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JPS6312504B2 - - Google Patents
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JPS6312504B2 - - Google Patents

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Publication number
JPS6312504B2
JPS6312504B2 JP57007178A JP717882A JPS6312504B2 JP S6312504 B2 JPS6312504 B2 JP S6312504B2 JP 57007178 A JP57007178 A JP 57007178A JP 717882 A JP717882 A JP 717882A JP S6312504 B2 JPS6312504 B2 JP S6312504B2
Authority
JP
Japan
Prior art keywords
working fluid
tfe
section
heat transfer
water
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
Application number
JP57007178A
Other languages
Japanese (ja)
Other versions
JPS58122980A (en
Inventor
Atsuyumi Ishikawa
Toshio Nakayama
Takeshi Kanai
Kazuhiro Shimura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP57007178A priority Critical patent/JPS58122980A/en
Publication of JPS58122980A publication Critical patent/JPS58122980A/en
Publication of JPS6312504B2 publication Critical patent/JPS6312504B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)
  • Other Air-Conditioning Systems (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はトリフルオロエタノール(以下、
TFEと略称する。)を作動流体とした熱移動装置
に関する。 作動流体を加熱して蒸発させる再生部と作動流
体を冷却して液化させる凝縮部とを循環する作動
流体の密閉循環系を形成し、作動流体の凝縮潜熱
を凝縮部から系外へ送り出して負荷に供給する熱
移動装置には、例えばヒートパイプやサーモサイ
フオンがその代表的なものとして知られており、
又その作動流体においても水、エタノール、フレ
オン等の種々の物質が従来知られている。 しかし乍ら、水、エタノール、フレオン、水
銀、セシウム、ペンタン、ヘプタン等を作動流体
とした従来の熱移動装置においては、その作動流
体の種類により、高温条件下の熱安定性の悪いも
の、装置の構造材(主として鉄材)に対する腐食
性の高いもの、人体に対する毒性や爆発の危険性
を有するもの、凍結点が高く寒冷気候での使用が
不適なもの、或いは高価なものとなる等様々の欠
点がある。また、此種熱移動装置の再生部への熱
供給方式には電気ヒーターによるもの、スチーム
によるもの、石油バーナーおよびガスバーナーな
どによるものがあるが、その中で効率が良く装置
を単純でコンパクトにし得る直火方式が一般に採
用され、この直火方式においては、特に作動流体
の高温条件下での熱安定性、装置の構造材に対す
る腐食性および安全性が問題となる。 本発明は、斯る点に鑑み、此種熱移動装置の作
動流体として、高温領域においても金属に対する
腐食力が弱く、かつ熱安定性に秀れたTFE若し
くはTFEと水との混合溶液(TFE水溶液と略称
する)を採用し、コンパクトで、且つ、直火方式
のような高温条件でも安定かつ安全に負荷への熱
供給を行なうことのできる熱移動装置を提供する
ものである。 熱移動装置の作動流体として使用するTFEの
物性並びにTFE水溶液の物性の一例は表1に示
される。
The present invention uses trifluoroethanol (hereinafter referred to as
It is abbreviated as TFE. ) as a working fluid. A closed circulation system for working fluid is formed that circulates between a regeneration section that heats and evaporates the working fluid and a condensation section that cools and liquefies the working fluid.The latent heat of condensation of the working fluid is sent out from the condensation section to the outside of the system to reduce the load. For example, heat pipes and thermosiphons are known as representative heat transfer devices that supply heat to the
Furthermore, various substances such as water, ethanol, Freon, etc. are conventionally known as the working fluid. However, in conventional heat transfer devices that use water, ethanol, Freon, mercury, cesium, pentane, heptane, etc. as working fluids, depending on the type of working fluid, some devices have poor thermal stability under high-temperature conditions. They have various drawbacks, such as being highly corrosive to structural materials (mainly iron materials), being toxic to the human body and at risk of explosion, having a high freezing point and being unsuitable for use in cold climates, and being expensive. There is. In addition, heat supply methods to the regeneration section of this type of heat transfer equipment include electric heaters, steam, oil burners, gas burners, etc., but among these, the most efficient and simple and compact equipment. In this direct fire method, problems arise particularly in terms of thermal stability of the working fluid under high temperature conditions, corrosiveness to the structural materials of the device, and safety. In view of this, the present invention uses TFE or a mixed solution of TFE and water (TFE), which has a weak corrosive force against metals even in high-temperature regions and has excellent thermal stability, as a working fluid for this type of heat transfer device. The purpose of the present invention is to provide a heat transfer device that is compact and capable of stably and safely supplying heat to a load even under high-temperature conditions such as an open flame method. Table 1 shows an example of the physical properties of TFE and the physical properties of an aqueous TFE solution used as a working fluid in a heat transfer device.

【表】 又、TFE水溶液の水重量%に対する凝固点
(融点)及び蒸発潜熱は第1図に示される。 TFEは、燃焼点を有さず(すなわち、TFEか
ら炎を放すと燃焼を続けなくなる)、万一TFEが
漏出する等の事故を起こしても水等で混和して容
易に除去することができ、又、空気との全蒸気濃
度において非爆発性であり、皮膚接触に関しても
無毒性基準を満足するものである。このような
TFEの物性から、家庭用の暖房機に前記熱移動
装置を利用する際の作動流体としてTFEを使用
することが好適である。 また、TFEは鉄、銅、鋼およびアルミニウム
等の金属に対して高温条件下においても腐食力が
小さく、TFE水溶液は純粋のTFEより更に腐食
力が小さいと云う性質を持つている。しかも、第
1図から明らかなように、TFE水溶液は、その
蒸発潜熱が水含有率を増すに比例して増加(例え
ば水15重量%の場合には155kcal/Kgとなり、
純粋のTFE(83kcal/Kg)より大きい。)するこ
とから、TFE水溶液の方が純粋のTFEよりも単
位量当たりの熱移動量が多くなり、又TFE水溶
液の凝固点についても、水3.0重量%において最
も低温(−64℃)となり寒冷気候においても作動
流体の凍結を生じる可能性が少ない。このように
TFE水溶液は純粋のTFEより作動流体として秀
れた一面を有する反面水の含有率が増大し過ぎる
と例えば凝固点が高くなる等逆に作動流体として
不利な面を有する。而して、水15重量%以下の
TFE水溶液及びTFEが此種熱移動装置の作動流
体として好適である。 また、TFE及びTFE水溶液は常温では液体で
あるから、前記熱移動装置の作動流体循環系内へ
の充填も容易である。 以上のようなTFE及びTFE水溶液の既知の物
性並びに実験による測定データに着目し、第2図
に示すサーモサイフオンにおいて水15重量%以下
の範囲内にあるTFE水溶液及びTFEを充填して
実験したところ、作動流体は安定した密閉循環サ
イクルを形成し、従来のものより5〜6%熱移動
の向上を達成し得た。 第2図において、1は再生部、2は作動流体の
流動状態を観察するためのサイトガラス部、3は
凝縮部及び4は貯液部で、これらは配管5,6,
7及び8に接続されて作動流体の循環系9を形成
し、前記凝縮部3を囲繞する放熱器10を介して
作動流体の凝縮潜熱及び顕熱エネルギーを前記系
9外の負荷側(図示せず)へ冷却水により送り出
すようにしたサーモサイフオンを構成している。 而して、再生部1で加熱された作動流体は蒸発
し配管5内壁に液相部11と配管5内中空部分に
気相部12とを形成する気液二相流の状態で配管
5、サイトガラス部2及び配管6内を上昇し、凝
縮部3に至る。凝縮部3に至つた作動流体は放熱
器10を流れる冷却水により凝縮冷却され配管7
内を流下して貯液部4、配管8を経由し再び再生
部1に戻り、作動流体は系9を循環する。 このようにして、凝縮部3から放熱部10を介
して負荷側へ作動流体の熱エネルギーが連続的に
供給される。 本発明は、以上のように、再生部と凝縮部とを
循環する作動流体の密閉循環系を形成し、再生部
で作動流体に与えられた熱エネルギーを凝縮部か
ら系外へ送り出すようにした熱移動装置において
作動流体に水が15重量%以下の範囲内にある
TFE水溶液及びTFEを用いたものであるから、
再生部の熱源供給方式を直火方式にしても作動流
体の安定性が保たれ、かつ装置の腐食も少なく安
全であり、装置全体をコンパクトにすることがで
きる。又、TFE若しくはTFE水溶液は人体に対
する毒性や爆発性がないので、本発明装置を家庭
用暖房及び給湯システムに利用することもでき、
寒冷地での利用にも適する等実用上有益なもので
ある。
[Table] Furthermore, the freezing point (melting point) and latent heat of vaporization of the TFE aqueous solution relative to the water weight % are shown in FIG. TFE does not have a combustion point (that is, if a flame is released from TFE, it will not continue burning), and even if an accident such as TFE leakage occurs, it can be easily removed by mixing with water etc. Furthermore, it is non-explosive at all vapor concentrations with air and satisfies non-toxicity standards regarding skin contact. like this
Due to the physical properties of TFE, it is preferable to use TFE as a working fluid when the heat transfer device is used in a home heater. Furthermore, TFE has a property that it has a low corrosive power against metals such as iron, copper, steel, and aluminum even under high temperature conditions, and a TFE aqueous solution has an even lower corrosive power than pure TFE. Furthermore, as is clear from Figure 1, the latent heat of vaporization of the TFE aqueous solution increases in proportion to the water content (for example, in the case of 15% water, it becomes 155 kcal/Kg,
Greater than pure TFE (83kcal/Kg). ), TFE aqueous solution has a larger amount of heat transfer per unit amount than pure TFE, and the freezing point of TFE aqueous solution is the lowest (-64℃) at 3.0% water by weight, making it difficult to use in cold climates. There is also less possibility of freezing of the working fluid. in this way
Although a TFE aqueous solution has one advantage over pure TFE as a working fluid, it has disadvantages as a working fluid, such as an increase in the freezing point if the water content increases too much. Therefore, the water content is less than 15% by weight.
Aqueous TFE solutions and TFE are suitable as working fluids for this type of heat transfer device. Furthermore, since TFE and TFE aqueous solution are liquids at room temperature, they can be easily filled into the working fluid circulation system of the heat transfer device. Focusing on the known physical properties of TFE and TFE aqueous solution as well as experimental measurement data as described above, an experiment was conducted by filling the thermosiphon shown in Figure 2 with TFE aqueous solution and TFE containing 15% by weight or less of water. However, the working fluid formed a stable closed circulation cycle, and the heat transfer was improved by 5 to 6% compared to the conventional one. In FIG. 2, 1 is a regeneration section, 2 is a sight glass section for observing the flow state of the working fluid, 3 is a condensation section, and 4 is a storage section, which are connected to pipes 5, 6,
7 and 8 to form a working fluid circulation system 9, and transfer the condensation latent heat and sensible heat energy of the working fluid to a load side (not shown) outside the system 9 through a radiator 10 surrounding the condensing section 3. The thermosiphon is configured to send cooling water to (1). Thus, the working fluid heated in the regeneration section 1 evaporates, forming a liquid phase part 11 on the inner wall of the pipe 5 and a gas phase part 12 in the hollow part of the pipe 5, in a gas-liquid two-phase flow state. It ascends inside the sight glass section 2 and piping 6 and reaches the condensing section 3. The working fluid that has reached the condensing section 3 is condensed and cooled by the cooling water flowing through the radiator 10 and then transferred to the piping 7.
The working fluid flows down through the storage section 4 and piping 8, returns to the regeneration section 1, and circulates through the system 9. In this way, the thermal energy of the working fluid is continuously supplied from the condensing section 3 to the load side via the heat radiating section 10. As described above, the present invention forms a closed circulation system for the working fluid that circulates between the regeneration section and the condensation section, and sends the thermal energy given to the working fluid in the regeneration section from the condensation section to the outside of the system. In heat transfer equipment, the working fluid contains water within a range of 15% by weight or less.
Since it uses a TFE aqueous solution and TFE,
Even if the heat source supply method for the regeneration section is a direct fire method, the stability of the working fluid is maintained, the equipment is safe with little corrosion, and the entire equipment can be made compact. Furthermore, since TFE or TFE aqueous solution is neither toxic nor explosive to the human body, the device of the present invention can also be used in home heating and hot water systems.
It is useful for practical use, as it is suitable for use in cold regions.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はTFE水溶液中の水の重量%とその凝
固点および一気圧下での蒸発潜熱との関係を示す
線図、第2図は本発明装置の一実施例であるサー
モサイフオンの系統概略図、第3図は本発明実施
例における再生部から凝縮部に至る作動流体の流
動状態を示した図面である。 1……再生部、3……凝縮部、9……循環系。
Figure 1 is a diagram showing the relationship between the weight percent of water in a TFE aqueous solution, its freezing point, and the latent heat of vaporization under one atmospheric pressure, and Figure 2 is a system diagram of a thermosiphon, which is an embodiment of the device of the present invention. 3 are views showing the flow state of the working fluid from the regeneration section to the condensation section in an embodiment of the present invention. 1... Regeneration section, 3... Condensation section, 9... Circulation system.

Claims (1)

【特許請求の範囲】 1 作動流体を加熱して蒸発させる再生部と作動
流体を冷却して液化させる凝縮部とを循環する作
動流体の密閉循環系を形成し、再生部で作動流体
に与えられた熱エネルギーを凝縮部から密閉循環
系外へ送り出すようにした熱移動装置において作
動流体がトリフルオロエタノールで成ることを特
徴とする熱移動装置。 2 作動流体が水を最高15重量%まで含有させた
トリフルオロエタノール水溶液で成る特許請求の
範囲第1項記載の熱移動装置。
[Claims] 1. A closed circulation system for working fluid is formed in which the working fluid is circulated through a regeneration section that heats and evaporates the working fluid and a condensation section that cools and liquefies the working fluid. 1. A heat transfer device configured to send out thermal energy from a condensing section to the outside of a closed circulation system, characterized in that the working fluid is made of trifluoroethanol. 2. A heat transfer device according to claim 1, wherein the working fluid is an aqueous trifluoroethanol solution containing up to 15% by weight of water.
JP57007178A 1982-01-19 1982-01-19 Heat transfer equipment Granted JPS58122980A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57007178A JPS58122980A (en) 1982-01-19 1982-01-19 Heat transfer equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57007178A JPS58122980A (en) 1982-01-19 1982-01-19 Heat transfer equipment

Publications (2)

Publication Number Publication Date
JPS58122980A JPS58122980A (en) 1983-07-21
JPS6312504B2 true JPS6312504B2 (en) 1988-03-19

Family

ID=11658816

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57007178A Granted JPS58122980A (en) 1982-01-19 1982-01-19 Heat transfer equipment

Country Status (1)

Country Link
JP (1) JPS58122980A (en)

Also Published As

Publication number Publication date
JPS58122980A (en) 1983-07-21

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