JPH01285726A - Heat pipe type heat accumulating water tank device - Google Patents

Heat pipe type heat accumulating water tank device

Info

Publication number
JPH01285726A
JPH01285726A JP11569688A JP11569688A JPH01285726A JP H01285726 A JPH01285726 A JP H01285726A JP 11569688 A JP11569688 A JP 11569688A JP 11569688 A JP11569688 A JP 11569688A JP H01285726 A JPH01285726 A JP H01285726A
Authority
JP
Japan
Prior art keywords
heat
heat exchanger
tube
exchanger tube
water tank
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
Application number
JP11569688A
Other languages
Japanese (ja)
Other versions
JPH0726748B2 (en
Inventor
Makoto Hori
誠 堀
Aritaka Tatsumi
辰己 有孝
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.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable 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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP11569688A priority Critical patent/JPH0726748B2/en
Publication of JPH01285726A publication Critical patent/JPH01285726A/en
Publication of JPH0726748B2 publication Critical patent/JPH0726748B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Abstract

PURPOSE:To drip condensed liquid produced by upper heat transfer tubes uniformly into a plurality of heat exchanging tubes by a method wherein a condensed liquid dripping unit such as green parts, discontinuous projections or the like is provided on the outer surface of the upper heat transfer tube with a space shorter than the arranging pitch of the heat exchanging tubes while projections or choked parts are provided on the inner surface of the upper sheath tube at positions before and after the heat exchanging tubes in accordance with necessity. CONSTITUTION:Condensed liquid 3g stops the lateral running thereof at the end of a condensed liquid dripping unit 5 and can be dripped at the end of the condensed liquid dripping unit 5. Since an upper sheath tube 3b is provided with projections or choked parts 6, the condensed liquid 3g dripped out of an upper heat transfer tube 3a can be guided into heat exchanging tubes 3e. Accordingly, the condensed liquid 3g produced by the upper heat transfer tubes 3a may be dripped uniformly into the heat exchanging tubes 3e while the production of ice 7 may be uniformized in accordance with the uniform dripping of the condensed liquid 3g.

Description

【発明の詳細な説明】 (産業上の利用分野〕 本発明はヒートパイプ式蓄熱水槽装置に関し、特に、上
部伝熱管から生じる凝縮液を複数の熱交換管に均一に滴
下させることにより熱交換性能を向上したヒートパイプ
式蓄熱水槽装置に関する。
[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a heat pipe type heat storage water tank device, and in particular, improves heat exchange performance by uniformly dripping condensate generated from an upper heat exchange tube onto a plurality of heat exchange tubes. This invention relates to a heat pipe type heat storage water tank device with improved properties.

(従来の技術〕 冷暖房用空調システムにおいて、水の潜熱あるいは顕熱
を利用する従来の蓄熱水槽装置として、例えば、ヒート
パイプ式蓄熱水槽装置があり、ヒートパイプの等温性に
より熱伝達の効率が大巾に改良されている。このシステ
ムは、第4図(a)に示すように、ヒートサイフオン式
熱交換器3は水中(図示せず)に沈設され、氷蓄熱時に
は上部に配設した鞘管3b中の伝熱管3aで冷媒を蒸発
させ、伝熱管3a表面を冷却し、鞘管3b中の作動液を
3gで示すように凝縮させ、凝縮した作動液を通ずる熱
交換管3eに接触する水を氷結させる。また、温水蓄熱
時には下部の作動液を通る鞘管中の伝熱管で冷媒を凝縮
させることにより鞘管中の作動液を蒸発させ、蒸発した
作動液を通す熱交換管3eに接触する水を加熱する。゛
このようにして、冷房用水蓄熱(潜熱利用)および暖房
用温水蓄熱(顕熱利用)が一つの蓄熱水槽のヒートサイ
フオン式熱交換器によって効率良く行われる。
(Prior art) In air conditioning systems for heating and cooling, there is a heat pipe type heat storage water tank device, for example, as a conventional heat storage water tank device that utilizes the latent heat or sensible heat of water. In this system, as shown in Figure 4(a), the heat siphon heat exchanger 3 is submerged in water (not shown), and during ice storage, a sheath placed on top The refrigerant is evaporated in the heat exchanger tube 3a in the tube 3b, the surface of the heat exchanger tube 3a is cooled, the working fluid in the sheath tube 3b is condensed as shown by 3g, and the condensed working fluid is brought into contact with the heat exchange tube 3e through which it passes. Freezes the water.Also, when storing hot water, the refrigerant is condensed in the heat transfer tube in the sheath tube that passes through the working fluid in the lower part, thereby evaporating the working fluid in the sheath tube. Heats the water it comes into contact with. In this way, cooling water heat storage (latent heat utilization) and heating hot water heat storage (sensible heat utilization) are efficiently performed by the heat siphon heat exchanger in one heat storage water tank.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかし、従来のヒートパイプ式蓄熱水槽装置によると、
冷媒側の蒸発条件の不均一、製作時の寸法誤差等が生じ
るため、複数の伝熱管3eを滴下する凝縮液3gの滴下
量が相違する(第4図(a))。また、第4図(b)に
示すように、自重によって伝熱管が傾斜すると、上部伝
熱管3aから生じる凝縮液3gの滴下位置および滴下量
が不均一なものとなり、各熱交換管3eへの液戻りに偏
りが生じるという不都合がある。従って、第5図に示す
ように、熱交換管3eの内面の一部がドライアウトし、
氷7が全く生成されない熱交換管3eが生じたり、氷7
の厚さが不均一となる。このため、システム全体の効率
を大幅に低下させることになる。
However, according to the conventional heat pipe type heat storage water tank device,
Due to non-uniform evaporation conditions on the refrigerant side, dimensional errors during manufacturing, etc., the amount of condensed liquid 3g dripped through the plurality of heat transfer tubes 3e is different (FIG. 4(a)). Moreover, as shown in FIG. 4(b), when the heat exchanger tubes are tilted due to their own weight, the dripping position and amount of the condensate 3g generated from the upper heat exchanger tubes 3a become uneven, and the amount of dripping to each heat exchanger tube 3e becomes uneven. There is a disadvantage that the liquid returns unevenly. Therefore, as shown in FIG. 5, a part of the inner surface of the heat exchange tube 3e dries out,
There may be heat exchange tubes 3e in which no ice 7 is generated, or ice 7
The thickness becomes uneven. This results in a significant reduction in the efficiency of the entire system.

従って、本発明の目的は上部伝熱管から住じる凝縮液を
複数の熱交換管へ均一に滴下させるようにしたヒートパ
イプ式蓄熱水槽装置を提供することである。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a heat pipe type heat storage water tank device in which condensed liquid from an upper heat exchanger tube is uniformly dripped into a plurality of heat exchange tubes.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は以上述べた目的を実現するため、上部伝熱管の
外面に未加工部もしくは不連続な突起等の凝縮液滴下部
を熱交換管の配設ピッチ以下の間隔で設け、必要に応じ
て上部鞘管の内面に突起部もしくは絞り部を熱交換管の
前後の位置に設けたヒートパイプ式蓄熱水槽装置を提供
する。
In order to achieve the above-mentioned object, the present invention provides condensate droplets such as unprocessed parts or discontinuous protrusions on the outer surface of the upper heat exchanger tube at intervals equal to or less than the arrangement pitch of the heat exchange tubes, and To provide a heat pipe type heat storage water tank device in which projections or constrictions are provided on the inner surface of an upper sheath tube at positions before and after a heat exchange tube.

即ち、本発明のヒートパイプ式蓄熱水槽装置は、蓄熱水
槽の水中に設けられて下部に作動液をプールすると共に
該作動液の蒸気を収容し、必要に応じて上部に突起もし
くは絞り部を有する密閉容器と、密閉容器の上部を貫通
して蒸気中を通され、かつ、外面に未加工部あるいは不
連続な突起等の凝縮液滴下部を所定のピッチで有する上
部伝熱管と、前記密閉容器の下部を貫通して前記作動液
中を通される下部伝熱管と、氷蓄熱時には前記上部伝熱
管に接続され、温水蓄熱時には前記下部伝熱管に接続さ
れる冷凍サイクル手段とを有する。前記密閉容器上部に
設けられた突起もしくは絞り部は前記上部伝熱管および
前記下部伝熱管の間に介在する複数の熱交換管の前後に
設けられており、前記上部伝熱管の外面に設けられた凝
縮液滴下部は前記熱交換管の配管ピッチ以下の間隔で設
けられている。この凝縮液滴下部は、上部伝熱管の表面
で生じた凝縮液が上部伝熱管の表面を横走りするのを防
止し、凝縮液の複数の熱交換管への滴下を均一にしてい
る。また、密閉容器上部に設けられた突起部もしくは絞
り部は、滴下した凝縮液を複数の熱交換管へ案内し、こ
れによって、より均一な複数の熱交換管への滴下を実現
している。このようなヒートパイプ式蓄熱水槽装置は、
氷蓄熱時には前記上部伝熱管へ0℃以下のブラインを流
すか、あるいは前記冷凍サイクル手段より前記上部伝熱
管・\冷媒を流してO′C以下で蒸発させる蒸発器を構
成し、温水蓄熱時には前記下部伝熱管へ所定の温度の熱
媒を流すか、あるいは前記冷凍サイクル手段より冷媒を
流して凝縮器を構成している。
That is, the heat pipe type heat storage water tank device of the present invention is provided underwater in the heat storage water tank, pools the working fluid in the lower part, accommodates the vapor of the working fluid, and has a protrusion or a constriction part in the upper part as necessary. a closed container, an upper heat exchanger tube that passes through the upper part of the closed container and passes through the steam, and has condensate droplets such as unprocessed parts or discontinuous protrusions on the outer surface at a predetermined pitch; and the closed container. and a refrigeration cycle means connected to the upper heat transfer tube during ice storage and to the lower heat transfer tube during hot water storage. The protrusion or constriction part provided on the upper part of the sealed container is provided before and after a plurality of heat exchange tubes interposed between the upper heat exchanger tube and the lower heat exchanger tube, and is provided on the outer surface of the upper heat exchanger tube. The condensate dripping portions are provided at intervals equal to or less than the piping pitch of the heat exchange tubes. This condensate dripping portion prevents the condensate generated on the surface of the upper heat exchanger tube from running sideways on the surface of the upper heat exchanger tube, and makes the condensate drip uniformly onto the plurality of heat exchange tubes. Furthermore, the protrusion or constriction provided at the top of the closed container guides the dripped condensate to the plurality of heat exchange tubes, thereby achieving more uniform dripping to the plurality of heat exchange tubes. This type of heat pipe type heat storage water tank device is
During ice storage, brine at a temperature of 0°C or lower is passed through the upper heat exchanger tube, or the refrigerant is passed through the upper heat exchanger tube from the refrigeration cycle means to evaporate at a temperature below O'C. A condenser is constructed by flowing a heat medium at a predetermined temperature into the lower heat transfer tube, or by flowing a refrigerant from the refrigeration cycle means.

〔実施例〕〔Example〕

以下、本発明のヒートパイプ式蓄熱水槽装置を詳細に説
明する。
Hereinafter, the heat pipe type heat storage water tank device of the present invention will be explained in detail.

第1図(a)、(b)および第2図は本発明の一実施例
を示し、伝熱用水2を満たした蓄熱水槽lと、蓄熱水槽
1の中に沈設されたヒートサイフオン式熱交換器3と、
コンプレッサ4a、熱交換器(氷蓄熱時にはコンデンサ
、温水蓄熱時にはエバポレータとして動作する)4b、
膨張弁4c、および配管4dより成る冷凍サイクル4か
ら構成される。
1(a), (b) and FIG. 2 show an embodiment of the present invention, in which a heat storage water tank l filled with heat transfer water 2 and a heat siphon type heat sink submerged in the heat storage water tank 1 are shown. exchanger 3,
Compressor 4a, heat exchanger (operates as a condenser during ice storage and as an evaporator during hot water storage) 4b,
It is composed of a refrigeration cycle 4 consisting of an expansion valve 4c and piping 4d.

第1図ら)の断面図に示すように、ヒートサイフオン式
熱交換器3は、上部伝熱管3aを内部に有する上部鞘管
3bと、下部伝熱管3Cを内部に有する下部鞘管3dと
、上部鞘管3bおよび下部鞘管3dを連結する複数の熱
交換管3eから成る一つの密閉空間を構成しており、該
密閉空間にはフロン等の作動液3f(液体および蒸気)
が封入されている。また、第3図において後述するが、
上部伝熱管3aの外面には未加工部もしくは不連続な突
起等の凝縮液滴下部が複数の熱交換管3eの配設ピッチ
以下に定間隔に多数設けられており、また、上部鞘管3
bの内面には必要に応じて突起もしくは絞り部が複数の
熱交換管3eの前後に設けられている。
As shown in the cross-sectional view of FIG. 1 et al., the heat siphon heat exchanger 3 includes an upper sheath tube 3b having an upper heat exchanger tube 3a therein, a lower sheath tube 3d having a lower heat exchanger tube 3C therein, A plurality of heat exchange tubes 3e connecting the upper sheath tube 3b and the lower sheath tube 3d form one sealed space, and a working fluid 3f (liquid and vapor) such as fluorocarbon is contained in the sealed space.
is included. Also, as will be described later in FIG. 3,
On the outer surface of the upper heat exchanger tube 3a, a large number of condensate droplets such as unprocessed parts or discontinuous protrusions are provided at regular intervals below the arrangement pitch of the plurality of heat exchange tubes 3e.
Projections or constricted portions are provided on the inner surface of b as required before and behind the plurality of heat exchange tubes 3e.

第3図はヒートサイフオン式熱交換器および上部伝熱管
3aから生じる凝縮液3gの滴下状態を示し、伝熱用水
2内に沈設されたヒートサイフオン式熱交換器3の上部
伝熱管3aの外面は未加工部もしくは不連続な突起等の
凝縮液滴下部5が形成されており、複数の熱交換管3e
の配設ピッ千P以下の間隔で多数設けられている。また
、上部鞘管3bの内面には突起部もしくは絞り部6が複
数の熱交換管3eの前後付近に設けられている。このよ
うに上部伝熱管3aの外面に凝縮液滴下部5が設けられ
ているため、ヒートサイフオン式熱交換器3が傾いた場
合でも凝縮液3gの横走りを防ぐことができる。即ち、
凝縮液3gは凝縮液滴下部5の端で凝縮液3gの横走り
を止め、その位置で滴下させることができる。また、上
部鞘管3bに突起部もしくは絞り部6が設けられている
ため、上部伝熱管3aから滴下した凝縮液3gを熱交換
管3eに案内することができる。このため、上部伝熱管
3aから生じる凝縮液3gを熱交換管3eへ均一に滴下
させることができ、それに伴って氷7の生成を均一にす
ることができる。
FIG. 3 shows the dripping state of 3 g of condensate generated from the heat siphon type heat exchanger and the upper heat exchanger tube 3a, and shows the dripping state of 3 g of condensate generated from the heat siphon type heat exchanger 3 and the upper heat exchanger tube 3a of the heat siphon type heat exchanger 3 submerged in the heat transfer water 2. The outer surface is formed with a condensate dripping part 5 such as an unprocessed part or a discontinuous protrusion, and a plurality of heat exchange tubes 3e.
A large number of them are provided at intervals of 1,000 P or less. Further, on the inner surface of the upper sheath tube 3b, protrusions or constricted portions 6 are provided near the front and back of the plurality of heat exchange tubes 3e. Since the condensate dripping portion 5 is provided on the outer surface of the upper heat transfer tube 3a in this manner, even if the heat siphon heat exchanger 3 is tilted, it is possible to prevent the condensate 3g from running sideways. That is,
The condensed liquid 3g can stop running horizontally at the end of the condensed liquid dripping part 5, and be allowed to drip at that position. Moreover, since the upper sheath tube 3b is provided with the protrusion or constriction portion 6, the condensed liquid 3g dripping from the upper heat exchanger tube 3a can be guided to the heat exchange tube 3e. Therefore, the condensed liquid 3g generated from the upper heat exchanger tube 3a can be uniformly dropped into the heat exchange tube 3e, and accordingly, the ice 7 can be generated uniformly.

以上の構成において、■氷蓄熱時の動作、■温水蓄熱時
の動作をそれぞれ第1図(a)、(b)、第2図および
第3図を用いて説明する。
In the above configuration, (1) operation during ice heat storage and (2) operation during hot water heat storage will be explained using FIGS. 1(a) and (b), FIGS. 2 and 3, respectively.

■氷蓄熱時の動作 氷蓄熱時において、コンプレッサ4a、熱交換器4b(
この場合、コンデンサとして動作する)、膨張弁4c、
および配管4dから成る冷凍サイクル4は、第1図(a
)に示すように配管され、ヒートサイフオン式熱交換器
3の上部伝熱管3aと連結される。このとき、上部伝熱
管3aは冷凍サイクル4のエバポレータとして動作する
。一方、下部伝熱管3cは図示していない閉鎖手段によ
って閉鎖され、冷凍サイクル4から切り離されている。
■Operation during ice heat storage During ice heat storage, compressor 4a, heat exchanger 4b (
In this case, it operates as a condenser), an expansion valve 4c,
The refrigeration cycle 4 consisting of the piping 4d is shown in FIG.
), and is connected to the upper heat transfer tube 3a of the heat siphon heat exchanger 3. At this time, the upper heat exchanger tube 3a operates as an evaporator of the refrigeration cycle 4. On the other hand, the lower heat exchanger tube 3c is closed by a closing means (not shown) and separated from the refrigeration cycle 4.

この状態で、冷凍サイクル4のコンプレッサ4aで圧縮
された高温になった冷媒ガスが熱交換器4bに導かれ、
ここで大気と接して放熱冷却されて凝縮される。この凝
縮した冷媒ガスは膨張弁4cを介してヒートサイフオン
式熱交換器3の上部伝熱管3aに送り込まれる。
In this state, the high temperature refrigerant gas compressed by the compressor 4a of the refrigeration cycle 4 is guided to the heat exchanger 4b,
Here, it comes into contact with the atmosphere and is cooled and condensed. This condensed refrigerant gas is sent to the upper heat transfer tube 3a of the heat siphon heat exchanger 3 via the expansion valve 4c.

このとき、上部伝熱管3aはエバポレータとして作用し
、冷媒ガスは上部伝熱管3aの表面から気化熱を奪って
蒸発する。一方、水2の有する熱で蒸発した作動液3「
は上部伝熱管3aおよび上部鞘管3bの周囲で熱交換を
行い凝縮する。このとき、第3図に示すように凝縮液3
gは上部伝熱管3a外面に設けられた凝縮液滴下部5の
端で横走りが防止されて滴下し、かつ、上部鞘管3bの
内面に設けられた突起部もしくは絞り部6によって複数
の熱交換管3eに案内される。このため、凝縮液3gは
複数の熱交換管3eへ均一に滴下する。このとき、熱交
換管3eの周囲の水が冷却されて氷7を生成する。この
場合、凝縮液3gが複数の熱交換管3eに均等に液戻り
するため、各熱交換管3eの氷7の生成、即ち、生成す
る氷厚が均一となり、ヒートサイフオン式熱交換器3に
おける熱交換が効率よく行われる。
At this time, the upper heat exchanger tube 3a acts as an evaporator, and the refrigerant gas takes vaporization heat from the surface of the upper heat exchanger tube 3a and evaporates. On the other hand, the working fluid 3 evaporated due to the heat of water 2.
is condensed through heat exchange around the upper heat exchanger tube 3a and upper sheath tube 3b. At this time, as shown in Fig. 3, the condensate 3
The condensate drips at the end of the condensate dripping part 5 provided on the outer surface of the upper heat exchanger tube 3a, and is prevented from running sideways, and the condensate drips at the end of the condensate dripping portion 5 provided on the outer surface of the upper heat exchanger tube 3a, and is heated by a projection or constriction portion 6 provided on the inner surface of the upper sheath tube 3b. It is guided to the exchange tube 3e. Therefore, the condensed liquid 3g drops uniformly into the plurality of heat exchange tubes 3e. At this time, water around the heat exchange tube 3e is cooled and ice 7 is generated. In this case, since the condensed liquid 3g returns evenly to the plurality of heat exchange tubes 3e, the generation of ice 7 in each heat exchange tube 3e, that is, the thickness of the generated ice becomes uniform, and the heat siphon type heat exchanger 3 heat exchange is performed efficiently.

■温水蓄熱時の動作 温水蓄熱時において、コンプレッサ4a。■Operation during hot water heat storage During hot water heat storage, the compressor 4a.

熱交換器4b(この場合、エバポレータとして動作する
)、膨張弁4C1および配管4dから成る冷凍サイクル
4は、第2図に示すように配管され、ヒートサイフオン
式熱交換器3の下部伝熱管3cと連結される。このとき
、下部伝熱管3cは冷凍サイクル4のコンデンサとして
動作する。一方、上部伝熱管3aは図示していない閉鎖
手段によって閉鎖され、冷凍サイクル4から切り離され
ている。この状態で、冷凍サイクル4より供給された冷
媒が下部伝熱管3C内で凝縮し、該凝縮によって作動液
3rが蒸発し熱交換管3Cを介して水2で冷却されて凝
縮する。換言すれば、熱交換管3eを介して水2が加熱
される。このとき、熱交換管3eの下方に下部伝熱管3
C(熱供給源)が位置するため、ボトムヒートモードと
なりヒートサイフオン式熱交換器3における熱交換が効
率よく行われる。
The refrigeration cycle 4, which consists of a heat exchanger 4b (in this case, operates as an evaporator), an expansion valve 4C1, and piping 4d, is piped as shown in FIG. is connected with. At this time, the lower heat exchanger tube 3c operates as a condenser of the refrigeration cycle 4. On the other hand, the upper heat exchanger tube 3a is closed by a closing means (not shown) and separated from the refrigeration cycle 4. In this state, the refrigerant supplied from the refrigeration cycle 4 condenses in the lower heat exchanger tube 3C, and the condensation causes the working fluid 3r to evaporate, and is cooled by water 2 through the heat exchange tube 3C and condensed. In other words, the water 2 is heated via the heat exchange tube 3e. At this time, the lower heat exchanger tube 3 is placed below the heat exchanger tube 3e.
Since C (heat supply source) is located, the bottom heat mode is set and heat exchange in the heat siphon type heat exchanger 3 is performed efficiently.

本実施例においては、冷凍サイクル4をコンプレッサ4
a、熱交換管4b、膨張弁4c、および配管4dより構
成したが、同様の機能を果たすものであれば特に限定す
るものではない、また、冷凍す・イクル4による冷媒の
供給に換えて所定の温度にしたブライン等を流すように
しても良い、氷蓄熱時および温水蓄熱時の配管切換は適
当な手段を設けることにより簡単に行うことができる。
In this embodiment, the refrigeration cycle 4 is connected to the compressor 4.
a, a heat exchange pipe 4b, an expansion valve 4c, and a pipe 4d, but there is no particular limitation as long as it performs the same function. It may be possible to flow brine or the like at a temperature of 200 to 3000. Piping switching during ice heat storage and hot water heat storage can be easily performed by providing appropriate means.

ヒートサイフオン式熱交換器3は蓄熱水槽1の大きさに
応じて複数個直列あるいは並列に使用しても良く、上・
下部伝熱管3a、3cが水平となる状態で全体を傾斜さ
せて使用しても良い。
A plurality of heat siphon heat exchangers 3 may be used in series or in parallel depending on the size of the heat storage water tank 1.
It is also possible to use the lower heat exchanger tubes 3a, 3c in a horizontal state, with the entire structure tilted.

上部伝熱管3aおよび下部伝熱管3cは何れも外面で作
動液3f−t−凝縮あるいは蒸発させるものであり、高
性能伝熱面加工を施すことにより一層の効果を期待でき
る。
Both the upper heat exchanger tube 3a and the lower heat exchanger tube 3c condense or evaporate the working fluid 3f-t on their outer surfaces, and further effects can be expected by applying high-performance heat transfer surface processing.

〔発明の効果] 以上説明した通り、本発明のヒートパイプ式蓄熱水槽装
置によると、上部伝熱管の外面に未加工部もしくは不連
続な突起等の凝縮液滴下部を熱交換管の配管ピッチ以下
の間隔で設け、必要に応じて上部鞘管の内面に突起部も
しくは絞り部を熱交換管前後の位置に設けたため、上部
伝熱管から住しる′a凝縮液複数の熱交換管へ均一に滴
下することができ、各熱交換管の性能差が減少され、ヒ
ートサイフオン式熱交換器全体の性能を向上することが
できる。
[Effects of the Invention] As explained above, according to the heat pipe type heat storage water tank device of the present invention, the condensate dripping portion, such as unprocessed parts or discontinuous protrusions, on the outer surface of the upper heat exchanger tube is set to be smaller than the piping pitch of the heat exchanger tube. , and if necessary, protrusions or constrictions were provided on the inner surface of the upper sheath tube at the front and rear positions of the heat exchange tubes, so that the condensate from the upper heat exchanger tube can be distributed uniformly to the multiple heat exchange tubes. The performance difference between each heat exchange tube can be reduced, and the performance of the entire heat siphon heat exchanger can be improved.

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

第1図(a)は本発明の一実施例の氷蓄熱時の状態を示
す説明図、第1図(t))は第1図(a)の断面図、第
2図は本発明の温水蓄熱時の状態を示す説明図、第3図
は本発明の上部伝熱管から生じる凝縮液の滴下状態を示
す説明図、第4図(a)、[有])は従来のと一トサイ
フォン式熱交換器の上部伝熱管を示す説明図、第5図は
従来のヒートサイフオン式熱交換器を示す説明図。 符号の説明 1・・−−一一−−−−−蓄熱水槽   2−一−−−
−・・水3・・・・−・、・、ヒートサイフオン式熱交
換器3a・・−・−・−・−上部伝熱管 3b・・・・
−・・上部鞘管3C−・−−m−・−下部伝熱管 3d
・・−m−−−・・・−下部鞘管3e−・−−−m−・
−熱交換管  3f・・−−−−一一一・・作動液3g
・・−・・・・・−・・凝縮液 4−・−一一一一・・冷凍サイクル 4 a−−−・−コンプレッサ 4b−・−・・・・・・熱交換器  4 c −−−一
・−膨張弁4d−・−m−−・・・・配管 5・−・−・・−・・−凝縮液滴下部 6−−−−一突起部もしくは絞り部 7−・・−−−−−一氷
FIG. 1(a) is an explanatory diagram showing the state during ice heat storage according to an embodiment of the present invention, FIG. 1(t)) is a sectional view of FIG. 1(a), and FIG. An explanatory diagram showing the state during heat storage, Fig. 3 is an explanatory diagram showing the dripping state of condensate generated from the upper heat exchanger tube of the present invention, and Fig. 4 (a) [Yes]) is an explanatory diagram showing the state of condensate dripping from the upper heat transfer tube of the present invention. FIG. 5 is an explanatory diagram showing an upper heat exchanger tube of a heat exchanger, and FIG. 5 is an explanatory diagram showing a conventional heat siphon type heat exchanger. Explanation of symbols 1...---11---- Heat storage water tank 2-1---
-・・Water 3・・・・・・Heat siphon type heat exchanger 3a・・・−・−・・Upper heat transfer tube 3b・・・
--- Upper sheath tube 3C----m---Lower heat exchanger tube 3d
・・−m−−−・−Lower sheath tube 3e−・−−m−・
-Heat exchange tube 3f...---111...3g of working fluid
・・−・・・・・−・・凝縮液4−・−一一一一・・冷凍サイクル4 a−−−・−コンプレッサ4b−・−・・・・・・熱交換器 4 c −− -1.-Expansion valve 4d--m--Piping 5--Condensate dripping part 6--Protrusion or constriction part 7-- ---One ice

Claims (2)

【特許請求の範囲】[Claims] (1)蓄熱水槽内の水の顕熱および/あるいは潜熱を利
用する蓄熱水槽装置において、 前記蓄熱水槽の水中に設けられて下部に作 動液をプールするとともに上部にその蒸気を収容し、必
要に応じて前記上部内面に突起もしくは絞り部を有する
密閉容器と、 前記密閉容器の上部を貫通して前記蒸気中 を通され、かつ、外面に未加工部あるいは不連続な突起
等の凝縮液滴下部を所定のピッチで有する上部伝熱管と
、 前記密閉容器の下部を貫通して前記作動液 中を通される下部伝熱管と、 氷蓄熱時には前記上部伝熱管に接続され、 温水蓄熱時には前記下部伝熱管に接続される冷凍サイク
ル手段を備え、 氷蓄熱時には前記上部伝熱管へ0℃以下の ブラインを流すか、あるいは前記冷凍サイクル手段より
前記上部伝熱管へ冷媒を流して0℃以下で蒸発させる蒸
発器を構成し、 温水蓄熱時には前記下部伝熱管へ所定の温 度の熱媒を流すか、あるいは前記冷凍サイクル手段より
冷媒を流して凝縮器を構成することを特徴とするヒート
パイプ式蓄熱水槽装置。
(1) In a heat storage water tank device that utilizes sensible heat and/or latent heat of water in a heat storage water tank, a heat storage tank is provided in the water of the heat storage tank, pools the working fluid in the lower part, and stores the steam in the upper part, and as needed. A closed container having a protrusion or a constriction on the inner surface of the upper part according to the requirements; and a condensate dripping part that passes through the upper part of the closed container and passes through the steam, and has an unprocessed part or discontinuous protrusions on the outer surface. an upper heat exchanger tube having a predetermined pitch at a predetermined pitch; a lower heat exchanger tube that penetrates the lower part of the closed container and passes through the working fluid; a lower heat exchanger tube that is connected to the upper heat exchanger tube during ice heat storage and is connected to the lower heat transfer tube during hot water heat storage; A refrigeration cycle means connected to the heat tube is provided, and during ice storage, brine at a temperature of 0°C or lower is flowed into the upper heat exchanger tube, or a refrigerant is flowed from the refrigeration cycle means to the upper heat exchanger tube to evaporate at a temperature of 0°C or lower. A heat pipe type heat storage water tank device, characterized in that when storing hot water, a heat medium at a predetermined temperature is passed through the lower heat transfer tube, or a refrigerant is flowed from the refrigeration cycle means to form a condenser.
(2)前記未加工部もしくは不連続な突起等の凝縮液滴
下部は、前記熱交換管の配設ピッチ以下の間隔で設けら
れている請求項第1項記載のヒートパイプ式蓄熱水槽装
置。 (2)前記密閉容器の上部内面に設けられた突起もしく
は絞り部は、前記上部伝熱管および前記下部伝熱管の間
に介在する複数の熱交換管の前後に設けられ、 前記上部伝熱管から滴下した凝縮液を前記 熱交換管に案内する請求項第1項記載のヒートパイプ式
蓄熱水槽装置。
(2) The heat pipe type heat storage water tank device according to claim 1, wherein the condensate dripping portions such as unprocessed portions or discontinuous projections are provided at intervals equal to or less than an arrangement pitch of the heat exchange tubes. (2) The protrusion or constriction provided on the inner surface of the upper part of the sealed container is provided before and after the plurality of heat exchange tubes interposed between the upper heat exchanger tube and the lower heat exchanger tube, and drips from the upper heat exchanger tube. The heat pipe type heat storage water tank device according to claim 1, wherein the condensed liquid is guided to the heat exchange tube.
JP11569688A 1988-05-12 1988-05-12 Heat pipe type heat storage water tank device Expired - Fee Related JPH0726748B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11569688A JPH0726748B2 (en) 1988-05-12 1988-05-12 Heat pipe type heat storage water tank device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11569688A JPH0726748B2 (en) 1988-05-12 1988-05-12 Heat pipe type heat storage water tank device

Publications (2)

Publication Number Publication Date
JPH01285726A true JPH01285726A (en) 1989-11-16
JPH0726748B2 JPH0726748B2 (en) 1995-03-29

Family

ID=14668976

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11569688A Expired - Fee Related JPH0726748B2 (en) 1988-05-12 1988-05-12 Heat pipe type heat storage water tank device

Country Status (1)

Country Link
JP (1) JPH0726748B2 (en)

Also Published As

Publication number Publication date
JPH0726748B2 (en) 1995-03-29

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