JPH0350465A - Control of air conditioner - Google Patents
Control of air conditionerInfo
- Publication number
- JPH0350465A JPH0350465A JP18502689A JP18502689A JPH0350465A JP H0350465 A JPH0350465 A JP H0350465A JP 18502689 A JP18502689 A JP 18502689A JP 18502689 A JP18502689 A JP 18502689A JP H0350465 A JPH0350465 A JP H0350465A
- Authority
- JP
- Japan
- Prior art keywords
- compressor
- metal
- hydrogen
- pump
- metal container
- 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
Links
- 229910052751 metal Inorganic materials 0.000 claims abstract description 55
- 239000002184 metal Substances 0.000 claims abstract description 55
- 239000001257 hydrogen Substances 0.000 claims description 42
- 229910052739 hydrogen Inorganic materials 0.000 claims description 42
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 40
- 229910052987 metal hydride Inorganic materials 0.000 claims description 22
- 150000004681 metal hydrides Chemical class 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 13
- 238000004378 air conditioning Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- 230000007423 decrease Effects 0.000 abstract description 6
- 238000007906 compression Methods 0.000 description 10
- 230000006835 compression Effects 0.000 description 9
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000005070 ripening Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical group N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- -1 metal hydride MH2 Chemical class 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】
「R業上の利用分野]
この発明は金属水素化物の吸熱作用及び発熱作用を利用
した冷暖房装置の制御方法に関するものである.
[従来の技術]
一般に、金属単体又は合金(以下、単に金属という)は
水素を吸蔵し,金屈水素化物を作ることが知られている
.又、使用環境温度で可逆的に、水素を放出する.この
金属水素化物より水素を放出する過程は、吸熱過程であ
り、逆に水素を吸蔵する過程は発熱過程である.すなわ
ち、放出
(Mit ) 十Q : (M) +nt吸藏
(Mは金属単体又は合金を示す)
なる関係がある.
ここで、金属(M)に対して水素雰囲気圧力を高くする
か、又は雰囲気温度を低くすれば、水素を吸蔵し易くな
る(前記の左向き反応》.又、金属水素化物( M l
−1 >に対して水素雰17ft気l.1{力を低くず
るか、又は雰囲気温度を高くすれば、水素を放出し易く
なる〈前式の右向き反応〉.以上の原理を用いた冷暖房
装置として特開昭61−119955号公報に開>71
されたものがある.この冷暖房装置の原理は、第3図に
示すように金属水素化物(Mlll)2,(MH2)4
を内蔵させた2つの熟交換型の金属容2i!1.3間に
圧縮816(又はポンプ)を説け、前j己圧縮R6より
水素の流れを切換え反転させ、金属水素化物MHIから
水素が放出過程にある金属容器1を介して冷房し、金属
水素化物M }l 2に水素が吸蔵過程にある金属容8
3を介して暖房する.
[発明が解決しようとする課題]
ところが、前述した冷暖房装置においては、冷房時に圧
縮機で強制的に金属水素化物MHIから水素を抜こうと
した場合、圧縮機の効率が極端に低下するという問題が
あった.すなわち、低圧側金属容器1内の水素雰囲気圧
力Pが第4図に示すようにP1の状態において止縮機6
により水素を抜き始め、金属容器1内の托力を低下させ
たとすると、金属容器1内では水素放出反応が活性化し
、吸熱が進行するので、同図に示すように自動的に圧力
が低下して低い圧力P2に達した時、飽和してしまい、
その後、圧縮vA6を運転し続けても、圧縮1!QI体
の問題として吐出量が減少して、圧縮機の効率ηく前記
騙動エネルギーに対する水素吐出景の比〉が第4図に示
すようにi端に低下するという問題があった.
上記問題を解消するため本願出願人は最近、金属容器内
の水素雰囲気圧力等の圧縮機の効率を間接的に検出する
効率センサからの検出信号が第1設定値となったとき、
前記圧縮槻を停止又はその容量を減少させ、その後、前
記効率センサからの検出信号が第1設定鎖よりも高い第
2設定値となったとき、前記圧amを起動又はその容量
をアップさせる動作を交互に行うことにより、LL a
mの効率の高いところのみで運転ずる制御方法を発明
した.
ところが、この制御方法には運転効率を向上することが
できるという優れた効果があるが、金属容器内の爆発性
の高い水素の圧力を検出するセンサとして防爆対策を備
えた高価なものを使用ずる必要があり、かつ制御上も入
力接点数が増加するため、制御装置のコストダウンを図
ることができないという別の問題が発生した.
この発明の目的は、安価な制御装置により圧縮機の運転
効率を向上することができる冷暖房装置の制御方法を提
供することにある.
[課題を解決するための手段]
この発り1は、上記目的を達成するため、金属水素化物
を内蔵した2以上の金属容器を圧縮機又はボン1を介し
て連結し、前記金属容器にはそれぞれ熱交換器を設け、
該熱交換器には室内用熱交換器を接続した冷I!!房装
置において、前記江縮機又はポンプの起動後タイマーに
より設定された所定時間圧縮機又はポンプの運転を行い
、前記タイマーがタイムアップしたとき、前記圧a機又
はポンプを停止又はその容量を減少させる動作と、この
動作からタイマーにより設定された所定時間経過後、前
記圧縮機又はポンプを起動又はその容量を増大させる動
作とを交互に行うという方法をとっている,
F作用]
この発明はタイマーにより圧縮機の効率が高い領域にお
いて圧縮機の断続運転又は容量増減運転が行われるので
、圧faRの運転効率を向−ヒさせることができるとと
もに、制御装置もタイマーを快用するのみで済むため、
安価に製造することができる.
[実施例]
以下、この発明を具体化したー・実施例を第1図及び第
2図に基づいて説明する.
第2図に示すように金属容器l内には金属水素化物(M
}11)2が収容され、金属容器3内には金属水素化物
(MH2)4が収容されている。前記両容器内部の空気
は窒素ガスで置換した後、水素ガスでさらに置換し、金
属容器lにのみ水素が飽和状態になるように水素供給口
(図示略)より供給し、完全密閉型としている.前記両
金属容器1,3は強制移動用管5により連通され、該移
動用管5には第1バルブ■1と圧縮機6が設番ラられて
いる.そして、前記第1バルブV1を開放し、圧WJn
6を動作させると、金属容器1内が減圧されると同時に
、金属容器3内が加圧状態となる.この時、水素は強制
移動用管5及び第1バルブV1を通って、金属容器1か
ら金属容器3に向って流れ、金属水素化物(M}II)
2から放出した水素は金屈水素化物(M}12>4に吸
蔵される.この過程で、金属容器1内の温度が低下し、
金属容器3の温度が−E昇ずる.
前記金属水素化物M]!1.MH2として、例えば’T
’iMn+ .s H2.7 、あるいはL a N
i sH−.1等がある.又、水素を吸蔵し得る水素吸
蔵合金は、全てこの発明に含まれる。[Detailed Description of the Invention] "Field of Application in the R Industry" This invention relates to a method for controlling air conditioning equipment that utilizes the endothermic and exothermic actions of metal hydrides. [Prior Art] In general, single metals or It is known that alloys (hereinafter simply referred to as metals) absorb hydrogen and form metal hydrides.They also release hydrogen reversibly at the operating temperature.Hydrogen is released from these metal hydrides. The process of absorbing hydrogen is an endothermic process, and conversely, the process of absorbing hydrogen is an exothermic process.In other words, the relationship is: release (Mit) 1Q: (M) + nt absorption (M indicates a metal or an alloy) Here, if the hydrogen atmospheric pressure is increased or the atmospheric temperature is lowered relative to the metal (M), it becomes easier to absorb hydrogen (the above-mentioned leftward reaction).
-1 > hydrogen atmosphere 17 ft.l. 1 {If the force is lowered or the ambient temperature is raised, it becomes easier to release hydrogen (rightward reaction in the previous equation). A heating and cooling device using the above principle was disclosed in Japanese Patent Application Laid-Open No. 119955/1986>71
There is something that has been done. The principle of this heating and cooling system is that metal hydrides (Mlll)2, (MH2)4 are
Two interchangeable metal containers with built-in 2i! During 1.3, turn on the compression 816 (or pump), switch and reverse the flow of hydrogen from the self-compression R6, and cool the metal hydride MHI through the metal container 1 in which hydrogen is being released. Metallic volume 8 in which hydrogen is in the process of occluding hydrogen in compound M }l 2
Heating is performed via 3. [Problem to be Solved by the Invention] However, in the above-mentioned air conditioning system, when the compressor attempts to forcibly remove hydrogen from the metal hydride MHI during cooling, the efficiency of the compressor is extremely reduced. was there. That is, when the hydrogen atmosphere pressure P in the low-pressure side metal container 1 is P1 as shown in FIG.
Assuming that hydrogen begins to be removed and the force inside the metal container 1 is reduced, the hydrogen release reaction is activated in the metal container 1 and heat absorption progresses, so the pressure automatically decreases as shown in the figure. When it reaches a low pressure P2, it becomes saturated,
After that, even if the compression vA6 continues to be operated, the compression 1! A problem with the QI body is that the discharge amount decreases and the compressor efficiency η (ratio of the hydrogen discharge profile to the deception energy) decreases to the i-end as shown in FIG. In order to solve the above-mentioned problem, the applicant of the present application has recently proposed that when the detection signal from the efficiency sensor that indirectly detects the efficiency of the compressor, such as the pressure of the hydrogen atmosphere inside the metal container, reaches the first set value,
An operation of stopping the compressor or reducing its capacity, and then starting the pressure am or increasing its capacity when the detection signal from the efficiency sensor becomes a second setting value higher than the first setting chain. By alternately performing LL a
We have invented a control method that allows operation only in areas with high efficiency. However, although this control method has the excellent effect of improving operational efficiency, it requires the use of an expensive sensor equipped with explosion-proof measures to detect the pressure of highly explosive hydrogen inside the metal container. Another problem arose in that it was not possible to reduce the cost of the control device, as the number of input contacts increased in terms of control. An object of the present invention is to provide a method of controlling an air-conditioning device that can improve the operating efficiency of a compressor using an inexpensive control device. [Means for solving the problem] In order to achieve the above object, this starter 1 connects two or more metal containers containing a metal hydride through a compressor or a bong 1, and the metal container has a Each is equipped with a heat exchanger,
A cold I! indoor heat exchanger is connected to the heat exchanger. ! In the compressor device, after the compressor or pump is started, the compressor or pump is operated for a predetermined time set by a timer, and when the timer times out, the compressor or pump is stopped or its capacity is reduced. The present invention employs a method of alternately performing an operation of starting the compressor or pump or increasing its capacity after a predetermined period of time set by a timer has elapsed from this operation. Since the compressor is operated intermittently or the capacity is increased or decreased in the region where the efficiency of the compressor is high, it is possible to improve the operating efficiency of the pressure faR, and the control device only needs to use a timer. ,
It can be manufactured at low cost. [Example] Hereinafter, an example that embodies this invention will be described based on FIGS. 1 and 2. As shown in Figure 2, metal hydride (M
}11) 2 is housed in the metal container 3, and a metal hydride (MH2) 4 is housed in the metal container 3. After the air inside both containers is replaced with nitrogen gas, it is further replaced with hydrogen gas, and hydrogen is supplied from a hydrogen supply port (not shown) so that only metal container L is saturated with hydrogen, making it a completely sealed type. .. Both metal containers 1 and 3 are communicated by a forced transfer pipe 5, and a first valve 1 and a compressor 6 are installed in the transfer pipe 5. Then, the first valve V1 is opened and the pressure WJn is
6 is operated, the pressure inside the metal container 1 is reduced, and at the same time, the inside of the metal container 3 is pressurized. At this time, hydrogen flows from the metal container 1 to the metal container 3 through the forced transfer pipe 5 and the first valve V1, and the metal hydride (M}II)
The hydrogen released from the metal container 1 is absorbed into the gold-flexible hydride (M}12>4. In this process, the temperature inside the metal container 1 decreases,
The temperature of metal container 3 rises by -E. Said metal hydride M]! 1. As MH2, for example 'T
'iMn+. s H2.7 or L a N
i sH-. There is a 1st prize. Further, all hydrogen storage alloys capable of storing hydrogen are included in the present invention.
さらに、前記両金属容器1.3は圧力差8!lJ用管7
により互いに連通され、第2バルブV2により開閉可能
となっている.前記金属容器1.3にはそれぞれ熟交換
器9.10が設けられ、両熟交挨器9,10は管路を介
して熟媒体切換allに接続され、該熱媒体切換器11
には熱媒体tl?tTM器12を介して送風器13を備
えた熱交yA器14に接続されている.又、熱媒体切換
器11には悲媒体循環器16を介して送風機17を備え
た熱交換815が接続されている.そして、金属容#t
ii内の低下した温度を金属容器1内の熱交換器9によ
り熱媒体切FA2911及び熱媒体循環器l2により熱
交換器14へ熱m送し、送風器13により室内に送り、
夏期に室内を冷房可能である.一方、金属容器3内の上
昇した温度は、金属容器3内の熱交換器lOにより熱媒
体切換器1l及び熱媒体循環器16により熱交換器15
に熟搬送し、送風機17により室内に送り、冬期に室内
のf!房に利用可能である.
前記圧縮機6にはリード線21によりコンピュータをA
61する制御装W22が1′tc続されている.そして
、制御装置22に内蔵したタイマーTの3<定時間に基
づいて、第1.第2バルブVl,V2の開閉時期、圧縮
機6の起動時期あるいは起動後の運転時間、さらには圧
縮機6の停止時間などがIt/J御されるようにしてい
る.
次に、前記のように梢成した冷暖房装置について、その
作用を説明する.
今、金属容at内の圧力が高圧で金属容器3内のn:力
が低圧の状態において、制御装置22からの指令により
第1図の時間toにおいて第2バルブv2がrJM放さ
れると、金属水素化物M}11がら水素が金属水素化物
MH2へ圧力差により移動する.また、前記第2バルブ
V2の開放と同期してタイマー1゛がカウントを開始し
、所定時間(t1》経過後、すなわち、両金属容器1.
3内の水素雰囲気圧力Pが等しくなる圧力P1となる時
期に、IF力差移動用管7の第2バルブ■2を制cn装
置22からの指令により閉鎖するとともに、第1バルブ
V1を開放し、かつ圧縮R6を起動する.すると、圧縮
機6は水素を金屈水素化′#JM}IIがらMII2へ
強制的に移動させ、金属容器1内はさらに冷却され金属
容器3内はさらに発熱される.前記圧11I116の起
動までの時間tlは金属容器1内の水素雰囲気圧力F)
が圧力P1となるまでの時間が予め分っているため、そ
の時間と同じに設定されている.
前記圧縮fi6の起動(時間tl)と同期して制御装I
!22のタイマーTが再びカウントを開始し、設定時間
(t2)が経過してタイムアップすると、制御装置22
から圧縮機6に停止信号が出力されて圧縮機6が停止さ
れる.この停止までの時間についても金属容器1内の水
素雰囲気圧力PがP1から最も低い圧力P2となるまで
の時間が予め分っているため、その時間と同じに設定さ
れている.そして、圧縮機6の停止動作と同期して前記
タイマー1゛が再びカウントを開始し、設定時間t3が
経過してタイムアップするまで圧#1816が停止され
る.この期間に、金属容器1内の金属水素化物MHI内
部で熱交換が進み、その温度が上昇し金属容器1内の水
素雰囲気圧力Pも■)2より高いP3となり、この時点
t3でタイマーTがタイムアップすると、制御装置22
から圧1?l@6に起動信号が出力され、圧縮R6が再
運転され、水素は金属水素化物MHIからM H 2
/\強制的に移動される.この起動(t3)までの時間
についても金属容器1内の水素雰囲気圧力I》が1〕2
からそれより高い圧力P3となるまでの時間が予め分っ
ているため、その時間と回しに段定されている.さらに
、前記タイ゛?−1゛が時間L3がらカウントを開始し
、所定時間〈t4)経過し、水素雰囲気圧力PがP3よ
り低いP2となると、制御装置22から圧縮R6へ再び
停止信号が送られ、圧縮機6が停止され、金屈容器1内
の水素雰囲気圧力PがP2からP3へと上昇される.
以上のような圧縮機6の断続運転動作をタイマー1゛に
より設定された設定侍間to〜unに従って繰り返し行
うことにより、第1図に示すように圧縮機6の効率ηの
高い領域のみで圧縮機6を断続的に運転することができ
、全体として圧縮機の効串を大幅に向上ずることができ
る.
以上のような動作が完了した後、前述した動作と全く逆
の動作により、金属容器3から金属容器1への水素の移
動が圧力差移動用g7により行われ、次に圧縮fi6に
より強制的に水素が移動され、金属容器3開で冷却作用
を、金属容器1 11QIて゛発か作用を行わせるが、
この場合にも前3己タイマー′I゛によりが1述した動
作と同様にしてル縮機6が断続運転されるため、圧縮機
の効率が161+する.なお、この発明は次のように具
体化することもできる.
fl+l記実施例では圧縮1fi6の断続運転を一定時
間繰返したが、これを所定回数繰返ずようにしたり、圧
縮機6を断続運転ずる代わりに、圧縮機の容量を段階的
にあるいは連続的に増減するようにしたりすること。Furthermore, the pressure difference between the two metal containers 1.3 is 8! LJ tube 7
The valves are connected to each other by the valves V2 and can be opened and closed by the second valve V2. Each of the metal containers 1.3 is provided with a ripening exchanger 9.10, and both of the heating medium exchangers 9 and 10 are connected to the ripening medium switch all via a pipe line, and the heating medium switching device 11
Is there a heat medium TL? It is connected to a heat exchanger 14 equipped with an air blower 13 via a tTM device 12. Further, a heat exchanger 815 equipped with an air blower 17 is connected to the heat medium switching device 11 via a sad medium circulator 16. And metal container #t
The reduced temperature inside ii is sent to the heat exchanger 14 by the heat medium cutoff FA2911 and the heat medium circulator l2 by the heat exchanger 9 in the metal container 1, and sent into the room by the blower 13,
It is possible to cool the room in the summer. On the other hand, the increased temperature inside the metal container 3 is transferred to the heat exchanger 15 by the heat medium switching device 1l and the heat medium circulator 16 by the heat exchanger lO in the metal container 3.
It is then transported indoors using a blower 17, and is heated indoors during the winter. It can be used for rooms. A computer is connected to the compressor 6 by a lead wire 21.
61 is connected to the controller W22 for 1'tc. Then, based on the timer T built in the control device 22, 3<fixed time, the first . The opening/closing timing of the second valves Vl and V2, the starting timing of the compressor 6 or the operating time after starting, and the stopping time of the compressor 6 are controlled by It/J. Next, we will explain the operation of the air-conditioning system constructed as described above. Now, when the pressure in the metal container at is high and the pressure n in the metal container 3 is low, when the second valve v2 is released rJM at time to in FIG. 1 by a command from the control device 22, Hydrogen moves from metal hydride M}11 to metal hydride MH2 due to the pressure difference. Further, in synchronization with the opening of the second valve V2, the timer 1' starts counting, and after a predetermined time (t1) has elapsed, that is, both metal containers 1.
At the time when the hydrogen atmosphere pressure P in 3 becomes equal to the pressure P1, the second valve 2 of the IF force difference transfer pipe 7 is closed by a command from the cn control device 22, and the first valve V1 is opened. , and start compression R6. Then, the compressor 6 forcibly moves the hydrogen from the metal container 1 to the MII 2, and the interior of the metal container 1 is further cooled and the interior of the metal container 3 is further heated. The time tl until the activation of the pressure 11I116 is the hydrogen atmosphere pressure F in the metal container 1)
Since the time required for pressure to reach P1 is known in advance, it is set to be the same as that time. In synchronization with the activation of the compression fi6 (time tl), the control device I
! The timer T of 22 starts counting again, and when the set time (t2) elapses and the time is up, the control device 22
A stop signal is output from the compressor 6 to the compressor 6, and the compressor 6 is stopped. The time until this stop is also set to be the same as the time required for the hydrogen atmosphere pressure P in the metal container 1 to go from P1 to the lowest pressure P2 since it is known in advance. Then, in synchronization with the stopping operation of the compressor 6, the timer 1' starts counting again, and the pressure #1816 is stopped until the set time t3 elapses and the time is up. During this period, heat exchange progresses inside the metal hydride MHI in the metal container 1, its temperature rises, and the hydrogen atmosphere pressure P in the metal container 1 also reaches P3, which is higher than ■)2, and at this point t3, the timer T is activated. When the time is up, the control device 22
From pressure 1? A start signal is output to l@6, compressor R6 is restarted, and hydrogen is converted from metal hydride MHI to M H2
/\Forcibly moved. Regarding the time until this startup (t3), the hydrogen atmosphere pressure I》 inside the metal container 1 is 1〕2
Since the time required for the pressure to reach the higher pressure P3 is known in advance, the time and rotation are determined in advance. Furthermore, the said tie? -1 starts counting from time L3, and when a predetermined time <t4) has elapsed and the hydrogen atmosphere pressure P reaches P2, which is lower than P3, the control device 22 sends a stop signal to the compression R6 again, and the compressor 6 starts. The operation is stopped, and the hydrogen atmosphere pressure P in the Konkutsu container 1 is increased from P2 to P3. By repeating the above-described intermittent operation of the compressor 6 according to the setting interval to to un set by the timer 1', compression is achieved only in the region where the efficiency η of the compressor 6 is high, as shown in Fig. 1. The compressor 6 can be operated intermittently, and the efficiency of the compressor as a whole can be greatly improved. After the above-mentioned operations are completed, hydrogen is transferred from the metal container 3 to the metal container 1 by the pressure difference transfer g7 by an operation completely opposite to the above-mentioned operation, and then it is forcibly transferred by the compression fi6. Hydrogen is transferred, and metal container 3 is opened to perform a cooling action, and metal container 1 11QI is used to perform a cooling action.
In this case as well, the compressor 6 is operated intermittently in the same way as the operation described in 1 above by the previous timer 'I', so that the efficiency of the compressor increases to 161+. Note that this invention can also be embodied as follows. In the example described in fl+l, the intermittent operation of compression 1fi6 was repeated for a certain period of time, but instead of repeating this a predetermined number of times, or instead of intermittent operation of the compressor 6, the capacity of the compressor could be increased stepwise or continuously. To increase or decrease.
[発明の効果]
以上訂述したように、この発明は圧縮機又はポンプを断
続運転又は容量増八制御ずることにより、圧縮機又はポ
ンプの運転効串をIt’l iすることができるととも
に、タイマーに上り制御するので制御装置のコストダウ
ンを図ることができる効果がある.[Effects of the Invention] As described above, the present invention can control the operating efficiency of the compressor or pump by intermittent operation or capacity increase control of the compressor or pump, and Since it is controlled by the timer, it has the effect of reducing the cost of the control device.
第l図は本発明の冷暖房装置における圧縮機の運転制御
方法を説明するためのグラフ、第2図は冷暖房装置の一
実施例を示す略体同路図、第3図は従来の冷暖房装置の
基本格成を示ず略体凹路図、第4図は従来の水素雰囲気
圧力と圧縮機の効率との関係を示すグラフである。Fig. 1 is a graph for explaining the compressor operation control method in the air-conditioning system of the present invention, Fig. 2 is a schematic diagram showing an embodiment of the air-conditioning system, and Fig. 3 is a graph of the conventional air-conditioning system. FIG. 4, which is a schematic concave diagram without showing the basic structure, is a graph showing the relationship between the conventional hydrogen atmosphere pressure and the efficiency of the compressor.
Claims (1)
又はポンプを介して連結し、前記金属容器にはそれぞれ
熱交換器を設け、該熱交換器には室内用熱交換器を接続
し、前記圧縮機又はポンプの駆動時に減圧される前記金
属容器内の金属水素化物から水素を放出させ、この水素
を増圧される別の金属容器の金属水素化物に吸蔵させる
過程から得られる低温と高温を熱源として冷房と暖房を
行う冷暖房装置において、 前記圧縮機又はポンプの起動後タイマーにより設定され
た所定時間圧縮機又はポンプの運転を行い、前記タイマ
ーがタイムアップしたとき、前記圧縮機又はポンプを停
止又はその容量を減少させる動作と、この動作からタイ
マーにより設定された所定時間経過後、前記圧縮機又は
ポンプを起動又はその容量を増大させる動作とを交互に
行う冷暖房装置の制御方法。[Scope of Claims] 1. Two or more metal containers containing metal hydrides are connected via a compressor or a pump, each of the metal containers is provided with a heat exchanger, and the heat exchanger is equipped with a heat exchanger for indoor use. A heat exchanger is connected, and hydrogen is released from the metal hydride in the metal container whose pressure is reduced when the compressor or pump is driven, and this hydrogen is stored in the metal hydride in another metal container whose pressure is increased. In an air conditioning system that performs cooling and heating using low and high temperatures obtained from the process as a heat source, after the compressor or pump is started, the compressor or pump is operated for a predetermined period of time set by a timer, and when the timer times out. , an air-conditioning/heating system in which the operation of stopping the compressor or pump or reducing its capacity and the operation of starting the compressor or pump or increasing its capacity after a predetermined time set by a timer has elapsed from this operation are performed. How to control the device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18502689A JP2504202B2 (en) | 1989-07-18 | 1989-07-18 | Control method for air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18502689A JP2504202B2 (en) | 1989-07-18 | 1989-07-18 | Control method for air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0350465A true JPH0350465A (en) | 1991-03-05 |
| JP2504202B2 JP2504202B2 (en) | 1996-06-05 |
Family
ID=16163484
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18502689A Expired - Lifetime JP2504202B2 (en) | 1989-07-18 | 1989-07-18 | Control method for air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2504202B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006111773A3 (en) * | 2005-04-21 | 2007-01-18 | Thermal Energy Systems Ltd | Heat pump |
-
1989
- 1989-07-18 JP JP18502689A patent/JP2504202B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006111773A3 (en) * | 2005-04-21 | 2007-01-18 | Thermal Energy Systems Ltd | Heat pump |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2504202B2 (en) | 1996-06-05 |
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