JPH04366371A - Cooling device - Google Patents

Cooling device

Info

Publication number
JPH04366371A
JPH04366371A JP14006691A JP14006691A JPH04366371A JP H04366371 A JPH04366371 A JP H04366371A JP 14006691 A JP14006691 A JP 14006691A JP 14006691 A JP14006691 A JP 14006691A JP H04366371 A JPH04366371 A JP H04366371A
Authority
JP
Japan
Prior art keywords
heat
cold
heat exchanger
space
cooling
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
JP14006691A
Other languages
Japanese (ja)
Other versions
JP2858995B2 (en
Inventor
Koji Akashi
幸治 明石
Naoki Ko
直樹 広
Masakazu Morozu
昌和 諸頭
Masato Osumi
正人 大隅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP14006691A priority Critical patent/JP2858995B2/en
Publication of JPH04366371A publication Critical patent/JPH04366371A/en
Application granted granted Critical
Publication of JP2858995B2 publication Critical patent/JP2858995B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Abstract

PURPOSE:To carry out efficient heating and cooling operation by feeding cold heat generated in a pair of heat exchangers which store mechanical hydride separately to a cold heat accumulator on one side ti cooling service on the other side by war of different routes and circulating the heat generated from the metallic hydride heating operation without passing through the cold accumulator. CONSTITUTION:A heat exchanger 1a which stores metallic hydride M1H with a lower hydrogen occlusion pressure is connected to a heat exchanger 1b which stores high pressure metallic hydride 2H by means of a hydrogen piping 14. Inthis case, the cold heat of the hear exchanger 1b is supplied to a cold heat accumulator 3 on one side whereas it is supplied to the cooling service for a space 13 to be cooled on the other side. In the regeneration process, dampers 15 and 16 are changed over so as to supply cold heat from a cold accumulation material of the cold heat accumulator 3. During heating operation, the dampers 15 and 16 are changed over so that no cold heat may pass through the cold heat accumulator 3. A heat circulation passage is controlled by means of dampers 4 to 8 so that the heat exchanger 1a side may heat-exchange with the heating space 13 while the heat exchanger 1b side may heat-exchange with outside air.

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 that combines a metal hydride and a regenerator 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。
[Prior Art] For example, in Japanese Patent Application No. 2-131664, a metal hydride and a cold storage material are combined, and the cold heat generated by the metal hydride during the cooling process is used to simultaneously cool the space to be cooled and store the cold in the cold storage material. In the regeneration process in which hydrogen is returned to the heat exchanger for cooling generation, a device has been proposed that cools the space to be cooled using cold energy stored in a cold storage material.

【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。
This device is shown in FIG. In the same figure,
In order to exchange heat between the metal hydride M2H side and the cooling space 13 and the storage unit 3 through the air path as shown in FIG. 2a, and
Metal hydride M1H is caused to exchange heat with the outside air, and when valve 2 is opened, M2H releases hydrogen endothermically due to the equilibrium pressure difference between both metal hydrides M1H and M2H, and M1H absorbs hydrogen exothermically. As a result, the cooling space is cooled and heat is removed from the cooler 3. At this time, by setting the temperature of the cooling air to be lower than the solidification temperature of the cold material, the cold material is solidified.

【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 finished moving from the M2H side to the M1H side, the valve 2 is closed and the dampers 4 to 8 are switched to flow high temperature air to the M1H side as shown in FIG.
When outside air flows to the M2H side, the equilibrium pressures on the M1H side and M2H side are reversed. At this time, when valve 2 is opened, hydrogen becomes M1H.
It moves from the side to the M2H side, and returns to the initial state in FIG. 2 after the movement is completed. Further, at this time, cooling is not generated from the metal hydride, but cooling is performed by extracting the cold heat (heat of fusion of the cold storage material) stored in the cold storage in the process shown in 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。
[0005] At this time, suppose the refrigerating capacity is 500Kcal.
/h, and if the air condition in the cooled space is maintained at 10℃ and the relative temperature is 80%, then using a cold storage material with a freezing point of about 9℃, the circulating air volume in the cooled space during the cooling process will be about 4m.
3/min, the circulating air volume in the space to be cooled during the regeneration process must be approximately 70 m3/min.
The influence of wind pressure on fan power, noise, and objects within the space to be cooled is 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。
[Problem to be solved by the invention] However, patent application No. 2-
In the heating and cooling system shown in No. 131664, the temperature in the space to be cooled is kept constant through a cooling process that uses the cold heat generated by metal hydrides and a regeneration process that uses the cold heat stored in the cold storage material. requires a large amount of air circulation into the cooled space during the regeneration process, and air circulation with the regenerator also occurs during heating, so the amount of sensible heat in the regenerator and the regenerator is lost compared to the heating heat output. 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。
[0007] The present invention has been made in view of these points, and in the cooling process, the cold heat generated from the metal hydride is circulated through separate routes for cooling the space to be cooled and for storing the cold in the cold storage material. Also, during heating, the heat generated from the metal hydride is circulated to the heated space 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。
[Means for Solving the Problems] The present invention provides a first heat exchanger containing a metal hydride with a low hydrogen storage pressure, and a second heat exchanger containing a metal hydride with a high hydrogen storage pressure. , hydrogen piping forming a hydrogen path between the first and second heat exchangers, high temperature application means for applying high temperature to the first heat exchanger, and cooling the second heat exchanger. a cooling means, a regenerator capable of exchanging heat with the second heat exchanger and the space to be cooled, the second heat exchanger, the regenerator, and the space to be cooled; and a switching means for switching the heat exchange state of the second heat exchanger, the regenerator, and the space to be cooled.

【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。
[Operation] With this configuration, the cold heat generated by a pair of cooling blocks made of metal hydrides is routed through separate routes, one for storing cold in the cold storage material, and the other for cooling the space to be cooled. If the cold energy stored in the cold storage material is supplied to the space to be cooled during the regeneration process, a stable supply of cold energy can be achieved with a relatively small amount of circulating air inside the refrigerator. moreover,
By providing a damper or the like, during heating operation, the heat output from the metal hydride does not pass through the regenerator and is circulated only with the space to be heated, thereby allowing heating operation with less sensible heat loss due to the regenerator and cold storage material.

【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] Examples of the present invention will be described below with reference to the drawings. First, Figure 1 shows metal hydrides M1H and M2 used in the present invention.
Figure 3 shows the temperature-equilibrium pressure characteristics of H and the cycle diagrams for cooling and heating, respectively. Figure 3 shows the configuration of a heating and cooling system constructed using a metal hydride having the characteristics shown in Figure 1, and its cooling and heating. The operating status 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 explained. In these figures, 1a and 1b are the first and second heat exchangers filled with the metal hydrides M1H and M2H shown in FIG. 1, respectively, and the metal hydride containers ( (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 containing metal hydride M2H for generating cold heat to the space to be cooled and the regenerator are arranged in parallel in the cooling process,
Operating conditions in Figure 2 above (refrigeration capacity 500Kcal/
h, air condition 10℃, 80%), by using a cold storage material with a freezing point of approximately 3℃, the circulating air volume to the space to be cooled during the cooling process can be reduced to approximately 2 m3/min, and the circulating air volume of the regenerator to approximately 15 m3/min. The regenerator in the regeneration process
The amount of circulating air in the space to be cooled may be approximately 4 m3/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。
[0013] As described above, when the operating system as shown in Fig. 3 is used, the amount of circulating air in the space to be cooled during cooling operation is significantly reduced compared to the operating system as shown in Fig. 2 (particularly in the regeneration process). ), fan power, noise, and the effects 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 controlling the air flow path using the dampers 4 to 8 as shown in FIG. 4a. When the valve 2 is opened, the equilibrium pressure relationship is M2H>M1H, so the M1H side absorbs hydrogen and generates heat, heating the space 13. At this time, hydrogen is released on the M2H side and an endothermic reaction occurs, 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 finished moving from the M2H side to the M1H side, valve 2 is closed, and the damper is switched to flow high temperature air to the M1H side as shown in Figure 4b.
When heat is exchanged with the heating space 13 on the side, the relationship of equilibrium pressures is reversed, and the pressure on the M2H side becomes smaller than the pressure on the M1H side. At this time, when valve 2 is opened again, the hydrogen is
It moves from the 1H side to the M2H side, and the M2H side absorbs hydrogen and generates heat to heat 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。
[0016] In this way, if the metal hydride and the regenerator and the metal hydride and the space 13 are circulated through separate routes, the dampers 15 and 16 are closed during heating, so that the heat output from the metal hydride is stored in the cold storage. Space 1 without passing through vessel 3
3 is circulated, and 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 utilized in both processes shown in 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。
In these embodiments, the regeneration process is carried out by sending high-temperature air, but this may also be carried out 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。
Effects of the Invention As described above, according to the present invention, it is possible to reduce the fan power (improve the overall efficiency) of a cooling device that combines a metal hydride and a regenerator, reduce noise, and reduce the wind pressure in the space to be cooled. reduction (improvement of practicality).

【図面の簡単な説明】[Brief explanation of 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 types of metal hydrides used in the 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 the operation of a conventional heating and cooling 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 the operation of the cooling device according to the present invention.

【符号の説明】[Explanation of symbols]

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 piping 15 Damper 16 Damper

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  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、を設けてなる冷
房装置。
Claim 1: A first heat exchanger containing a metal hydride with a low hydrogen storage pressure; a second heat exchanger containing a metal hydride with a high hydrogen storage pressure;
a hydrogen pipe forming a hydrogen path between the heat exchangers; a high temperature application means for applying a high temperature to the first heat exchanger; a cooling means for cooling the second heat exchanger; An air circulation system comprising a heat exchanger and a regenerator capable of exchanging heat with the cooled space, the second heat exchanger, the regenerator, and the cooled space, and the regenerator and the cooled space are provided in parallel. A cooling device comprising: a path; and switching means for switching the heat exchange state of the second heat exchanger, the regenerator, and the space to be cooled.
JP14006691A 1991-06-12 1991-06-12 Cooling device Expired - Fee Related JP2858995B2 (en)

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 true JPH04366371A (en) 1992-12-18
JP2858995B2 JP2858995B2 (en) 1999-02-17

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JP14006691A Expired - Fee Related JP2858995B2 (en) 1991-06-12 1991-06-12 Cooling device

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JP2858995B2 (en) 1999-02-17

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