JPS62119365A - Heat transfer device of heat drive type - Google Patents
Heat transfer device of heat drive typeInfo
- Publication number
- JPS62119365A JPS62119365A JP60259038A JP25903885A JPS62119365A JP S62119365 A JPS62119365 A JP S62119365A JP 60259038 A JP60259038 A JP 60259038A JP 25903885 A JP25903885 A JP 25903885A JP S62119365 A JPS62119365 A JP S62119365A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- temperature side
- side tank
- heat
- pipe
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
Abstract
Description
【発明の詳細な説明】
(イ)産業上の利用分野
この発明は太陽熱集熱装置や暖房装置などに利用され、
を動ポンプを使用することなく搬送すべき熱自身のエネ
ルギーを利用して熱媒液を循環させるようにした熱駆動
型熱搬送装置に関する。[Detailed description of the invention] (a) Industrial application field This invention is used in solar heat collection devices, heating devices, etc.
The present invention relates to a heat-driven heat transfer device that circulates a heat medium liquid using the energy of the heat to be transferred without using a dynamic pump.
(ロ)従来の技術
この種の熱駆動型熱搬送装置として特開昭60−133
264号公報に開示されているものが知られている。こ
のものは第5因に示すように、熱媒液を貯溜し、その熱
媒液な太陽熱集熱器等の加熱袋[1を用いて蒸発させる
高温側タンク2と、この高温側タンク2よりも高い位置
に配設された低温側タンク3と、高温側タンク2よりも
低い位置に配設された蓄熱槽4内に収容された熱交換器
5と、この熱交換器5を介して高温側タンク2の熱媒液
を低温側タンク3に導く揚流管6と、低温側タンク3の
熱媒液を逆止弁7を介して高温側タンク2に導く還流管
8と、両タンク2.3P′3の蒸気層を連通する連通管
9と、高温側タンク2内の低液位時のみ連通管9を開口
し両タンク2.3内を均圧にする開閉弁10とを備えた
構成であり。(b) Conventional technology This type of heat-driven heat transfer device is disclosed in Japanese Patent Application Laid-Open No. 60-133.
The one disclosed in Japanese Patent No. 264 is known. As shown in the fifth factor, there is a high-temperature side tank 2 that stores a heat medium liquid and evaporates it using a heating bag [1] such as a solar heat collector, and a high-temperature side tank 2 that A low-temperature side tank 3 is arranged at a higher position than the high-temperature side tank 2, and a heat exchanger 5 is housed in a heat storage tank 4 which is arranged at a lower position than the high-temperature side tank 2. A lift pipe 6 that guides the heat medium liquid in the side tank 2 to the low temperature side tank 3, a reflux pipe 8 that leads the heat medium liquid in the low temperature side tank 3 to the high temperature side tank 2 via the check valve 7, and both tanks 2. Equipped with a communication pipe 9 that communicates the steam layer of .3P'3, and an on-off valve 10 that opens the communication pipe 9 only when the liquid level in the high temperature side tank 2 is low and equalizes the pressure in both tanks 2.3. It is the composition.
高温側タンク2内に熱媒液が満たされたとき開閉弁10
を閉とし、加熱装置1で熱媒液を蒸発させ、高温側タン
ク2内の圧力を上昇させることにより。When the high temperature side tank 2 is filled with heat medium liquid, the on-off valve 10
by closing the tank, evaporating the heat transfer liquid with the heating device 1, and increasing the pressure in the high temperature side tank 2.
高温側タンク2の熱媒液を揚流管6を介して低温側タン
ク3へ移動させ、熱交換器5で蓄熱槽4内の水等を加熱
するようにしている。また、高温側タンク2円の低液位
時に開閉弁10を開とし1両タンク2.3内を均圧にす
ることにより、液位の高い低温側タンク3から高温側タ
ンク2へ熱媒液を戻すようにしている。The heat medium liquid in the high-temperature side tank 2 is moved to the low-temperature side tank 3 via the uplift pipe 6, and the water and the like in the heat storage tank 4 are heated by the heat exchanger 5. In addition, by opening the on-off valve 10 when the liquid level in the high-temperature side tank 2 is low and equalizing the pressure inside the single-car tank 2.3, the heat transfer liquid is transferred from the low-temperature side tank 3, which has a high liquid level, to the high-temperature side tank 2. I'm trying to get it back.
上述した従来装置は蒸気の圧力差で熱媒液を上方へ移動
させ1重力作用により熱媒液を元の位置に戻すものであ
り、加えられた熱自身によって熱媒液が循環するため電
動ポンプが不要となり、大幅な軽量化が図れるとともに
、無電力で熱搬送のコストも不要となる利点がある。The conventional device described above moves the heat medium liquid upward by the pressure difference of steam and returns it to its original position by the action of gravity.The heat medium liquid is circulated by the added heat itself, so an electric pump It has the advantage of not only being able to achieve a significant weight reduction, but also eliminating the need for electricity and the cost of heat transfer.
pi 発明が解決しようとする問題点しかしながら、
上述した従来itは熱媒液の揚流、還流の繰返しの応答
を良好にし、応答時間を短縮してボンピングサイクルを
多くするために。pi The problem that the invention seeks to solveHowever,
The above-mentioned conventional IT is intended to improve the response to repeated pumping and reflux of the heat transfer fluid, shorten the response time, and increase the number of pumping cycles.
複雑な構造の開閉弁を使用しなければならず、耐久性、
信頼性が乏しい欠点があった。また、このことが実用化
の妨げになっていた。It is necessary to use an on-off valve with a complicated structure, and the durability and
It had the drawback of poor reliability. This also hindered its practical application.
この発明は上述した事実に鑑みてなされたもので、開閉
弁等の機械的可動部分を極力少なくし、装置の耐久性お
よび信頼性を向上させることを目的とする。This invention was made in view of the above-mentioned facts, and aims to improve the durability and reliability of the device by minimizing the number of mechanically movable parts such as on-off valves.
に)問題点を解決するための手段
上記の目的を達成するため、この発明では熱媒液を貯溜
し、その熱媒液を加熱装置を用いて蒸発させる高温側タ
ンクと、この高温側タンクよりも高い位置に配設された
低温側タンクと、高温側タンクよりも低い位置に配設さ
れた熱交換器と、この熱交換器を介して高温側夕/りの
熱媒液を低温側タンクに導く揚流管と、低温側タンクの
熱媒液を逆上弁を介して高温側タンクに導く還流管と、
両タンク内の蒸気層を連通ずるとともに、高温側タンク
の側方において下方へ屈曲させた部分を有する連通管と
、この連通管の屈曲部に装設された補助タンクと、この
補助タンクと上記高温側タンクの上部とを連通するサイ
フオン管とを備えた構成である。B) Means for Solving the Problems In order to achieve the above object, the present invention includes a high-temperature side tank that stores a heat medium liquid and evaporates the heat medium liquid using a heating device, and a high-temperature side tank that stores a heat medium liquid and evaporates the heat medium liquid using a heating device. A low-temperature side tank is installed at a higher position than the high-temperature side tank, and a heat exchanger is installed at a lower position than the high-temperature side tank. a lift pipe that guides the heat medium liquid from the low-temperature side tank to the high-temperature side tank via a reverse valve;
A communication pipe that communicates the vapor layers in both tanks and has a downwardly bent part on the side of the high temperature side tank, an auxiliary tank installed at the bent part of this communication pipe, and this auxiliary tank and the above. The structure includes a siphon pipe that communicates with the upper part of the high temperature side tank.
(ホ)作用
この発明では補助タンク、連結管およびサイフオン管に
熱媒液がないとき、高温側タンクおよび低温側タンク内
が均圧となり、両タンクの液面レベルのヘッド差によっ
て熱媒液が低温側タンクから高温側タンクへ還流すると
ともに、サイフオン管を介して補助タンク内へ熱媒液が
入る。その後。(E) Effect In this invention, when there is no heat medium liquid in the auxiliary tank, connecting pipe, and siphon pipe, the pressure in the high temperature side tank and the low temperature side tank becomes equal, and the heat medium liquid is increased due to the head difference in the liquid level of both tanks. The heat transfer liquid flows back from the low-temperature side tank to the high-temperature side tank, and also enters the auxiliary tank via the siphon pipe. after that.
高温側タンクの熱媒液が加熱装置にて加熱され、蒸発す
ると、高温側タンク内の圧力の上昇に伴なって連通管の
液面レベルが上昇していく。また。When the heat medium liquid in the high-temperature side tank is heated by the heating device and evaporated, the liquid level in the communication pipe increases as the pressure in the high-temperature side tank increases. Also.
高温側タンク内の圧力か低温側タンクよりも十分に高く
なると、高温側タンクの熱媒液が熱交換器を装設した揚
流管を介して低温側タンクへ移動する。この結果高温側
タンク内の液面レベルがサイフオン管の開口高さ位置よ
り低くなると、高温側タンクから補助タンクへの熱媒液
の移動はなくなる。その後、高温側タンク内の圧力がさ
らに上昇すると、揚流管での熱媒液の移動が行なわれる
とともに、補助タンク内の熱媒液が連通管を介して低温
側タンクへ移IMJする。このようにして補助タンク内
の熱媒液がなくなると、高温側タンクの蒸気が連通管を
介して低温側タンクへ移動し、両タンク内が均圧となる
。このため、両タンクの液面レベルのヘッド差により、
低温側タンクから高温側タンクへ熱媒液が還流する。以
上の繰返しにより、加熱装置の熱が熱交換器へ間欠的に
搬送される。When the pressure in the high-temperature tank becomes sufficiently higher than that in the low-temperature tank, the heat medium liquid in the high-temperature tank moves to the low-temperature tank via an uplift pipe equipped with a heat exchanger. As a result, when the liquid level in the high-temperature side tank becomes lower than the opening height of the siphon tube, the heat transfer liquid no longer moves from the high-temperature side tank to the auxiliary tank. Thereafter, when the pressure in the high-temperature side tank further increases, the heat medium liquid is moved in the lift pipe, and the heat medium liquid in the auxiliary tank is transferred to the low-temperature side tank via the communication pipe. When the heat medium liquid in the auxiliary tank runs out in this way, the steam in the high temperature side tank moves to the low temperature side tank via the communication pipe, and the pressure in both tanks becomes equal. For this reason, due to the head difference in the liquid level of both tanks,
The heat transfer liquid flows back from the low-temperature side tank to the high-temperature side tank. By repeating the above steps, the heat of the heating device is intermittently transferred to the heat exchanger.
(へ)実施例
以下、この発明を図面に示す実施例に基づいて詳細に説
明する。(F) Embodiments The present invention will be described in detail below based on embodiments shown in the drawings.
第1図および第2図はこの発明の一実施例装置を示すも
のである。これらの図において、11は加熱装置として
の太陽熱集熱器、12は集熱器11よりも高い位置に配
設され、下端部が集熱器11の上端部に接続された高温
側タンク、13は高温側タンク12よりも高い位置に配
設され、下端部が逆止弁14を有する還流管15を介し
て集熱器11の下端部に接続された低温側タンク、16
は高温側タンク12の下端部と低温側タンク13内の蒸
気層13Aとを連通する揚流管であり、この揚流管16
には逆止弁17と熱交換器18とが頌次装設され、熱交
換器18は蓄熱槽19内に収納されている。20は高温
側タンク12の上端部と低温側タンク13の上端部を接
続して両タンク12.13の内部の蒸気層12A、13
Aを連通てる連通管であり、高温側タンク12の側方に
おいて下方へ屈曲させた部分20Aを有している。FIGS. 1 and 2 show an embodiment of the present invention. In these figures, 11 is a solar heat collector as a heating device, 12 is a high temperature side tank that is disposed at a higher position than the heat collector 11 and whose lower end is connected to the upper end of the heat collector 11, and 13 A low temperature side tank 16 is disposed at a higher position than the high temperature side tank 12 and is connected to the lower end of the heat collector 11 via a reflux pipe 15 having a check valve 14 at its lower end.
is a lift pipe that communicates the lower end of the high-temperature side tank 12 with the steam layer 13A in the low-temperature side tank 13;
is equipped with a check valve 17 and a heat exchanger 18, and the heat exchanger 18 is housed in a heat storage tank 19. Reference numeral 20 connects the upper end of the high temperature side tank 12 and the upper end of the low temperature side tank 13 to form vapor layers 12A, 13 inside both tanks 12.13.
It is a communication pipe that communicates with A, and has a portion 20A that is bent downward on the side of the high temperature side tank 12.
21は連通管20の屈曲部2OAに装設された補助タン
ク、22はこの補助タンク21と高温側タンク12内の
上部とを連通ずるサイフオン管である。高温側タンク1
2.低温側タンク13、補助タンク21を装設した連通
f20およびサイフオン管22は筐体23内に収納され
、この筺体23と集熱器11とが建物24の屋根25上
に設置されている。また、熱交換器18を収納した蓄熱
槽19は建物240軒下等の低所に設置されている。Reference numeral 21 indicates an auxiliary tank installed at the bending portion 2OA of the communication pipe 20, and 22 indicates a siphon pipe that communicates the auxiliary tank 21 with the upper part of the high temperature side tank 12. High temperature side tank 1
2. The low temperature side tank 13, the communication f20 equipped with the auxiliary tank 21, and the siphon pipe 22 are housed in a housing 23, and the housing 23 and the heat collector 11 are installed on the roof 25 of a building 24. Further, a heat storage tank 19 containing a heat exchanger 18 is installed at a low place such as under 240 buildings.
なお、高1側タンク12や低温側タンク13に充填する
熱媒液は気漱2相に変化するフロン冷媒(例えばR−1
14)などが使用される。Note that the heating medium liquid filled in the high-1 side tank 12 and the low-temperature side tank 13 is a fluorocarbon refrigerant (for example, R-1
14) etc. are used.
次に、上述した実施例装置の動作を説明する。Next, the operation of the above-described embodiment device will be explained.
■ 補助タンク21、連通管20およびサイフオン管2
2に熱媒液がなく、これらがガスで満たされているもの
とすると、高温側タンク12および低温側タンク13内
は均圧している。このため、両タンク12.13の液面
レベルのヘッド差によって低温側タンク13の熱媒液が
還流管15および集熱器11を通って高温側タンク12
へ移動する。■ Auxiliary tank 21, communication pipe 20 and siphon pipe 2
Assuming that there is no heat transfer liquid in tank 2 and that these are filled with gas, the pressure inside the high temperature side tank 12 and the low temperature side tank 13 is equalized. Therefore, due to the head difference between the liquid levels of both tanks 12 and 13, the heat medium liquid in the low temperature side tank 13 passes through the reflux pipe 15 and the heat collector 11 to the high temperature side tank 12.
Move to.
■ 高温側タンク12の液面レベルがサイフオン管22
の最上部の高さくX−X線)以上になると、高温側タン
ク12の熱媒液の一部がサイフオン管22を通って補助
タンク21へ移動する。■ The liquid level of the high-temperature side tank 12 is the same as that of the siphon tube 22.
When the height of the top of the temperature rises above (X-X line), a part of the heat transfer liquid in the high temperature side tank 12 moves to the auxiliary tank 21 through the siphon pipe 22.
■ 集熱器11が日射を受けると、集熱器11内の熱媒
液が蒸発しながら高温側タンク12へ移動するため、高
温側タンク12内の圧力が上昇する。(2) When the heat collector 11 receives solar radiation, the heat medium liquid in the heat collector 11 evaporates and moves to the high temperature side tank 12, so that the pressure in the high temperature side tank 12 increases.
■ 高温側タンク12FF3の圧力上昇に伴ない、補助
タンク21内の熱媒液が連通管20V3を上昇していく
。連通管20の液面レベルは高温側タンク12および低
温側タンク13内の圧力着に相半てる位置で均衡する。(2) As the pressure of the high temperature side tank 12FF3 increases, the heat medium liquid in the auxiliary tank 21 rises through the communication pipe 20V3. The liquid level in the communication pipe 20 is balanced at a position relative to the pressure bonds in the high temperature side tank 12 and the low temperature side tank 13.
■ 高温側タンク12内の圧力が低温側タンク13内の
圧力よりも十分に高くなると、高温側タンク12内の熱
媒液は逆止弁1γおよび熱交換器18を装設した揚流管
16を通って低温側タンク13へ移動する。■ When the pressure in the high temperature side tank 12 becomes sufficiently higher than the pressure in the low temperature side tank 13, the heat medium liquid in the high temperature side tank 12 flows through the lift pipe 16 equipped with the check valve 1γ and the heat exchanger 18. and then moves to the low temperature side tank 13.
■ この結果、高温側タンク12内の液面レベルがサイ
フオン管22の開口高さくY−Yi)より低くなると、
サイフオン管22内の熱媒液が補助タンク21または高
温側タンク12へ抜は落ち、高温側タンク12から補助
タンク21への液の移動がなくなる。■ As a result, when the liquid level in the high temperature side tank 12 becomes lower than the opening height of the siphon tube 22 (Y-Yi),
The heat medium liquid in the siphon tube 22 is drained and falls into the auxiliary tank 21 or the high temperature side tank 12, and the liquid does not move from the high temperature side tank 12 to the auxiliary tank 21.
■ さらに、高温側タンク12内の圧力が上昇すると、
熱媒液が高温側タンク12から低温側タンク13へ移動
するとともに、連通管20の液面レベルが上昇し、補助
タンク21内の熱媒液が低温側タンク13へ移動する。■ Furthermore, when the pressure inside the high temperature side tank 12 increases,
As the heat medium liquid moves from the high temperature side tank 12 to the low temperature side tank 13, the liquid level in the communication pipe 20 rises, and the heat medium liquid in the auxiliary tank 21 moves to the low temperature side tank 13.
■ 補助タンク21および連通管20円の熱媒液がなく
なると、高温側タンク12内のガスが連通管20を通っ
て低温側タンク13へ移動する。(2) When the heat medium liquid in the auxiliary tank 21 and the communication pipe 20 is used up, the gas in the high temperature side tank 12 passes through the communication pipe 20 and moves to the low temperature side tank 13.
液に比べてガスの体積流量は大きいので、高温側タンク
12および低温側タンク13内の圧力は速やかに均等に
なる。Since the volumetric flow rate of the gas is larger than that of the liquid, the pressures in the high-temperature side tank 12 and the low-temperature side tank 13 quickly become equal.
■ この結果、両タンク12.13の液面レベルの違い
によるヘッド差で、低温側タンク13の熱媒液が高温側
タンク12へ還流する。(2) As a result, the heat medium liquid in the low-temperature side tank 13 flows back to the high-temperature side tank 12 due to the head difference due to the difference in liquid level in both tanks 12,13.
以上の繰返しにより、集熱器11で集熱された太陽熱が
間欠的に熱交換器18へ搬送され、蓄熱槽19内の水を
加熱するのに利用される。By repeating the above steps, the solar heat collected by the heat collector 11 is intermittently conveyed to the heat exchanger 18 and used to heat the water in the heat storage tank 19.
本実施例装置は従来の開閉弁の代わりにサイホン作用と
液面レベルの違いによるヘッド差とを利用して熱媒液を
循環させるよつにしているので。This embodiment uses a siphon action and a head difference due to a difference in liquid level to circulate the heat medium liquid instead of the conventional on-off valve.
逆止弁14.1T以外に機械的可動部分がなく。There are no mechanically moving parts other than the check valve 14.1T.
装置の耐久性および信頼性の向上が図れるものである。The durability and reliability of the device can be improved.
なお、逆止弁14.1rはともに逆流防止用であるか、
逆上弁1γは省略可能である。In addition, are the check valves 14.1r both for backflow prevention?
The reverse valve 1γ can be omitted.
第3図はこの発明の他の実施例装置を示すものであり、
第1図に示すものと共通する部分には同一符号を付しで
ある。第3図において、第1図のものと異なるのは逆止
弁14を有する還流管15を高温側タンク12および低
温側タンク13の下端部に接続したことと、集熱器11
0両端部を高温側タンク12の下部に接続したことであ
る。第3図の実施例装置の動作は第1図のものと同様で
あるので説明を省略する。FIG. 3 shows another embodiment of the invention,
Components common to those shown in FIG. 1 are given the same reference numerals. In FIG. 3, the difference from that in FIG.
0 and both ends thereof are connected to the lower part of the high temperature side tank 12. The operation of the embodiment shown in FIG. 3 is the same as that shown in FIG. 1, so the explanation thereof will be omitted.
なお、上述した実施例装置は加熱装置として太陽熱集熱
器11を使用したが、加熱装置はヒータやバーナ等の熱
源でも良く、高温側タンク12に加熱装置を内蔵したり
、高温側タンク12自身で太陽熱の集熱な行なうように
しても良い。また、屈曲部20Aと低温側タンク13と
の間の立上り高さが十分にとれないときは第4図に示す
ように連通管20を蛇行状にしても良い。Although the above-described embodiment device uses the solar heat collector 11 as a heating device, the heating device may be a heat source such as a heater or a burner, and the heating device may be built into the high-temperature side tank 12 or the high-temperature side tank 12 itself may be used as a heating device. It may also be possible to collect solar heat. Further, when the rising height between the bent portion 20A and the low temperature side tank 13 cannot be sufficiently secured, the communication pipe 20 may be formed into a meandering shape as shown in FIG. 4.
(ト)発明の効果 この発明は以上のように構成されているので。(g) Effects of the invention This invention is configured as described above.
サイフオン作用と液面レベルの違いによるヘッド差とを
利用して間欠的に熱媒液を循環させ、熱搬送を行なうこ
とができ、逆止弁以外の機械的可動部分が不要となり、
装置の耐久性および信頼性を大幅に向上できるものであ
り、無電力で、搬送コストが不要な熱駆動型熱搬送装置
の普及に貢献できるものである。Heat transfer can be carried out by intermittently circulating the heat transfer liquid using the siphon effect and head differences due to differences in liquid level, eliminating the need for mechanical moving parts other than check valves.
This can significantly improve the durability and reliability of the device, and can contribute to the spread of heat-driven heat transfer devices that require no electricity and no transportation costs.
【図面の簡単な説明】
第1図はこの発明の一実施例を示す熱駆動型熱搬送装置
の系統図、第2図は同じく設置状態を示す説明図、第3
図はこの発明の他の実施例装置の系統図、第4図は連通
管の変形例を示す配管図、第5図は従来装置の1例を示
す系統図である。
11・・・太陽熱集熱器、 12・・・高温側タンク、
13・・・低温側タンク、 14・・・逆止弁、15・
・・還流管、 16・・・揚流管、 18・・・熱交換
器、20・・・連通管、 20A・・・屈曲部、 21
・・・補助タンク、 22・・・サイフオン管。
出願人 三洋電機株式会社 外1名
代理人 弁理士 佐 野 靜 矢
筒1 図
第2図
第5図[BRIEF DESCRIPTION OF THE DRAWINGS] Fig. 1 is a system diagram of a thermally driven heat transfer device showing an embodiment of the present invention, Fig. 2 is an explanatory drawing showing the installation state, and Fig. 3 is an explanatory diagram showing the installed state.
FIG. 4 is a system diagram of a device according to another embodiment of the present invention, FIG. 4 is a piping diagram showing a modification of the communication pipe, and FIG. 5 is a system diagram showing an example of a conventional device. 11...Solar heat collector, 12...High temperature side tank,
13... Low temperature side tank, 14... Check valve, 15...
... Reflux pipe, 16... Uplift pipe, 18... Heat exchanger, 20... Communication pipe, 20A... Bent part, 21
...Auxiliary tank, 22...Siphon tube. Applicant Sanyo Electric Co., Ltd. and 1 other agent Patent attorney Makoto Sano Quiver 1 Figure 2 Figure 5
Claims (1)
蒸発させる高温側タンクと、この高温側タンクよりも高
い位置に配設された低温側タンクと、高温側タンクより
も低い位置に配設された熱交換器と、この熱交換器を介
して高温側タンクの熱媒液を低温側タンクに導く揚流管
と、低温側タンクの熱媒液を逆止弁を介して高温側タン
クに導く還流管と、両タンク内の蒸気層を連通するとと
もに、高温側タンクの側方において下方へ屈曲させた部
分を有する連通管と、この連通管の屈曲部に装設された
補助タンクと、この補助タンクと上記高温側タンクの上
部とを連通するサイフォン管とを備えたことを特徴とす
る熱駆動型熱搬送装置。(1) A high-temperature side tank that stores heat transfer fluid and evaporates the heat transfer fluid using a heating device, a low-temperature tank that is located higher than the high-temperature tank, and a lower temperature tank that is located higher than the high-temperature tank. A heat exchanger installed at a low position, a lifting pipe that leads the heat medium liquid from the high temperature side tank to the low temperature side tank through the heat exchanger, and a lift pipe that leads the heat medium liquid from the low temperature side tank to the low temperature side tank through a check valve. A reflux pipe that leads to the high-temperature side tank, a communication pipe that communicates the vapor layers in both tanks and has a downwardly bent portion on the side of the high-temperature side tank, and a communication pipe that is installed at the bent part of the communication pipe. 1. A thermally driven heat transfer device comprising: an auxiliary tank with a high temperature side; and a siphon pipe that communicates the auxiliary tank with the upper part of the high temperature side tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60259038A JPS62119365A (en) | 1985-11-19 | 1985-11-19 | Heat transfer device of heat drive type |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60259038A JPS62119365A (en) | 1985-11-19 | 1985-11-19 | Heat transfer device of heat drive type |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62119365A true JPS62119365A (en) | 1987-05-30 |
Family
ID=17328468
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60259038A Pending JPS62119365A (en) | 1985-11-19 | 1985-11-19 | Heat transfer device of heat drive type |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62119365A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013504032A (en) * | 2009-09-08 | 2013-02-04 | ダブリュ アンド イー インターナショナル(カナダ) コーポレーション | Self-supporting pump for heated liquid, and heat-driven liquid closed-loop automatic circulation system using the same |
-
1985
- 1985-11-19 JP JP60259038A patent/JPS62119365A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013504032A (en) * | 2009-09-08 | 2013-02-04 | ダブリュ アンド イー インターナショナル(カナダ) コーポレーション | Self-supporting pump for heated liquid, and heat-driven liquid closed-loop automatic circulation system using the same |
EP2475894A4 (en) * | 2009-09-08 | 2017-08-30 | Huazi Lin | Self-powered pump for heated liquid and heat driven liquid close - loop automatic circulating system employing same |
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