JP2858995B2 - Cooling device - Google Patents
Cooling deviceInfo
- Publication number
- JP2858995B2 JP2858995B2 JP14006691A JP14006691A JP2858995B2 JP 2858995 B2 JP2858995 B2 JP 2858995B2 JP 14006691 A JP14006691 A JP 14006691A JP 14006691 A JP14006691 A JP 14006691A JP 2858995 B2 JP2858995 B2 JP 2858995B2
- Authority
- JP
- Japan
- Prior art keywords
- space
- cooling
- cooled
- heat
- regenerator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000001816 cooling Methods 0.000 title claims description 33
- 229910052987 metal hydride Inorganic materials 0.000 claims description 27
- 150000004681 metal hydrides Chemical class 0.000 claims description 27
- 229910052739 hydrogen Inorganic materials 0.000 claims description 21
- 239000001257 hydrogen Substances 0.000 claims description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 20
- 238000000034 method Methods 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 16
- 239000011232 storage material Substances 0.000 description 9
- 230000008929 regeneration Effects 0.000 description 8
- 238000011069 regeneration method Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は金属水素化物と蓄冷材を
組み合わせた冷房装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling device using a combination of a metal hydride and a cold storage material.
【0002】[0002]
【従来の技術】例えば、特願平2−131664号では
金属水素化物と蓄冷材を組み合わせて、冷房過程で金属
水素化物より発生する冷熱を被冷却空間の冷房と同時に
蓄冷材への蓄冷にも用い、水素を冷房発生用熱交換器に
戻してやる再生過程では蓄冷材に蓄えられた冷熱により
被冷却空間の冷房を行う装置が提案されている。2. Description of the Related Art For example, in Japanese Patent Application No. 2-131664, a metal hydride and a regenerator material are combined so that cold generated from the metal hydride in a cooling process can be used for both cooling of a space to be cooled and cold storage in the regenerator material. An apparatus has been proposed which cools a space to be cooled by using cold stored in a cold storage material in a regeneration process in which hydrogen is returned to a cooling-generation heat exchanger.
【0003】この装置を図2に示す。同図においては、
図2aのような空気経路で金属水素化物M2H側を冷房
空間13及び蓄令器3と熱交換させるように、そして、
金属水素化物M1Hを外気と熱交換させるようにし、バ
ルブ2を開けると両金属水素化物M1H、M2Hの平衡
圧力差によりM2Hは吸熱的に水素を放出し、M1Hは
発熱的に水素を吸蔵する。これにより冷房空間が冷却さ
れるとともに、冷却器3より熱を奪う。この時、冷却風
の温度を畜冷材の凝固温度より低く設定しておくことに
より蓄令材は凝固する。FIG. 2 shows this apparatus. In the figure,
In order to make the metal hydride M2H side exchange heat with the cooling space 13 and the accumulator 3 in the air path as shown in FIG.
The metal hydride M1H is allowed to exchange heat with the outside air, and when the valve 2 is opened, M2H endothermically releases hydrogen and M1H exothermically stores hydrogen due to the equilibrium pressure difference between the two metal hydrides M1H and M2H. Thereby, the cooling space is cooled and heat is taken from the cooler 3. At this time, the storage material solidifies by setting the temperature of the cooling air lower than the solidification temperature of the animal cooling material.
【0004】次に、水素がM2H側からM1H側へ移動
し終わった後、バルブ2を閉じ、ダンパー4〜8の切り
換えによって図2のようにM1H側へ高温空気を流し、
M2H側へ外気を流すとM1H側とM2H側の平衡圧力
は逆転する。このときバルブ2を開けると水素はM1H
側からM2H側へと移動し、移動終了後には図2の最初
の状態に戻る。また、このとき金属水素化物からの冷房
発生は行なわれないが、先の図2の過程で蓄冷器内に蓄
えられた冷熱(蓄冷材の融解熱)を取り出すことによっ
て冷房が行なわれる。Next, after the hydrogen has moved from the M2H side to the M1H side, the valve 2 is closed, and high-temperature air is flown to the M1H side by switching the dampers 4 to 8 as shown in FIG.
When the outside air flows to the M2H side, the equilibrium pressures on the M1H side and the M2H side are reversed. At this time, if valve 2 is opened, hydrogen will be M1H
From the side to the M2H side, and returns to the initial state in FIG. 2 after the movement is completed. At this time, cooling is not generated from the metal hydride, but cooling is performed by extracting the cold heat (the heat of fusion of the cold storage material) stored in the regenerator in the process of FIG.
【0005】このとき仮に、冷凍能力を500Kcal
/hとし、被冷却空間内の空気状態を10℃、相対温度
80%に保つものとすれば、凝固点約9℃の蓄冷材を用
い、冷房過程における被冷却空間内の循環風量を約4m
3/minとすれば、再生過程における被冷却空間内の
循環風量は約70m3/minにもしなければならず、
ファン動力、騒音、被冷却空間内の物体に及ぼす風圧の
影響は大である。At this time, if the refrigerating capacity is assumed to be 500 Kcal
/ H, the air condition in the space to be cooled is maintained at 10 ° C. and the relative temperature is 80%, and a regenerative material having a freezing point of about 9 ° C. is used.
If 3 / min, amount of circulating air to be cooled within the space in the regeneration process must be about 70m 3 / min,
The effects of fan power, noise, and wind pressure on objects in the cooled space are significant.
【0006】[0006]
【発明が解決しようとする課題】しかるに、特願平2−
131664号に示されているような冷暖房方式では金
属水素化物より発生する冷熱を利用する冷房過程と蓄冷
材に蓄えられた冷熱を利用する再生過程とで被冷却空間
内の温度を一定に保つためには再生過程において被冷却
空間内へ多量の空気循環が必要になり、また、暖房時に
おいても蓄冷器との空気循環が行われるため、蓄冷材及
び蓄冷器の顕熱量が暖房出熱に対する損失となる。SUMMARY OF THE INVENTION However, Japanese Patent Application No. Hei.
In a cooling and heating system such as that described in Japanese Patent No. 131664, a temperature in a space to be cooled is kept constant during a cooling process using cold generated from metal hydride and a regeneration process using cold stored in a cold storage material. Requires a large amount of air circulation into the space to be cooled during the regeneration process, and also air circulation with the regenerator during heating. Becomes
【0007】本発明はこのような点に鑑みてなされたも
のであって、冷房過程では金属水素化物より発生する冷
熱を被冷却空間の冷却用と蓄冷材への蓄冷用にそれぞれ
別経路で循環させ、また暖房時においては、金属水素化
物より発生する熱を蓄冷器を通さず被暖房空間へ循環さ
せる。The present invention has been made in view of the above points, and circulates cold generated from a metal hydride in separate paths for cooling a space to be cooled and for storing cold in a cold storage material in a cooling process. During heating, heat generated from the metal hydride is circulated to the space to be heated without passing through the regenerator.
【0008】[0008]
【課題を解決するための手段】本発明では、水素吸蔵圧
力の低い金属水素化物を内蔵した第1の熱交換器と、水
素吸蔵圧力の高い金属水素化物を内蔵した第2の熱交換
器と、これら、第1、第2の熱交換器間の水素経路を形
成する水素配管と、上記第1の熱交換器に高温を付与す
る高温付与手段と、上記第2の熱交換器を冷却する冷却
手段と、上記第2の熱交換器及び被冷却空間と熱交換可
能な蓄冷器と、上記第2の熱交換器、上記蓄冷器及び被
冷却空間からなり、上記蓄冷器と被冷却空間とを並列に
設けてなる空気循環経路と、上記第2の熱交換器、上記
蓄冷器及び被冷却空間の熱交換状態を切り換える切り換
え手段と、を設けている。According to the present invention, a first heat exchanger containing a metal hydride having a low hydrogen storage pressure and a second heat exchanger containing a metal hydride having a high hydrogen storage pressure are provided. A hydrogen pipe for forming a hydrogen path between the first and second heat exchangers, a high-temperature applying means for applying a high temperature to the first heat exchanger, and cooling the second heat exchanger. A cooling unit, a regenerator capable of exchanging heat with the second heat exchanger and the space to be cooled, and the second heat exchanger, the regenerator and the space to be cooled, and the regenerator and the space to be cooled. Are provided in parallel, and switching means for switching the heat exchange state of the second heat exchanger, the regenerator and the space to be cooled is provided.
【0009】[0009]
【作用】このような構成にすることにより、一対の金属
水素化物からな一組みの冷房ブロックより発生する冷熱
を別々の経路で一方は蓄冷材への蓄冷用に、他方は被冷
却空間の冷房用に供給し、再生過程においては蓄冷材に
蓄えられた冷熱を被冷却空間へ供給すれば、比較的少な
い庫内循環風量で安定した冷熱供給を行える。さらに、
ダンパー等を設けることによって暖房運転時に金属水素
化物からの出熱を蓄冷器を通さず、被暖房空間とのみ循
環させることにより、蓄冷材及び蓄冷材による顕熱損失
の少ない暖房運転が行える。With such a construction, the cooling heat generated from a pair of cooling blocks made of a pair of metal hydrides is separated into separate paths, one for storing the cold storage material, and the other for cooling the space to be cooled. If the cold heat stored in the cold storage material is supplied to the space to be cooled in the regeneration process, stable cold heat supply can be performed with a relatively small amount of circulation air in the refrigerator. further,
By providing a damper or the like, the heat output from the metal hydride is circulated only in the space to be heated without passing through the regenerator during the heating operation, so that the heating operation with less sensible heat loss due to the regenerator material and the regenerator material can be performed.
【0010】[0010]
【実施例】以下本発明実施例を図面とともに説明する。
まず図1は本発明で使用する金属水素化物M1HとM2
Hの温度−平衡圧特性及び冷房時と暖房時それぞれのサ
イクル線図を示したもので、図3は図1の特性を有する
金属水素化物を使用して構成した冷暖房装置の構成及び
冷房、暖房それぞれの場合の動作状態を示す。Embodiments of the present invention will be described below with reference to the drawings.
First, FIG. 1 shows the metal hydrides M1H and M2 used in the present invention.
FIG. 3 shows a temperature-equilibrium pressure characteristic of H, and a cycle diagram for each of cooling and heating. FIG. 3 shows a configuration of a cooling / heating device and a cooling / heating system configured using a metal hydride having the characteristics of FIG. The operation state in each case is shown.
【0011】まず、図3、図4について、説明する。こ
れらの図において、1a及び1bはそれぞれ図1に示し
た金属水素化物M1H、M2Hを充填した第1、第2の
熱交換器であり、これら2種類の熱交換器内の金属水素
化物容器(図示せず)は互いに水素配管2で繋がれてい
る。First, FIGS. 3 and 4 will be described. In these figures, reference numerals 1a and 1b denote first and second heat exchangers filled with the metal hydrides M1H and M2H shown in FIG. 1, respectively, and the metal hydride containers (in these two types of heat exchangers) (Not shown) are connected to each other by a hydrogen pipe 2.
【0012】図3に示すように、冷房過程において冷熱
発生用の金属水素化物M2H内蔵の熱交換器から、被冷
却空間および蓄冷器への循環経路を並列に配置すれば、
上記図2における運転条件(冷凍能力500Kcal/
h、空気状態10℃、80%)では、凝固点約3℃の蓄
冷材を用いることによって、冷房過程における被冷却空
間への循環風量を約2m3/min、蓄冷器の循環風量
を約15m3/minとし、再生過程における蓄冷器−
被冷却空間の循環風量を約4m3/minとすればよ
い。As shown in FIG. 3, if the circulation paths from the heat exchanger with the built-in metal hydride M2H for generating cold heat to the space to be cooled and the regenerator are arranged in parallel in the cooling process,
The operating conditions in FIG. 2 (refrigeration capacity 500 Kcal /
h, air condition 10 ° C., 80%), by using a regenerator material having a freezing point of about 3 ° C., the circulating air volume to the space to be cooled in the cooling process is about 2 m 3 / min, and the circulating air volume of the regenerator is about 15 m 3. / Min, and the regenerator in the regeneration process
The amount of circulating air in the space to be cooled may be about 4 m 3 / min.
【0013】以上のように、図3のような運転方式にす
れば、図2のような運転方式に比べ、冷房運転時の被冷
却空間内の循環風量が大幅に少なくなり(特に再生過程
において)、ファン動力、騒音、被冷却空間内の物体に
及ぼす風圧の影響が低減され、システムの総合効率の向
上にもつながる。As described above, the operation method as shown in FIG. 3 greatly reduces the amount of circulating air in the space to be cooled during the cooling operation (particularly in the regeneration process) as compared with the operation method as shown in FIG. ), Fan power, noise, and the effect of wind pressure on objects in the space to be cooled are reduced, leading to an improvement in the overall efficiency of the system.
【0014】次に図4は、本発明の装置による暖房運転
方式を示したもので、まず最初に図4aのようなダンパ
ー4〜8による空気流路制御により、M1H側を暖房空
間13と熱交換させるように、またM2H側を外気と熱
交換させるようにし、バルブ2を開けると平衡圧の関係
はM2H>M1HであるからM1H側は水素を吸蔵して
発熱し、空間13を暖房する。このときM2H側では水
素を放出して吸熱反応が起こるが、外気より熱を供給す
ることによってM1H側との平衡圧差が保たれる。Next, FIG. 4 shows a heating operation method using the apparatus of the present invention. First, the M1H side is connected to the heating space 13 by the air flow control by the dampers 4 to 8 as shown in FIG. When the valve 2 is opened, the relationship between the equilibrium pressures is M2H> M1H, so that the M1H side absorbs hydrogen and generates heat, thereby heating the space 13. At this time, the endothermic reaction occurs by releasing hydrogen on the M2H side, but the equilibrium pressure difference with the M1H side is maintained by supplying heat from the outside air.
【0015】次にM2H側からM1H側へ水素が移動し
終わった後、バルブ2を閉じ、ダンパーの切り換えによ
って図4bのようにM1H側へ高温空気を流し、M2H
側は暖房空間13と熱交換されるようにすると、平衡圧
の関係は逆転し、M2H側の圧力はM1H側の圧力より
小さくなる。このとき再びバルブ2を開けると水素はM
1H側からM2H側へと移動し、M2H側は水素を吸蔵
し、発熱し空間13を暖房する。Next, after the hydrogen has been moved from the M2H side to the M1H side, the valve 2 is closed, and by switching the damper, high-temperature air is flown to the M1H side as shown in FIG.
If the side is made to exchange heat with the heating space 13, the relationship of the equilibrium pressure is reversed, and the pressure on the M2H side becomes smaller than the pressure on the M1H side. At this time, if valve 2 is opened again, hydrogen
It moves from the 1H side to the M2H side, and the M2H side absorbs hydrogen, generates heat, and heats the space 13.
【0016】このように金属水素化物と蓄冷器、および
金属水素化物と空間13の循環をそれぞれ別経路にする
と、暖房時もはダンパー15、16を閉じることによっ
て金属水素化物からの出熱は蓄冷器3を通らず、空間1
3のみを循環することになり、蓄冷材、および蓄冷器に
よる顕熱損失を防ぐことができる。As described above, when the circulation of the metal hydride and the regenerator and the circulation of the metal hydride and the space 13 are made different routes, the heat output from the metal hydride is stored by closing the dampers 15 and 16 even during heating. Space 1 without passing through vessel 3
Since only 3 is circulated, sensible heat loss due to the cold storage material and the cold storage device can be prevented.
【0017】このように暖房モードでは図3abの両過
程において金属水素化物の発熱を利用することができ
る。As described above, in the heating mode, the heat generated by the metal hydride can be used in both processes of FIG. 3ab.
【0018】尚、これ等の実施例において再生過程は高
温空気を送ることで行っているが、これはヒータ等の直
接加熱によって行っても良い。Although the regeneration process is performed by sending high-temperature air in these embodiments, it may be performed by direct heating with a heater or the like.
【0019】[0019]
【発明の効果】以上述べた如く本発明によれば、金属水
素化物と蓄冷器とを組み合わせた冷房装置のファン動力
の低減(総合効率の向上)、騒音の低減、被冷却空間内
の風圧の低減(実用性の向上)を行うことができる。As described above, according to the present invention, the fan power of the cooling device combining the metal hydride and the regenerator (improving the overall efficiency), the noise, and the wind pressure in the space to be cooled are reduced. Reduction (improvement of practicality) can be performed.
【図面の簡単な説明】[Brief description of the drawings]
【図1】本発明の冷房装置に用いられる2種類の金属水
素化物の水素圧力−温度平衡特性図である。FIG. 1 is a hydrogen pressure-temperature equilibrium characteristic diagram of two kinds of metal hydrides used in a cooling device of the present invention.
【図2】従来の冷暖房装置の動作を説明する動作説明図
である。FIG. 2 is an operation explanatory diagram illustrating an operation of a conventional cooling and heating device.
【図3】本発明による冷房装置の動作を説明する動作説
明図である。FIG. 3 is an operation explanatory diagram illustrating the operation of the cooling device according to the present invention.
【図4】本発明による冷房装置の動作を説明する動作説
明図である。FIG. 4 is an operation explanatory diagram illustrating an operation of the cooling device according to the present invention.
1a 第1の熱交換器 1b 第2の熱交換器 2 バルブ 3 蓄冷器 4 ダンパー 5 ダンパー 6 ダンパー 7 ダンパー 8 ダンパー 9 ダクト 11 ファン 12 ファン 13 ファン 14 水素配管 15 ダンパー 16 ダンパー 1a first heat exchanger 1b second heat exchanger 2 valve 3 regenerator 4 damper 5 damper 6 damper 7 damper 8 damper 9 duct 11 fan 12 fan 13 fan 14 hydrogen pipe 15 damper 16 damper
───────────────────────────────────────────────────── フロントページの続き (72)発明者 大隅 正人 守口市京阪本通2丁目18番地 三洋電機 株式会社内 (56)参考文献 特開 昭63−183353(JP,A) 特開 平4−28973(JP,A) (58)調査した分野(Int.Cl.6,DB名) F25B 17/12 F25D 11/00 101──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Masato Osumi 2--18 Keihanhondori, Moriguchi City Sanyo Electric Co., Ltd. (56) References JP-A-63-183353 (JP, A) JP-A-4-28973 (JP, A) (58) Field surveyed (Int. Cl. 6 , DB name) F25B 17/12 F25D 11/00 101
Claims (1)
した第1の熱交換器と、水素吸蔵圧力の高い金属水素化
物を内蔵した第2の熱交換器と、これら、第1、第2の
熱交換器間の水素経路を形成する水素配管と、上記第1
の熱交換器に高温を付与する高温付与手段と、上記第2
の熱交換器を冷却する冷却手段と、上記第2の熱交換器
及び被冷却空間と熱交換可能な蓄冷器と、上記第2の熱
交換器、上記蓄冷器及び被冷却空間からなり、上記蓄冷
器と被冷却空間とを並列に設けてなる空気循環経路と、
上記第2の熱交換器、上記蓄冷器及び被冷却空間の熱交
換状態を切り換える切り換え手段と、を設けてなる冷房
装置。1. A first heat exchanger containing a metal hydride having a low hydrogen storage pressure, a second heat exchanger containing a metal hydride having a high hydrogen storage pressure, and the first and second heat exchangers. A hydrogen pipe forming a hydrogen path between the heat exchangers of the first embodiment;
Means for applying a high temperature to the heat exchanger of
Cooling means for cooling the heat exchanger, a regenerator capable of exchanging heat with the second heat exchanger and the space to be cooled, and the second heat exchanger, the regenerator and the space to be cooled. An air circulation path in which a regenerator and a space to be cooled are provided in parallel,
A cooling device comprising: the second heat exchanger, the regenerator, and switching means for switching a heat exchange state of the space to be cooled.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14006691A JP2858995B2 (en) | 1991-06-12 | 1991-06-12 | Cooling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14006691A JP2858995B2 (en) | 1991-06-12 | 1991-06-12 | Cooling device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04366371A JPH04366371A (en) | 1992-12-18 |
| JP2858995B2 true JP2858995B2 (en) | 1999-02-17 |
Family
ID=15260186
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14006691A Expired - Fee Related JP2858995B2 (en) | 1991-06-12 | 1991-06-12 | Cooling device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2858995B2 (en) |
-
1991
- 1991-06-12 JP JP14006691A patent/JP2858995B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04366371A (en) | 1992-12-18 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |