JPH07253257A - Adsorption type refrigerating apparatus - Google Patents

Adsorption type refrigerating apparatus

Info

Publication number
JPH07253257A
JPH07253257A JP6046877A JP4687794A JPH07253257A JP H07253257 A JPH07253257 A JP H07253257A JP 6046877 A JP6046877 A JP 6046877A JP 4687794 A JP4687794 A JP 4687794A JP H07253257 A JPH07253257 A JP H07253257A
Authority
JP
Japan
Prior art keywords
evaporator
refrigerant
condenser
temperature
adsorption
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
JP6046877A
Other languages
Japanese (ja)
Inventor
Shin Honda
伸 本田
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.)
Denso Corp
Original Assignee
NipponDenso 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 NipponDenso Co Ltd filed Critical NipponDenso Co Ltd
Priority to JP6046877A priority Critical patent/JPH07253257A/en
Publication of JPH07253257A publication Critical patent/JPH07253257A/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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • 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
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To eliminate the possibility of causing a problem in that supplying of a refrigerant liquid to an evaporator is insufficient and the refrigerant liquid is collected in the evaporator, even when heat load is large in an evaporator. CONSTITUTION:When the temperature detected by a temperature sensor 77 of an evaporator 64 is higher than a temperature detected by a temperature sensor 76 of a condenser 58, a solenoid opening and closing valve 75 of a communicating pipe 74 is opened. Then a refrigerant vapor having evaporated in the evaporator 64 flows into the condenser 58 through the communicating pipe 74 to be again condensed. Accordingly, even when a large quantity of refrigerant liquid is supplied to the evaporator 64, it evaporates wholly, and a receiver 60 will not run short of the refrigerant liquid.

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、冷媒を吸・脱着する吸
・脱着器を備えた吸着式冷凍装置に係わり、特に、蒸発
器の熱的負荷が大きい場合の蒸発器への冷媒液の供給不
足を解消するようにした吸着式冷凍装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorption type refrigerating apparatus equipped with an adsorbing / desorbing device for adsorbing / desorbing a refrigerant, and more particularly, to a refrigerant liquid for the evaporator when the thermal load of the evaporator is large. The present invention relates to an adsorption type refrigerating device which is designed to eliminate supply shortage.

【0002】[0002]

【従来の技術】従来の吸着式冷凍装置としては、例えば
実開平5−42966号公報に示されたものがある。同
公報には空気調和用として用いたものが例示されてお
り、これを図4により説明するに、この吸着式冷凍装置
は、内部に吸着剤1,2が充填された第1,第2の吸・
脱着器3,4を備えている。今、第1の吸・脱着器3で
冷媒蒸気を脱着し、第2の吸・脱着器4で冷媒蒸気を吸
着させる場合には、加熱流体が供給パイプ5、三方切換
弁6、第1の吸・脱着器3内に設けられた熱交換器7、
三方切換弁8を経て排出パイプ9から排出されると共
に、冷却流体が供給パイプ10、三方切換弁11、第2
の吸・脱着器4内に設けられた熱交換器12、三方切換
弁13を経て排出パイプ14から排出される。
2. Description of the Related Art As a conventional adsorption type refrigerating apparatus, for example, there is one shown in Japanese Utility Model Laid-Open No. 5-42966. The same publication exemplifies the one used for air conditioning, and this will be described with reference to FIG. 4. In this adsorption type refrigerating apparatus, first and second adsorbents 1 and 2 filled with adsorbents are provided. Sucking
The desorption devices 3 and 4 are provided. When the refrigerant vapor is desorbed by the first adsorber / desorber 3 and the refrigerant vapor is adsorbed by the second adsorber / desorber 4, the heating fluid is supplied to the supply pipe 5, the three-way switching valve 6, and the first A heat exchanger 7 provided in the adsorption / desorption device 3,
The cooling fluid is discharged from the discharge pipe 9 via the three-way switching valve 8, and the cooling fluid is supplied to the supply pipe 10, the three-way switching valve 11, and the second pipe.
It is discharged from the discharge pipe 14 through the heat exchanger 12 and the three-way switching valve 13 provided in the suction / desorption device 4.

【0003】加熱流体が熱交換器7を流通することによ
り、第1の吸・脱着器3内の吸着剤1が加熱され、これ
に吸着されていた冷媒が蒸発して脱着される。この冷媒
蒸気は三方切換弁15を介して凝縮器16に入り、ここ
で供給パイプ10から分流して凝縮器16を経て排出パ
イプ14へと流れる冷却流体と熱交換して凝縮し、冷媒
液となる。凝縮器16から流出した冷媒液はレシーバ1
7に一時的に貯留された後、ポンプ18により蒸発器1
9に供給され、ここで室内空気を冷却することにより蒸
発気化する。この冷媒蒸気は三方切換弁20を経て第2
の吸・脱着器4に入り、吸着材2に吸着される。この冷
媒蒸気の吸着の際に発生する熱は熱交換器12を流通す
る冷却流体に奪い去られる。
When the heating fluid flows through the heat exchanger 7, the adsorbent 1 in the first adsorption / desorption device 3 is heated, and the refrigerant adsorbed by the adsorbent 1 is evaporated and desorbed. This refrigerant vapor enters the condenser 16 via the three-way switching valve 15, where it is branched from the supply pipe 10 and exchanges heat with the cooling fluid flowing to the discharge pipe 14 via the condenser 16 to condense and become the refrigerant liquid. Become. The refrigerant liquid flowing out from the condenser 16 is the receiver 1
After being temporarily stored in the evaporator 7, the evaporator 1 is pumped by the pump 18.
9, the room air is cooled to evaporate and vaporize. This refrigerant vapor is passed through the three-way switching valve 20 to the second
The adsorbing / desorbing device 4 enters and is adsorbed by the adsorbent 2. The heat generated during the adsorption of the refrigerant vapor is taken away by the cooling fluid flowing through the heat exchanger 12.

【0004】上記の運転により、吸着剤1から所定量の
冷媒が脱着され、或いは吸着材2が所定量の冷媒を吸着
すると、各三方切換弁6,8,11,13,15,20
が実線で示す状態から破線で示す状態に切り換えられ
る。これにより前述とは逆に加熱流体が第2の吸・脱着
器4の熱交換器12を流通し、冷却流体が第1の吸・脱
着器3の熱交換器7を流通する状態となるので、第2の
吸・脱着器4が脱着側、第1の吸・脱着器3が吸着側と
なり、吸着剤2から脱着された冷媒蒸気は凝縮器16に
より凝縮された後、蒸発器19で蒸発して吸着剤1に吸
着されるようになり、その吸着時に発生する熱は熱交換
器7を流通する冷却流体に奪い去られる。
By the above operation, when a predetermined amount of refrigerant is desorbed from the adsorbent 1 or when the adsorbent 2 adsorbs a predetermined amount of refrigerant, the three-way switching valves 6, 8, 11, 13, 15, 20.
Is switched from the state shown by the solid line to the state shown by the broken line. As a result, contrary to the above, the heating fluid flows through the heat exchanger 12 of the second adsorption / desorption device 4, and the cooling fluid flows through the heat exchanger 7 of the first adsorption / desorption device 3. , The second adsorption / desorption device 4 is on the desorption side, the first adsorption / desorption device 3 is on the adsorption side, and the refrigerant vapor desorbed from the adsorbent 2 is condensed by the condenser 16 and then evaporated by the evaporator 19. Then, it is adsorbed by the adsorbent 1, and the heat generated during the adsorption is taken away by the cooling fluid flowing through the heat exchanger 7.

【0005】この実開平5−42966号公報に示され
た吸着式冷凍装置では、レシーバ17と蒸発器19の出
口側とがバイパス路21により接続されており、このバ
イパス路21の途中には、電磁開閉弁22が設けられて
いる。このバイパス路21は、運転開始時に電磁開閉弁
22が開放されることにより、レシーバ17内の蒸気を
蒸発器19の出口側に流し、これにより運転開始時に、
レシーバ17及びその周辺の配管で蒸発気化した冷媒蒸
気をポンプ18が吸入することのないようにするための
ものである。
In the adsorption type refrigerating apparatus shown in Japanese Utility Model Laid-Open No. 5-42966, the receiver 17 and the outlet side of the evaporator 19 are connected by a bypass passage 21. In the middle of the bypass passage 21, An electromagnetic opening / closing valve 22 is provided. The bypass passage 21 allows the steam in the receiver 17 to flow to the outlet side of the evaporator 19 by opening the electromagnetic opening / closing valve 22 at the start of the operation, and at the start of the operation,
This is for preventing the pump 18 from sucking the refrigerant vapor that has been vaporized and vaporized in the receiver 17 and the pipes around it.

【0006】[0006]

【発明が解決しようとする課題】ところで、この種の吸
着式冷凍装置では、一般に、ポンプ18による蒸発器1
9への冷媒液供給量は、蒸発器19の熱的負荷が大きい
程、多くなるように制御される。このため、上記の吸着
式冷凍装置では、蒸発器19の温度が高い状態で運転が
開始された場合、ポンプ18はそれに応じた多量の冷媒
を蒸発器19に供給するようになるため、レシーバ17
内の冷媒液が枯渇し、結果として、蒸発器19にその熱
的負荷に見合った多量の冷媒液を送ることができなくな
る。
By the way, in the adsorption type refrigerating apparatus of this type, generally, the evaporator 1 by the pump 18 is used.
The refrigerant liquid supply amount to 9 is controlled to increase as the thermal load on the evaporator 19 increases. Therefore, in the adsorption refrigeration system described above, when the operation is started in a state where the temperature of the evaporator 19 is high, the pump 18 supplies a large amount of refrigerant to the evaporator 19 accordingly, so that the receiver 17
The refrigerant liquid inside is depleted, and as a result, a large amount of refrigerant liquid commensurate with its thermal load cannot be sent to the evaporator 19.

【0007】また、蒸発器19に供給された冷媒液は、
その蒸発器19内で急激に沸騰し、多量の冷媒蒸気を発
生するので、この多量の冷媒蒸気を吸着側の吸着剤が十
分に吸着できなくなり、蒸発器19内の圧力が上昇して
しまう。すると、蒸発器19で冷媒液が完全に蒸発でき
ず、該蒸発器19内に冷媒液が溜まるという現象が生ず
る。特に、図4に示すように、レシーバ17内の冷媒蒸
気をバイパス路21を介して蒸発器19の出口側にバイ
パスさせる構成のものでは、逆に蒸発器19内の圧力を
高めることとなり、蒸発器19内に溜まる冷媒液の増量
化を招くという不具合を生ずる。
The refrigerant liquid supplied to the evaporator 19 is
Since it rapidly boiles in the evaporator 19 and a large amount of refrigerant vapor is generated, the adsorbent on the adsorption side cannot sufficiently adsorb the large amount of refrigerant vapor, and the pressure in the evaporator 19 rises. Then, the refrigerant liquid cannot be completely evaporated in the evaporator 19, and the refrigerant liquid accumulates in the evaporator 19. In particular, as shown in FIG. 4, in the configuration in which the refrigerant vapor in the receiver 17 is bypassed to the outlet side of the evaporator 19 via the bypass passage 21, the pressure in the evaporator 19 is increased, and the evaporation is reversed. This causes a problem that the amount of the refrigerant liquid accumulated in the container 19 is increased.

【0008】上述のような蒸発器19への冷媒供給量不
足、蒸発器19の冷媒液溜まりの現象は、特に自動車用
の空気調和機として用いた場合に顕著に現れ、運転開始
時に車内を急速に冷やしたいという要求に対応できなく
なる。かかる問題を解消するためには、吸着剤1,2の
量を多くして、冷媒蒸気の吸・脱着量が多くなるように
すれば良いが、これでは吸・脱着器1,2が大形化して
しまう。
The above-described phenomena of insufficient refrigerant supply to the evaporator 19 and refrigerant pooling in the evaporator 19 are particularly noticeable when used as an air conditioner for automobiles, and the inside of the automobile rapidly starts when operation is started. It becomes impossible to meet the demand for cooling. In order to solve such a problem, the adsorbents 1 and 2 may be increased in amount so as to increase the adsorption / desorption amount of the refrigerant vapor. Will turn into.

【0009】本発明は上記の事情に鑑みてなされたもの
で、その目的は、吸着剤を多くすることなく、運転開始
時等に蒸発器へ供給すべき冷媒液が不足したり、冷媒液
が蒸発器で蒸発できずに溜まったりするという問題を解
消できる吸着式冷凍装置を提供するにある。
The present invention has been made in view of the above circumstances, and an object thereof is to provide a shortage of the refrigerant liquid to be supplied to the evaporator at the time of starting the operation or to increase the amount of the refrigerant liquid without increasing the adsorbent. It is an object of the present invention to provide an adsorption type refrigerating apparatus which can solve the problem that the vaporizer cannot evaporate and accumulates.

【0010】[0010]

【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、本発明の吸着式冷凍装置は、冷媒蒸気を吸・脱着
する吸着剤が充填された吸・脱着器と、この吸・脱着器
から脱着された冷媒蒸気を凝縮させる凝縮器と、冷媒液
を被冷却流体と熱交換させることにより蒸発させる蒸発
器と、前記凝縮器で凝縮された冷媒液を前記蒸発器に送
るポンプとを備えたものにおいて、前記蒸発器の出口側
と凝縮器の入口側とを連通する連通路を設けると共に、
この連通路を所定時期に開放する開閉手段を設けたこと
を特徴とするものである。
In order to achieve the above object, an adsorption type refrigerating apparatus of the present invention comprises an adsorbing / desorbing device filled with an adsorbent for adsorbing / desorbing refrigerant vapor, and the adsorbing / desorbing device. A condenser for condensing the refrigerant vapor desorbed from the evaporator, an evaporator for evaporating the refrigerant liquid by exchanging heat with the fluid to be cooled, and a pump for sending the refrigerant liquid condensed in the condenser to the evaporator. In the provided, while providing a communication passage for communicating the outlet side of the evaporator and the inlet side of the condenser,
An opening / closing means for opening the communication passage at a predetermined time is provided.

【0011】また、本発明の吸着式冷凍装置は、蒸発器
の温度を検出する温度センサと、この温度センサの検出
温度を基準温度と比較し、温度センサの検出温度が基準
温度を越えたとき、開閉手段を開放する制御手段とを設
けることができる。
Further, the adsorption refrigeration system of the present invention compares a temperature sensor for detecting the temperature of the evaporator with the reference temperature, and when the temperature detected by the temperature sensor exceeds the reference temperature. , And a control means for opening the opening / closing means.

【0012】[0012]

【作用】蒸発器の熱的負荷が大きい場合、開閉手段を開
放する。すると、蒸発器で多量に発生した冷媒蒸気は連
通路を通じて凝縮器に戻されるので、蒸発器内の圧力上
昇を防止でき、また凝縮器に戻された冷媒蒸気はここで
再凝縮してポンプにより蒸発器へと供給されるので、蒸
発器へ供給すべき冷媒液量が不足するおそれもない。
When the thermal load on the evaporator is large, the opening / closing means is opened. Then, a large amount of the refrigerant vapor generated in the evaporator is returned to the condenser through the communication passage, so that the pressure increase in the evaporator can be prevented, and the refrigerant vapor returned to the condenser is re-condensed here by the pump. Since it is supplied to the evaporator, there is no fear that the amount of refrigerant liquid to be supplied to the evaporator will be insufficient.

【0013】この場合、制御手段が温度センサの検出温
度を基準温度と比較し、その検出温度が基準温度を越え
たとき、開閉手段を開放する構成とすれば、蒸発器の熱
的負荷の大小を適正に判断して蒸発器で蒸発気化する冷
媒蒸気量が多い場合に開閉手段を開放することができ
る。
In this case, if the control means compares the detected temperature of the temperature sensor with the reference temperature and opens the opening / closing means when the detected temperature exceeds the reference temperature, the thermal load of the evaporator is large or small. The opening / closing means can be opened when the amount of the refrigerant vapor evaporated and vaporized in the evaporator is large by properly judging the above.

【0014】[0014]

【実施例】以下、本発明をカーエアコンと称される自動
車の空気調和機に適用した一実施例につき、図1〜図3
を参照しながら説明する。吸着式冷凍装置の全体構成は
図1に示されている。同図のように、この吸着式冷凍装
置は、第1及び第2の吸・脱着器31及び32を備えて
いる。これら吸・脱着器31及び32は、中空容器内に
冷媒を吸・脱着する吸着剤33及び34を充填して構成
されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment in which the present invention is applied to an automobile air conditioner called a car air conditioner will be described with reference to FIGS.
Will be described with reference to. The overall structure of the adsorption refrigeration system is shown in FIG. As shown in the figure, this adsorption type refrigerating apparatus is provided with first and second adsorbing / desorbing devices 31 and 32. These adsorbing / desorbing devices 31 and 32 are configured by filling a hollow container with adsorbents 33 and 34 for adsorbing / desorbing a refrigerant.

【0015】なお、冷媒としては、水、水にアルコール
を加えたアルコール水溶液、フロン系冷媒等が用いられ
るが、潜熱の大きい水が好ましく、アルコール水溶液と
した場合には、凍結防止効果がある。また、吸着剤3
3,34としては、冷媒を吸着し易いもの、例えばシリ
カゲル、ゼオライト、活性炭、活性アルミナ等が用いら
れる。
As the refrigerant, water, an alcohol aqueous solution obtained by adding alcohol to water, a chlorofluorocarbon refrigerant, or the like is used. However, water having a large latent heat is preferable, and the alcohol aqueous solution has an antifreezing effect. Also, the adsorbent 3
As 3, 34, a material that easily adsorbs a refrigerant, for example, silica gel, zeolite, activated carbon, activated alumina or the like is used.

【0016】上記第1,第2の吸・脱着器31,32の
内部には、熱交換器35,36が設けられており、これ
ら熱交換器35,36には、エンジンの冷却水が加熱流
体として供給されると共に、車外空気により冷却される
タンクからの水が冷却流体として供給されるようになっ
ている。すなわち、加熱流体の供給パイプ37は三方切
換弁38の入口38aに接続され、その三方切換弁38
の出口38b,38cはそれぞれ熱交換器35,36の
一端側にパイプ39,40を介して接続されている。ま
た、冷却流体の供給パイプ41は三方切換弁42の入口
42aに接続され、その三方切換弁42の出口42b,
42cはそれぞれ熱交換器35,36の一端側にパイプ
43,44を介して接続されている。そして、熱交換器
35,36の他端側は、パイプ45,46を介して三方
切換弁47の入口47a,47bに接続されていると共
に、パイプ48,49を介して三方切換弁50の入口5
0a,50bに接続されており、三方切換弁47の出口
47cには加熱流体をエンジンに戻す排出パイプ51が
接続され、三方切換弁50の出口50cには冷却流体を
タンクに戻す排出パイプ52が接続されている。
Heat exchangers 35 and 36 are provided inside the first and second adsorbing / desorbing devices 31 and 32. The heat exchangers 35 and 36 are heated by engine cooling water. Water is supplied as a fluid, and water from a tank cooled by the air outside the vehicle is supplied as a cooling fluid. That is, the heating fluid supply pipe 37 is connected to the inlet 38 a of the three-way switching valve 38, and the three-way switching valve 38 is connected to the inlet 38 a.
The outlets 38b and 38c are connected to one ends of the heat exchangers 35 and 36 through pipes 39 and 40, respectively. The cooling fluid supply pipe 41 is connected to the inlet 42a of the three-way switching valve 42, and the outlet 42b of the three-way switching valve 42,
42c is connected to one end sides of the heat exchangers 35 and 36 via pipes 43 and 44, respectively. The other ends of the heat exchangers 35 and 36 are connected to the inlets 47a and 47b of the three-way switching valve 47 via the pipes 45 and 46, and the inlet of the three-way switching valve 50 via the pipes 48 and 49. 5
0a, 50b, a discharge pipe 51 for returning the heating fluid to the engine is connected to the outlet 47c of the three-way switching valve 47, and a discharge pipe 52 for returning the cooling fluid to the tank is connected to the outlet 50c of the three-way switching valve 50. It is connected.

【0017】さて、前記第1,第2の吸・脱着器31,
32の一端側は、途中に電磁開閉弁53,54を設けた
流出パイプ55,56を介して三方切換弁57の入口5
7a,57bに接続されており、熱交換器35,36に
よって加熱されることにより吸着剤33,34から脱着
された冷媒蒸気はこれら流出パイプ55,56から流出
する。そして、三方切換弁57の出口57cは冷媒蒸気
を凝縮させるための凝縮器58の入口58aに中間パイ
プ59を介して接続され、凝縮器58の出口58bは凝
縮された冷媒液を一時的に貯留するためのレシーバ60
に中間パイプ61を介して接続されている。
Now, the first and second suction / desorption devices 31,
One end side of 32 is provided with an inlet 5 of a three-way switching valve 57 through outflow pipes 55 and 56 provided with electromagnetic switching valves 53 and 54 on the way.
The refrigerant vapors that are connected to 7a and 57b and are desorbed from the adsorbents 33 and 34 by being heated by the heat exchangers 35 and 36 flow out from these outflow pipes 55 and 56. The outlet 57c of the three-way switching valve 57 is connected to the inlet 58a of the condenser 58 for condensing the refrigerant vapor via the intermediate pipe 59, and the outlet 58b of the condenser 58 temporarily stores the condensed refrigerant liquid. Receiver 60 for
To the intermediate pipe 61.

【0018】上記レシーバ60はポンプ62の吸入口6
2aに吸入パイプ63を介して接続され、このポンプ6
2の出口62bは冷媒液を蒸発させるための蒸発器64
の入口64aに吐出パイプ65を介して接続されてい
る。そして、蒸発器64の出口64bは中間パイプ66
を介して三方切換弁67の入口67aに接続され、この
三方切換弁67の出口67b,67cは電磁開閉弁6
8,69を途中に設けた戻しパイプ70,71を介して
第1,第2の吸・脱着器31,32の他端側に接続され
ている。
The receiver 60 is the suction port 6 of the pump 62.
2a is connected via a suction pipe 63 to the pump 6
The second outlet 62b is an evaporator 64 for evaporating the refrigerant liquid.
Is connected to the inlet 64a of the through a discharge pipe 65. The outlet 64b of the evaporator 64 is connected to the intermediate pipe 66.
Is connected to the inlet 67a of the three-way switching valve 67, and the outlets 67b and 67c of the three-way switching valve 67 are connected to the solenoid opening / closing valve 6
8 and 69 are connected to the other end sides of the first and second suction / desorption devices 31 and 32 via return pipes 70 and 71 provided on the way.

【0019】ここで、前記凝縮器58には、送風機72
により車外空気が吹き当てらるようになっており、凝縮
器58に供給された冷媒蒸気はこの車外空気と熱交換し
て冷却されるようになっている。また、前記蒸発器64
は、被冷却流体、すなわち送風機73により車内に供給
される空気と熱交換してその空気を冷却するように構成
されている。なお、前記三方切換弁38,42,47,
50,57,67は電磁石或いはモータ等を駆動源とす
るものである。
Here, a blower 72 is attached to the condenser 58.
As a result, the air outside the vehicle is blown, and the refrigerant vapor supplied to the condenser 58 is cooled by exchanging heat with the air outside the vehicle. In addition, the evaporator 64
Is configured to exchange heat with the fluid to be cooled, that is, the air supplied into the vehicle by the blower 73 to cool the air. The three-way switching valves 38, 42, 47,
Numerals 50, 57 and 67 are driven by electromagnets or motors.

【0020】しかして、前記蒸発器64の出口64b側
は、連通路としての連通パイプ74により凝縮器58の
入口58a側に接続されており、この連通パイプ74の
途中には、開閉手段としての電磁開閉弁75が設けられ
ている。また、凝縮器58及び蒸発器64には、それぞ
れ温度センサ76及び77が設けられており、これら温
度センサ76,77の検出信号は制御手段としての図示
しない制御回路に入力される。この制御回路はマイクロ
コンピュータを主体とするもので、予め設定されたプロ
グラムに従って吸着式冷凍装置全体の制御を行う。
However, the outlet 64b side of the evaporator 64 is connected to the inlet 58a side of the condenser 58 by a communication pipe 74 as a communication passage, and an opening / closing means is provided in the middle of the communication pipe 74. An electromagnetic opening / closing valve 75 is provided. Further, the condenser 58 and the evaporator 64 are provided with temperature sensors 76 and 77, respectively, and detection signals of these temperature sensors 76 and 77 are input to a control circuit (not shown) serving as control means. This control circuit is mainly composed of a microcomputer and controls the entire adsorption refrigeration system according to a preset program.

【0021】次に上記構成の作用を、制御回路の制御内
容を示す図2のフローチャートをも参照しながら説明す
る。制御回路は、電源投入に伴い、図2のフローチャー
トに示す制御プログラムの実行を開始し、まず吸着式冷
凍装置の運転開始操作がなされたか否かを監視する状態
になり、開始操作がなされるまでの運転停止中は電磁開
閉弁53,54,68,69,75を全て閉状態に維持
する(ステップS1,S2の繰り返し)。そして、制御
回路は、運転開始操作がなされると(ステップS2で
「YES」)、連通パイプ74の電磁開閉弁75を除く
他の電磁開閉弁53,54,68,69を開放し(ステ
ップS3)、三方切換弁38,42,47,50,5
7,67を例えば図1に実線で示す状態にすると共に、
加熱流体及び冷却流体の供給用ポンプ(図示せず)を起
動させて吸着式冷凍装置の運転を開始する(ステップS
4)。なお、制御回路は運転中、蒸発器64の熱的負
荷、例えば温度センサ77の検出温度に応じてポンプ6
2による蒸発器64への冷媒液供給量を制御するように
なっている。
Next, the operation of the above configuration will be described with reference to the flowchart of FIG. 2 showing the control contents of the control circuit. When the power is turned on, the control circuit starts executing the control program shown in the flowchart of FIG. 2, and first becomes in a state of monitoring whether or not the operation start operation of the adsorption refrigeration system is performed, until the start operation is performed. While the operation is stopped, all the solenoid on-off valves 53, 54, 68, 69, 75 are maintained in the closed state (repeat of steps S1 and S2). Then, when the operation start operation is performed (“YES” in step S2), the control circuit opens the other electromagnetic opening / closing valves 53, 54, 68, 69 of the communication pipe 74 excluding the electromagnetic opening / closing valve 75 (step S3). ), Three-way switching valves 38, 42, 47, 50, 5
7 and 67, for example, in the state shown by the solid line in FIG.
A pump (not shown) for supplying the heating fluid and the cooling fluid is started to start the operation of the adsorption refrigeration system (step S).
4). During operation, the control circuit operates according to the thermal load of the evaporator 64, for example, the temperature detected by the temperature sensor 77, to the pump 6
The amount of refrigerant liquid supplied to the evaporator 64 by 2 is controlled.

【0022】さて、図1に実線で示す三方切換弁38,
42,47,50,57,67の切り換え状態は、第1
の吸・脱着器31が冷媒蒸気の脱着側で、第2の吸・脱
着器32が冷媒蒸気の吸着側となる状態であり、加熱流
体が供給パイプ37、三方切換弁38、第1の吸・脱着
器31内に設けられた熱交換器35、三方切換弁47を
経て排出パイプ51から排出されると共に、冷却流体が
供給パイプ41、三方切換弁42、第2の吸・脱着器3
2内に設けられた熱交換器36、三方切換弁50を経て
排出パイプ52から排出される。
Now, the three-way switching valve 38 shown by the solid line in FIG.
The switching state of 42, 47, 50, 57, 67 is the first
In this state, the suction / desorption device 31 is on the refrigerant vapor desorption side and the second suction / desorption device 32 is on the refrigerant vapor adsorption side, and the heating fluid is the supply pipe 37, the three-way switching valve 38, and the first suction valve. -The heat exchanger 35 and the three-way switching valve 47 provided in the desorber 31 are discharged from the discharge pipe 51, and the cooling fluid is supplied to the supply pipe 41, the three-way switching valve 42, and the second suction / desorption device 3.
The heat is discharged from the discharge pipe 52 via the heat exchanger 36 and the three-way switching valve 50 provided in the inside 2.

【0023】加熱流体が熱交換器35を流通することに
より、第1の吸・脱着器31内の吸着剤33が加熱さ
れ、これに吸着されていた冷媒が蒸発して脱着される。
この冷媒蒸気は電磁開閉弁53、三方切換弁57を介し
て凝縮器58に入り、ここで送風機72からの送風空気
と熱交換して凝縮し、冷媒液となる。凝縮器58から流
出した冷媒液はレシーバ60に一時的に貯留された後、
ポンプ62により蒸発器64に供給され、ここで室内空
気を冷却することにより蒸発気化する。この冷媒蒸気は
三方切換弁67、電磁開閉弁69を経て第2の吸・脱着
器32に入り、吸着材34に吸着される。この冷媒蒸気
の吸着の際に発生する熱は熱交換器36を流通する冷却
流体に奪い去られる。
When the heating fluid flows through the heat exchanger 35, the adsorbent 33 in the first adsorber / desorber 31 is heated, and the refrigerant adsorbed by the adsorbent 33 is evaporated and desorbed.
This refrigerant vapor enters the condenser 58 via the electromagnetic on-off valve 53 and the three-way switching valve 57, where it exchanges heat with the air blown from the blower 72 to be condensed and becomes a refrigerant liquid. After the refrigerant liquid flowing out from the condenser 58 is temporarily stored in the receiver 60,
It is supplied to the evaporator 64 by the pump 62, and the room air is cooled there to evaporate and vaporize. This refrigerant vapor enters the second adsorption / desorption device 32 via the three-way switching valve 67 and the electromagnetic opening / closing valve 69, and is adsorbed by the adsorbent 34. The heat generated during the adsorption of the refrigerant vapor is taken away by the cooling fluid flowing through the heat exchanger 36.

【0024】制御回路は、上述のようにして吸着式冷凍
装置の運転を開始すると、次に運転停止操作が成された
か否かを判断するステップS5を実行した後、蒸発器6
4の温度センサ77の検出温度Teを基準温度である凝
縮器58の温度センサ76の検出温度Tcと比較してそ
の大小関係を判断するステップS6を実行する。このス
テップS6において、Te>Tcならば「YES」とな
って連通パイプ74の電磁開閉弁75を開放動作させ
(ステップS7)、Te≦Tcならば「NO」となって
電磁開閉弁75を閉じたままとする(ステップS8)。
When the control circuit starts the operation of the adsorption type refrigerating apparatus as described above, it executes step S5 for judging whether or not the operation of stopping the operation is carried out next, and then the evaporator 6
Step S6 of comparing the detected temperature Te of the temperature sensor 77 of No. 4 with the detected temperature Tc of the temperature sensor 76 of the condenser 58, which is the reference temperature, and judging the magnitude relationship is executed. In step S6, if Te> Tc, "YES" is set and the electromagnetic opening / closing valve 75 of the communication pipe 74 is opened (step S7). If Te≤Tc, "NO" is set and the electromagnetic opening / closing valve 75 is closed. It is left as it is (step S8).

【0025】今、運転開始時において、Te≦Tcであ
るときには、電磁開閉弁75は閉じたままにされるが、
このときには蒸発器64の熱的負荷はそれ程大きくない
ので、ポンプ62から蒸発器64に送られる冷媒液量も
それ程多くはなく、このため、蒸発器64で蒸発気化し
た冷媒蒸気は円滑に第2の吸・脱着器32の吸着剤34
に吸着される。ところが、運転開始時において、Te>
Tcであるときには、蒸発器64の熱的負荷が大きい状
態にあるので、ポンプ62から多量の冷媒液が蒸発器6
4に送られる。
At the start of the operation, when Te ≦ Tc, the electromagnetic opening / closing valve 75 is kept closed,
At this time, since the thermal load of the evaporator 64 is not so large, the amount of the refrigerant liquid sent from the pump 62 to the evaporator 64 is not so large, so that the refrigerant vapor evaporated and vaporized in the evaporator 64 is smoothly transferred to the second Adsorbent 34 of adsorption / desorption device 32
Is adsorbed on. However, at the start of operation, Te>
When it is Tc, the thermal load on the evaporator 64 is large, so that a large amount of the refrigerant liquid is discharged from the pump 62 to the evaporator 6.
Sent to 4.

【0026】そして、蒸発器64に送られた多量の冷媒
液は、ここで急激に沸騰して多量の冷媒蒸気を発生す
る。すると、第2の吸・脱着器32の吸着剤34は、そ
の急激に多量に発生する冷媒蒸気を吸着し切れなくな
り、そのために蒸発器64の圧力が上昇する傾向とな
る。ところが、このときには、制御回路はステップS6
で「YES」と判断し、次のステップS7で連通パイプ
74の電磁開閉弁75を開放しているので、蒸発器64
で蒸発気化した冷媒蒸気は、連通パイプ74を通って低
圧側である凝縮器58の入口58a側に流れ、そして第
1の吸・脱着器31からの冷媒蒸気と共に凝縮器58に
流入し、ここで再び凝縮されてレシーバ60に溜められ
る。
Then, a large amount of the refrigerant liquid sent to the evaporator 64 abruptly boils here to generate a large amount of the refrigerant vapor. Then, the adsorbent 34 of the second adsorbing / desorbing device 32 cannot completely adsorb the rapidly generated refrigerant vapor, and therefore the pressure of the evaporator 64 tends to increase. However, at this time, the control circuit proceeds to step S6.
In step S7, the electromagnetic on-off valve 75 of the communication pipe 74 is opened, so that the evaporator 64 is opened.
The refrigerant vapor that has been vaporized and vaporized in the above flows through the communication pipe 74 to the inlet 58a side of the condenser 58 on the low pressure side, and then flows into the condenser 58 together with the refrigerant vapor from the first adsorber / desorber 31. Is condensed again and stored in the receiver 60.

【0027】このように、蒸発器64で多量の冷媒蒸気
が発生しても、その冷媒蒸気を凝縮器58に戻して再凝
縮させることができる。このため、第2の吸・脱着器3
2の吸着能力に限界があっても、蒸発器64内に冷媒蒸
気が滞って該蒸発器64の内圧が上昇し、この内圧上昇
により蒸発器64に供給された冷媒液が蒸発気化できず
に液のまま溜まるという不具合を生ずるおそれはなく、
蒸発器64内に供給された冷媒液を円滑に蒸発気化させ
ることができる。しかも、蒸発器64の熱的負荷が大き
い場合には、ポンプ62によりレシーバ60から蒸発器
64に送られる冷媒液量が多いという事情があっても、
蒸発器64で蒸発気化した冷媒蒸気は再び凝縮器58で
液化されてレシーバ60に溜まるようになる。このた
め、吸着剤33の冷媒蒸気の供給能力に限界があって
も、レシーバ60の冷媒液が枯渇するおそれはなく、蒸
発器64にその熱的負荷に応じた多量の冷媒液を送るこ
とができる。
As described above, even if a large amount of refrigerant vapor is generated in the evaporator 64, the refrigerant vapor can be returned to the condenser 58 and recondensed. Therefore, the second suction / desorption device 3
Even if the adsorption capacity of 2 is limited, the refrigerant vapor is stagnated in the evaporator 64 and the internal pressure of the evaporator 64 rises, and the refrigerant liquid supplied to the evaporator 64 cannot evaporate and vaporize due to this internal pressure rise. There is no possibility of causing a problem that the liquid remains as it is,
The refrigerant liquid supplied into the evaporator 64 can be smoothly evaporated and vaporized. Moreover, when the thermal load on the evaporator 64 is large, even if there is a large amount of refrigerant liquid sent from the receiver 60 to the evaporator 64 by the pump 62,
The refrigerant vapor evaporated and vaporized in the evaporator 64 is liquefied again in the condenser 58 and accumulated in the receiver 60. Therefore, even if the refrigerant vapor supply capacity of the adsorbent 33 is limited, the refrigerant liquid in the receiver 60 may not be exhausted, and a large amount of refrigerant liquid corresponding to the thermal load can be sent to the evaporator 64. it can.

【0028】そして、この電磁開閉弁75を開いた状態
で運転が継続されることにより蒸発器64の温度が低下
してTe≦Tcになると、制御回路はステップS6で
「NO」と判断し、次のステップS8で電磁開閉弁75
を閉じる。このときには、ポンプ62から蒸発器64へ
の冷媒液供給量は減少し、且つ蒸発器64の温度も低く
なっているので、蒸発器64で蒸発気化した冷媒蒸気は
すべて第2の吸・脱着器32の吸着剤34に円滑に吸着
される。
When the temperature of the evaporator 64 is lowered to Te≤Tc by continuing the operation with the electromagnetic opening / closing valve 75 opened, the control circuit determines "NO" in step S6, In the next step S8, the solenoid on-off valve 75
Close. At this time, the supply amount of the refrigerant liquid from the pump 62 to the evaporator 64 is reduced and the temperature of the evaporator 64 is also lowered, so that all the refrigerant vapor evaporated and vaporized in the evaporator 64 is in the second intake / desorption device. It is smoothly adsorbed by the adsorbent 34 of 32.

【0029】さて、運転開始から所定時間経過すると、
吸着剤33から所定量の冷媒が脱着され、或いは吸着材
34が所定量の冷媒を吸着した状態となるので、制御回
路はステップS4で各三方切換弁38,42,47,5
0,57,67を実線で示す状態から破線で示す状態に
切り換える。これにより、前述とは逆に加熱流体が第2
の吸・脱着器32の熱交換器36を流通し、冷却流体が
第1の吸・脱着器31の熱交換器35を流通する状態と
なるので、第2の吸・脱着器32が脱着側、第1の吸・
脱着器31が吸着側となり、吸着剤34から脱着された
冷媒蒸気が凝縮器58により凝縮された後、蒸発器64
で蒸発して吸着剤33に吸着されるようになり、その吸
着時に発生する熱は熱交換器35を流通する冷却流体に
奪い去られる。
Now, when a predetermined time has passed from the start of operation,
A predetermined amount of the refrigerant is desorbed from the adsorbent 33, or the adsorbent 34 is in a state of adsorbing the predetermined amount of the refrigerant, so that the control circuit in step S4 operates the three-way switching valves 38, 42, 47, 5 respectively.
0, 57 and 67 are switched from the state shown by the solid line to the state shown by the broken line. As a result, contrary to the above, the heating fluid is
Since the cooling fluid flows through the heat exchanger 36 of the first adsorption / desorption device 32 and the cooling fluid flows through the heat exchanger 35 of the first adsorption / desorption device 31, the second adsorption / desorption device 32 is attached to the desorption side. , The first sucker
The desorber 31 is on the adsorption side, and the refrigerant vapor desorbed from the adsorbent 34 is condensed by the condenser 58, and then the evaporator 64.
Then, it is evaporated and is adsorbed by the adsorbent 33, and the heat generated during the adsorption is taken away by the cooling fluid flowing through the heat exchanger 35.

【0030】このように、第1,第2の吸・脱着器3
1,32を交互に脱着側、吸着側とする運転を繰り返す
ことにより、吸着剤33,34が交互に冷媒の脱着及び
吸着を繰り返し、蒸発器64により車内が冷却される。
このような運転中、蒸発器64の温度センサ77の検出
温度Teが凝縮器58の温度センサ76の検出温度Tc
を越えた場合には、上述のようにして連通パイプ74の
電磁開閉弁75が開放される。そして、運転停止操作が
なされると、制御回路はステップS5で「YES」と判
断してステップS1に戻り、電磁開閉弁53,54,6
8,69,75を閉じると共に、加熱流体及び冷却流体
の供給用ポンプを停止させる。
Thus, the first and second suction / desorption devices 3
By repeating the operation in which 1 and 32 are alternately on the desorption side and the adsorption side, the adsorbents 33 and 34 alternately repeat desorption and adsorption of the refrigerant, and the interior of the vehicle is cooled by the evaporator 64.
During such operation, the temperature Te detected by the temperature sensor 77 of the evaporator 64 is the temperature Tc detected by the temperature sensor 76 of the condenser 58.
When it exceeds the value, the electromagnetic opening / closing valve 75 of the communication pipe 74 is opened as described above. Then, when the operation to stop the operation is performed, the control circuit determines “YES” in step S5, returns to step S1, and returns to the electromagnetic opening / closing valves 53, 54, 6
8, 69 and 75 are closed and the pumps for supplying the heating fluid and the cooling fluid are stopped.

【0031】このように本実施例によれば、蒸発器64
の熱的負荷が大きい場合には、電磁開閉弁75を開放し
て蒸発器64で蒸発気化した冷媒蒸気を凝縮器58の入
口58a側に戻すので、レシーバ60の冷媒液不足の問
題を生ずることなく、蒸発器64に多量の冷媒液を供給
してこれをすべて蒸発気化させることができ、当該蒸発
器64により冷却された空気の供給を受ける車内も早期
に温度低下する。
As described above, according to this embodiment, the evaporator 64
When the thermal load is large, the electromagnetic on-off valve 75 is opened to return the refrigerant vapor evaporated and vaporized in the evaporator 64 to the inlet 58a side of the condenser 58, which causes a problem of insufficient refrigerant liquid in the receiver 60. Instead, it is possible to supply a large amount of refrigerant liquid to the evaporator 64 and to vaporize and vaporize the entire liquid, and the temperature of the interior of the vehicle receiving the air cooled by the evaporator 64 is also lowered at an early stage.

【0032】図3は本発明の吸着式冷凍装置による場合
と、従来の吸着式冷凍装置による場合とで、蒸発器の熱
的負荷が大きいとき、その運転開始からの時間経過に伴
う車内温度の変化を実測した結果を示すもので、同図か
ら、実線で示す本発明によるものの方が、破線で示す従
来のものよりも、早期に温度低下し、冷却の立上り性に
優れることが理解される。
FIG. 3 shows the temperature inside the vehicle with the elapse of time from the start of the operation when the thermal load on the evaporator is large in the case of the adsorption refrigeration system of the present invention and in the case of the conventional adsorption refrigeration system. From the figure, it is understood that the present invention shown by the solid line has a lower temperature and a superior cooling rising property than the conventional one shown by the broken line. .

【0033】また、特に本実施例では、電磁開閉弁75
の開放時期を、蒸発器64の温度センサ77の検出温度
Teと凝縮器58の温度センサ76の検出温度TCとの
比較により判断するようにしたので、蒸発器64の熱的
負荷が大きく多量の冷媒蒸気が急激に発生する時期を適
正に判断して連通パイプ74の電磁開閉弁75を開放す
ることができる。
Further, particularly in this embodiment, the solenoid opening / closing valve 75
Is determined by comparing the temperature Te detected by the temperature sensor 77 of the evaporator 64 and the temperature TC detected by the temperature sensor 76 of the condenser 58, the thermal load of the evaporator 64 is large and a large amount of The electromagnetic opening / closing valve 75 of the communication pipe 74 can be opened by properly determining the time when the refrigerant vapor is rapidly generated.

【0034】なお、本発明は、上記の各実施例に限定さ
れるものではなく、次のように変形または拡張できる。
蒸発器64の温度センサ77の検出温度と比較する基準
温度は一定温度としても良い。温度センサ76,77は
凝縮器58,蒸発器64の表面温度を検出するようにし
たが、これに限らず、例えば凝縮器58,蒸発器64を
流れる冷媒温度を検出すること、或いは凝縮器58,蒸
発器64と熱交換した後の空気温度を検出することによ
り、凝縮器58,蒸発器64の温度を検出するようにし
ても良い。
The present invention is not limited to the above embodiments, but can be modified or expanded as follows.
The reference temperature to be compared with the temperature detected by the temperature sensor 77 of the evaporator 64 may be a constant temperature. Although the temperature sensors 76 and 77 detect the surface temperatures of the condenser 58 and the evaporator 64, the present invention is not limited to this. For example, the temperature sensors 76 and 77 may detect the temperature of the refrigerant flowing through the condenser 58 and the evaporator 64, or the condenser 58. The temperature of the condenser 58 and the evaporator 64 may be detected by detecting the air temperature after heat exchange with the evaporator 64.

【0035】連通パイプ74の電磁開閉弁75を開放す
る時期は、運転開始から一定時間に定めても良い。パイ
プ55,59,61,63,65,66,68,69
は、冷媒通路を構成するものであるが、これらはホース
に換えても良い。三方切換弁57,67は、第1,第2
の吸・脱着器31,32を交互に脱着側、吸着側に切り
換える切換手段に相当するが、これら三方切換弁57,
67を省略し、電磁開閉弁53,54,68,69の選
択的開閉により第1,第2の吸・脱着器31,32を交
互に脱着側、吸着側に切り換える構成としても良い。
The timing for opening the electromagnetic opening / closing valve 75 of the communication pipe 74 may be set to a fixed time from the start of operation. Pipes 55, 59, 61, 63, 65, 66, 68, 69
Constitute a refrigerant passage, but these may be replaced with a hose. The three-way switching valves 57 and 67 are the first and second
Which corresponds to switching means for alternately switching the suction / desorption devices 31, 32 to the desorption side or the adsorption side.
67 may be omitted, and the first and second suction / desorption devices 31, 32 may be alternately switched to the desorption side and the adsorption side by selectively opening / closing the electromagnetic opening / closing valves 53, 54, 68, 69.

【0036】開閉手段は電磁開閉弁75に限られず、例
えば蒸発器64側から凝縮器58側に向かってのみ流通
可能で、且つ蒸発器64の出口側と凝縮器58の入口側
との圧力差が所定値になったとき開放する逆止弁として
も良い。このようにすることにより、温度センサ76,
77及び開閉手段を制御するの制御手段を不要とするこ
とができる。本発明の吸着式冷凍装置は、自動車の空気
調和機だけでなく、一般の空気調和機、冷凍庫、冷蔵庫
等に用いることができる。
The opening / closing means is not limited to the electromagnetic opening / closing valve 75, for example, it can flow only from the evaporator 64 side to the condenser 58 side, and the pressure difference between the outlet side of the evaporator 64 and the inlet side of the condenser 58. It is also possible to use a check valve that opens when is a predetermined value. By doing so, the temperature sensor 76,
It is possible to eliminate the control means for controlling the 77 and the opening / closing means. INDUSTRIAL APPLICABILITY The adsorption refrigeration system of the present invention can be used not only for automobile air conditioners but also for general air conditioners, freezers, refrigerators, and the like.

【0037】[0037]

【発明の効果】以上説明したように本発明によれば、次
のような効果を得ることができる。請求項1記載の吸着
式冷凍装置では、蒸発器の熱的負荷が大きい状態で運転
が開始される等、蒸発器での冷媒の蒸発量が多い場合
に、蒸発器の出口側と凝縮器の入口側とを連通路により
連通させることができるので、吸着剤の量を多くしなく
ても、蒸発器に冷媒液が蒸発し切れずに溜まるおそれが
なく、しかも蒸発器で蒸発気化した冷媒蒸気は凝縮器に
戻されてここで再び凝縮されるので、蒸発器への冷媒液
供給量が不足するおそれがなく、急速冷却の要求等に対
応することができる。
As described above, according to the present invention, the following effects can be obtained. In the adsorption refrigeration apparatus according to claim 1, when the amount of refrigerant evaporated in the evaporator is large, such as when the evaporator starts to operate with a large thermal load, the outlet side of the evaporator and the condenser are cooled. Since it is possible to communicate with the inlet side by a communication passage, even if the amount of adsorbent is not increased, there is no risk that the refrigerant liquid will not completely evaporate and accumulate in the evaporator, and the refrigerant vapor that has evaporated and vaporized in the evaporator Is returned to the condenser and is condensed again there, so that there is no fear that the amount of the refrigerant liquid supplied to the evaporator will be insufficient, and it is possible to meet the demand for rapid cooling and the like.

【0038】請求項2記載の吸着式冷凍装置では、制御
手段が温度センサの検出温度を基準温度と比較し、その
検出温度が基準温度を越えたとき、開閉手段を開放する
ので、蒸発器の熱的負荷の大小を適正に判断して蒸発器
で蒸発気化する冷媒蒸気量が多い場合に開閉手段を開放
することができる。
In the adsorption type refrigerating apparatus according to the second aspect, the control means compares the temperature detected by the temperature sensor with the reference temperature, and when the detected temperature exceeds the reference temperature, the opening / closing means is opened. The opening / closing means can be opened when the amount of the thermal load is properly judged and the amount of the refrigerant vapor evaporated and vaporized in the evaporator is large.

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

【図1】本発明の一実施例を示す吸着式冷凍装置の配管
構成図
FIG. 1 is a piping configuration diagram of an adsorption refrigeration system showing an embodiment of the present invention.

【図2】制御内容を示すフローチャートFIG. 2 is a flowchart showing control contents.

【図3】吸着式冷凍装置の運転に伴う車内の温度変化を
示す図
FIG. 3 is a diagram showing a temperature change in the vehicle accompanying the operation of the adsorption refrigeration system.

【図4】従来の吸着式冷凍装置を示す図1相当図FIG. 4 is a view corresponding to FIG. 1 showing a conventional adsorption type refrigeration system.

【符号の説明】[Explanation of symbols]

31,32は第1,第2の吸・脱着器、33,34は吸
着剤、35,36は熱交換器、58は凝縮器、60はレ
シーバ、62はポンプ、64は蒸発器、74は連通パイ
プ(連通路)、75は電磁開閉弁(開閉手段)、76,
77は温度センサである。
31 and 32 are first and second adsorbing / desorbing devices, 33 and 34 are adsorbents, 35 and 36 are heat exchangers, 58 is a condenser, 60 is a receiver, 62 is a pump, 64 is an evaporator, and 74 is Communication pipe (communication passage), 75 is an electromagnetic opening / closing valve (opening / closing means), 76,
Reference numeral 77 is a temperature sensor.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 冷媒蒸気を吸・脱着する吸着剤が充填さ
れた吸・脱着器と、 この吸・脱着器から脱着された冷媒蒸気を凝縮させる凝
縮器と、 冷媒液を被冷却流体と熱交換させることにより蒸発させ
る蒸発器と、 前記凝縮器で凝縮された冷媒液を前記蒸発器に送るポン
プとを備えた吸着式冷凍装置において、 前記蒸発器の出口側と凝縮器の入口側とを連通する連通
路を設けると共に、この連通路を所定時期に開放する開
閉手段を設けたことを特徴とする吸着式冷凍装置。
1. An adsorber / desorber filled with an adsorbent for adsorbing / desorbing a refrigerant vapor, a condenser for condensing the refrigerant vapor desorbed from the adsorber / desorber, and a refrigerant liquid and a cooled fluid. In an adsorption type refrigeration system equipped with an evaporator that evaporates by being exchanged, and a pump that sends the refrigerant liquid condensed in the condenser to the evaporator, the outlet side of the evaporator and the inlet side of the condenser are An adsorption type refrigerating apparatus, characterized in that a communication passage communicating with the communication passage is provided and an opening / closing means for opening the communication passage at a predetermined time is provided.
【請求項2】 蒸発器の温度を検出する温度センサと、 この温度センサの検出温度を基準温度と比較し、温度セ
ンサの検出温度が基準温度を越えたとき、開閉手段を開
放する制御手段とを設けたことを特徴とする請求項1記
載の吸着式冷凍装置。
2. A temperature sensor for detecting the temperature of the evaporator, and a control means for comparing the detected temperature of the temperature sensor with a reference temperature and opening the opening / closing means when the detected temperature of the temperature sensor exceeds the reference temperature. The adsorption type refrigerating apparatus according to claim 1, further comprising:
JP6046877A 1994-03-17 1994-03-17 Adsorption type refrigerating apparatus Pending JPH07253257A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6046877A JPH07253257A (en) 1994-03-17 1994-03-17 Adsorption type refrigerating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6046877A JPH07253257A (en) 1994-03-17 1994-03-17 Adsorption type refrigerating apparatus

Publications (1)

Publication Number Publication Date
JPH07253257A true JPH07253257A (en) 1995-10-03

Family

ID=12759591

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6046877A Pending JPH07253257A (en) 1994-03-17 1994-03-17 Adsorption type refrigerating apparatus

Country Status (1)

Country Link
JP (1) JPH07253257A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009080415A1 (en) * 2007-12-20 2009-07-02 Sortech Ag Method for controlling the power of a sorption refrigeration system and device therefor
JP2011190947A (en) * 2010-03-12 2011-09-29 Denso Corp Chemical heat pump device
JP2011530057A (en) * 2007-08-09 2011-12-15 インターナショナル フォー エナジー テクノロジー インダストリーズ エル.エル.シー. Two-stage low-temperature air-cooled adsorption cooling system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011530057A (en) * 2007-08-09 2011-12-15 インターナショナル フォー エナジー テクノロジー インダストリーズ エル.エル.シー. Two-stage low-temperature air-cooled adsorption cooling system
WO2009080415A1 (en) * 2007-12-20 2009-07-02 Sortech Ag Method for controlling the power of a sorption refrigeration system and device therefor
JP2011510247A (en) * 2007-12-20 2011-03-31 ゾルテッヒ アーゲー Method and apparatus for controlling the output of a sorption refrigeration system
US8539782B2 (en) 2007-12-20 2013-09-24 Sortech Ag Method for controlling the power of a sorption refrigeration system and device therefor
JP2011190947A (en) * 2010-03-12 2011-09-29 Denso Corp Chemical heat pump device

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