowing down in the vertical pipe and flowing through the outer periphery of the vertical pipe, the vertical pipe of the liquid heating means, the vertical pipe of the liquid high temperature holding means, and the vertical pipe of the liquid cooling means Are provided in communication with each other, and further under the liquid cooling means. A sealed hopper for collecting the liquid flowing down the vertical tube of the liquid cooling means provided, characterized by comprising a liquid discharge means for discharging the collected liquid discharge pump in a closed hopper.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, a liquid containing solids such as meat pieces or vegetables, or a highly viscous liquid can be suitably processed, but a normal liquid can also be processed. A liquid heat treatment apparatus according to an embodiment of the present invention will be described below with reference to FIGS. The liquid heat treatment apparatus includes a liquid feeding means A, a sealed tank 4 for storing the liquid fed thereby, a liquid stirring means B for stirring the liquid stored in the sealed layer 4, and a lower portion of the sealed layer 4 A multi-tube heat exchanger 8A having a plurality of vertically installed vertical tubes 8d, and a liquid heating means C for heating the liquid, and a plurality of vertical installations provided below the liquid heating means C. A multi-tube heat having a liquid high-temperature holding means D composed of a multi-tube heat exchanger that causes liquid to flow down into the vertical pipe 12d, and a plurality of vertically installed vertical tubes 14a provided below the liquid high-temperature holding means D. The exchangers 14A, 14B, 14C, and 14D are provided in four layers in a stacked state, and the liquid cooling means E that cools the liquid and the liquid that flows down in the vertical pipe of the liquid cooling means E provided below the liquid cooling means E are collected. Sealed hopper 17 and liquid collected in sealed hopper 17 And the liquid discharge means F for exhausting discharged by the discharge pump, comprising a controller G.
[0008]
The present invention is not limited to the apparatus of the above-described embodiment that heats a liquid, maintains the temperature for a certain period of time, sterilizes, and then cools. The present invention includes a device that heats the liquid and then cools it. In this case, the device is obtained by removing the liquid high temperature holding means D from the device shown in FIG. The vertical tubes 8d, 12d, and 14a are preferably copper tubes having a high heat conduction ratio, but are preferably stainless steel tubes from the viewpoint of durability and rust prevention.
[ 0009 ]
The liquid feeding means A is a rotary that can block curry cooked in a cauldron (not shown) and other solid-containing liquid into the open hopper 1 to block the outside air and crush the solid in the liquid. The feed pump 2 such as a pump is fed to the upper part of the closed tank 4 of the liquid stirring means B through the pipe 3. The feed pump 2 supplies a predetermined flow rate of liquid.
[ 0010 ]
The liquid stirring means B has ring flanges 4b and 4c attached to the upper and lower ends of the large-diameter cylinder 4a of the sealed tank 4, and a top plate 4d is put on the upper ring flange 4b and fastened and fixed with bolts and nuts 4e. The ring flange 4c is fastened and fixed by the upper end plate 8b constituting the sealed tank 8 of the liquid heating means C and the bolt / nut 4f to form a closed space. The stirring blade 6 is fixed to the lower end of the rotating shaft 5 whose upper end is pivotally supported at the center of the end plate 4d, and the output shaft of the motor 7 attached to the upper surface of the end plate 4d and the upper end of the rotating shaft 5 are fixedly connected. ing. The stirring blade 6 is normally driven at a constant rotational speed. The stirring blade 6 stirs the liquid in the sealed tank 8 to prevent solidification of the liquid at the corners and distributes solids in the liquid uniformly, and prevents the solids from depositing on the end plate 8b. It plays the role of supplying uniformly into the vertical tube 8d of the liquid heating means C.
[ 0011 ]
The liquid heating means C includes a multi-tube heat exchanger 8A having a large number of vertical tubes 8d. The multi-tube heat exchanger 8A includes end plates 8b and 8c at the upper and lower ends of the large-diameter tube 8a, and the upper and lower ends of the small holes provided in the plates 8b and 8c are connected to the sealed tank 4 and a vertical tube 12d to be described later. A large number of communicating vertical pipes 8d are installed. And in order to form the meandering space 8n which meanders the space of the outer periphery of the vertical pipe 8d in the vertical direction, the partition plates 8e are horizontally installed on the inner wall of the large-diameter tube 8a, and are provided on the multi-stage partition plates 8e. A vertical tube 8d is inserted through the small hole. In addition, an indirect heating medium inlet 8f and an indirect heating medium outlet 8g are installed at the ends of the lowermost part of the meandering space 8n and the uppermost part of the space 8n of the large diameter cylinder 8a, and further downstream of the vertical pipe 8d. A temperature sensor 9 is attached to the side. Further, a drain 8h is installed at the lower part of the large diameter cylinder 8a. As the indirect heating medium used in the liquid heating means C, for example, hot water or steam is used. They are introduced into the sealed tank 8 from the indirect heating medium inlet 8 f through the control valve 11 from the line 10. The heating medium flows through the meandering space 8n of the large-diameter cylinder 8a and is discharged from the indirect heating medium outlet 8g. Thereby, the vertical pipe 8d is heated with an indirect heating medium, and the liquid flowing through the vertical pipe 8d is indirectly heated.
[ 0012 ]
The controller G receives a signal from the temperature sensor 9 that detects the temperature of the liquid downstream of the vertical tube 8d, compares it with the target value, adjusts the supply amount of the indirect heating medium by the control valve 11, and controls the heating temperature. I do. The liquid heating means C allows the liquid containing the solids to flow through the numerous vertical tubes 8d so that the liquid does not accumulate in the tubes 8d and flows down by its own weight, and the heating water flowing through the outer periphery of the vertical tube 8d meanders. The flow is an ascending flow, which is a counter flow with respect to the liquid, and has a structure in which high thermal efficiency is obtained.
[ 0013 ]
The liquid high temperature holding means D is provided with end plates 12b and 12c at the upper and lower ends of the large-diameter tube 12a, and provided with a large number of vertical tubes 12d having upper and lower ends released in small holes provided in the end plates 12b and 12c. The space on the outer periphery of the vertical tube 12d in the cylinder 12a is sealed, and heat exchange with the outside air is minimized. The upper ends of the multiple vertical tubes 12d of the liquid high temperature holding means D communicate with the multiple vertical tubes 8d of the liquid heating means C in correspondence with each other as described above, and continue to guide the liquid to flow down. On the other hand, the lower end communicates with a vertical tube 14a described later. Since the liquid flows down in the vertical pipe 12d, there is no possibility that the liquid will accumulate in the pipe 12d. The temperature sensor 9 may be provided on the downstream side of the vertical pipe 12d. The liquid high temperature holding means D is formed by joining the upper end plate 12b and the lower end plate 8c of the liquid heating means C and fastening them with bolts and nuts 13, and the temperature of the liquid flowing down in the vertical tube 12d is adjusted. It plays the role of sterilizing by keeping.
[ 0014 ]
The liquid cooling means E includes, for example, four-stage multi-tubular heat exchangers 14A to 14D including a plurality of vertical tubes 14a stacked and connected by bolts and nuts 15a to 15c. The uppermost multi-tubular heat exchanger 14D is stacked below the liquid high temperature holding means D and connected to the means D by bolts and nuts 15c. A large number of vertical tubes 14a of the four-stage multitubular heat exchangers 14A to 14D communicate with each other, and communicate with the large number of vertical tubes 12d of the liquid high temperature holding means D as described above. Subsequently, the liquid is guided to flow down. On the other hand, the lower end portion of the vertical pipe 14a communicates with a sealing hopper 17 described later.
[ 0015 ]
The multitubular heat exchangers 14A to 14D have substantially the same structure as the multitubular heat exchanger 8A of the liquid heating means C. That is, the meandering space 14m is formed by the partition plate 14n, and an indirect heating medium flows through the space 14m to indirectly heat the liquid. The cooling water outlet 14c of the first multi-tubular heat exchanger 14A located at the bottom and the cooling water inlet 14d of the second multi-tubular heat exchanger 14B thereabove connect the first three-way valve 16a. Connected through. Then, the cooling water outlet 14e of the second multi-tubular heat exchanger 14B and the cooling water inlet 14f of the third multi-tubular heat exchanger 14C thereon are connected via the second three-way valve 16b. ing. Further, the cooling water outlet 14g of the third multi-tube heat exchanger 14C and the cooling water inlet 14h of the fourth multi-tube heat exchanger 14D thereon are connected via a third three-way valve 16c. ing. Each of the multi-tube heat exchangers 14A to 14D has a drain 14j.
[ 0016 ]
The liquid discharge means F collects the liquid flowing down the vertical pipe 14a of the first multitubular heat exchanger 14A in the hermetic hopper 17, can block the upstream and downstream, and does not possibly crush solids in the liquid. A feed pump 18 such as a rotary pump is configured to feed a filling and packaging machine (not shown) through a pipe 19. The hermetic hopper 17 is provided with a cooling jacket 20 that covers the conical surface as necessary. The cooling jacket 20 is provided with a cooling water inlet 20a at the lower part and a cooling water outlet 20b at the upper part on the opposite side. The controller H receives a signal from the pressure sensor 21 that detects the pressure in the hermetic hopper 17 and compares it with the target value pressure. When the signal is high, the flow rate of the feed pump 18 is increased. Control to reduce the flow rate. The ring flange 17a of the hermetic hopper 17 and the end plate 14k of the multi-tube heat exchanger 14A are placed on a mount 26 and connected and fixed by bolts and nuts 15e.
[ 0017 ]
The cooling water outlet 20b is communicated with the cooling water inlet 14b of the first multi-tubular heat exchanger 14A through the pipe 22, and the cooling water inlet 20a is connected to the pump 23 and the cooling device 24 via the pipe 22. The inlet of the cooling device 24 is connected to the return ports 16d, 16e, 16f of the first to third three-way valves 16a, 16b, 16c and the cooling water outlet 14i by a return pipe 25. The water cooled to, for example, about 10 ° C. by the cooling device 24 is fed by the pump 23 and flows into the cooling jacket 20 to cool the liquid in the sealed hopper 17. The liquid which flows through the outer periphery of the vertical tube 14a of the tubular heat exchangers 14A to 14D and cools down in the vertical tube 14a is cooled.
[ 0018 ]
When the high temperature holding time is too short in the liquid high temperature holding means D, the fourth multitubular heat exchanger 14D can be used as the liquid high temperature holding means. In this case, the third three-way valve 16c is operated so that the return port 16f and the cooling water outlet 14g of the third multi-tube heat exchanger 14C communicate with each other, and the first to third multi-tube heat The exchangers 14A, 14B, and 14C are brought into a communication state via the first and second three-way valves 16a and 16b, and the cooling water is returned to the return pipe 25 on the way from the return port 16f of the third three-way valve 16c. When the multi-tube heat exchanger 14C is also used as the liquid high temperature holding means, the second three-way valve 16b also has a return side port 16e and a cooling water outlet 14l of the second multi-tube heat exchanger 14B. The cooling water is returned to the return pipe 25 from the return port 16e of the second three-way valve 16b. Further, when the multi-tube heat exchanger 14B is also used as the liquid high temperature holding means, the first three-way valve 16a also communicates the return side port with the connection port of the first multi-tube heat exchanger 14A, The cooling water is returned to the circulation path from the return port of the first three-way valve 16a. Therefore, this liquid cooling means E includes four stages of multi-tubular heat exchangers in a stacked state, and the remaining heat exchangers 14B, 14C, 14D excluding at least one stage from the lower side are used as the liquid high temperature holding means. It can also be used selectively.
[0019]
[Action]
A liquid in which solids such as meat pieces or utensils are mixed is first stored in the open hopper 1, and then supplied to the sealed tank 4 by the liquid supply pump 2. Therefore, the liquid flows down in the vertical tube 8d of the liquid heating means C while being stirred so as not to separate from the solid matter, and is sterilized by heating with the liquid heating means C. Thereafter, the liquid is held at a high temperature by the liquid high temperature holding means D while flowing down through the vertical pipes 12 d and 14 a, then cooled by the liquid cooling means E, and reaches the sealed hopper 17. Thereafter, it is sent to the next process by the liquid supply pump 18. In the liquid heating means, the temperature of the liquid is controlled by the temperature controller G, and the pressure is controlled by the controller H, so that the liquid is always filled in the vertical tubes 8d, 12d, and 14a.
[0020]
【The invention's effect】
As described above, according to claim 1 in this application, the reservoir fluid is flowing down, during flow, the liquid can be heated and then cooled, so that in particular fillings containing sauce or retort curry, comparison As raw cryogenic liquid containing large solids or cooked hot liquid flows down in the vertical pipe due to gravity action, it saves energy and there is no risk of a large amount of liquid remaining in the pipe, making it economical compared to conventional devices It is. Furthermore, according to claim 2 , the liquid can be accumulated and flowed down, and during the flow, the liquid can be heated and kept at a certain temperature for sterilization and then cooled, particularly like a sauce or a retort curry. , Raw cryogenic liquid containing relatively large solids or cooked hot liquid flows down the vertical pipe due to gravity action, saving energy, and there is no fear that a large amount of liquid will remain in the pipe, compared to conventional devices Economical. Furthermore, since nothing is installed in the vertical pipe, the entire liquid can be discharged after the work is completed, and then the vertical pipe can be cleaned simply by sending water.
[0021]
[Brief description of the drawings]
FIG. 1 is a front view of a liquid heat treatment apparatus.
FIG. 2 is an enlarged front sectional view of a liquid heating means, a liquid heating means, and a liquid high temperature holding means section in a liquid heat treatment apparatus. FIG. 3 is an enlarged front sectional view of a liquid cooling means and a liquid cooling means section in a liquid heat treatment apparatus. Figure [Explanation of symbols]
A Liquid feeding means B Liquid stirring means C Liquid heating means D Liquid high temperature holding means E Liquid cooling means F Liquid discharging means 4 Sealed tank 6 Stirring blade 8d Vertical tube 12d of liquid heating means Vertical tube 14a of liquid high temperature holding means Liquid cooling Means vertical pipe 17 Sealed hopper 18 Discharge pump

Claims (3)

液体給送手段により給送される液体を貯留する密閉槽と、密閉槽内の液体を攪拌する攪拌手段と、密閉槽の下部に設けた多数の縦管を有する多管式熱交換器からなり該密閉槽に貯留された液体を縦管内で流下させその外周を通流する加熱流体で液体を加熱する液体加熱手段と、液体加熱手段の下部に設けた多数の縦管を有する多管式熱交換器からなり該液体加熱手段で加熱された液体を縦管内で流下させその外周を通流する冷却水で液体を冷却する液体冷却手段とを備え、液体加熱手段の縦管と液体冷却手段の縦管はそれぞれ連通して設けられ、さらに、液体冷却手段の下部に設けた液体冷却手段の縦管内を流下する液体を集める密閉ホッパと、密閉ホッパに集められた液体を排出ポンプによって排出する液体排出手段とを備えてなることを特徴とする液体の熱処理装置。It consists of a sealed tank for storing the liquid fed by the liquid feeding means, a stirring means for stirring the liquid in the sealed tank, and a multi-tube heat exchanger having a number of vertical tubes provided at the bottom of the sealed tank. A multi-tube heat having a liquid heating means for heating the liquid stored in the sealed tank in a vertical pipe and heating the liquid with a heating fluid flowing through the outer periphery thereof, and a number of vertical pipes provided below the liquid heating means. And a liquid cooling means for cooling the liquid heated by the liquid heating means and cooling the liquid with cooling water flowing through the outer periphery of the liquid heating means. the vertical pipe is provided to communicate with each addition, the liquid to be discharged and sealed hopper to collect the liquid flowing down the vertical tube of the liquid cooling means provided in the lower part of the liquid cooling means, the collected liquid in a sealed hopper by the discharge pump Having a discharge means Heat treatment apparatus of the liquid to symptoms. 液体給送手段により給送される液体を貯留する密閉槽と、密閉槽内の液体を攪拌する攪拌手段と、密閉槽の下部に設けた多数の縦管を有する多管式熱交換器からなり該密閉槽に貯留された液体を縦管内で流下させその外周を通流する加熱流体で液体を加熱する液体加熱手段と、液体加熱手段の下部に設けた多数の縦管内に該液体加熱手段で加熱された液体を流下させ液体を加熱された液体の温度に保持する液体高温保持手段と、液体高温保持手段の下部に設けた多数の縦管を有する多管式熱交換器からなり縦管内で液体を流下させその外周を通流する冷却水で液体を冷却する液体冷却手段とを備え、液体加熱手段の縦管と液体高温保持手段の縦管と液体冷却手段の縦管とはそれぞれ連通して設けられ、さらに、液体冷却手段の下部に設けた液体冷却手段の縦管内を流下する液体を集める密閉ホッパと、密閉ホッパに集められた液体を排出ポンプによって排出する液体排出手段とを備えてなることを特徴とする液体の熱処理装置。It consists of a sealed tank for storing the liquid fed by the liquid feeding means, a stirring means for stirring the liquid in the sealed tank, and a multi-tube heat exchanger having a number of vertical tubes provided at the bottom of the sealed tank. Liquid heating means for heating the liquid stored in the hermetic tank in the vertical tube and heating the liquid with a heating fluid flowing through the outer periphery of the liquid, and a number of vertical tubes provided in the lower part of the liquid heating means with the liquid heating means. A liquid high temperature holding means for letting the heated liquid flow down and holding the liquid at the temperature of the heated liquid, and a multi-tubular heat exchanger having a number of vertical tubes provided below the liquid high temperature holding means , Liquid cooling means for cooling the liquid with cooling water flowing down and flowing through the outer periphery thereof, and the vertical tube of the liquid heating means, the vertical tube of the liquid high temperature holding means, and the vertical tube of the liquid cooling means communicate with each other. provided Te, further, a liquid which is provided in the lower part of the liquid cooling means A sealed hopper for collecting the liquid flowing down the vertical tube of the cooling means, the heat treatment apparatus of the liquid, characterized by comprising a liquid discharge means for discharging the collected liquid discharge pump in a closed hopper. 液体冷却手段は、多管式熱交換器を積層状態に2段以上備えて、下側から少なくとも1段目の液体冷却手段を除く残りの液体冷却手段を、該液体高温保持手段に選択使用できる構成としたことを特徴とする請求項3に記載の液体の熱処理装置。 The liquid cooling means includes two or more stages of multi-tubular heat exchangers in a stacked state, and the remaining liquid cooling means excluding at least the first stage liquid cooling means from the lower side can be selectively used as the liquid high temperature holding means. The liquid heat treatment apparatus according to claim 3, wherein the liquid heat treatment apparatus is configured.
JP9758198A 1998-04-09 1998-04-09 Liquid heat treatment equipment Expired - Fee Related JP4012954B2 (en)

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