JPH08152162A - Internal melting type ice storage tank - Google Patents

Internal melting type ice storage tank

Info

Publication number
JPH08152162A
JPH08152162A JP6319178A JP31917894A JPH08152162A JP H08152162 A JPH08152162 A JP H08152162A JP 6319178 A JP6319178 A JP 6319178A JP 31917894 A JP31917894 A JP 31917894A JP H08152162 A JPH08152162 A JP H08152162A
Authority
JP
Japan
Prior art keywords
ice
heat transfer
transfer tube
water
heat
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
Application number
JP6319178A
Other languages
Japanese (ja)
Inventor
Akihiko Ogawa
彰彦 小川
Senji Niwa
宣治 丹羽
Seiichi Nakanishi
誠一 中西
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP6319178A priority Critical patent/JPH08152162A/en
Publication of JPH08152162A publication Critical patent/JPH08152162A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

Landscapes

  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Abstract

(57)【要約】 【目的】 氷蓄熱取り出し速度等の改善及び氷量の簡易
な計測を可能とした内融式氷蓄熱槽の提供を目的とす
る。 【構成】 水槽7と、水槽7内に浸漬した蓄熱氷形成用
の伝熱管8と、伝熱管8を水槽7内に支持する支持部材
9とを備え、熱伝達媒体を冷凍機又はヒートポンプの蒸
発機6と伝熱管8との間で循環させ、冷凍機又はヒート
ポンプの蒸発機6での熱交換により温度降下した熱伝達
媒体と、水槽7内の水15との熱交換により、伝熱管8
の外周部に氷を形成する内融式氷蓄熱槽2において、支
持部材9を金属製とし、伝熱管8に対し所定の間隔で設
け、伝熱管8の下方に空気を吐出する散気管18と、散
気管18に空気を送るブロア19を備えるものである。
(57) [Summary] [Purpose] The objective is to provide an internal melting type ice heat storage tank that enables improvement of the ice heat extraction rate and simple measurement of ice quantity. A water tank 7, a heat transfer tube 8 for forming heat storage ice immersed in the water tank 7, and a support member 9 for supporting the heat transfer tube 8 in the water tank 7 are provided, and a heat transfer medium is evaporated by a refrigerator or a heat pump. The heat transfer medium is circulated between the machine 6 and the heat transfer tube 8, and the heat transfer medium whose temperature has dropped due to heat exchange in the evaporator 6 of the refrigerator or heat pump and the water 15 in the water tank 7 are exchanged.
In the internal melting type ice heat storage tank 2 that forms ice on the outer peripheral portion of the support member 9, the support member 9 is made of metal, is provided at a predetermined interval with respect to the heat transfer tube 8, and is provided with an air diffuser tube 18 that discharges air below the heat transfer tube 8. A blower 19 for sending air to the air diffuser 18 is provided.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、冷凍機及びヒートポン
プに付設される内融式氷蓄熱槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an internal melting type ice heat storage tank attached to a refrigerator and a heat pump.

【0002】[0002]

【従来の技術】近年、ビルの空調や地域冷房などの空調
装置において、深夜電力の有効利用による運転費用の低
減や、深夜と昼間の消費電力の平準化、さらに空調装置
に関する初期投資額の削減等を目的として氷蓄熱槽が付
設されることが多くなりつつある。
2. Description of the Related Art In recent years, in air conditioners for building air conditioning and district cooling, operating costs are reduced by effective use of late-night power, power consumption is leveled during midnight and daytime, and initial investment in air conditioners is reduced. Ice storage tanks are increasingly being installed for the purpose of such as.

【0003】氷蓄熱槽を備えた従来の空調装置につい
て、図9を参照しつつ説明する。図9は従来公知の空調
装置の一つを示す概略構成図であり、冷凍機101及び
氷蓄熱槽102からなる。冷凍機101は、圧縮機10
3、凝縮機104、膨張弁105、及び蒸発機106に
より閉ループが形成され、冷媒がこの閉ループで冷凍サ
イクルを行いながら循環している。また、氷蓄熱槽10
2は、水槽107と、蓄熱氷形成用の伝熱管108と、
この伝熱管108を前記水槽107内に支持する支持体
109とが備えられている。かかる伝熱管8は、図9に
示すように前記水槽107内でU字形の湾曲と直線部分
とを交互に繰り返すことにより、水槽7に浸漬できる伝
熱管8を長くし、伝熱面積を可能な限り大きくする構造
が取られている。また伝熱管108は、蒸発機106、
ポンプ112に連結される管路110、111に接続さ
れ閉ループが形成されている。かかる閉ループには、液
相状態を保つようにエチレングリコール等を主成分とす
るブラインが還流可能に充填されている。また、前記管
路111に設けられた切換弁113により、伝熱管10
8と蒸発機106との間の管路111aを通る循環に代
えて、管路111bを経て、熱交換器114を通り管路
111に戻る循環に切換え可能に構成されている。
A conventional air conditioner having an ice heat storage tank will be described with reference to FIG. FIG. 9 is a schematic configuration diagram showing one of conventionally known air conditioners, which includes a refrigerator 101 and an ice heat storage tank 102. The refrigerator 101 is the compressor 10
3, the condenser 104, the expansion valve 105, and the evaporator 106 form a closed loop, and the refrigerant circulates while performing a refrigeration cycle in this closed loop. In addition, the ice heat storage tank 10
2 is a water tank 107, a heat transfer tube 108 for forming heat storage ice,
A support 109 for supporting the heat transfer tube 108 in the water tank 107 is provided. As shown in FIG. 9, the heat transfer tube 8 is formed by alternately repeating a U-shaped curve and a straight line portion in the water tank 107 to elongate the heat transfer tube 8 that can be immersed in the water tank 7, thereby enabling a heat transfer area. The structure is made to be as large as possible. In addition, the heat transfer tube 108 includes the evaporator 106,
A closed loop is formed by being connected to the pipelines 110 and 111 connected to the pump 112. In such a closed loop, brine containing ethylene glycol or the like as a main component is reflowably filled so as to maintain a liquid state. In addition, the heat transfer pipe 10 is provided by the switching valve 113 provided in the pipe line 111.
8 and the evaporator 106, instead of the circulation through the pipeline 111a, the circulation through the pipeline 111b, the heat exchanger 114 and the return to the pipeline 111 can be switched.

【0004】前記氷蓄熱槽102に冷熱を蓄積する場合
は、前記切換弁113により管路111aを通る循環に
する。ここで前記冷凍機101の冷媒が循環し冷凍サイ
クルを行い、蒸発器106において冷媒が蒸発し蒸発熱
を奪うことから、冷媒と熱交換するブラインは奪熱され
る。この蒸発機106で冷却されたブラインは、ポンプ
112により管路110を経て伝熱管108に導かれ、
ここで水槽107内の水との間で熱交換させ、その後管
路111及び管路111aを経て蒸発機106に戻され
る。かかる閉ループでブラインが循環することで、伝熱
管108の外周部に氷が形成される。
When cold energy is stored in the ice heat storage tank 102, the switching valve 113 is used to circulate through the pipe 111a. Here, the refrigerant of the refrigerator 101 circulates to perform a refrigerating cycle, and the refrigerant evaporates in the evaporator 106 to take heat of evaporation, so that the brine that exchanges heat with the refrigerant is taken away. The brine cooled by the evaporator 106 is guided by the pump 112 to the heat transfer tube 108 via the conduit 110,
Here, heat is exchanged with the water in the water tank 107, and then it is returned to the evaporator 106 via the pipe line 111 and the pipe line 111a. By circulating the brine in such a closed loop, ice is formed on the outer peripheral portion of the heat transfer tube 108.

【0005】一方、前記氷蓄熱槽102から冷熱を取り
出す場合、冷凍機101の運転を中止し、切換弁113
を切換え、管路111bを通る循環にする。これにより
伝熱管108の外周部の氷が融解する際に周囲から奪う
大きな融解熱を利用し、伝熱管108を流動するブライ
ンを冷却し、冷却されたブラインを管路111bを介し
熱交換器114に流動させる。この熱交換器114によ
り冷房が可能になる。つまり、深夜電力を使って氷の形
成を行い、冷熱を蓄積し、昼間はこの氷蓄熱を利用して
冷房を行うことにより、電力消費量の昼夜間での平準化
を図ることができる。
On the other hand, when the cold heat is taken out from the ice heat storage tank 102, the operation of the refrigerator 101 is stopped and the switching valve 113 is used.
To switch to the circulation through the pipeline 111b. As a result, the large amount of heat of melting taken from the surroundings when the ice on the outer periphery of the heat transfer tube 108 is melted is used to cool the brine flowing through the heat transfer tube 108, and the cooled brine is passed through the pipe 111b to the heat exchanger 114. Fluidize. This heat exchanger 114 enables cooling. In other words, by forming ice using midnight power, accumulating cold heat, and using this ice heat storage for cooling during the daytime, the power consumption can be leveled during the day and night.

【0006】以上で説明した氷蓄熱槽102、つまり氷
蓄熱利用時に伝熱管108にブラインを流動させて、伝
熱管108の内側から間接的に伝熱管108の外周部の
氷を融解させる氷蓄熱槽102は、一般的に内融式と定
義されるものである。上述の内融式氷蓄熱槽102に水
を循環させる装置を設けた従来技術として特開平6−1
1158号がある。
[0006] The ice heat storage tank 102 described above, that is, the ice heat storage tank that causes the brine to flow through the heat transfer tube 108 when the ice heat is used to indirectly melt the ice on the outer peripheral portion of the heat transfer tube 108 from the inside of the heat transfer tube 108. 102 is generally defined as an internal fusion type. As a prior art in which a device for circulating water is provided in the above-mentioned internal melting type ice heat storage tank 102, Japanese Patent Laid-Open No. 6-1
There is No. 1158.

【0007】[0007]

【発明が解決しようとする課題】以上で紹介した、冷凍
機101等に付設された従来の内融式氷蓄熱槽102に
は、次に示すような不都合がある。
The conventional internal melting type ice heat storage tank 102 attached to the refrigerator 101 and the like introduced above has the following inconveniences.

【0008】図10に示すように、内融式氷蓄熱槽10
2では、伝熱管108内にブラインを流動させて氷11
5aを融解させるため、氷115aは伝熱管8の周囲か
ら融解し円筒状になる。この円筒状の氷115aと伝熱
管108の間に水115bが略密閉状態で滞留するた
め、伝熱管108と氷115aとは、周囲の水115b
の自然対流でしか熱伝達されないこととなる。このため
毎時間当たりの熱伝達量が比較的小さく、氷蓄熱の取り
出し速度及び温度に制約が生じる。これは自然対流では
強制対流に比較し温度境界層が厚くなり熱伝達率が小さ
くなることからである。さらに、氷115aの外周部の
水115はほとんど静止し、伝熱管108と氷115a
との間に存する水115bと対流し混合することがほと
んどないことも、氷蓄熱の取り出し速度及び温度に制約
を与える要因になっている。なお従来技術の特開平6−
11158号のごとく、氷蓄熱槽102内の水115を
循環させても、伝熱管108と氷115aとの間に略密
閉状態で存する水115bをほとんど循環させることが
できないので、伝熱管108と氷115aとの熱伝達率
を増大させる効果は小さい。
As shown in FIG. 10, an internal melting type ice heat storage tank 10
In No. 2, the brine is caused to flow in the heat transfer tube 108 so that the ice 11
In order to melt 5a, the ice 115a is melted from the periphery of the heat transfer tube 8 into a cylindrical shape. Since water 115b stays between the cylindrical ice 115a and the heat transfer tube 108 in a substantially sealed state, the heat transfer tube 108 and the ice 115a are different from each other in the surrounding water 115b.
The heat will be transferred only by natural convection. For this reason, the amount of heat transfer per hour is relatively small, and the extraction speed and temperature of the ice heat storage are restricted. This is because in natural convection, the thermal boundary layer becomes thicker and the heat transfer coefficient becomes smaller than in forced convection. Further, the water 115 around the outer periphery of the ice 115a is almost stationary, and the heat transfer tube 108 and the ice 115a
The fact that there is almost no convection and mixing with the water 115b that exists between the ice and water is also a factor that limits the extraction rate and temperature of the ice heat storage. It should be noted that the prior art of JP-A-6-
As in No. 11158, even if the water 115 in the ice heat storage tank 102 is circulated, almost no water 115b existing in a substantially sealed state can be circulated between the heat transfer tube 108 and the ice 115a. The effect of increasing the heat transfer coefficient with 115a is small.

【0009】また、水115と氷115aとの比体積の
違いから、氷蓄熱槽102内の水位の変化を計測すれば
氷115aの量がわかるが、上述の従来技術の場合、伝
熱管108と氷115aとの間に存する水115bが略
密閉状態で、氷115aの外部の水115と自由に流動
していないことから、氷115aが伝熱管108の周囲
から融解しても、氷115aの内部に気泡が発生し、氷
115aの量の変化が水位の変化に直接現れない。この
ため簡易に測定できる水位の変化により、氷量を計算す
ることが困難となる。
Also, the amount of ice 115a can be known by measuring the change in the water level in the ice heat storage tank 102 from the difference in the specific volume between the water 115 and ice 115a. Since the water 115b existing between the ice 115a and the ice 115a is substantially sealed and does not flow freely with the water 115 outside the ice 115a, even if the ice 115a melts from the periphery of the heat transfer tube 108, the inside of the ice 115a Bubbles are generated in the water, and the change in the amount of ice 115a does not directly appear in the change in the water level. For this reason, it becomes difficult to calculate the amount of ice due to changes in the water level that can be easily measured.

【0010】ところで、上述の内融式の氷蓄熱槽102
以外に外融式のものがある。これは図9において、切換
弁113及び管路111bの代わりに、氷蓄熱槽102
の水槽107に2本の管路X、Y(図9において仮想線
で示す)を開口し、伝熱管108の周囲に形成された氷
115aの外部の水115を循環させることにより、氷
115aを融解させ氷蓄熱を取り出すものである。かか
る外融式氷蓄熱槽によれば、伝熱管108の外周部の氷
115aを直接水槽107内の水115で融解させるこ
とから、上述の不都合、つまり融解した水115b(図
10参照)が密閉されていることから生じる氷蓄熱取り
出し速度の制約等の不都合は発生しないが、図11に示
すように、製氷時伝熱管108の外周部に形成される氷
115a同志がつながる、いわゆるブリッジング現象が
生じて、水115が流動しないゾーン115cが発生す
る。このためこのゾーン115cでは、水槽107内の
水115を熱交換させつつ循環させても、水115の融
解が起こらず、氷蓄熱取り出し速度に著しい制約を受け
る。また、かかるブリッジング現象を発生させないため
には、氷蓄熱槽102内の水115を氷115aに相転
移させる割合である氷充填率(IPF)が制限され、氷
蓄熱容量が小さくなる。かかる観点から、内融式氷蓄熱
槽102において、上述の不都合を解決したい。
By the way, the above-mentioned internal melting type ice heat storage tank 102 is used.
There is also an external fusion type. In FIG. 9, instead of the switching valve 113 and the pipe line 111b, the ice heat storage tank 102 is shown.
The two water pipes X and Y (shown by phantom lines in FIG. 9) are opened in the water tank 107, and the water 115 outside the ice 115 a formed around the heat transfer tube 108 is circulated to thereby remove the ice 115 a. It melts and takes out ice heat. According to this external melting type ice heat storage tank, since the ice 115a on the outer peripheral portion of the heat transfer tube 108 is directly melted by the water 115 in the water tank 107, the above-mentioned disadvantage, that is, the melted water 115b (see FIG. 10) is sealed. Although there is no inconvenience such as the restriction of the ice heat extraction rate resulting from the above, the so-called bridging phenomenon in which the ice 115a formed on the outer peripheral portion of the heat transfer tube 108 during ice making is connected as shown in FIG. As a result, a zone 115c where the water 115 does not flow is generated. Therefore, in this zone 115c, even if the water 115 in the water tank 107 is circulated while exchanging heat, the water 115 does not melt, and the ice heat extraction rate is significantly restricted. Further, in order to prevent the bridging phenomenon from occurring, the ice filling rate (IPF), which is the rate at which the water 115 in the ice heat storage tank 102 undergoes the phase transition to the ice 115a, is limited, and the ice heat storage capacity becomes small. From this point of view, in the internal melting type ice heat storage tank 102, it is desired to solve the above-mentioned inconvenience.

【0011】本発明は上述の従来の不都合を解決するた
めになされたもので、氷蓄熱取り出し速度等の改善及び
氷量の簡易な計測を可能とした内融式氷蓄熱槽の提供を
目的とする。
The present invention has been made to solve the above-mentioned conventional inconvenience, and an object of the present invention is to provide an internal melting type ice heat storage tank capable of improving an ice heat extraction rate and the like and easily measuring the amount of ice. To do.

【0012】[0012]

【課題を解決するための手段】上記の目的を達成するた
めに本発明の内融式氷蓄熱槽は、 (1)水槽と、前記水槽内に浸漬した蓄熱氷形成用の伝
熱管と、前記伝熱管を前記水槽内に支持する支持部材と
を備え、熱伝達媒体を冷凍機又はヒートポンプの蒸発機
と伝熱管との間で循環させ、冷凍機又はヒートポンプの
蒸発機での熱交換により温度降下した熱伝達媒体と、水
槽内の水との熱交換により、伝熱管の外周部に氷を形成
する内融式氷蓄熱槽において、前記支持部材を金属製と
し、前記伝熱管に対し所定の間隔で設けるものである。
In order to achieve the above-mentioned object, an internal melting type ice heat storage tank of the present invention comprises (1) a water tank, a heat transfer tube for forming heat storage ice immersed in the water tank, and A support member for supporting the heat transfer tube in the water tank is provided, the heat transfer medium is circulated between the evaporator of the refrigerator or heat pump and the heat transfer tube, and the temperature is lowered by heat exchange in the evaporator of the refrigerator or heat pump. In the internal melting type ice heat storage tank in which ice is formed on the outer peripheral portion of the heat transfer tube by heat exchange between the heat transfer medium and the water in the water tank, the supporting member is made of metal and has a predetermined interval with respect to the heat transfer tube. It is provided in.

【0013】(2)請求項2記載のように、前記支持部
材の前記伝熱管に対する間隔を、伝熱管の外径の10倍
から50倍とするとよい。
(2) As described in claim 2, the distance between the support member and the heat transfer tube may be 10 to 50 times the outer diameter of the heat transfer tube.

【0014】(3)請求項3記載のように、前記伝熱管
の外周部に金属製のスタッドを突設するとよい。
(3) As described in claim 3, metal studs may be provided so as to protrude from the outer peripheral portion of the heat transfer tube.

【0015】(4)請求項4記載のように、前記伝熱管
の外周部に金属製のフィンを突設するとよい。
(4) As described in claim 4, metal fins may be provided so as to protrude from the outer peripheral portion of the heat transfer tube.

【0016】(5)請求項5記載のように、前記伝熱管
の下方に空気を吐出する散気管と、散気管に空気を送る
ブロアを備えるとよい。
(5) As described in claim 5, it is preferable to provide a diffusing tube for discharging air below the heat transfer tube and a blower for feeding air to the diffusing tube.

【0017】(6)請求項6記載のように、一端が前記
水槽の上方に開口した吸込管と、一端が前記水槽の下方
に開口した吐出管と、前記吸込管を介して水槽内上部の
水を吸込み、この吸込んだ水を前記吐出管を介して水槽
内下部に吐出する水ポンプとからなる水循環装置を備え
るとよい。
(6) As described in claim 6, one end of the suction pipe whose one end is opened above the water tank, one end of which is a discharge pipe opened below the water tank, and the upper part of the inside of the water tank through the suction pipe. It is preferable to include a water circulation device including a water pump that sucks water and discharges the sucked water to the lower portion inside the water tank through the discharge pipe.

【0018】[0018]

【作用】上記の構成を有する本発明の内融式氷蓄熱槽に
よれば、下記の作用がある。
According to the internal melting type ice heat storage tank of the present invention having the above-mentioned structure, the following effects can be obtained.

【0019】(1)支持部材が金属製であり熱伝導が良
好であることに起因し、解氷時、伝熱管の外周部の氷が
融解していくと同時に、前記伝熱管に対し所定の間隔で
設けられた金属製の支持部材周辺の氷も融解し、従来技
術では円筒状になる氷に前記支持部材周辺で穴があき、
円筒状の氷の内部に存する水の略密閉状態が解除され
る。この支持部材の間隔を調整することで、伝熱管と円
筒状の氷との間に存する水と、円筒状の氷の外周部に存
する水との、自然対流による流動を促進することができ
る。このため、伝熱管周辺の温度境界層を薄くすること
が促進でき、氷蓄熱取り出し速度の向上及び氷蓄熱取り
出し温度の降下を図ることができる。
(1) Due to the fact that the support member is made of metal and has good heat conduction, the ice on the outer peripheral portion of the heat transfer tube is melted at the same time when the ice is thawed, and at the same time, a predetermined amount of heat is transferred to the heat transfer tube. Ice around the metal support member provided at intervals also melts, and in the prior art, there is a hole in the cylindrical ice around the support member,
The substantially sealed state of water existing inside the cylindrical ice is released. By adjusting the distance between the support members, it is possible to promote the flow of water existing between the heat transfer tube and the cylindrical ice and the water existing on the outer peripheral portion of the cylindrical ice by natural convection. Therefore, it is possible to promote the thinning of the temperature boundary layer around the heat transfer tube, and it is possible to improve the ice heat extraction speed and lower the ice heat extraction temperature.

【0020】また上述のように、伝熱管と円筒状の氷と
の間に存する水と、円筒状の氷の外周部に存する水との
流路ができ、円筒状の氷の内部に存する水の略密閉状態
が解除されているため、円筒状の氷の内部に気泡が封入
されることもなく、氷量と水槽内の水位との関係が線形
となる。このため水位の変化を測定することにより正確
に氷量が計測できる。
Further, as described above, a flow path is formed between the water existing between the heat transfer tube and the cylindrical ice and the water existing on the outer peripheral portion of the cylindrical ice, and the water existing inside the cylindrical ice is formed. Since the substantially closed state has been released, air bubbles are not enclosed inside the cylindrical ice, and the relationship between the amount of ice and the water level in the water tank is linear. Therefore, the amount of ice can be accurately measured by measuring the change in water level.

【0021】(2)請求項2記載の内融式氷蓄熱槽によ
れば、上記(1)記載の作用が有効に発揮される。伝熱
管に対する支持部材の間隔が短ければ短いほど、円筒状
の氷にあける穴が増加し、円筒状の氷の内部に存する水
と外部に存する水との流動が促進され、氷蓄熱取り出し
速度等の向上を図ることができるが、材料費、加工費等
が増加し経済的に好ましくないことから、上記(1)記
載の作用が有効に発揮される支持部材の間隔として、伝
熱管の外径の50倍を上限としている。また、支持部材
があまり接近しすぎると、製氷時、支持部材を包むよう
に氷が形成されるため、解氷時、逆に氷の内部に水が密
閉され、上記(1)記載の作用が発揮できないこととな
る。かかる観点から、伝熱管に対する支持部材の間隔と
して、伝熱管の外径の10倍を下限としている。
(2) According to the internal melting type ice heat storage tank of the second aspect, the action of the above (1) is effectively exhibited. The shorter the distance between the support member and the heat transfer tube, the more holes that can be made in the cylindrical ice, which promotes the flow of water inside the cylindrical ice and the water that exists outside the ice, and the ice heat extraction speed, etc. However, since it is economically unfavorable because the material cost, the processing cost, etc. increase, the outer diameter of the heat transfer tube is set as the interval between the supporting members that effectively exhibits the action described in (1) above. The upper limit is 50 times. Further, if the supporting members are too close to each other, ice is formed so as to wrap the supporting members during ice making, so that when the ice is thawed, water is confined to the inside of the ice, and the action described in the above (1) is exerted. It will not be possible. From this viewpoint, the lower limit of the distance between the support member and the heat transfer tube is 10 times the outer diameter of the heat transfer tube.

【0022】(3)請求項3記載の内融式氷蓄熱槽によ
れば、前記伝熱管の外周部に金属製のスタッドを突設す
ることから、請求項1又は2記載の内融式氷蓄熱槽のご
とく伝熱管に対し金属製の前記支持部材を設ける構造よ
りも、簡易かつ積極的に円筒状の氷に穴をあけることが
できる。このため、伝熱管と円筒状の氷との間に存する
水と、円筒状の氷の外周部に存する水との、自然対流に
よる流動をより一層促進することができ、氷蓄熱取り出
し速度の向上及び氷蓄熱取り出し温度の降下をさらに促
進できる。また、円筒状の氷の内部に存する水の略密閉
状態の解除がより完全になるため、水位の変化から氷量
を計測することの正確性が増す。
(3) According to the inner melting type ice heat storage tank of the third aspect, the inner melting type ice storage tank of the first or second aspect is provided because the metal stud is provided on the outer peripheral portion of the heat transfer tube. It is possible to make holes in the cylindrical ice more easily and positively than in the structure in which the metal support member is provided for the heat transfer tube as in the heat storage tank. Therefore, the flow of water existing between the heat transfer tube and the cylindrical ice and the water existing in the outer peripheral portion of the cylindrical ice due to natural convection can be further promoted, and the ice heat extraction rate can be improved. And, it is possible to further promote the decrease of the ice heat storage temperature. Further, since the release of the substantially sealed state of the water existing inside the cylindrical ice becomes more complete, the accuracy of measuring the amount of ice from the change in the water level increases.

【0023】(4)請求項4記載の内融式氷蓄熱槽によ
れば、前記伝熱管の外周部に金属製のフィンを突設する
ことから、伝熱管の外周部の形成される円筒状の氷の側
面に前記フィンに沿った裂け目を作ることができる。こ
の金属製のフィンを伝熱管の側面にスパイラル状又はリ
ング状等に設けることで、円筒状の氷の側面に線状の裂
け目を作ることができ、伝熱管と円筒状の氷との間に存
する水と、円筒状の氷の外周部に存する水との、自然対
流による流動をさらに一層促進することができる。この
ため、上述の氷蓄熱取り出し速度の向上、及び氷蓄熱取
り出し温度の降下、又は水位の変化から氷量を計測する
ことの正確性をさらに促進できる。
(4) According to the internal melting type ice heat storage tank of the fourth aspect, since the fins made of metal are projected on the outer peripheral portion of the heat transfer tube, the outer peripheral portion of the heat transfer tube is formed into a cylindrical shape. A crevice can be made along the fin on the side of the ice. By providing this metal fin on the side surface of the heat transfer tube in a spiral shape or a ring shape, a linear crack can be made on the side surface of the cylindrical ice, and between the heat transfer tube and the cylindrical ice. The flow of the existing water and the water existing in the outer peripheral portion of the cylindrical ice due to natural convection can be further promoted. Therefore, it is possible to further improve the above-mentioned speed of ice heat extraction, and further improve the accuracy of measuring the amount of ice from a drop in the temperature of ice heat extraction or a change in the water level.

【0024】(5)請求項5記載の内融式氷蓄熱槽によ
れば、ブロアから空気が送られる散気管を伝熱管の下方
に設け、空気を吐出することから、氷蓄熱槽内の水を強
制的に対流させ撹拌することができる。この氷蓄熱槽内
の強制対流は、上述のような円筒状の氷にあけられた穴
を流路とし、伝熱管と円筒状の氷との間に存する水にも
強制的に対流を生じさせる。このため、伝熱管の周囲の
温度境界層が薄くなり熱伝達率が著しく向上すると共
に、円筒状の氷の外面に存する冷水が流入、混合するた
め、氷蓄熱取り出し速度の向上を著しく図ることができ
る。また氷蓄熱取り出し温度も解氷温度である0℃近く
まで降下させることができる。
(5) According to the internal melting type ice heat storage tank of claim 5, since the air diffuser pipe to which the air is sent from the blower is provided below the heat transfer pipe and the air is discharged, the water in the ice heat storage tank is discharged. Can be forcibly convected and stirred. The forced convection in the ice heat storage tank uses the holes formed in the cylindrical ice as a flow path to forcibly generate convection in the water existing between the heat transfer tube and the cylindrical ice. . For this reason, the temperature boundary layer around the heat transfer tube becomes thin and the heat transfer coefficient is significantly improved, and the cold water existing on the outer surface of the cylindrical ice flows in and mixes, so that the ice heat extraction rate can be significantly improved. it can. Further, the ice heat extraction temperature can be lowered to near 0 ° C. which is the melting temperature.

【0025】(6)請求項6記載の内融式氷蓄熱槽によ
れば、一端が前記水槽の上方に開口した吸込管と、一端
が前記水槽の下方に開口した吐出管と、前記吸込管を介
して水槽内上部の水を吸込み、この吸込んだ水を前記吐
出管を介して水槽内下部に吐出する水ポンプとからなる
水循環装置を備えることから、請求項4記載の内融式氷
蓄熱槽に装備する散気管及びブロアと同様に、氷蓄熱槽
内はもとより伝熱管と円筒状の氷との間に存する水まで
強制的に対流させることができる。従って、上記(5)
記載の作用と同様の作用が発揮できる。
(6) According to the internal melting type ice heat storage tank of the sixth aspect, a suction pipe having one end opened above the water tank, a discharge pipe having one end opened below the water tank, and the suction pipe. 5. The internal melting type ice heat storage system according to claim 4, further comprising a water circulation device including a water pump for sucking water in the upper part of the water tank through the water and discharging the sucked water to the lower part of the water tank through the discharge pipe. Like the air diffuser and blower equipped in the tank, it is possible to forcibly convect not only the water inside the ice storage tank but also the water existing between the heat transfer tube and the cylindrical ice. Therefore, the above (5)
The same effect as described can be exhibited.

【0026】[0026]

【実施例】以下、本発明の内融式氷蓄熱槽を装備した空
調装置を具体化した実施例を図を参照して説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of an air conditioner equipped with an internal melting type ice heat storage tank of the present invention will be described below with reference to the drawings.

【0027】(1)本発明の内融式氷蓄熱槽を装備した
空調装置 本発明に係る内融式氷蓄熱槽を装備した空調装置の概略
構成図を図1に示す。図1に示す空調装置は、図9に示
す従来の空調装置とは氷蓄熱槽102に代えて氷蓄熱槽
2を採用した点を除き、他の点例えば冷凍機101は、
冷媒が圧縮機103等を含む閉ループにおいて冷凍サイ
クルを行いつつ循環している点、及び氷蓄熱槽102の
冷凍機101に対する関係やその役割等は実質的に同一
であり、互いに共通する箇所については同一の番号(下
2桁を同一とする)を付して説明を省略する。
(1) Air Conditioning Apparatus Equipped with Inner Melting Ice Heat Storage Tank of the Present Invention FIG. 1 is a schematic block diagram of an air conditioning apparatus equipped with the inner melting ice storage tank of the present invention. The air conditioner shown in FIG. 1 is different from the conventional air conditioner shown in FIG. 9 in that the ice heat storage tank 2 is used in place of the ice heat storage tank 102.
The point that the refrigerant circulates while performing the refrigeration cycle in the closed loop including the compressor 103, the relationship of the ice heat storage tank 102 to the refrigerator 101, the role thereof, and the like are substantially the same. The same number (the last two digits are the same) is given and the description is omitted.

【0028】氷蓄熱槽2は、水槽7と、蓄熱氷形成用の
伝熱管8と、支持部材9とを備えている。前記支持部材
9は、前記水槽7の底面から上向きに立設された金属製
の柱状体であり、柱状体の側面に設けられた凹部に伝熱
管8を付着させることにより伝熱管8を支持している。
また前記伝熱管8は、略同一平面内で直線部分とU字形
の湾曲部分とを横方向に交互に繰り返し、水槽7内の水
15に対する伝熱面積を多くしている。このように略同
一平面内で、横方向に引き伸ばされた蛇行形状をなす伝
熱管8は、紙面垂直方向に多数並設してあり、ヘッダー
16、17に接合し合流している。このヘッダー16、
17は、それぞれ紙面垂直方向に伸びている一本の管路
である。また、このヘッダー16、17は、管路10、
11と接合し、蒸発器6との間で閉ループを形成し、ポ
ンプ12によりブラインを循環させている。ここまでの
説明は、図9に示す従来の技術と同様であるが、上述の
従来の技術では、理解を容易にすること等のため伝熱管
8を簡略化して説明したので、ここで説明を加えた。
The ice heat storage tank 2 includes a water tank 7, a heat transfer tube 8 for forming heat storage ice, and a support member 9. The support member 9 is a metal columnar body that is erected upward from the bottom surface of the water tank 7, and supports the heat transfer tube 8 by attaching the heat transfer tube 8 to a recess provided on the side surface of the columnar body. ing.
Further, the heat transfer tube 8 has a straight line portion and a U-shaped curved portion which are alternately repeated in a horizontal direction in a substantially same plane to increase a heat transfer area for the water 15 in the water tank 7. As described above, a large number of the heat transfer tubes 8 having a meandering shape which are stretched in the horizontal direction are arranged side by side in the direction perpendicular to the plane of the drawing on the substantially same plane, and are joined to the headers 16 and 17 to join. This header 16,
Reference numeral 17 is a single conduit extending in the direction perpendicular to the plane of the drawing. Also, the headers 16 and 17 are
It joins with 11, forms a closed loop with the evaporator 6, and circulates brine by the pump 12. The description so far is similar to the conventional technique shown in FIG. 9, but in the above-described conventional technique, the heat transfer tube 8 has been simplified for the sake of easy understanding, and therefore the description will be given here. added.

【0029】本実施例では、金属製の支持部材9を伝熱
管8に対し所定の間隔で設けた。氷蓄熱取り出し時、図
2に示すように、伝熱管8の周囲の氷は伝熱管8の周囲
から解氷し水15bとなり、伝熱管8の外周部に円筒状
の氷15aが残る。これと同時に、前記支持部材9は金
属製であり熱伝導が良好であるため、支持部材9の周囲
でも解氷し、円筒状の氷15aに穴20があく。このた
め、円筒状の氷15aの内部の水15bと外部の水15
とに流路ができ、従来技術のような円筒状の氷15a内
部に存する水15bの略密閉性が解除される。従って水
15bが密閉状態にある場合のように、氷と水との比体
積の違いから融解時円筒状の氷15aの内部に気泡が発
生し、水位と氷量とがリンクしなくなることもなく、円
筒状の氷15aの量が水位の変化に直接現れ、水位の変
化を測定することで、簡易に氷量を知ることができる。
また、上述のように支持部材9を所定の間隔に設け、円
筒状の氷15aの内部の水15bと外部の水15とに流
路を作るだけでも、図2に示す矢印(仮想線)のような
自然対流を発生させ、伝熱管に対する熱伝達率を向上で
きる。
In this embodiment, the metal support member 9 is provided at a predetermined distance from the heat transfer tube 8. When the ice heat storage is taken out, as shown in FIG. 2, the ice around the heat transfer tube 8 is thawed from the periphery of the heat transfer tube 8 to become water 15b, and the cylindrical ice 15a remains on the outer peripheral portion of the heat transfer tube 8. At the same time, since the supporting member 9 is made of metal and has good heat conduction, the supporting member 9 is also thawed around the supporting member 9 and a hole 20 is formed in the cylindrical ice 15a. Therefore, the water 15b inside the cylindrical ice 15a and the water 15 outside
A channel is formed in the water, and the water 15b existing inside the cylindrical ice 15a as in the prior art is released from the substantially hermeticity. Therefore, unlike the case where the water 15b is in a sealed state, bubbles are generated inside the cylindrical ice 15a during melting due to the difference in specific volume between ice and water, and the water level and the ice amount are not linked. The amount of the cylindrical ice 15a directly appears in the change in the water level, and the amount of ice can be easily known by measuring the change in the water level.
Further, by providing the support members 9 at predetermined intervals as described above and forming a flow path between the water 15b inside the cylindrical ice 15a and the water 15 outside, the arrow (phantom line) shown in FIG. Such natural convection can be generated to improve the heat transfer coefficient to the heat transfer tube.

【0030】また本実施例では、図1に示すように、氷
蓄熱槽2内で伝熱管8の下方に散気管18を設け、その
散気管18に空気を送るブロア19を設けた。前記散気
管18は、空気を吐出するための細孔を有する管路であ
る。この散気装置により、水槽7の底部から空気を吐出
することで、水槽7内の水15に強制的に対流を起こさ
せ、撹拌することができる。この強制対流は、図2に示
す円筒状の氷15aの内部に存する水15bにも及び、
図2の矢印(仮想線)に示すような強制対流を起こさせ
ることができる。このため、伝熱管8近傍での温度境界
層が薄くなり熱伝達率が著しく向上する。また、水槽7
内の水15を氷15aの解氷温度である0℃に近くでき
ることも冷熱取り出し温度の低下を促進する。
Further, in the present embodiment, as shown in FIG. 1, an air diffuser 18 is provided below the heat transfer tube 8 in the ice heat storage tank 2, and a blower 19 for sending air to the air diffuser 18 is provided. The air diffuser 18 is a conduit having fine holes for discharging air. By discharging air from the bottom of the water tank 7 by this air diffuser, the water 15 in the water tank 7 can be forcibly convected and stirred. This forced convection extends to the water 15b existing inside the cylindrical ice 15a shown in FIG.
Forced convection as shown by the arrow (phantom line) in FIG. 2 can be caused. Therefore, the temperature boundary layer near the heat transfer tube 8 is thinned, and the heat transfer coefficient is significantly improved. Also, water tank 7
The fact that the water 15 in the inside can be close to 0 ° C. which is the melting temperature of the ice 15 a also promotes the reduction of the cold heat extraction temperature.

【0031】なお、伝熱管8に対し支持部材9を設ける
間隔は、短いほど円筒状の氷の内側の水と外側の水との
流路が増加し対流を促進できるため、冷熱取り出し速度
等の向上を図ることができるが、伝熱管8の外径の30
〜50倍の距離間隔でも効果が有効に発揮できる。但
し、伝熱管8に対する支持部材9の間隔が短すぎると、
製氷時、支持部材9を包むように氷が形成されてしまう
事態が生じ、これでは逆に解氷時には氷の内部に密閉状
態の水の層が発生することになる。従って、伝熱管8に
対する支持部材9の間隔は、伝熱管8の外径の10倍以
上にする必要がある。また、支持部材9は、鉄、銅、ア
ルミニュームが好ましい。さらに、散気装置を設け空気
を吐出することによる撹拌は、後述する水を循環させる
ことによる撹拌よりも単位エネルギー当たりの撹拌効果
が高い。
It should be noted that the shorter the interval at which the support member 9 is provided with respect to the heat transfer tube 8, the more the flow paths between the water inside the cylindrical ice and the water outside the cylindrical ice and the convection can be promoted. Although it can be improved, the outer diameter of the heat transfer tube 8 is 30
The effect can be effectively exhibited even at a distance interval of up to 50 times. However, if the distance between the support member 9 and the heat transfer tube 8 is too short,
When ice is made, a situation occurs in which ice is formed so as to wrap the support member 9, and conversely, when ice is thawed, a sealed water layer is generated inside the ice. Therefore, the distance between the support member 9 and the heat transfer tube 8 must be 10 times or more the outer diameter of the heat transfer tube 8. Further, the support member 9 is preferably iron, copper, or aluminum. Further, the stirring effect by providing the air diffuser and discharging the air has a higher stirring effect per unit energy than the stirring effect by circulating water described later.

【0032】(2)伝熱管の外周部に金属製のスタッド
を突設する実施例 伝熱管8の外周部に金属製のスタッド21を突設するこ
とも可能であり、この場合の伝熱管8周辺の解氷状態を
示す横断面図を図3(a)に、縦断面図を図3(b)に
示す。このスタッド21は金属製であり熱伝導が良好で
あるため、解氷時には伝熱管8の周囲から融解し円筒状
に残る氷15aに、スタッド21周辺部で穴22があけ
られる。この穴22が円筒状の氷15aの外部の水15
と内部の水15bとの流路となり、上述の支持部材9の
周辺部での穴20と同様の作用をもたらす。上述の支持
部材9を伝熱管8に対し増設するのは、材料費、加工費
等の上昇をもたらし経済性の面で好ましくないが、本実
施例のスタッド22は比較的簡易な構造であるため、経
済性を考慮しつつ増設できる。本実施例のスタッド22
は、上述の実施例(1)の支持部材9と同様に、鉄、
銅、アルミニューム等が好ましい。また、このスタッド
22の長さは、蓄熱時の氷の厚さより長くする必要があ
る。
(2) Embodiment in which a metal stud is provided on the outer peripheral portion of the heat transfer tube It is also possible to project a metal stud 21 on the outer peripheral portion of the heat transfer tube 8. In this case, the heat transfer tube 8 is provided. FIG. 3 (a) is a cross-sectional view showing the ice-melting state of the periphery, and FIG. 3 (b) is a vertical cross-sectional view. Since this stud 21 is made of metal and has good heat conduction, a hole 22 is formed in the peripheral portion of the stud 21 in the ice 15a that melts from the periphery of the heat transfer tube 8 and remains in a cylindrical shape at the time of thawing. This hole 22 is used for water 15 outside the cylindrical ice 15a.
And the water 15b in the inside of the support member 9 serve as a flow path, which has the same effect as the hole 20 in the peripheral portion of the support member 9 described above. It is not preferable to add the above-mentioned support member 9 to the heat transfer tube 8 because it causes an increase in material cost, processing cost and the like from the economical aspect, but the stud 22 of this embodiment has a relatively simple structure. , It can be expanded while considering economy. The stud 22 of this embodiment
Is iron, similar to the support member 9 of the above-mentioned embodiment (1).
Copper, aluminum and the like are preferable. Further, the length of the stud 22 needs to be longer than the thickness of ice during heat storage.

【0033】(3)伝熱管の外周部に金属製のフィンを
突設する実施例 伝熱管8の外周部に金属製のフィン23を突設すること
も可能である。このフィン23がリング状の場合の斜視
図を図4(a)に、スパイラル状の場合の斜視図を図4
(b)に示す。かかるフィン23も金属製であり熱伝導
が良好であるため、解氷時、円筒状に残る氷15aにフ
ィン23に沿って裂け目が入る。図3に示す上記スタッ
ド21による穴22と同様に、この裂け目が円筒状の氷
15aの内部の水15bと外部の水15との流路とな
り、円筒状の氷15aの内部の水15bの略密閉性が解
除され、上述の実施例(1)の支持部材9と同様の作用
がある。このフィン23も前記スタッド22と同様に比
較的簡易な構造であり経済性に優れる。また、フィン2
3は図4に示す形状に限定されず、例えば伝熱管8と平
行に付設する構造等も可能である。なお、材質は鉄、
銅、アルミニューム等が好適で、蓄熱時生成される氷の
厚さよりも高くしなければならない点は上述の実施例
(2)のスタッド22と同様である。
(3) Embodiment in which metal fins are provided on the outer peripheral portion of the heat transfer tube It is also possible to provide metal fins 23 on the outer peripheral portion of the heat transfer tube 8. FIG. 4A is a perspective view of the fin 23 having a ring shape, and FIG. 4 is a perspective view of the fin 23 having a spiral shape.
It shows in (b). Since the fins 23 are also made of metal and have good heat conduction, a crack is formed along the fins 23 in the ice 15a that remains in the cylindrical shape when the ice is thawed. Similar to the hole 22 formed by the stud 21 shown in FIG. 3, this rupture serves as a flow path between the water 15b inside the cylindrical ice 15a and the water 15 outside, and the water 15b inside the cylindrical ice 15a is substantially abbreviated. The hermeticity is released, and the same operation as the support member 9 of the above-described embodiment (1) is achieved. Like the stud 22, the fin 23 has a relatively simple structure and is excellent in economy. Also fin 2
The shape of 3 is not limited to the shape shown in FIG. 4, and, for example, a structure provided in parallel with the heat transfer tube 8 or the like is also possible. The material is iron,
Copper, aluminum, etc. are preferable, and the thickness is the same as that of the stud 22 of the above-described embodiment (2) in that it must be thicker than the thickness of ice generated during heat storage.

【0034】(4)水循環装置を備える実施例 図5に示すように、一端が水槽7の上方に開口した吸込
管24と、一端が水槽7の下方に開口した吐出管25
と、前記吸込管24を介して水槽7内上部の水15を吸
込み、この吸込んだ水15を前記吐出管25を介して水
槽7内下部に吐出する水ポンプ26とからなる水循環装
置を備えることことも可能である。上述の実施例(1)
に装備した散気管18及びブロア19と同様に、前記支
持部材9、前記スタッド21、及び前記フィン23によ
り円筒状の氷15aにあけられた穴20、22と相俟っ
て、伝熱管8と円筒状の氷15aとの間に存する水15
bまで強制的に対流させることができる(図2、図3参
照)。このため、伝熱管8の周囲の温度境界層を薄く
し、熱伝達を良好にすることができる。従って氷蓄熱取
り出し温度を低下させ、かつ氷蓄熱取り出し速度を向上
させることができる。
(4) Embodiment with Water Circulation Device As shown in FIG. 5, a suction pipe 24 having one end opened above the water tank 7 and a discharge pipe 25 having one end opened below the water tank 7.
And a water pump 26 that sucks the water 15 in the upper part of the water tank 7 through the suction pipe 24 and discharges the sucked water 15 into the lower part of the water tank 7 through the discharge pipe 25. It is also possible. The above embodiment (1)
Similarly to the air diffuser 18 and the blower 19 equipped on the heat transfer tube 8, the support member 9, the stud 21, and the fin 23 cooperate with the holes 20 and 22 formed in the cylindrical ice 15a to form the heat transfer tube 8. Water 15 existing between the cylindrical ice 15a
It is possible to force convection up to b (see FIGS. 2 and 3). Therefore, the temperature boundary layer around the heat transfer tube 8 can be thinned to improve heat transfer. Therefore, the ice heat extraction temperature can be lowered and the ice heat extraction speed can be improved.

【0035】(5)上述の実施例の詳細、効果検討、及
び運転方法 本発明に係る内融式氷蓄熱槽2の詳細な実施例を図6に
示す。伝熱管8は、JIS−25A鋼管で、伝熱管ブロ
ック28を構成した。この伝熱管ブロック28は、図6
に示すように、折り曲げる間隔Aが3.5m、ピッチC
が120mmで、15回折り曲げた蛇行状の管からな
り、2本の蛇行状管の一端をUベント27で接合し、他
端をブライン流入側のヘッダー16及びブライン流出側
のヘッダー17にそれぞれ連結した構造とした。また、
2本の蛇行状管の間隔Dは、110mmとした。伝熱管
ブロック28の支持部材9は、柱状の鋼材であり、伝熱
管8の直線部の間隔Bが1.25mとなるように設置し
た。伝熱管8の湾曲部には、長さ60mm、直径5mm
の鋼材のスタッド21を突設した。また水槽7(図1参
照)は、深さ2.2m、巾7.6m、奥行き2.8mと
し、伝熱管ブロック28を6ブロック浸漬させた。
(5) Details of the above-mentioned embodiment, examination of effects, and operating method FIG. 6 shows a detailed embodiment of the internal melting type ice heat storage tank 2 according to the present invention. The heat transfer tube 8 was a JIS-25A steel tube and constituted a heat transfer tube block 28. This heat transfer tube block 28 is shown in FIG.
As shown in, the bending interval A is 3.5 m and the pitch C is
Has a meandering length of 120 mm and consists of a meandering tube bent 15 times, and one end of each of the two meandering tubes is joined by a U vent 27, and the other ends are connected to a brine inlet side header 16 and a brine outlet side header 17, respectively. It has a structure. Also,
The distance D between the two meandering tubes was 110 mm. The support member 9 of the heat transfer tube block 28 was a columnar steel material, and was installed so that the distance B between the straight portions of the heat transfer tube 8 was 1.25 m. The curved portion of the heat transfer tube 8 has a length of 60 mm and a diameter of 5 mm.
The steel stud 21 of No. 2 was projected. The water tank 7 (see FIG. 1) had a depth of 2.2 m, a width of 7.6 m, and a depth of 2.8 m, and six heat transfer tube blocks 28 were immersed therein.

【0036】図7は、本実施例の熱伝達率と氷の融解度
との関係で、縦軸は対数目盛で熱伝達率(Kcal/m
h℃)を、横軸には氷の融解度を示す。ここで、●は
ブロア19(図1参照)による空気吐出をしない場合で
あり、○は単位面積当たりの空気吐出量を0.6m3
2・hとした場合であり、▲は単位面積当たりの空気
吐出量を1.1m3/m2・hとした場合である。図から
明らかなように、空気の吐出量を増やし、水槽内の水の
強制的な対流を大きくすることにより、熱伝達率が著し
く向上している。これは氷の融解が進み円筒形にのこる
氷のうち、支持部材周辺で作られる穴を流路とし、円筒
形の氷の内部に存する水をも強制的に対流させ、撹拌で
きることからである。但し、本実験においてはスタッド
を設けない伝熱管で行った。
FIG. 7 shows the relationship between the heat transfer coefficient and the melting degree of ice in this embodiment. The vertical axis is a logarithmic scale and the heat transfer coefficient (Kcal / m).
2 h ° C.) and the horizontal axis shows the melting degree of ice. Here, ● indicates the case where air is not discharged by the blower 19 (see FIG. 1), and ○ indicates the air discharge amount per unit area of 0.6 m 3 /
m 2 · h, and ▲ is the case where the air discharge amount per unit area is 1.1 m 3 / m 2 · h. As is clear from the figure, the heat transfer coefficient is remarkably improved by increasing the discharge amount of air and increasing the forced convection of water in the water tank. This is because, out of the cylindrical ice that has melted, the holes formed around the support member are used as a flow path, and water existing inside the cylindrical ice can be forcibly convected and stirred. However, in this experiment, heat transfer tubes without studs were used.

【0037】図8は、本実施例において、ブラインの流
量と伝熱管出入り口のエンタルピー変化とから熱収支計
算し求めた氷量と水位の変化から求めた氷量との関係
で、縦軸に熱収支から求めた氷量、横軸に水位から求め
た氷量を示す。図から明らかなように、二つの方法で求
めた氷量はほとんど等しく、水位の変化から正確に氷量
が計測できることがわかる。ここで、図8の表の両軸に
示す氷量の単位は、伝熱管8の1m当たりの重さであ
る。
FIG. 8 shows the relationship between the amount of ice calculated by calculating the heat balance from the flow rate of brine and the change in enthalpy at the entrance and exit of the heat transfer tube and the amount of ice calculated from the change in the water level in the present embodiment. The amount of ice obtained from the balance is shown, and the horizontal axis shows the amount of ice obtained from the water level. As is clear from the figure, the ice amounts obtained by the two methods are almost equal, and it can be seen that the ice amount can be accurately measured from the change in the water level. Here, the unit of the ice amount shown on both axes of the table of FIG. 8 is the weight per 1 m of the heat transfer tube 8.

【0038】上述の氷蓄熱槽により冷熱を蓄える場合、
冷凍機の蒸発機で−10℃に冷却されたブラインを伝熱
管に還流させ、伝熱管の外周部に平均厚さ40mm、氷
充填率75%(IPF)の状態まで製氷する。この冷熱
を蓄える作業を、夜間電力料金適用時間の午後10時か
ら午前8時までの10時間で行うことにより、運転費用
の低減を図ることができる。また、このようにして蓄え
た冷熱を氷蓄熱槽から取り出す場合、伝熱管と熱交換器
との間でブラインを還流させ、熱交換器での冷房負荷に
より5〜10℃になったブラインを、氷蓄熱槽で0〜5
℃に冷却することによる。また、冷熱の取り出し初期に
は、散気管により空気を吐出しない。冷熱の取り出し初
期においては、伝熱管の外周部に氷が接触しているた
め、伝熱管の外周部を撹拌する必要がないためである。
冷熱の取り出しが進み、伝熱管の外周部やスタッド等の
周辺部で氷の融解が開始され、伝熱管と円筒形に残る氷
との間に流路ができた段階で、散気管により空気を吐出
する。これにより前記流路に強制的に対流を生じさせ、
熱伝達率を向上させることができる。
When cold heat is stored by the above-mentioned ice heat storage tank,
Brine cooled to −10 ° C. is circulated to the heat transfer tube by the evaporator of the refrigerator, and ice is produced on the outer peripheral portion of the heat transfer tube until the average thickness is 40 mm and the ice filling rate is 75% (IPF). The operation cost can be reduced by performing the work of storing the cold energy in 10 hours from 10 pm to 8:00 am of the nighttime electricity charge application time. Further, when the cold energy stored in this way is taken out from the ice heat storage tank, the brine is circulated between the heat transfer tube and the heat exchanger, and the brine heated to 5 to 10 ° C. due to the cooling load in the heat exchanger, 0-5 in ice heat storage tank
By cooling to ° C. Also, in the initial stage of taking out cold heat, air is not discharged through the air diffuser. This is because in the initial stage of taking out cold heat, ice is in contact with the outer peripheral portion of the heat transfer tube, and therefore it is not necessary to stir the outer peripheral portion of the heat transfer tube.
When the cold heat is taken out and ice starts to melt at the outer periphery of the heat transfer tube and the periphery of the studs, etc., when air flow is created between the heat transfer tube and the ice remaining in the cylindrical shape, air is blown by the air diffuser. Discharge. This forces convection in the flow path,
The heat transfer rate can be improved.

【0039】[0039]

【発明の効果】以上説明したことから明らか名用に、本
発明に係る内融式氷蓄熱槽によれば、次のような効果が
ある。
EFFECTS OF THE INVENTION As is apparent from the above description, the internal melting type ice heat storage tank according to the present invention has the following effects.

【0040】(1)解氷時、従来技術では円筒状になる
氷に熱伝導のよい金属製の支持部材周辺で穴があき、伝
熱管と円筒状の氷との間に存する水と、円筒状の氷の外
周部に存する水との、自然対流による流動を促進するこ
とができる。このため、伝熱管周辺の温度境界層を薄く
することが促進でき、氷蓄熱取り出し速度の向上及び氷
蓄熱取り出し温度の降下を図ることができる。従って、
所定の場所を急速に冷房することが可能となる。
(1) When the ice is thawed, according to the prior art, the cylindrical ice has a hole around the metal supporting member having good heat conduction, and the water existing between the heat transfer tube and the cylindrical ice and the cylinder are It is possible to promote flow due to natural convection with water existing on the outer peripheral portion of the ice cube. Therefore, it is possible to promote the thinning of the temperature boundary layer around the heat transfer tube, and it is possible to improve the ice heat extraction speed and lower the ice heat extraction temperature. Therefore,
It is possible to rapidly cool a predetermined place.

【0041】また上述のように、伝熱管と円筒状の氷と
の間に存する水と、円筒状の氷の外周部に存する水との
流路ができ、円筒状の氷の内部に存する水の略密閉状態
が解除されているため、水位の変化を測定することによ
り正確に氷量が計測できる。氷蓄熱槽による冷房能力を
管理するためには、氷蓄熱槽の蓄熱量つまり氷量を把握
する必要があるが、本発明の氷蓄熱槽によれば水位の変
化を計測することで簡易にこれを達成することができ
る。
As described above, a flow path is formed between the water existing between the heat transfer tube and the cylindrical ice and the water existing on the outer peripheral portion of the cylindrical ice, and the water existing inside the cylindrical ice is formed. Since the substantially closed state of is released, the amount of ice can be accurately measured by measuring the change in water level. In order to manage the cooling capacity of the ice heat storage tank, it is necessary to grasp the heat storage amount of the ice heat storage tank, that is, the amount of ice, but according to the ice heat storage tank of the present invention, this can be easily done by measuring the change of the water level. Can be achieved.

【0042】(2)請求項2記載の内融式氷蓄熱槽によ
れば、上記(1)記載の効果が有効に発揮される。伝熱
管に対する支持部材の間隔が短いほど、氷蓄熱取り出し
速度等の向上を図ることができるが、材料費、加工費等
が増加し経済的に好ましくないことから、上記(1)記
載の効果が有効に発揮される支持部材の間隔として、伝
熱管の外径の50倍を上限としている。また、支持部材
があまり接近しすぎると、製氷時、支持部材を包むよう
に氷が形成されるため、解氷時、逆に氷の内部に水が密
閉され、上記(1)記載の作用が発揮できないこととな
る。かかる観点から、伝熱管に対する支持部材の間隔と
して、伝熱管の外径の10倍を下限としている。
(2) According to the internal melting type ice heat storage tank of the second aspect, the effect described in the above (1) is effectively exhibited. As the distance between the support member and the heat transfer tube is shorter, the ice storage heat extraction speed and the like can be improved, but the material cost, the processing cost, and the like increase, which is economically unfavorable. Therefore, the effect described in (1) above is obtained. The upper limit is 50 times the outer diameter of the heat transfer tube as the distance between the supporting members that is effectively exhibited. Further, if the supporting members are too close to each other, ice is formed so as to wrap the supporting members during ice making, so that when the ice is thawed, water is confined to the inside of the ice, and the action described in the above (1) is exerted. It will not be possible. From this viewpoint, the lower limit of the distance between the support member and the heat transfer tube is 10 times the outer diameter of the heat transfer tube.

【0043】(3)請求項3記載の内融式氷蓄熱槽によ
れば、伝熱管の外周部に金属製のスタッドを突設するこ
とから、請求項1記載の内融式氷蓄熱槽の如く伝熱管に
対し金属製の前記支持部材を設ける構造よりも、簡易か
つ積極的に円筒状の氷に穴をあけることができる。この
ため、伝熱管と円筒状の氷との間に存する水と、円筒状
の氷の外周部に存する水との、自然対流による流動をよ
り一層促進することができ、氷蓄熱取り出し速度の向上
及び氷蓄熱取り出し温度の降下にさらに寄与する。ま
た、円筒状の氷の内部に存する水の略密閉状態の解除が
より完全になるため、水位の変化から氷量を計測するこ
との正確性が増す。
(3) According to the inner melting type ice heat storage tank of the third aspect, since the metal studs are provided on the outer peripheral portion of the heat transfer tube, the inner melting type ice heat storage tank of the first aspect is provided. As described above, it is possible to easily and positively make a hole in the cylindrical ice as compared with the structure in which the metal support member is provided for the heat transfer tube. Therefore, the flow of water existing between the heat transfer tube and the cylindrical ice and the water existing in the outer peripheral portion of the cylindrical ice due to natural convection can be further promoted, and the ice heat extraction rate can be improved. And further contributes to the drop in the temperature for extracting ice heat. Further, since the release of the substantially sealed state of the water existing inside the cylindrical ice becomes more complete, the accuracy of measuring the amount of ice from the change in the water level increases.

【0044】(4)請求項4記載の内融式氷蓄熱槽によ
れば、伝熱管の外周部に金属製のフィンを突設すること
から、伝熱管の外周部の形成される円筒状の氷の側面に
前記フィンに沿った裂け目を作ることができる。この裂
け目が、上述の請求項2記載の氷蓄熱槽に突設されたス
タッドによる穴と同様の効果を有し、氷蓄熱取り出し速
度の向上、及び氷蓄熱取り出し温度の降下、又は水位の
変化から氷量を計測することの正確性にさらに寄与す
る。また、この金属製のフィンを伝熱管の側面にスパイ
ラル状又はリング状等に設けることで、円筒状の氷の側
面に線状の裂け目を作ることができ、伝熱管と円筒状の
氷との間に存する水と、円筒状の氷の外周部に存する水
との、流路を多くすることができる。さらに、金属製の
フィンを伝熱管に突設することから、伝熱管の表面積を
増加させる効果があり、このことも氷蓄熱取り出し速度
の向上等を図る要因となる。
(4) According to the internal melting type ice heat storage tank of the fourth aspect, since the fins made of metal are projected on the outer peripheral portion of the heat transfer tube, the cylindrical outer peripheral portion of the heat transfer tube is formed. A crevice can be made along the fin on the side of the ice. This rift has the same effect as the hole formed by the stud projecting in the ice heat storage tank according to the above-mentioned claim 2, and it is possible to improve the ice heat extraction speed and decrease the ice heat extraction temperature or change the water level. It further contributes to the accuracy of measuring the amount of ice. In addition, by providing the metal fins in a spiral shape or a ring shape on the side surface of the heat transfer tube, it is possible to make a linear crevice on the side surface of the cylindrical ice, and the heat transfer tube and the cylindrical ice can be separated from each other. It is possible to increase the number of flow paths between the water existing between the water and the water existing on the outer peripheral portion of the cylindrical ice. Furthermore, since the metal fins are provided so as to project from the heat transfer tube, there is an effect of increasing the surface area of the heat transfer tube, which is also a factor for improving the ice heat extraction rate.

【0045】(5)請求項5記載の内融式氷蓄熱槽によ
れば、ブロアから空気が送られる散気管を伝熱管の下方
に設け、空気を吐出することにより、氷蓄熱槽内の水に
強制対流を起こすことができるのみならず、上述のよう
な円筒状の氷にあけられた穴及び裂け目を流路とし、伝
熱管と円筒状の氷との間に存する水にも強制的に対流を
生じさせる。このため、伝熱管の周囲の温度境界層が薄
くなり、熱伝達率が著しく向上する結果、氷蓄熱取り出
し速度の向上を著しく図ることができる。また氷蓄熱取
り出し温度も解氷温度である0℃近くまで降下させるこ
とができる。
(5) According to the internal melting type ice heat storage tank of claim 5, the air diffuser pipe to which the air is sent from the blower is provided below the heat transfer pipe, and the air is discharged so that the water in the ice heat storage tank is discharged. Not only can forced convection be generated in the water, but the holes and crevices formed in the cylindrical ice as described above are used as flow paths, and the water existing between the heat transfer tube and the cylindrical ice is forcibly forced. Cause convection. Therefore, the temperature boundary layer around the heat transfer tube becomes thin, and the heat transfer coefficient is remarkably improved. As a result, it is possible to remarkably improve the ice heat extraction rate. Further, the ice heat extraction temperature can be lowered to near 0 ° C. which is the melting temperature.

【0046】(6)請求項6記載の内融式氷蓄熱槽によ
れば、一端が水槽の上方に開口した吸込管と、一端が水
槽の下方に開口した吐出管と、前記吸込管を介して水槽
内上部の水を吸込み、この吸込んだ水を前記吐出管を介
して水槽内下部に吐出する水ポンプとからなる水循環装
置を備えることから、請求項4記載の内融式氷蓄熱槽に
装備する散気管及びブロアと同様に、氷蓄熱槽内はもと
より伝熱管と円筒状の氷との間に存する水まで強制的に
対流させることができる。従って、上記(4)記載の作
用と同様の作用が発揮できる。
(6) According to the internal melting type ice heat storage tank of the sixth aspect, the suction pipe having one end opened above the water tank, the discharge pipe having one end opened below the water tank, and the suction pipe are provided. 5. The internal melting type ice heat storage tank according to claim 4, comprising a water circulation device comprising a water pump for sucking water in the upper part of the water tank and discharging the sucked water to the lower part in the water tank through the discharge pipe. Like the air diffuser and blower equipped, it is possible to forcibly convect not only the water inside the ice storage tank but also the water existing between the heat transfer tube and the cylindrical ice. Therefore, the same action as the action described in (4) above can be exhibited.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例(所定間隔の支持部材と散気装
置とを備えた場合)に係る内融式氷蓄熱槽を備えた冷凍
機を示す概略構成図である。
FIG. 1 is a schematic configuration diagram showing a refrigerator including an internal melting type ice heat storage tank according to an embodiment of the present invention (when a supporting member and a diffuser are provided at predetermined intervals).

【図2】図1の内融式氷蓄熱槽における伝熱管周辺の解
氷状態を示す断面図である。
FIG. 2 is a cross-sectional view showing a defrosted state around a heat transfer tube in the internal melting type ice heat storage tank of FIG.

【図3】本発明の実施例(スタッドを突設した場合)に
係る内融式氷蓄熱槽における伝熱管周辺の解氷状態を示
すもので、同図(a)は横断面図で、同図(b)は縦断
面図である。
FIG. 3 is a cross-sectional view showing a defrosting state around a heat transfer tube in an internal melting type ice heat storage tank according to an embodiment of the present invention (when a stud is projecting); Figure (b) is a vertical sectional view.

【図4】本発明の実施例(フィンを突設した場合)に係
る内融式氷蓄熱槽の伝熱管を示す側面図である。但し、
同図(a)はリング状のフィンを示し、同図(b)はス
パイラル状のフィンを示す。
FIG. 4 is a side view showing a heat transfer tube of an internal melting type ice heat storage tank according to an embodiment of the present invention (when fins are provided to project). However,
The figure (a) shows a ring-shaped fin and the figure (b) shows a spiral fin.

【図5】本発明の実施例(所定間隔の支持部材と水循環
装置とを備えた場合)に係る内融式氷蓄熱槽を示す概略
構成図である。
FIG. 5 is a schematic configuration diagram showing an inner melting type ice heat storage tank according to an embodiment of the present invention (when a supporting member and a water circulating device are provided at predetermined intervals).

【図6】本発明の実施例(所定間隔の支持部材とスタッ
ドとを備えた場合)に係る内融式氷蓄熱槽における伝熱
管の製造過程を示すもので、同図(a)は正面図で、同
図(b)は側面図である。
FIG. 6 shows a manufacturing process of a heat transfer tube in an internal melting type ice heat storage tank according to an embodiment of the present invention (when a supporting member and a stud are provided at predetermined intervals), and FIG. Then, FIG. 3B is a side view.

【図7】本発明の実施例(所定間隔の支持部材と散気装
置とを備えた場合)に係る内融式氷蓄熱槽における熱伝
達率と融解度との関係を示す図である。但し熱伝達率を
示す縦軸は対数目盛りである。
FIG. 7 is a diagram showing a relationship between a heat transfer coefficient and a melting degree in an internal melting type ice heat storage tank according to an embodiment of the present invention (when a supporting member and a diffuser are provided at predetermined intervals). However, the vertical axis indicating the heat transfer coefficient is on a logarithmic scale.

【図8】本発明の実施例(所定間隔の支持部材、スタッ
ド、及び散気装置を備えた場合)に係る内融式氷蓄熱槽
における、製氷管を還流する冷媒の熱収支計算から求め
た氷量と水位の変化から求めた氷量との関係を示す図で
ある。
FIG. 8: Obtained from the heat balance calculation of the refrigerant flowing back into the ice making tube in the internal melting type ice heat storage tank according to the embodiment of the present invention (when the supporting member at a predetermined interval, the stud, and the air diffuser are provided). It is a figure which shows the relationship between the amount of ices and the amount of ices calculated from the change of a water level.

【図9】従来の内融式氷蓄熱槽を備えた冷凍機を示す概
略構成図である。
FIG. 9 is a schematic configuration diagram showing a refrigerator provided with a conventional internal melting type ice heat storage tank.

【図10】図9の内融式氷蓄熱槽における伝熱管周辺の
解氷状態を示すもので、同図(a)は横断面図で、同図
(b)は縦断面図である。
10A and 10B show a state of thawing around a heat transfer tube in the internal melting type ice heat storage tank of FIG. 9, where FIG. 10A is a horizontal sectional view and FIG. 10B is a vertical sectional view.

【図11】外融式氷蓄熱槽の伝熱管周辺の製氷状態を示
す縦断面図である。
FIG. 11 is a vertical cross-sectional view showing an ice making state around the heat transfer tube of the outer melting type ice heat storage tank.

【符号の説明】[Explanation of symbols]

1 冷凍機 2 氷蓄熱槽 3 圧縮機 4 凝縮器 5 膨張弁 6 蒸発器 7 水槽 8 伝熱管 9 支持部材 12 ポンプ 13 切換弁 14 熱交換器 15 水 16・17 ヘッダー 18 散気管 19 ブロア 21 スタッド 23 フィン 24 吸込管 25 吐出管 26 水ポンプ 27 Uベント 28 伝熱管ブロック 1 Refrigerator 2 Ice heat storage tank 3 Compressor 4 Condenser 5 Expansion valve 6 Evaporator 7 Water tank 8 Heat transfer tube 9 Support member 12 Pump 13 Switching valve 14 Heat exchanger 15 Water 16/17 Header 18 Air diffuser tube 19 Blower 21 Stud 23 Fins 24 suction pipes 25 discharge pipes 26 water pumps 27 U vents 28 heat transfer tube blocks

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 水槽と、前記水槽内に浸漬した蓄熱氷形
成用の伝熱管と、前記伝熱管を前記水槽内に支持する支
持部材とを備え、熱伝達媒体を冷凍機又はヒートポンプ
の蒸発機と伝熱管との間で循環させ、冷凍機又はヒート
ポンプの蒸発機での熱交換により温度降下した熱伝達媒
体と、水槽内の水との熱交換により、伝熱管の外周部に
氷を形成する内融式氷蓄熱槽において、 前記支持部材を金属製とし、前記伝熱管に対し所定の間
隔で設けたことを特徴とする内融式氷蓄熱槽。
1. A water tank, a heat transfer tube for forming heat storage ice immersed in the water tank, and a support member for supporting the heat transfer tube in the water tank, wherein the heat transfer medium is a refrigerator or a heat pump evaporator. Between the heat transfer tube and the heat transfer tube, and heat is exchanged between the heat transfer medium whose temperature has dropped due to heat exchange in the evaporator of the refrigerator or heat pump and the water in the water tank to form ice on the outer circumference of the heat transfer tube. In the internal melting type ice heat storage tank, the supporting member is made of metal and is provided at a predetermined interval with respect to the heat transfer tube.
【請求項2】 前記支持部材の前記伝熱管に対する間隔
を、伝熱管の外径の10倍から50倍とした請求項1記
載の内融式氷蓄熱槽。
2. The internal melting type ice heat storage tank according to claim 1, wherein the distance between the support member and the heat transfer tube is 10 to 50 times the outer diameter of the heat transfer tube.
【請求項3】 前記伝熱管の外周部に金属製のスタッド
を突設した請求項1又は2記載の内融式氷蓄熱槽。
3. The internal melting type ice heat storage tank according to claim 1, wherein a metal stud is provided on the outer peripheral portion of the heat transfer tube.
【請求項4】 前記伝熱管の外周部に金属製のフィンを
突設した請求項1、2又は3記載の内融式氷蓄熱槽。
4. The internal melting type ice heat storage tank according to claim 1, 2 or 3, wherein metal fins are provided so as to protrude from the outer peripheral portion of said heat transfer tube.
【請求項5】 前記伝熱管の下方に空気を吐出する散気
管と、散気管に空気を送るブロアを備えた請求項1〜4
のいずれかに記載の内融式氷蓄熱槽。
5. An air diffuser for discharging air below the heat transfer tube, and a blower for sending air to the air diffuser.
The internal melting type ice heat storage tank according to any one of 1.
【請求項6】 一端が前記水槽の上方に開口した吸込管
と、一端が前記水槽の下方に開口した吐出管と、前記吸
込管を介して水槽内上部の水を吸込み、この吸込んだ水
を前記吐出管を介して水槽内下部に吐出する水ポンプと
からなる水循環装置を備えた請求項1〜4のいずれかに
記載の内融式氷蓄熱槽。
6. A suction pipe whose one end is opened above the water tank, a discharge pipe whose one end is opened below the water tank, and water in the upper part of the water tank is sucked through the suction pipe. The internal melting type ice heat storage tank according to any one of claims 1 to 4, further comprising a water circulation device including a water pump that discharges the water through the discharge pipe to a lower portion inside the water tank.
JP6319178A 1994-11-28 1994-11-28 Internal melting type ice storage tank Pending JPH08152162A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6319178A JPH08152162A (en) 1994-11-28 1994-11-28 Internal melting type ice storage tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6319178A JPH08152162A (en) 1994-11-28 1994-11-28 Internal melting type ice storage tank

Publications (1)

Publication Number Publication Date
JPH08152162A true JPH08152162A (en) 1996-06-11

Family

ID=18107296

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6319178A Pending JPH08152162A (en) 1994-11-28 1994-11-28 Internal melting type ice storage tank

Country Status (1)

Country Link
JP (1) JPH08152162A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002250547A (en) * 2000-12-22 2002-09-06 Sekisui Plant Systems Co Ltd Ice storage device
EP1684035A3 (en) * 2005-01-24 2008-07-16 Franz Haslinger Apparatus for ice thermal storage and direct cooling
US20100064704A1 (en) * 2006-12-22 2010-03-18 BSH Bosch und Siemens Hausgeräte GmbH Refrigerating appliance comprising an ice-making machine
KR101219390B1 (en) * 2012-02-29 2013-01-09 (주)경진티알엠 Immersion heat exchanger packaged heat pump unit installed
US20170023309A1 (en) * 2015-03-24 2017-01-26 Evapco, Inc. Thermal storage ice breaker apparatus
CN110770320A (en) * 2017-06-30 2020-02-07 达泰豪化学工业株式会社 Chemical heat storage material and method for producing the same, and chemical heat pump and method for operating the same
JP2020041725A (en) * 2018-09-07 2020-03-19 株式会社前川製作所 Cooling pipe
WO2020202487A1 (en) * 2019-04-03 2020-10-08 三菱電機株式会社 Heat storage device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04320738A (en) * 1991-04-19 1992-11-11 Misawa Homes Co Ltd Ice heat accumulating tank
JPH0611158A (en) * 1992-06-24 1994-01-21 Kansai Electric Power Co Inc:The Internal melting type ice heat storing tank for heat pump
JPH06300321A (en) * 1993-04-13 1994-10-28 Daikin Ind Ltd Ice heat storing tank

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04320738A (en) * 1991-04-19 1992-11-11 Misawa Homes Co Ltd Ice heat accumulating tank
JPH0611158A (en) * 1992-06-24 1994-01-21 Kansai Electric Power Co Inc:The Internal melting type ice heat storing tank for heat pump
JPH06300321A (en) * 1993-04-13 1994-10-28 Daikin Ind Ltd Ice heat storing tank

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002250547A (en) * 2000-12-22 2002-09-06 Sekisui Plant Systems Co Ltd Ice storage device
EP1684035A3 (en) * 2005-01-24 2008-07-16 Franz Haslinger Apparatus for ice thermal storage and direct cooling
US20100064704A1 (en) * 2006-12-22 2010-03-18 BSH Bosch und Siemens Hausgeräte GmbH Refrigerating appliance comprising an ice-making machine
US8353171B2 (en) * 2006-12-22 2013-01-15 Bsh Bosch Und Siemens Hausgeraete Gmbh Refrigerating appliance comprising an ice-making machine
KR101219390B1 (en) * 2012-02-29 2013-01-09 (주)경진티알엠 Immersion heat exchanger packaged heat pump unit installed
US20170023309A1 (en) * 2015-03-24 2017-01-26 Evapco, Inc. Thermal storage ice breaker apparatus
US10465994B2 (en) * 2015-03-24 2019-11-05 Evapco, Inc. Thermal storage ice breaker apparatus
CN110770320A (en) * 2017-06-30 2020-02-07 达泰豪化学工业株式会社 Chemical heat storage material and method for producing the same, and chemical heat pump and method for operating the same
CN110770320B (en) * 2017-06-30 2021-12-14 达泰豪化学工业株式会社 Chemical heat storage material and method for producing the same, and chemical heat pump and method for operating the same
JP2020041725A (en) * 2018-09-07 2020-03-19 株式会社前川製作所 Cooling pipe
WO2020202487A1 (en) * 2019-04-03 2020-10-08 三菱電機株式会社 Heat storage device
JPWO2020202487A1 (en) * 2019-04-03 2021-04-30 三菱電機株式会社 Heat storage device

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