JP2003014299A - Method and system for heating target liquid being heated - Google Patents
Method and system for heating target liquid being heatedInfo
- Publication number
- JP2003014299A JP2003014299A JP2001201690A JP2001201690A JP2003014299A JP 2003014299 A JP2003014299 A JP 2003014299A JP 2001201690 A JP2001201690 A JP 2001201690A JP 2001201690 A JP2001201690 A JP 2001201690A JP 2003014299 A JP2003014299 A JP 2003014299A
- Authority
- JP
- Japan
- Prior art keywords
- heated
- liquid
- heating
- fluorine
- target liquid
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 145
- 238000010438 heat treatment Methods 0.000 title claims abstract description 75
- 238000000034 method Methods 0.000 title claims description 27
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims abstract description 51
- 229910052731 fluorine Inorganic materials 0.000 claims abstract description 51
- 239000011737 fluorine Substances 0.000 claims abstract description 51
- 238000009835 boiling Methods 0.000 claims abstract description 29
- 239000010702 perfluoropolyether Substances 0.000 claims description 5
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims description 4
- 238000005265 energy consumption Methods 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 9
- 238000004891 communication Methods 0.000 description 3
- 102220547770 Inducible T-cell costimulator_A23L_mutation Human genes 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/0009—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters of the reduced pressure or vacuum steam type
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
- General Preparation And Processing Of Foods (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、洗浄用液体、洗浄使用
後の汚染された液体、食品加工用の液体等の被加熱目的
液の間接加熱を、簡易な装置により廉価に可能とすると
共に温度管理を厳密に行うことが出来るようにしたもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention enables indirect heating of a target liquid to be heated, such as a cleaning liquid, a contaminated liquid after cleaning and a food processing liquid, at a low cost with a simple device. It is designed so that temperature control can be strictly performed.
【0002】[0002]
【従来の技術】従来、洗浄用液体、洗浄使用後の汚染さ
れた液体、食品加工用の液体等の被加熱目的液の間接加
熱を行う方法としては、加圧スチームを用いた間接加熱
方式、熱媒体液を用いた間接加熱方式、熱風、温風等を
用いた間接加熱方式が存在した。2. Description of the Related Art Conventionally, as a method for indirectly heating a liquid to be heated such as a cleaning liquid, a contaminated liquid after cleaning and a food processing liquid, an indirect heating method using pressurized steam, There are an indirect heating method using a heat medium liquid and an indirect heating method using hot air, warm air, and the like.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、加圧ス
チームを用いた間接加熱方式では、加圧スチームを発生
させるための圧力ボイラーが必要となり、設備が大型化
したり、加圧スチーム発生部への水の供給が常時必要で
あったり、加圧スチームとラップからのドレンによる廃
水処理が必要で、設備費、管理費等が多額となる欠点を
有している。また、圧力ボイラーを使用するため安全対
策にも充分な配慮が必要となるものであった。However, in the indirect heating method using pressure steam, a pressure boiler for generating pressure steam is required, the equipment becomes large, and the water to the pressure steam generation section is increased. However, there is a drawback that the equipment cost, the management cost, and the like are large because it is necessary to constantly supply the waste water and to treat the waste water by draining from the pressurized steam and the wrap. Also, since a pressure boiler is used, it is necessary to give sufficient consideration to safety measures.
【0004】また、熱媒体液を用いた間接加熱方式で
は、加熱する熱媒体液の液量が多くなり熱エネルギーの
消費が大きなものとなる。また、洗浄用液体、洗浄使用
後の汚染された液体等の間接加熱を行う場合には、当然
の事ながら、液温を一定に保つために精密な温度管理が
必要となるが、熱媒体液を用いる場合には精密な温度制
御が困難なものであった。また、熱媒体液を用いる場合
には、熱交換率を高めるために循環ポンプを用いるのが
効率的であるが、設備費を高価なものとする。また、熱
媒体液は一般的に加熱による熱劣化が生じ易いものであ
り、熱劣化を生じないフッ素系液体は高価である欠点を
有している。Further, in the indirect heating method using the heat medium liquid, the amount of the heat medium liquid to be heated is large and the consumption of heat energy is large. In addition, when performing indirect heating of cleaning liquid, contaminated liquid after cleaning, etc., of course, precise temperature control is required to keep the liquid temperature constant. When using, it was difficult to precisely control the temperature. Further, when the heat medium liquid is used, it is effective to use the circulation pump in order to increase the heat exchange rate, but the equipment cost becomes expensive. Further, the heat medium liquid is generally liable to be thermally deteriorated by heating, and the fluorine-based liquid which does not cause heat deterioration has a drawback that it is expensive.
【0005】また、熱風、温風を用いた間接加熱方式で
は、ランニングコストが高くなると共に熱ロスが多く、
送風機等も必要となり不経済となる欠点を有している。In addition, in the indirect heating method using hot air or warm air, running costs are high and heat loss is large.
It also has the drawback of being uneconomical because it requires a blower and the like.
【0006】本発明は上述の如き課題を解決するため、
圧力ボイラー等の設備を大型化することなく簡易な装置
により設備費を廉価なものとする。また、熱エネルギー
の消費量を小さなものとすると共に精密な温度管理を簡
易に可能とするものである。In order to solve the above problems, the present invention provides
The equipment cost will be reduced by a simple device without increasing the size of equipment such as a pressure boiler. In addition, the consumption of heat energy can be reduced, and precise temperature control can be easily performed.
【0007】[0007]
【課題を解決するための手段】本発明は上述の如き課題
を解決するため、沸点の異なるフッ素系液体を選択的に
用いて、常圧下で沸点まで加熱し、この沸点加熱により
発生した蒸気を用いて被加熱目的液の加熱を行うことを
特徴とするものである。In order to solve the above-mentioned problems, the present invention selectively heats fluorine-based liquids having different boiling points to heat them up to the boiling point under normal pressure, It is characterized in that the target liquid to be heated is heated by using it.
【0008】また、上記方法の発明を具体化する装置と
しては、沸点の異なるフッ素系液体を選択的に収納し、
常圧下で加熱体によりフッ素系液体を沸点まで加熱し蒸
気を発生させる加熱槽と、このフッ素系液体の蒸気に加
熱されて被加熱目的液と熱交換を行う熱交換体とから成
るものである。As an apparatus for embodying the invention of the above method, fluorine-containing liquids having different boiling points are selectively stored,
It consists of a heating tank that heats the fluorinated liquid to the boiling point with a heating body under normal pressure to generate steam, and a heat exchanger that is heated by the steam of the fluorinated liquid and exchanges heat with the target liquid to be heated. .
【0009】また、フッ素系液体は、パーフロロカーボ
ン、パーフロロポリエーテル、ハイドロフロロエーテ
ル、ハイドロフロロカーボンの1種または複数種を選択
的に用いるものであっても良い。Further, the fluorine-based liquid may selectively use one or more of perfluorocarbon, perfluoropolyether, hydrofluoroether and hydrofluorocarbon.
【0010】また、熱交換体は、被加熱目的液を収納し
た収納槽であり、この収納槽にフッ素系液体の蒸気を接
触させて内部の被加熱目的液を加熱するものであっても
良い。The heat exchanger may be a storage tank for storing the target liquid to be heated, and the vapor may be brought into contact with the storage tank to heat the target liquid to be heated inside. .
【0011】また、熱交換体は、被加熱目的液内に挿入
しフッ素系液体の蒸気を流通させた流通管であっても良
い。Further, the heat exchange element may be a flow pipe which is inserted into the target liquid to be heated and through which the vapor of the fluorinated liquid is passed.
【0012】また、熱交換体は、フッ素系液体の蒸気を
流通させた流通管に着脱可能に接続してこの蒸気を内部
に流通させると共に、被加熱目的液内に挿入可能とした
ものであっても良い。Further, the heat exchange element is detachably connected to a flow pipe through which the vapor of the fluorinated liquid is circulated so as to circulate the vapor inside and can be inserted into the target liquid to be heated. May be.
【0013】また、被加熱目的液内には、温度センサー
を配置し、この温度センサーの感知信号に従って、熱交
換体へのフッ素系液体の蒸気の供給を制御するものであ
っても良い。Further, a temperature sensor may be arranged in the target liquid to be heated, and the supply of the vapor of the fluorine-based liquid to the heat exchanger may be controlled according to the detection signal of the temperature sensor.
【0014】[0014]
【作用】本発明は上述の如く、沸点の異なるフッ素系液
体を選択的に用いて、常圧下で沸点まで加熱し、この沸
点加熱により発生した蒸気を用いて被加熱目的液の加熱
を行うものであるから、被加熱目的液の加熱目的温度に
対応したフッ素系液体を選択的に用いて沸点以上に加熱
すれば、この加熱により発生する蒸気は、選択したフッ
素系液体の沸点に保たれる。この蒸気を用いて被加熱目
的液を加熱すれば、選択したフッ素系液体の沸点以上に
加熱されることはなく、確実な温度管理を容易に行うこ
とが出来る。また、選択したフッ素系液体の加熱部と、
被加熱目的液の収納部との連通を遮断すれば、直ちに被
加熱目的液の加熱は停止されるから、この加熱は停止の
面からの温度管理も容易に行うことが出来るものであ
る。As described above, the present invention selectively uses fluorine-based liquids having different boiling points to heat them to the boiling point under normal pressure, and heats the target liquid to be heated using the vapor generated by the heating of the boiling points. Therefore, if the fluorine-based liquid corresponding to the heating target temperature of the target liquid to be heated is selectively used and heated to the boiling point or higher, the vapor generated by this heating is kept at the boiling point of the selected fluorine-based liquid. . If the target liquid to be heated is heated using this vapor, it will not be heated above the boiling point of the selected fluorine-based liquid, and reliable temperature control can be easily performed. In addition, with the heating section of the selected fluorine-based liquid,
If the communication with the storage unit for the target liquid to be heated is cut off, the heating of the target liquid to be heated is immediately stopped. Therefore, this heating can easily control the temperature from the side of stopping.
【0015】また、選択したフッ素系液体は常圧下で沸
点まで加熱して行うものであるから、加圧スチームを用
いた間接加熱方式の如く、加圧スチームを発生させるた
めの圧力ボイラー等は不要であり、設備を小型で簡易な
ものとし、圧力制御が不要となるから安全性の高いもの
となる。また、選択したフッ素系液体は蒸気を発生する
のに必要な量だけ加熱すればよいものであるから、少量
のフッ素系液体を加熱し、必要量を順次補給することが
可能であり、使用エネルギーを最小限とすることが出来
る。また、本発明に於いては、熱媒体液を用いた間接加
熱方式の如く、加熱する熱媒体液の液量が多くなり熱エ
ネルギーの消費が大きなものとなる欠点を除去できるも
のである。また、フッ素系液体の蒸気を用いて被加熱目
的液を加熱するものであるから、循環ポンプ等の温度管
理のための複雑な設備を不要とし、廉価に被加熱目的液
の正確な加熱を可能とするものである。Further, since the selected fluorine-based liquid is heated to the boiling point under normal pressure, a pressure boiler or the like for generating pressurized steam is not required unlike the indirect heating method using pressurized steam. Therefore, the equipment is small and simple, and the pressure control is not required, so the safety is high. Also, since the selected fluorine-based liquid only needs to be heated by the amount necessary to generate steam, it is possible to heat a small amount of the fluorine-based liquid and replenish the required amount in sequence. Can be minimized. Further, in the present invention, it is possible to eliminate the disadvantage that the amount of the heating medium liquid to be heated is large and the consumption of heat energy is large like the indirect heating method using the heating medium liquid. Also, since the target liquid to be heated is heated using the vapor of a fluorine-based liquid, complicated equipment for temperature control such as a circulation pump is not required, and accurate heating of the target liquid to be heated is possible at low cost. It is what
【0016】また、フッ素系液体は、パーフロロカーボ
ン、パーフロロポリエーテル、ハイドロフロロエーテ
ル、ハイドロフロロカーボンの1種または複数種を選択
的に用いる事ができる。そして、フッ素系液体の蒸気に
加熱されて被加熱目的液と熱交換を行う熱交換体は、被
加熱目的液を収納した収納槽によって形成し、この収納
槽にフッ素系液体の蒸気を接触させて内部の被加熱目的
液を加熱するように構成する。As the fluorine-based liquid, one or more of perfluorocarbon, perfluoropolyether, hydrofluoroether and hydrofluorocarbon can be selectively used. The heat exchange element that is heated by the vapor of the fluorine-based liquid and exchanges heat with the target liquid to be heated is formed by a storage tank that stores the target liquid to be heated, and the vapor of the fluorine-based liquid is brought into contact with this storage tank. And heats the target liquid to be heated inside.
【0017】また、熱交換体は、被加熱目的液内に挿入
しフッ素系液体の蒸気を流通させた流通管であっても良
いし、フッ素系液体の蒸気を流通させた流通路に着脱可
能に接続してこの蒸気を内部に流通させると共に、被加
熱目的液内に挿入可能としたものにより熱交換体を形成
しても良い。Further, the heat exchange element may be a flow pipe which is inserted into the target liquid to be heated and through which the vapor of the fluorinated liquid is circulated, or is attachable to and detachable from the flow passage through which the fluorinated liquid vapor is circulated. The heat exchanger may be formed by connecting to the above to allow the vapor to flow inside and to be inserted into the target liquid to be heated.
【0018】また、被加熱目的液内に、温度センサーを
配置し、この温度センサーの感知信号に従って、熱交換
体へのフッ素系液体蒸気の供給を制御するものとすれ
ば、被加熱目的液の加熱、非加熱を迅速に制御すること
が可能となる。特に本発明に於いては、加圧スチーム
や、加熱液体を熱源として用いるものではないから、熱
交換体へのフッ素系液体蒸気の供給を停止すれば、熱交
換体の加熱エネルギーは急速に消失し、被加熱目的液へ
の加熱を停止することが可能となり、被加熱目的液の精
密な温度制御が可能となる。If a temperature sensor is arranged in the target liquid to be heated and the supply of the fluorine-based liquid vapor to the heat exchanger is controlled according to the detection signal of the temperature sensor, the target liquid to be heated is It is possible to quickly control heating and non-heating. In particular, in the present invention, since pressurized steam or heating liquid is not used as a heat source, the heating energy of the heat exchanger rapidly disappears if the supply of the fluorine-based liquid vapor to the heat exchanger is stopped. However, it is possible to stop the heating of the target liquid to be heated, and it is possible to precisely control the temperature of the target liquid to be heated.
【0019】[0019]
【実施例】以下、本発明の一実施例を図1に於て説明す
れば、(1)は加熱槽で、パーフロロカーボン、パーフロ
ロポリエーテル、ハイドロフロロエーテル、ハイドロフ
ロロカーボン等の、沸点の異なるフッ素系液体(2)の1
種または複数種を選択的に収納し、常圧下で加熱体(3)
によりフッ素系液体(2)を沸点まで加熱し蒸気を発生さ
せるものである。そして、この加熱槽(1)内に熱交換体
(4)の下端を挿入している。この熱交換体(4)は、被加
熱目的液(5)を導入管(9)から導入して収納した収納槽
(6)であり、この収納槽(6)にフッ素系液体(2)の蒸気
を接触させて、内部の被加熱目的液(5)を加熱するもの
である。この加熱により発生する蒸気は、選択したフッ
素系液体(2)の沸点に保たれる。この蒸気を用いて被加
熱目的液(5)を加熱すれば、選択したフッ素系液体(2)
の沸点以上に加熱されることはなく、確実な温度管理を
容易に行うことが出来る。EXAMPLE An example of the present invention will be described below with reference to FIG. 1. (1) is a heating tank, which has different boiling points such as perfluorocarbon, perfluoropolyether, hydrofluoroether, hydrofluorocarbon, etc. Fluorine-based liquid (2) 1
Heated body (3) under normal pressure, containing one or more species selectively
The fluorinated liquid (2) is heated to the boiling point to generate steam. And, in this heating tank (1)
The lower end of (4) is inserted. The heat exchanger (4) is a storage tank in which the target liquid to be heated (5) is introduced and stored through the introduction pipe (9).
(6) The vapor of the fluorine-based liquid (2) is brought into contact with the storage tank (6) to heat the target liquid to be heated (5) inside. The vapor generated by this heating is kept at the boiling point of the selected fluorine-based liquid (2). If the target liquid (5) to be heated is heated using this vapor, the selected fluorine-based liquid (2)
It is not heated above the boiling point of, and reliable temperature control can be easily performed.
【0020】この確実な温度管理によって、被加熱目的
液(5)を加熱することにより優れた技術効果を得ること
が可能となる。例えば被加熱目的液(5)が被洗浄物の洗
浄を完了した汚染洗浄液である場合には、汚染洗浄液中
の特定の物質の沸点に合わせて加熱することにより、こ
の物質のみを蒸留して回収することが出来る。また、厳
密に温度管理された被加熱目的液(5)で、食品の加熱を
行う場合には、食品の特性に合わせた調理や、特定の栄
養成分を破壊することのない調理等を可能とするもので
ある。また、加熱槽(1)には冷却水(7)を流通させた凝
縮器(8)を接続し、フッ素系液体(2)の蒸気を凝縮して
回収する。With this reliable temperature control, it is possible to obtain excellent technical effects by heating the target liquid (5) to be heated. For example, when the target liquid to be heated (5) is a contaminated cleaning liquid in which the cleaning of the object to be cleaned has been completed, by heating according to the boiling point of a specific substance in the contaminated cleaning liquid, only this substance is distilled and recovered. You can do it. In addition, when the food is heated with the target liquid (5) to be heated whose temperature is strictly controlled, it is possible to cook according to the characteristics of the food or cook without destroying specific nutrients. To do. Further, a condenser (8) in which cooling water (7) is circulated is connected to the heating tank (1) to condense and recover the vapor of the fluorine-based liquid (2).
【0021】また、被加熱目的液(5)内には、温度セン
サー(14)を配置し、この温度センサー(14)の感知信
号に従って、熱交換体(4)へのフッ素系液体(2)蒸気の
供給を制御するものとすれば、被加熱目的液(5)の加
熱、非加熱を迅速に制御することが可能となる。特に本
発明に於いては、加圧スチームや、加熱液体を熱源とし
て用いるものではないから、熱交換体(4)へのフッ素系
液体(2)蒸気の供給を停止すれば、熱交換体(4)の加熱
エネルギーは急速に消失し、被加熱目的液(5)への加熱
を停止することが可能となり、被加熱目的液(5)の精密
な温度制御が可能となる。Further, a temperature sensor (14) is arranged in the target liquid (5) to be heated, and the fluorine-based liquid (2) to the heat exchanger (4) is responsive to the detection signal of the temperature sensor (14). If the supply of steam is controlled, it becomes possible to quickly control heating and non-heating of the target liquid to be heated (5). In particular, in the present invention, pressurized steam or heated liquid is not used as a heat source. Therefore, if the supply of the fluorine-based liquid (2) vapor to the heat exchanger (4) is stopped, the heat exchanger ( The heating energy of 4) rapidly disappears, and it becomes possible to stop the heating of the liquid to be heated (5), and it becomes possible to precisely control the temperature of the liquid to be heated (5).
【0022】また、上記実施例に於いて熱交換体(4)
は、被加熱目的液(5)を収納した収納槽(6)により形成
したが、異なる第2実施例では、図2に示す如く、熱交
換体(4)は、被加熱目的液(5)内に挿入し、フッ素系液
体(2)の蒸気を流通させた流通管(10)であっても良
い。この流通管(10)は被加熱目的液(5)の収納槽(6)
の内面にコイル状に配置して形成する。また、加熱槽
(1)と熱交換体(4)である流通管(10)とは蒸気の導入
バルブ(11)を介して接続する。また、熱交換体(4)で
ある流通管(10)の蒸気排出側には、排出バルブ(12)
を介して凝縮器(8)に接続し、この凝縮器(8)で凝縮液
化したフッ素系液体(2)を加熱槽(1)に配管を介して還
元している。Further, in the above embodiment, the heat exchanger (4)
Was formed by the storage tank (6) containing the target liquid to be heated (5), but in the second different embodiment, as shown in FIG. 2, the heat exchanger (4) is the target liquid to be heated (5). It may be a flow pipe (10) which is inserted into the inside and through which the vapor of the fluorine-based liquid (2) is passed. This flow pipe (10) is a storage tank (6) for the target liquid (5) to be heated.
It is formed by arranging in a coil shape on the inner surface of. Also, heating tank
(1) and the flow pipe (10), which is the heat exchanger (4), are connected via a steam introduction valve (11). Further, a discharge valve (12) is provided on the steam discharge side of the flow pipe (10) which is the heat exchanger (4).
Is connected to a condenser (8) via a condenser, and the fluorine-based liquid (2) condensed and liquefied in the condenser (8) is reduced to the heating tank (1) through a pipe.
【0023】また、異なる第3実施例に於いて熱交換体
(4)は、図3に示す如く、フッ素系液体(2)の蒸気を流
通させた流通管(10)に着脱可能に接続して、この蒸気
を内部に流通させると共に、被加熱目的液(5)内に挿入
可能としたものである。また、加熱槽(1)の熱交換体
(4)と流通管(10)とは、蒸気の導入バルブ(11)を介
して接続する。また、熱交換体(4)の蒸気排出側には、
排出バルブ(12)を設けた流通路(13)介して加熱槽
(1)に接続し、被加熱目的液(5)との熱交換を完了した
フッ素系液体(2)の蒸気を加熱槽(1)に還元している。
また、排出バルブ(12)と加熱槽(1)との間の流通路
(13)との間には、連通管(15)を介して凝縮器(8)を
接続し、導入バルブ(11)と排出バルブ(12)の双方が
閉弁したときに、加熱槽(1)内の蒸気を凝縮器に(8)導
き、加熱槽(1)の異常昇圧を防止している。In addition, in a different third embodiment, the heat exchanger
As shown in FIG. 3, (4) is detachably connected to a flow pipe (10) in which vapor of the fluorine-based liquid (2) is circulated so that the vapor is circulated inside and the target liquid to be heated ( 5) It can be inserted into the inside. In addition, the heat exchanger of the heating tank (1)
(4) and the flow pipe (10) are connected via a steam introduction valve (11). Also, on the steam discharge side of the heat exchanger (4),
Heating tank through the flow passage (13) provided with the discharge valve (12)
The vapor of the fluorine-based liquid (2) connected to (1) and having completed heat exchange with the target liquid to be heated (5) is reduced to the heating tank (1).
Also, the flow passage between the discharge valve (12) and the heating tank (1)
A condenser (8) is connected to (13) via a communication pipe (15), and when both the introduction valve (11) and the discharge valve (12) are closed, the heating tank (1 The steam in () is guided to the condenser (8) to prevent abnormal pressurization of the heating tank (1).
【0024】[0024]
【発明の効果】本発明は被加熱目的液の加熱目的温度に
対応したフッ素系液体を選択的に用いて沸点以上に加熱
するものであるから、この加熱により発生する蒸気は、
選択したフッ素系液体の沸点に保たれ、この蒸気を用い
て間接加熱される被加熱目的液も選択したフッ素系液体
の沸点以上に加熱されることはなく、確実な温度管理を
容易に行うことが出来る。また、フッ素系液体の加熱部
と被加熱目的液の収納部との連通を遮断すれば、直ちに
被加熱目的液の加熱は停止され、温度管理も容易に行う
ことが出来る。EFFECTS OF THE INVENTION Since the present invention selectively heats the fluorine-based liquid corresponding to the target heating temperature of the target liquid to be heated to the boiling point or higher, the vapor generated by this heating is
The target liquid to be heated, which is maintained at the boiling point of the selected fluorine-based liquid and is indirectly heated using this vapor, will not be heated above the boiling point of the selected fluorine-based liquid, and reliable temperature control can be performed easily. Can be done. Further, if the communication between the heating portion for the fluorine-based liquid and the storage portion for the target liquid to be heated is cut off, the heating of the target liquid to be heated is immediately stopped and the temperature can be easily controlled.
【0025】また、フッ素系液体は常圧下で沸点まで加
熱するものであるから、スチームを用いた間接加熱方式
の如く、圧力ボイラー等を不要とし、設備を小型で簡易
なものとし、安全性の高いものとなる。また、選択した
フッ素系液体は蒸気を発生するのに必要な量だけ加熱す
ればよく、少量のフッ素系液体を加熱し、必要量を順次
補給することが可能で、使用エネルギーを最小限とする
ことが出来る。また、循環ポンプ等の温度管理のための
複雑な設備を不要とし、廉価に被加熱目的液の正確な加
熱を可能とするものである。Further, since the fluorine-based liquid is heated to the boiling point under normal pressure, there is no need for a pressure boiler or the like as in the indirect heating method using steam, the equipment is small and simple, and safety is improved. It will be expensive. Further, the selected fluorinated liquid needs to be heated by the amount necessary to generate the vapor, and it is possible to heat a small amount of the fluorinated liquid and replenish the required amount sequentially, minimizing the energy used. You can Further, it is possible to accurately heat the target liquid to be heated at low cost without requiring complicated equipment such as a circulation pump for temperature control.
【図1】第1実施例の断面図。FIG. 1 is a sectional view of a first embodiment.
【図2】第2実施例の断面図。FIG. 2 is a sectional view of a second embodiment.
【図3】第3実施例の断面図。FIG. 3 is a sectional view of a third embodiment.
1 加熱槽 2 フッ素系液体 4 熱交換体 5 被加熱目的液 6 収納槽 10 流通管 13 流通路 14 温度センサー 1 heating tank 2 Fluorine-based liquid 4 heat exchanger 5 Target liquid to be heated 6 storage tanks 10 distribution pipes 13 flow passage 14 Temperature sensor
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成14年1月29日(2002.1.2
9)[Submission date] January 29, 2002 (2002.1.2
9)
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】請求項3[Name of item to be corrected] Claim 3
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【手続補正2】[Procedure Amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】請求項4[Name of item to be corrected] Claim 4
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【手続補正3】[Procedure 3]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】請求項5[Name of item to be corrected] Claim 5
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【手続補正4】[Procedure amendment 4]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】符号の説明[Correction target item name] Explanation of code
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【符号の説明】
1 加熱槽
2 フッ素系液体3 加熱体
4 熱交換体
5 被加熱目的液
6 収納槽
10 流通管
14 温度センサー
[Explanation of reference numerals] 1 heating tank 2 fluorine-based liquid 3 heating element 4 heat exchange element 5 target liquid to be heated 6 storage tank 10 flow pipe 14 temperature sensor
【手続補正書】[Procedure amendment]
【提出日】平成14年4月26日(2002.4.2
6)[Submission date] April 26, 2002 (2002.4.2)
6)
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0003[Name of item to be corrected] 0003
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0003】しかしながら、加圧スチームを用いた間接
加熱方式では、加圧スチームを発生させるための圧力ボ
イラーが必要となり、設備が大型化したり、加圧スチー
ム発生部への水の供給が常時必要であったり、加圧スチ
ームとトラップからのドレンによる廃水処理が必要で、
設備費、管理費等が多額となる欠点を有している。ま
た、圧力ボイラーを使用するため安全対策にも充分な配
慮が必要となるものであった。However, in the indirect heating method using pressurized steam, a pressure boiler for generating pressurized steam is required, the equipment becomes large, and water is always required to be supplied to the pressurized steam generating portion. Attari, is required wastewater treatment due to drain from the pressurized steam and traps,
It has the drawback that equipment costs and management costs are large. Also, since a pressure boiler is used, it is necessary to give sufficient consideration to safety measures.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // A23L 1/01 A23L 1/01 A ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) // A23L 1/01 A23L 1/01 A
Claims (8)
いて、常圧下で沸点まで加熱し、この沸点加熱により発
生した蒸気を用いて被加熱目的液の加熱を行うことを特
徴とする被加熱目的液の加熱方法。1. A fluorine-containing liquid having a different boiling point is selectively used to heat to a boiling point under normal pressure, and the target liquid to be heated is heated using the vapor generated by the boiling point heating. Method of heating target liquid.
納し、常圧下で加熱体によりフッ素系液体を沸点まで加
熱し蒸気を発生させる加熱槽と、このフッ素系液体の蒸
気に加熱されて被加熱目的液と熱交換を行う熱交換体と
から成ることを特徴とする被加熱目的液の加熱装置。2. A heating tank for selectively storing fluorine-based liquids having different boiling points and heating the fluorine-based liquid to a boiling point by a heating body under normal pressure to generate steam, and a heating tank heated by the steam of the fluorine-based liquid. A heating device for a target liquid to be heated, which comprises a target liquid to be heated and a heat exchange element for exchanging heat.
パーフロロポリエーテル、ハイドロフロロエーテル、ハ
イドロフロロカーボンの1種または複数種を選択的に用
いるものであることを特徴する請求項1の被加熱目的液
の加熱方法。3. The fluorine-based liquid is perfluorocarbon,
The method for heating a target liquid to be heated according to claim 1, wherein one or more of perfluoropolyether, hydrofluoroether and hydrofluorocarbon are selectively used.
パーフロロポリエーテル、ハイドロフロロエーテル、ハ
イドロフロロカーボンの1種または複数種を選択的に用
いるものであることを特徴する請求項2の被加熱目的液
の加熱装置。4. The fluorine-based liquid is perfluorocarbon,
3. The heating apparatus for heating a target liquid to be heated according to claim 2, wherein one or more of perfluoropolyether, hydrofluoroether and hydrofluorocarbon are selectively used.
納槽であり、この収納槽にフッ素系液体の蒸気を接触さ
せて内部の被加熱目的液を加熱するものであることを特
徴する請求項2の被加熱目的液の加熱装置。5. The heat exchanger is a storage tank that stores the target liquid to be heated, and the vapor of the fluorine-based liquid is brought into contact with the storage tank to heat the target liquid to be heated inside. The heating device for the target liquid to be heated according to claim 2.
ッ素系液体の蒸気を流通させた流通管であることを特徴
する請求項2の被加熱目的液の加熱装置。6. The heating apparatus for heating a target liquid to be heated according to claim 2, wherein the heat exchange element is a flow pipe inserted in the target liquid to be heated and allowing vapor of the fluorine-based liquid to flow therethrough.
させた流通管に着脱可能に接続してこの蒸気を内部に流
通させると共に、被加熱目的液内に挿入可能としたもの
であることを特徴する請求項2の被加熱目的液の加熱装
置。7. The heat exchange element is detachably connected to a flow pipe in which vapor of a fluorine-based liquid is circulated so that the vapor can be circulated therein and can be inserted into a target liquid to be heated. The heating device for the target liquid to be heated according to claim 2.
置し、この温度センサーの感知信号に従って、熱交換体
へのフッ素系液体の蒸気の供給を制御することを特徴す
る請求項2、4、5、6又は7の被加熱目的液の加熱装
置。8. A temperature sensor is arranged in the target liquid to be heated, and the supply of the vapor of the fluorine-based liquid to the heat exchange element is controlled according to the detection signal of the temperature sensor. 4, 5, 6 or 7 heating device for the target liquid to be heated.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001201690A JP3704063B2 (en) | 2001-07-03 | 2001-07-03 | Method and apparatus for heating target liquid to be heated |
| PCT/JP2002/006102 WO2003004941A1 (en) | 2001-07-03 | 2002-06-19 | Method and device for heating heated liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001201690A JP3704063B2 (en) | 2001-07-03 | 2001-07-03 | Method and apparatus for heating target liquid to be heated |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2003014299A true JP2003014299A (en) | 2003-01-15 |
| JP3704063B2 JP3704063B2 (en) | 2005-10-05 |
Family
ID=19038609
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001201690A Expired - Fee Related JP3704063B2 (en) | 2001-07-03 | 2001-07-03 | Method and apparatus for heating target liquid to be heated |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP3704063B2 (en) |
| WO (1) | WO2003004941A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008136135A1 (en) * | 2007-05-01 | 2008-11-13 | Japan Field Co., Ltd. | Method of heating heating object liquid and apparatus therefor |
| JP2009222251A (en) * | 2008-03-13 | 2009-10-01 | Japan Field Kk | Heating method of heating target liquid and its device |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103175186A (en) * | 2013-03-01 | 2013-06-26 | 龚胜 | Atmospheric steam domestic boiler |
| EP3298335A1 (en) * | 2015-05-20 | 2018-03-28 | Joto Solutions AB | A liquid heating system and a method for heating liquid |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2659831B2 (en) * | 1989-11-10 | 1997-09-30 | 工業技術院長 | Boiling evaporation method and apparatus |
| JPH05237471A (en) * | 1992-02-27 | 1993-09-17 | Japan Field Kk | Vaporizing thickening apparatus for waste water |
| JP3231747B2 (en) * | 1999-12-08 | 2001-11-26 | ジャパン・フィールド株式会社 | Contaminated cleaning liquid boiler |
-
2001
- 2001-07-03 JP JP2001201690A patent/JP3704063B2/en not_active Expired - Fee Related
-
2002
- 2002-06-19 WO PCT/JP2002/006102 patent/WO2003004941A1/en not_active Ceased
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008136135A1 (en) * | 2007-05-01 | 2008-11-13 | Japan Field Co., Ltd. | Method of heating heating object liquid and apparatus therefor |
| JPWO2008136135A1 (en) * | 2007-05-01 | 2010-07-29 | ジャパン・フィールド株式会社 | Method and apparatus for heating target liquid to be heated |
| JP2009222251A (en) * | 2008-03-13 | 2009-10-01 | Japan Field Kk | Heating method of heating target liquid and its device |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3704063B2 (en) | 2005-10-05 |
| WO2003004941A1 (en) | 2003-01-16 |
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