JPH0581297B2 - - Google Patents
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- Publication number
- JPH0581297B2 JPH0581297B2 JP23879689A JP23879689A JPH0581297B2 JP H0581297 B2 JPH0581297 B2 JP H0581297B2 JP 23879689 A JP23879689 A JP 23879689A JP 23879689 A JP23879689 A JP 23879689A JP H0581297 B2 JPH0581297 B2 JP H0581297B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- cooling
- tank
- pump
- heating
- 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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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 239000012530 fluid Substances 0.000 claims description 39
- 238000001816 cooling Methods 0.000 claims description 36
- 238000010438 heat treatment Methods 0.000 claims description 34
- 239000000498 cooling water Substances 0.000 claims description 18
- 238000007599 discharging Methods 0.000 claims 1
- 239000002994 raw material Substances 0.000 description 11
- 230000007423 decrease Effects 0.000 description 3
- 239000003990 capacitor Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
【発明の詳細な説明】
<産業上の利用分野>
本発明は加熱と冷却を交互に行う加熱冷却装置
に関する。上記の加熱冷却装置としては、各種加
硫装置や食品の洗浄、殺菌装置等がある。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a heating and cooling device that alternately performs heating and cooling. Examples of the above-mentioned heating and cooling devices include various vulcanizing devices, food washing and sterilization devices, and the like.
<従来の技術>
従来の加熱冷却装置として、第2図に示す様な
加熱冷却装置がある。図において、1は加熱冷却
用の流体室であり、原料の被加熱及び被冷却物を
該流体室に入れて加熱冷却を行う。流体室1に蒸
気供給管10及び冷却水排出管11を接続し、そ
の一方には冷却水供給管8及びドレン排出管9を
接続する。各管の途中に弁V1,V2,V3,V
4を設けてある。この流体室1内の原料を加熱す
る場合は、弁V2,V4を閉じ、弁V1,V3を
開く。これによつて蒸気が管10から流体室1内
に供給されて加熱が行なわれる。その時発生する
ドレンは、弁V3、ドレン排出管9を通つて排出
される。図中12はスチームトラツプでドレンの
みを排出する。<Prior Art> As a conventional heating/cooling device, there is a heating/cooling device as shown in FIG. In the figure, reference numeral 1 denotes a fluid chamber for heating and cooling, and materials to be heated and cooled, such as raw materials, are placed in the fluid chamber and heated and cooled. A steam supply pipe 10 and a cooling water discharge pipe 11 are connected to the fluid chamber 1, and a cooling water supply pipe 8 and a drain discharge pipe 9 are connected to one of them. Valve V1, V2, V3, V in the middle of each pipe
4 is provided. When heating the raw material in this fluid chamber 1, valves V2 and V4 are closed and valves V1 and V3 are opened. As a result, steam is supplied from the pipe 10 into the fluid chamber 1 for heating. Drain generated at that time is discharged through valve V3 and drain discharge pipe 9. In the figure, 12 is a steam trap that discharges only the drain.
また冷却する場合は、弁V1,V3を閉じ、弁
V2,V4を開く。これによつて冷却水が管8を
通つて流体室1内に供給されて冷却が行なわれ
る。供給された冷却水は冷却水排出管11を通つ
て排出される。 When cooling, valves V1 and V3 are closed and valves V2 and V4 are opened. As a result, cooling water is supplied into the fluid chamber 1 through the pipe 8 for cooling. The supplied cooling water is discharged through a cooling water discharge pipe 11.
<発明が解決しようとする課題>
上記従来の加熱冷却装置は、冷却に続いて加熱
あるいは加熱に続いて冷却が行なわれるような場
合にハンマー現象が発生して、その振動及び衝撃
により、原料としての被加熱物及び被冷却物、並
びに、装置が損傷する問題がある。この原因は、
加熱と冷却の切換時には、流体室1及びその内部
に連通している管8,9,10,11の部分の温
度並びにこれらの各部に残存している流体の温度
に対して、新たに供給される流体の温度に大きな
温度差があるためである。<Problems to be Solved by the Invention> In the conventional heating/cooling device described above, a hammer phenomenon occurs when heating is performed after cooling, or when cooling is performed following heating, and the vibration and impact cause the raw material to There is a problem that the objects to be heated and cooled, as well as the equipment, may be damaged. The cause of this is
When switching between heating and cooling, the temperature of the fluid chamber 1 and the portions of the pipes 8, 9, 10, and 11 communicating therein, as well as the temperature of the fluid remaining in each of these portions, is adjusted to the temperature of the fluid that is newly supplied. This is because there is a large temperature difference between the fluid temperatures.
また、冷却時において、原料を均一に冷却でき
ず、部分的な異常昇温が発生しやすく、この温度
ムラによつて製品の品質を一定に維持し難い問題
がある。この原因は、冷却水による冷却であるた
め、冷却水の顕熱のみによる冷却となり熱容量が
小さいためである。 Furthermore, during cooling, the raw material cannot be cooled uniformly, and local abnormal temperature increases tend to occur, and this temperature unevenness makes it difficult to maintain constant product quality. The reason for this is that since cooling is performed using cooling water, the cooling is performed only by the sensible heat of the cooling water, and the heat capacity is small.
従つて本発明の技術的課題は、加熱冷却装置に
おいて、加熱と冷却との切換時の前記温度差を小
さくすることができ、冷却時の前記熱容量を大き
くすることができるようにすることである。 Therefore, the technical problem of the present invention is to enable a heating and cooling device to reduce the temperature difference when switching between heating and cooling, and to increase the heat capacity during cooling. .
<課題を解決する為の手段>
上記課題を解決する為に講じた本発明の技術的
手段は、エゼクタのデイフユーザとポンプの吸込
口とをタンクを介して連通し、該タンク内へ冷却
水を供給してタンク内水温を制御する制御部を設
け、前記ポンプの吐出口を前記エゼクタのノズル
に接続し、ポンプによる循環水の余剰水を系外に
排出する排出手段を配したポンプ装置を設け、該
ポンプ装置のエゼクタ部と蒸気加熱及び気化冷却
用の流体室とを連通し、該流体室に加熱用蒸気と
前記ポンプの吐出水の一部とを切替え供給できる
ように供給通路及び弁装置を設けたものである。<Means for Solving the Problems> The technical means of the present invention taken to solve the above problems is to communicate the diff user of the ejector and the suction port of the pump through a tank, and to supply cooling water into the tank. A pump device is provided, which includes a control unit that controls water temperature in the tank by supplying the water, a discharge port of the pump that is connected to a nozzle of the ejector, and a discharge means that discharges surplus water circulated by the pump to the outside of the system. , a supply passage and a valve device for communicating the ejector portion of the pump device with a fluid chamber for steam heating and vaporization cooling, and for selectively supplying heating steam and a portion of water discharged from the pump to the fluid chamber; It has been established.
<作用>
原料を加熱する場合は、弁装置により流体室へ
蒸気を供給する。蒸気は原料を加熱してドレンと
なつてエゼクタに吸引され、タンク内に至り、タ
ンク内の水温は上昇する。<Function> When heating the raw material, steam is supplied to the fluid chamber by the valve device. The steam heats the raw material and becomes drain, which is sucked into the ejector and reaches the tank, increasing the water temperature in the tank.
加熱から冷却に切換える場合は、弁装置により
蒸気の供給を停止しポンプ吐出水の一部を流体室
に供給するようにする。流体室の残留高温蒸気と
供給された吐出水はエゼクタに吸引されタンク内
に戻る。従つて、流体室に供給される吐出水は初
期には高温であるために問題の温度差は小さく、
残留蒸気が急凝縮してハンマー現象を発生するこ
とはない。そしてタンク内に冷却水を供給してポ
ンプの循環水温が徐々に下がるようにする。水温
が低下すると、エゼクタの吸引作用により、流体
室が減圧され、これにより供給される吐出水は迅
速に気化して被冷却物を気化冷却する。 When switching from heating to cooling, the valve device stops the supply of steam and supplies part of the pump discharge water to the fluid chamber. The residual high temperature steam in the fluid chamber and the supplied discharge water are sucked into the ejector and returned into the tank. Therefore, since the discharge water supplied to the fluid chamber is initially at a high temperature, the temperature difference in question is small;
Residual steam will not rapidly condense and cause a hammer effect. Cooling water is then supplied into the tank to gradually lower the temperature of the water circulating in the pump. When the water temperature decreases, the fluid chamber is depressurized by the suction action of the ejector, and the discharged water thus supplied quickly vaporizes and evaporatively cools the object to be cooled.
次に冷却から加熱に切換える場合は、気化冷却
状態からまずタンク内への冷却水の供給を停止す
ると、ポンプの吐出水は、流体室とエゼクタ及び
タンクを循環し、被冷却物からの熱及び循環によ
る熱で徐々に昇温する。ある程度昇温した時点で
弁装置により流体室への吐出水の供給を停止し加
熱蒸気を供給するようにすると、問題の温度差は
小さく蒸気が急凝縮することなく、被加熱物は蒸
気加熱される。 Next, when switching from cooling to heating, first stop the supply of cooling water into the tank from the evaporative cooling state, and the water discharged from the pump circulates through the fluid chamber, ejector, and tank, and the heat from the object to be cooled and The temperature gradually rises due to the heat generated by circulation. When the temperature rises to a certain degree, if the valve device stops the supply of discharged water to the fluid chamber and supplies heated steam, the temperature difference in question will be small and the steam will not suddenly condense, and the object to be heated will be heated by the steam. Ru.
<実施例>
上記の技術的手段の具体例を示す実施例を説明
する。(第1図参照)
第1図において、21は蒸気加熱及び気化冷却
用の流体室で内部に原料を挿入する。22はポン
プ装置、23a,23bは弁装置、24は水温制
御部である。<Example> An example showing a specific example of the above technical means will be described. (See Figure 1) In Figure 1, numeral 21 denotes a fluid chamber for steam heating and evaporative cooling into which raw materials are inserted. 22 is a pump device, 23a and 23b are valve devices, and 24 is a water temperature control section.
流体室21には、蒸気供給通路27及び吐出水
供給通路28が弁装置23a,23bを介して接
続されている。弁装置23a,23bは自動弁で
コントロール部29からの信号により開閉動作す
る。 A steam supply passage 27 and a discharge water supply passage 28 are connected to the fluid chamber 21 via valve devices 23a and 23b. The valve devices 23a and 23b are automatic valves that open and close according to signals from the control section 29.
ポンプ装置22は、ポンプ30がタンク31に
吸込側を接続され吐出側をエゼクタ32のノズル
33に接続し、エゼクタ32のデイフユーザ34
がタンク31の上部空間に接続された構成のもの
であり、エゼクタ32と流体室21がコンデンサ
50を介して接続されている。このポンプ装置2
2は、ポンプ30の作動によりタンク31内の水
をエゼクタ32に供給して吸引作用させ、タンク
31に戻すようになつている。 In the pump device 22, a pump 30 has a suction side connected to a tank 31, a discharge side connected to a nozzle 33 of an ejector 32, and a differential user 34 of the ejector 32.
is connected to the upper space of the tank 31, and the ejector 32 and the fluid chamber 21 are connected via a capacitor 50. This pump device 2
2 is configured to supply water in a tank 31 to an ejector 32 by operation of a pump 30, cause it to be suctioned, and return it to the tank 31.
水温制御部24は、タンク31内の水温を制御
するように設けたものであり、タンク31内に冷
却水を供給することによつて制御するようになつ
ている。タンク31に接続した冷却水供給管40
の途中に自動弁70を設け、タンク内の水温を検
出する温度センサー41からの信号により開閉す
る。自動弁70の一端は、コンデンサ50の下部
にも接続されている。参照番号51はコンデンサ
50からの冷却水排出管である。 The water temperature control section 24 is provided to control the water temperature in the tank 31, and is designed to perform control by supplying cooling water into the tank 31. Cooling water supply pipe 40 connected to tank 31
An automatic valve 70 is provided in the middle of the tank, and is opened and closed by a signal from a temperature sensor 41 that detects the water temperature in the tank. One end of the automatic valve 70 is also connected to the lower part of the capacitor 50. Reference number 51 is a cooling water discharge pipe from the condenser 50.
余剰水排出手段25は、ポンプ装置22の一部
に自動弁71を取付け、タンク31内の水位セン
サー42a,42bからの信号により、タンク3
1内の水位を所定範囲に保つものである。 The surplus water discharge means 25 has an automatic valve 71 attached to a part of the pump device 22, and the tank 3
1 to maintain the water level within a predetermined range.
流体室21を加熱する場合は、コントロール部
29からの信号により、弁装置23aが開き蒸気
を流体室21に供給して、原料を蒸気加熱する。
加熱により生じたドレンは、エゼクタ32に吸引
されタンク31に至る。ドレンによつてタンク3
1内の水位が上限水位に達すると、水位センサー
42aが検知し、自動弁71が開き、余剰水を系
外に排出する。タンク31内の水温はドレンの流
入により上昇する。 When heating the fluid chamber 21, the valve device 23a opens in response to a signal from the control unit 29 to supply steam to the fluid chamber 21, thereby heating the raw material with steam.
Drain generated by heating is sucked into the ejector 32 and reaches the tank 31. Tank 3 by drain
When the water level in the tank 1 reaches the upper limit water level, the water level sensor 42a detects this, and the automatic valve 71 opens to discharge excess water to the outside of the system. The water temperature in the tank 31 rises due to the inflow of drain.
加熱から冷却に切換える場合は、弁装置23a
により蒸気の供給を停止し、弁装置23bを開い
てポンプ30からの吐出水の一部を流体室21に
供給する。流体室21に供給された吐出水と残留
蒸気はエゼクタ32により吸引されタンク31に
至る。加熱から冷却に切換えた初期においては、
ポンプ30の吐出水は加熱の時に高温になつてい
るので、残留高温蒸気が急凝縮することはない。
従つて、この場合にハンマー現象は発生しない。
タンク31内に冷却水を供給することにより、タ
ンク31内の水温は徐々に低下する。水温の低下
に伴いエゼクタ32に生じる吸引作用すなわち減
圧度が高くなり、流体室21内も減圧される。流
体室21が減圧されると、供給される吐出水は原
料の熱により気化して冷却する。 When switching from heating to cooling, the valve device 23a
The supply of steam is stopped, the valve device 23b is opened, and a portion of the water discharged from the pump 30 is supplied to the fluid chamber 21. The discharge water and residual steam supplied to the fluid chamber 21 are sucked by the ejector 32 and reach the tank 31. In the initial stage of switching from heating to cooling,
Since the water discharged from the pump 30 is heated to a high temperature, the residual high temperature steam does not suddenly condense.
Therefore, no hammer phenomenon occurs in this case.
By supplying cooling water into the tank 31, the water temperature within the tank 31 gradually decreases. As the water temperature decreases, the suction action, ie, the degree of pressure reduction, generated in the ejector 32 increases, and the pressure inside the fluid chamber 21 is also reduced. When the pressure in the fluid chamber 21 is reduced, the supplied discharge water is vaporized by the heat of the raw material and cooled.
気化した吐出水は、コンデンサ50で再び凝縮
されてエゼクタ32に吸引される。 The vaporized discharged water is condensed again in the condenser 50 and sucked into the ejector 32.
流体室21の減圧度は、タンク31の水温を制
御することにより調整することができる。 The degree of pressure reduction in the fluid chamber 21 can be adjusted by controlling the water temperature in the tank 31.
冷却から加熱に切換える場合は、冷却水供給管
40の自動弁70を閉弁し冷却水の供給を停止す
る。流体はタンク31、ポンプ30、流体室2
1、エゼクタ32を循環し、原料からの熱及び循
環による熱で徐々に昇温する。温度センサー41
の検出により水温がある程度上昇した時点で、弁
装置23bを閉じ、吐出水の供給を停止するとと
もに、弁装置23aを開き加熱蒸気を流体室21
に供給する。蒸気が流体室21に供給されるが、
このときの流体室21内の流体温度は上昇してい
るために、蒸気の急凝縮は発生せず、ハンマー現
象も生じない。 When switching from cooling to heating, the automatic valve 70 of the cooling water supply pipe 40 is closed to stop the supply of cooling water. Fluid is in tank 31, pump 30, fluid chamber 2
1. The material is circulated through the ejector 32, and the temperature is gradually raised by the heat from the raw material and the heat generated by the circulation. Temperature sensor 41
When the water temperature rises to a certain extent by detection of
supply to. Steam is supplied to the fluid chamber 21,
Since the fluid temperature in the fluid chamber 21 at this time is rising, rapid condensation of steam does not occur, and no hammer phenomenon occurs.
<発明の効果>
本発明によれば、加熱から冷却へまた冷却から
加熱へと切換えるときに、流体室へ供給する流体
の温度を徐々に変化させて蒸気の急凝縮を防止す
ることができ、ハンマー現象が発生することはな
く、原料並びに加熱冷却装置の損傷を防止でき
る。更に、冷却時に冷却室を減圧して気化冷却す
るから、大きな熱容量を確保でき、冷却ムラを防
止して、製品の品質を一定に維持できる。<Effects of the Invention> According to the present invention, when switching from heating to cooling or from cooling to heating, the temperature of the fluid supplied to the fluid chamber can be gradually changed to prevent rapid condensation of steam. Hammer phenomenon does not occur, and damage to raw materials and heating/cooling equipment can be prevented. Furthermore, since the cooling chamber is depressurized and evaporatively cooled during cooling, a large heat capacity can be secured, uneven cooling can be prevented, and product quality can be maintained at a constant level.
第1図は本発明の蒸気加熱及び気化冷却装置の
実施例の概略の構成を示す構成図、第2図は従来
の加熱冷却装置の一例を示す概略構成図である。
21……流体室、22……ポンプ装置、23
a,23b……弁装置、24……水温制御部、2
5……余剰水排出手段、27……蒸気供給通路、
28……吐出水供給通路、30……ポンプ、31
……タンク、32……エゼクタ、33……ノズ
ル、40……冷却水供給通路、50……コンデン
サ。
FIG. 1 is a block diagram showing a schematic structure of an embodiment of a steam heating and evaporative cooling device of the present invention, and FIG. 2 is a schematic block diagram showing an example of a conventional heating and cooling device. 21...Fluid chamber, 22...Pump device, 23
a, 23b... Valve device, 24... Water temperature control section, 2
5... Surplus water discharge means, 27... Steam supply passage,
28...Discharge water supply passage, 30...Pump, 31
... Tank, 32 ... Ejector, 33 ... Nozzle, 40 ... Cooling water supply passage, 50 ... Condenser.
Claims (1)
をタンクを介して連通し、該タンク内へ冷却水を
供給してタンク内水温を制御する制御部を設け、
前記ポンプの吐出口を前記エゼクタのノズルに接
続し、ポンプによる循環水の余剰水を系外に排出
する排出手段を配したポンプ装置を設け、該ポン
プ装置のエゼクタ部と蒸気加熱及び気化冷却用の
流体室とを連通し、該流体室に加熱用蒸気と前記
ポンプの吐出水の一部とを切替え供給できるよう
に供給通路及び弁装置を設けた、蒸気加熱及び気
化冷却装置。1. A control unit is provided that communicates the diff user of the ejector and the suction port of the pump via a tank, supplies cooling water into the tank, and controls the water temperature in the tank,
A pump device is provided that connects the discharge port of the pump to the nozzle of the ejector and is equipped with a discharge means for discharging surplus water circulated by the pump to the outside of the system, and is connected to the ejector portion of the pump device for steam heating and evaporative cooling. A steam heating and evaporative cooling device that communicates with a fluid chamber and is provided with a supply passage and a valve device so that heating steam and a portion of water discharged from the pump can be selectively supplied to the fluid chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23879689A JPH03101832A (en) | 1989-09-14 | 1989-09-14 | Steam heating and vaporization cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23879689A JPH03101832A (en) | 1989-09-14 | 1989-09-14 | Steam heating and vaporization cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03101832A JPH03101832A (en) | 1991-04-26 |
| JPH0581297B2 true JPH0581297B2 (en) | 1993-11-12 |
Family
ID=17035414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23879689A Granted JPH03101832A (en) | 1989-09-14 | 1989-09-14 | Steam heating and vaporization cooling device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03101832A (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4472103B2 (en) * | 2000-04-14 | 2010-06-02 | 株式会社テイエルブイ | Steam heating device |
| JP5047425B2 (en) * | 2001-04-13 | 2012-10-10 | 株式会社テイエルブイ | Steam heating device |
| JP5047426B2 (en) * | 2001-04-13 | 2012-10-10 | 株式会社テイエルブイ | Steam heating device |
| JP2002370235A (en) * | 2001-06-15 | 2002-12-24 | Tlv Co Ltd | Steam vulcanizing equipment |
| JP4597425B2 (en) * | 2001-06-15 | 2010-12-15 | 株式会社テイエルブイ | Steam vulcanizer |
| JP4597426B2 (en) * | 2001-06-15 | 2010-12-15 | 株式会社テイエルブイ | Steam vulcanizer |
| JP4624606B2 (en) * | 2001-08-10 | 2011-02-02 | 株式会社テイエルブイ | Steam vulcanizer |
| EP2644264A1 (en) * | 2012-03-28 | 2013-10-02 | Aurotec GmbH | Pressure-controlled multi-reactor system |
| JP6812077B2 (en) * | 2017-02-16 | 2021-01-13 | 株式会社テイエルブイ | Heat exchanger |
| JP7189792B2 (en) * | 2019-02-08 | 2022-12-14 | 株式会社テイエルブイ | Drain recovery device |
-
1989
- 1989-09-14 JP JP23879689A patent/JPH03101832A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03101832A (en) | 1991-04-26 |
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