JPH04316966A - Adsorption type refrigerating machine and operating method thereof - Google Patents
Adsorption type refrigerating machine and operating method thereofInfo
- Publication number
- JPH04316966A JPH04316966A JP11073091A JP11073091A JPH04316966A JP H04316966 A JPH04316966 A JP H04316966A JP 11073091 A JP11073091 A JP 11073091A JP 11073091 A JP11073091 A JP 11073091A JP H04316966 A JPH04316966 A JP H04316966A
- Authority
- JP
- Japan
- Prior art keywords
- adsorption
- adsorbing
- desorption
- adsorbent
- refrigerant
- 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.)
- Withdrawn
Links
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 35
- 238000011017 operating method Methods 0.000 title 1
- 239000003507 refrigerant Substances 0.000 claims abstract description 48
- 238000003795 desorption Methods 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 11
- 239000003463 adsorbent Substances 0.000 claims description 42
- 238000002336 sorption--desorption measurement Methods 0.000 claims description 31
- 239000007788 liquid Substances 0.000 claims description 10
- 230000000694 effects Effects 0.000 abstract description 4
- 230000001105 regulatory effect Effects 0.000 abstract description 4
- 238000001704 evaporation Methods 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract 5
- 238000011084 recovery Methods 0.000 abstract 1
- 239000012809 cooling fluid Substances 0.000 description 11
- 239000012530 fluid Substances 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
Abstract
Description
【０００１】0001
【産業上の利用分野】本発明は冷凍機、冷蔵庫、空気調
和機等として用いられる吸着式冷凍機及びその運転方法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorption refrigerator used as a refrigerator, refrigerator, air conditioner, etc., and a method of operating the same.
【０００２】0002
【従来の技術】従来の吸着式空気調和機の配管系統図が
図３に示されている。１ａ、１ｂは吸・脱着器で、この
中にはそれぞれ冷媒蒸気を吸・脱着する吸着剤２ａ、２
ｂが充填されている。４は吸・脱着器１ａ、１ｂで吸着
剤２ａ、２ｂから脱着された冷媒蒸気を凝縮させる凝縮
器、５はレシーバ、６は冷媒液の流量を調節する流量調
節弁、７は冷媒液を蒸発させる蒸発器、３ａ、３ｂ、３
ｃ、３ｄ、３ｅ、３ｆは三方切換弁、１１は排熱によっ
て加熱された高温水等の加熱流体供給管、１２は加熱流
体の排出管、１３は外気等によって冷却された冷水等の
冷却流体供給管、１４は冷却流体の排出管である。吸・
脱着器１ａで冷媒を脱着し、吸・脱着器１ｂで冷媒を吸
着させる場合には、加熱流体が供給管１１、三方切換弁
３ｃ、吸・脱着器１ａ、三方切換弁３ｄを経て排出管１
２から流出し、冷却流体が供給管１３、三方切換弁３ｅ
、吸・脱着器１ｂ、三方切換弁３ｆを経て排出管１４か
ら流出すると同時にその一部が供給管１３から分岐して
凝縮器４を流過し排出管１４から流出する。2. Description of the Related Art A piping system diagram of a conventional adsorption type air conditioner is shown in FIG. 1a and 1b are adsorption/desorption devices, which contain adsorbents 2a and 2 that adsorb and desorb refrigerant vapor, respectively.
b is filled. 4 is a condenser that condenses the refrigerant vapor desorbed from the adsorbents 2a and 2b by the adsorption/desorption devices 1a and 1b, 5 is a receiver, 6 is a flow rate control valve that adjusts the flow rate of the refrigerant liquid, and 7 is a evaporator for the refrigerant liquid. evaporator, 3a, 3b, 3
c, 3d, 3e, and 3f are three-way switching valves, 11 is a heating fluid supply pipe such as high-temperature water heated by exhaust heat, 12 is a heating fluid discharge pipe, and 13 is a cooling fluid such as cold water cooled by outside air, etc. The supply pipe 14 is a cooling fluid discharge pipe. Suction/
When the refrigerant is desorbed by the desorber 1a and the refrigerant is adsorbed by the suction/desorber 1b, the heated fluid passes through the supply pipe 11, the three-way switching valve 3c, the suction/desorber 1a, and the three-way switching valve 3d, and then enters the discharge pipe 1.
2, the cooling fluid flows through the supply pipe 13 and the three-way switching valve 3e.
, the suction/desorber 1b, and the three-way switching valve 3f, and flows out from the discharge pipe 14, and at the same time, a part of it branches off from the supply pipe 13, flows through the condenser 4, and flows out from the discharge pipe 14.
【０００３】加熱流体が吸・脱着器１ａを流過すると、
この中に充填されている吸着剤２ａが加熱されることに
より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３ａを経て凝縮器４に入り、
ここで冷却流体に放熱することにより凝縮液化して冷媒
液となる。凝縮器４から流出した冷媒液はレシーバ５内
に一時的に貯溜された後、流量調節弁６を経て蒸発器７
に入り、ここで室内空気を冷却することにより蒸発気化
して冷媒蒸気となる。この冷媒蒸気は三方切換弁３ｂを
経て吸・脱着器１ｂ内に入り、この中に充填されている
吸着剤２ｂに吸着される。なお、吸着剤２ｂが冷媒蒸気
を吸着する際に発生する熱は吸・脱着器１ｂを流過する
冷却流体によって奪われる。[0003] When the heated fluid flows through the adsorption/desorption device 1a,
When the adsorbent 2a filled therein is heated, the refrigerant adsorbed thereto evaporates and is desorbed. This refrigerant vapor enters the condenser 4 via the three-way switching valve 3a,
Here, heat is radiated to the cooling fluid, which condenses and becomes a liquid refrigerant. The refrigerant liquid flowing out from the condenser 4 is temporarily stored in the receiver 5, and then passes through the flow rate control valve 6 to the evaporator 7.
The indoor air is cooled here and evaporated into refrigerant vapor. This refrigerant vapor enters the adsorption/desorption device 1b through the three-way switching valve 3b and is adsorbed by the adsorbent 2b filled therein. Note that the heat generated when the adsorbent 2b adsorbs refrigerant vapor is removed by the cooling fluid flowing through the adsorption/desorption device 1b.
【０００４】上記運転を暫時継続することによって吸着
剤２ｂが所定量の冷媒蒸気を吸着し又は吸着剤２ａから
所定量の冷媒蒸気が脱着したとき、各三方切換弁３ａ〜
３ｆが切り換えられ、加熱流体が吸・脱着器１ｂを循環
し、冷却流体が吸・脱着器１ａを循環する。かくして、
吸着剤２ｂから脱着された冷媒が三方切換弁３ａ、凝縮
器４、レシーバ５、流量調節弁６、蒸発器７、三方切換
弁３ｂを経て吸着剤２ａに吸着される。上記運転を交互
に繰り返すことにより吸着剤２ａ、２ｂが冷媒の吸着及
び脱着を繰り返し、蒸発器７によって室内空気が冷却さ
れる。When the adsorbent 2b adsorbs a predetermined amount of refrigerant vapor or a predetermined amount of refrigerant vapor is desorbed from the adsorbent 2a by continuing the above operation for a while, each of the three-way switching valves 3a to
3f is switched, the heating fluid circulates through the adsorption/desorption device 1b, and the cooling fluid circulates through the adsorption/desorption device 1a. Thus,
The refrigerant desorbed from the adsorbent 2b passes through the three-way switching valve 3a, the condenser 4, the receiver 5, the flow control valve 6, the evaporator 7, and the three-way switching valve 3b, and is adsorbed by the adsorbent 2a. By repeating the above operation alternately, the adsorbents 2a and 2b repeatedly adsorb and desorb the refrigerant, and the indoor air is cooled by the evaporator 7.
【０００５】[0005]
【発明が解決しようとする課題】上記従来の吸着式空気
調和機においては、吸着剤２ａ、２ｂは冷媒蒸気の脱着
時に加熱されて高温となり、吸着時に冷却されて低温と
なるが、脱着から吸着に切り換えた直後は吸着剤が所定
の温度以下に低下するまで吸着作用を行わず、また、吸
着から脱着に切り換えた直後は吸着剤が所定の温度以上
に昇温するまで脱着作用を行わない。従って、切り換え
直後若干の時間中、吸着式空気調和機はその空調能力を
失うという不具合があった。[Problems to be Solved by the Invention] In the conventional adsorption type air conditioner described above, the adsorbents 2a and 2b are heated to a high temperature during desorption of refrigerant vapor, and cooled to a low temperature during adsorption. Immediately after switching from adsorption to desorption, no adsorption action is performed until the temperature of the adsorbent drops below a predetermined temperature, and immediately after switching from adsorption to desorption, no desorption action is performed until the temperature of the adsorbent rises to a predetermined temperature or higher. Therefore, there was a problem in that the adsorption type air conditioner lost its air conditioning capacity for some time immediately after switching.
【０００６】[0006]
【課題を解決するための手段】本発明は上記課題を解決
するために発明されたものであって、第１の発明の要旨
とするところは、冷媒蒸気を吸・脱着する吸着剤が充填
された吸・脱着器と、上記吸着剤から脱着された冷媒蒸
気を凝縮させる凝縮器と、この凝縮器から流出した冷媒
液流量を調節する流量調節弁と、この流量調節弁を経て
流入する冷媒液を蒸発させる蒸発器とを備え、上記蒸発
器で蒸発した冷媒蒸気を上記吸着剤に吸着させる吸着式
冷凍機において、上記吸・脱着器を少なくとも３個以上
並列に接続したことを特徴とする吸着式冷凍機にある。
第２の発明の要旨とするところは、３個以上の吸・脱着
器がそれぞれ吸着、脱着、冷却の各工程をこの順に順次
行ない、かつ、各吸・脱着器が同時に吸着工程にならな
いように運転することを特徴とする請求項（１）記載の
吸着式冷凍機の運転方法にある。[Means for Solving the Problems] The present invention was invented to solve the above-mentioned problems. a condenser that condenses the refrigerant vapor desorbed from the adsorbent, a flow rate control valve that adjusts the flow rate of the refrigerant liquid flowing out from the condenser, and a refrigerant liquid that flows in through the flow rate control valve. and an evaporator for evaporating refrigerant vapor, the adsorption refrigerator adsorbs the refrigerant vapor evaporated by the evaporator onto the adsorbent, characterized in that at least three or more of the adsorption/desorption devices are connected in parallel. It is in the type refrigerator. The gist of the second invention is that three or more adsorption/desorption devices sequentially perform the adsorption, desorption, and cooling steps in this order, and each adsorption/desorption device does not perform the adsorption process at the same time. A method of operating an adsorption refrigerator according to claim (1), characterized in that:
【０００７】[0007]
【作用】本発明においては、上記構成を具えているため
、３個以上の吸・脱着器がそれぞれ吸着、脱着、冷却の
各工程をこの順に順次行うので、吸・脱着器を吸着工程
に切り換えると、吸着剤は直ちに吸着を開始する。[Operation] In the present invention, since the above structure is provided, three or more adsorption/desorption devices sequentially perform each step of adsorption, desorption, and cooling in this order, so that the adsorption/desorption devices are switched to the adsorption step. The adsorbent immediately begins adsorption.
【０００８】[0008]
【実施例】本発明の１実施例を図１及び図２を参照しな
がら具体的に説明する。図１において、１ａ、１ｂ、１
ｃはそれぞれ吸着剤２ａ、２ｂ、２ｃが充填された吸・
脱着器で、並列に接続されている。４は凝縮器、５はレ
シーバ、６は流量調節弁、７は蒸発器、８ａ、８ｂ、８
ｃ、８ｄ、８ｅ、８ｆ、９ａ、９ｂ、９ｃ、９ｄ、９ｅ
、９ｆ、１０ａ 、１０ｂ 、１０ｃ 、１０ｄ 、１
０ｅ 、１０ｆ は電磁弁である。吸・脱着器１ａが脱
着工程、吸・脱着器１ｂが吸着工程、吸・脱着器１ｃが
冷却工程を行う場合、電磁弁８ａ、８ｅ、９ａ、９ｄ、
１０ｂ 、１０ｃ 、１０ｅ 、１０ｆ が開とされ、
電磁弁８ｂ、８ｃ、８ｄ、８ｆ、９ｂ、９ｃ、９ｅ、９
ｆ、１０ａ 、１０ｄ が閉じられる。加熱流体は供給
管１１、電磁弁９ａを経て吸・脱着器１ａに導かれ、こ
こで吸着剤２ａを加熱することによって吸着剤２ａより
冷媒を脱着させ、しかる後、電磁弁９ｅ、排出管１２を
経て流出する。吸着剤２ａから脱着された冷媒蒸気は電
磁弁８ａを経て凝縮器４に入り、ここで冷却流体に放熱
することによって凝縮液化して液冷媒となる。凝縮器４
を出た液冷媒はレシーバ５内に一時的に貯えられた後流
量調節弁６に入って流量を調節され、かつ、断熱膨張す
る。次いで、この冷媒は蒸発器７に入り、ここで室内空
気等を冷却することによって蒸発気化して冷媒蒸気とな
る。蒸発器７を出た冷媒蒸気は電磁弁８ｅを経て吸・脱
着器１ｂに入り、ここで吸着剤２ｂに吸着される。この
間、吸・脱着器１ｂ内の吸着剤２ｂは電磁弁１０ｂ 、
吸・脱着器１ｂ、電磁弁１０ｅ をこの順に流過する冷
却流体によって冷却される。また、吸・脱着器１ｃ内の
吸着剤２ｃは電磁弁１０ｃ 、吸・脱着器１ｃ、電磁弁
１０ｆ をこの順に流過する冷却流体によって冷却され
る。[Embodiment] An embodiment of the present invention will be explained in detail with reference to FIGS. 1 and 2. In FIG. 1, 1a, 1b, 1
c is a vacuum chamber filled with adsorbents 2a, 2b, and 2c, respectively.
Connected in parallel with detachers. 4 is a condenser, 5 is a receiver, 6 is a flow rate control valve, 7 is an evaporator, 8a, 8b, 8
c, 8d, 8e, 8f, 9a, 9b, 9c, 9d, 9e
, 9f, 10a, 10b, 10c, 10d, 1
0e and 10f are solenoid valves. When the suction/desorption device 1a performs the desorption process, the suction/desorption device 1b performs the adsorption process, and the suction/desorption device 1c performs the cooling process, the solenoid valves 8a, 8e, 9a, 9d,
10b, 10c, 10e, 10f are open,
Solenoid valves 8b, 8c, 8d, 8f, 9b, 9c, 9e, 9
f, 10a, 10d are closed. The heated fluid is led to the suction/desorption device 1a via the supply pipe 11 and the solenoid valve 9a, where the refrigerant is desorbed from the adsorbent 2a by heating the adsorbent 2a, and then the solenoid valve 9e and the discharge pipe 12 It flows out through the process. The refrigerant vapor desorbed from the adsorbent 2a enters the condenser 4 via the electromagnetic valve 8a, where it radiates heat to the cooling fluid and is condensed and liquefied to become a liquid refrigerant. Condenser 4
The liquid refrigerant that has exited the receiver 5 is temporarily stored in the receiver 5, and then enters the flow rate control valve 6, where the flow rate is regulated and adiabatically expanded. Next, this refrigerant enters the evaporator 7, where it evaporates and becomes refrigerant vapor by cooling indoor air and the like. The refrigerant vapor leaving the evaporator 7 passes through the electromagnetic valve 8e and enters the adsorption/desorption device 1b, where it is adsorbed by the adsorbent 2b. During this time, the adsorbent 2b in the adsorption/desorption device 1b is removed by the solenoid valve 10b,
It is cooled by the cooling fluid that flows through the suction/desorption device 1b and the solenoid valve 10e in this order. Further, the adsorbent 2c in the adsorption/desorption device 1c is cooled by the cooling fluid flowing through the solenoid valve 10c, the adsorption/desorption device 1c, and the solenoid valve 10f in this order.
【０００９】上記運転を継続することによって吸・脱着
器１ｂ内の吸着剤２ｂが一定量の冷媒を吸着し又は吸・
脱着器１ａ内の吸着剤２ａが一定量の冷媒を脱着した時
、電磁弁８ａ、８ｃ、８ｄ、８ｅ、９ａ、９ｃ、９ｄ、
９ｆ、１０ｂ 、１０ｅ を閉じ、電磁弁８ｂ、８ｆ、
９ｂ、９ｅ、１０ａ、１０ｃ 、１０ｄ 、１０ｆ を
開ける。すると、加熱流体は電磁弁９ｂ、吸・脱着器１
ｂ、電磁弁９ｅをこの順に流過し、冷却流体は電磁弁１
０ｃ 、吸・脱着器１ｃ、電磁弁１０ｆ をこの順に流
過するとともに電磁弁１０ａ 、吸・脱着器１ａ、電磁
弁１０ｄ を経て流出する。かくして、吸着剤２ｂから
冷媒が脱着し、この冷媒蒸気は電磁弁８ｂ、凝縮器４、
レシーバ５、流量調節弁６、蒸発器７、電磁弁８ｆを経
て吸・脱着器１ｃに入り、吸着剤２ｃに吸着される。こ
のようにして、吸・脱着器１ｂは脱着工程、吸・脱着器
１ｃは吸着工程、吸・脱着器１ａは冷却工程を行う。By continuing the above operation, the adsorbent 2b in the adsorption/desorption device 1b adsorbs or absorbs a certain amount of refrigerant.
When a certain amount of refrigerant is desorbed by the adsorbent 2a in the desorber 1a, the solenoid valves 8a, 8c, 8d, 8e, 9a, 9c, 9d,
9f, 10b, 10e are closed, solenoid valves 8b, 8f,
Open 9b, 9e, 10a, 10c, 10d, 10f. Then, the heated fluid flows through the solenoid valve 9b and the suction/desorption device 1.
b, the cooling fluid flows through the solenoid valve 9e in this order, and the cooling fluid passes through the solenoid valve 1.
0c, suction/desorption device 1c, and solenoid valve 10f in this order, and also flows out through solenoid valve 10a, suction/desorption device 1a, and solenoid valve 10d. In this way, the refrigerant is desorbed from the adsorbent 2b, and this refrigerant vapor flows through the solenoid valve 8b, the condenser 4,
It enters the adsorption/desorption device 1c via the receiver 5, flow control valve 6, evaporator 7, and electromagnetic valve 8f, and is adsorbed by the adsorbent 2c. In this way, the adsorption/desorption device 1b performs the desorption process, the adsorption/desorption device 1c performs the adsorption process, and the adsorption/desorption device 1a performs the cooling process.
【００１０】吸・脱着器１ｃ内の吸着剤２ｃが一定量の
冷媒を吸着し又は吸・脱着器１ｂ内の吸着剤２ｂが一定
量の冷媒を脱着したとき、電磁弁８ａ、８ｂ、８ｅ、８
ｆ、９ａ、９ｂ、９ｄ、９ｅ、１０ｃ 、１０ｆ を閉
じ、電磁弁８ｃ、８ｄ、９ｃ、９ｆ、１０ａ 、１０ｂ
、１０ｄ 、１０ｅを開ける。かくして、吸着剤２ｃ
から脱着した冷媒が吸着剤２ａに吸着され、吸着剤２ｂ
は冷却される。上記を繰り返すことによって、図２に示
すように、各吸・脱着器１ａ、１ｂ、１ｃは吸着、脱着
、冷却の各工程をこの順に繰り返し、蒸発器７で室内空
気等を冷却する。When the adsorbent 2c in the adsorbent/desorber 1c adsorbs a certain amount of refrigerant or the adsorbent 2b in the adsorbent/desorber 1b desorbs a certain amount of refrigerant, the solenoid valves 8a, 8b, 8e, 8
Close solenoid valves 8c, 8d, 9c, 9f, 10a, 10b.
, 10d and 10e are opened. Thus, adsorbent 2c
The refrigerant desorbed from the adsorbent 2a is adsorbed by the adsorbent 2b.
is cooled. By repeating the above, each adsorption/desorption device 1a, 1b, 1c repeats the steps of adsorption, desorption, and cooling in this order, and the evaporator 7 cools the indoor air, etc., as shown in FIG.
【００１１】吸・脱着器１ａ、１ｂ、１ｃが３個の場合
を説明したが、４個又はそれ以上でも良く、その場合も
同様に各吸・脱着器が吸着、脱着、冷却の各工程をこの
順に繰り返すが、この場合、吸・脱着器の個数から１を
引いた数以上の吸・脱着器が吸着工程を同時に行なわな
いように制御される。Although the case where there are three adsorption/desorption devices 1a, 1b, and 1c has been described, it is also possible to use four or more, and in that case, each adsorption/desorption device performs each step of adsorption, desorption, and cooling. This order is repeated, but in this case, the number of adsorption/desorption devices greater than or equal to the number of adsorption/desorption devices minus 1 is controlled so as not to perform the adsorption step at the same time.
【００１２】0012
【発明の効果】本発明においては、並列に接続された３
個以上の吸・脱着器がそれぞれ吸着、脱着、冷却の各工
程をこの順に順次行い、かつ、各吸・脱着器が同時に吸
着工程にならないように運転されるので、吸着剤は脱着
後冷却され、従って、吸着工程に切り換えると、吸着剤
は直ちに冷媒蒸気を吸着することができるので連続して
冷却客体を冷却できる。[Effect of the invention] In the present invention, three
Each adsorption/desorption device performs the adsorption, desorption, and cooling steps in this order, and each adsorption/desorption device is operated so that it does not perform the adsorption process at the same time, so the adsorbent is cooled after desorption. Therefore, when switching to the adsorption process, the adsorbent can immediately adsorb refrigerant vapor, so that the object to be cooled can be continuously cooled.
【図１】本発明の１実施例を示す配管系統図である。FIG. 1 is a piping system diagram showing one embodiment of the present invention.
【図２】上記実施例における各工程の切換態様を示すタ
イムチャートである。FIG. 2 is a time chart showing switching modes of each process in the above embodiment.
【図３】従来の吸着式空気調和機の配管系統図である。FIG. 3 is a piping system diagram of a conventional adsorption air conditioner.
１ａ 吸・脱着器 １ｂ 吸・脱着器 １ｃ 吸・脱着器 ２ａ 吸着剤 ２ｂ 吸着剤 ２ｃ 吸着剤 ４ 凝縮器 ６ 流量調節弁 ７ 蒸発器 1a Suction/desorption device 1b Suction/desorption device 1c Suction/desorption device 2a Adsorbent 2b Adsorbent 2c Adsorbent 4 Condenser 6 Flow control valve 7 Evaporator
Claims (2)
された吸・脱着器と、上記吸着剤から脱着された冷媒蒸
気を凝縮させる凝縮器と、この凝縮器から流出した冷媒
液の流量を調節する流量調節弁と、この流量調節弁を経
て流入する冷媒液を蒸発させる蒸発器とを備え、上記蒸
発器で蒸発した冷媒蒸気を上記吸着剤に吸着させる吸着
式冷凍機において、上記吸・脱着器を少なくとも３個以
上並列に接続したことを特徴とする吸着式冷凍機。Claim 1: An adsorption/desorption device filled with an adsorbent that adsorbs and desorbs refrigerant vapor, a condenser that condenses the refrigerant vapor desorbed from the adsorbent, and a flow rate of the refrigerant liquid flowing out from the condenser. In an adsorption refrigerator, the adsorption refrigerator is equipped with a flow rate control valve that adjusts the flow rate, and an evaporator that evaporates the refrigerant liquid that flows in through the flow rate control valve, and in which the refrigerant vapor evaporated in the evaporator is adsorbed on the adsorbent. - An adsorption refrigerator characterized by having at least three desorbers connected in parallel.
、脱着、冷却の各工程をこの順に順次行ない、かつ、各
吸・脱着器が同時に吸着工程にならないように運転する
ことを特徴とする請求項（１）記載の吸着式冷凍機の運
転方法。[Claim 2] Three or more adsorption/desorption devices sequentially perform adsorption, desorption, and cooling steps in this order, and each adsorption/desorption device is operated so as not to be in the adsorption step at the same time. The method of operating an adsorption refrigerator according to claim (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11073091A JPH04316966A (en) | 1991-04-17 | 1991-04-17 | Adsorption type refrigerating machine and operating method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11073091A JPH04316966A (en) | 1991-04-17 | 1991-04-17 | Adsorption type refrigerating machine and operating method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04316966A true JPH04316966A (en) | 1992-11-09 |
Family
ID=14543055
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11073091A Withdrawn JPH04316966A (en) | 1991-04-17 | 1991-04-17 | Adsorption type refrigerating machine and operating method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04316966A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995014898A1 (en) * | 1993-11-29 | 1995-06-01 | Mayekawa Mfg. Co., Ltd. | Adsorption type cooling apparatus, method of controlling cold output of same, and fin type adsorbent heat exchanger for use in same |
| WO2002035161A1 (en) * | 2000-10-23 | 2002-05-02 | Dingyu Li | Adsorption refrigeration system with multiple generators |
| JP2009518614A (en) * | 2005-12-07 | 2009-05-07 | ゾルテッヒ アーゲー | Adsorption machine with heat recovery |
| KR20110033226A (en) * | 2008-06-19 | 2011-03-30 | 소르테크 아게 | Method for carrying out a heat transfer between alternately working adsorbers and device |
| KR20170048400A (en) * | 2014-09-02 | 2017-05-08 | 네덜란제 오르가니자티에 포오르 토에게파스트-나투우르베텐샤펠리즈크 온데르조에크 테엔오 | System and method for thermochemical storage of energy |
-
1991
- 1991-04-17 JP JP11073091A patent/JPH04316966A/en not_active Withdrawn
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995014898A1 (en) * | 1993-11-29 | 1995-06-01 | Mayekawa Mfg. Co., Ltd. | Adsorption type cooling apparatus, method of controlling cold output of same, and fin type adsorbent heat exchanger for use in same |
| US5732569A (en) * | 1993-11-29 | 1998-03-31 | Mayekawa Mfg. Co., Ltd. | Adsorption type cooling apparatus, method of controlling cold output of same, and fin type adsorbent heat exchanger for use in the same |
| US6041617A (en) * | 1993-11-29 | 2000-03-28 | Mayekawa Mfg. Co., Ltd. | Adsorption type cooling apparatus, method of controlling cold output of same, and fin type adsorbent heat exchanger for use in same |
| WO2002035161A1 (en) * | 2000-10-23 | 2002-05-02 | Dingyu Li | Adsorption refrigeration system with multiple generators |
| JP2009518614A (en) * | 2005-12-07 | 2009-05-07 | ゾルテッヒ アーゲー | Adsorption machine with heat recovery |
| KR101333682B1 (en) * | 2005-12-07 | 2013-12-02 | 소르테크 아게 | Adsorption apparatus comprising a heat recovery system |
| KR20110033226A (en) * | 2008-06-19 | 2011-03-30 | 소르테크 아게 | Method for carrying out a heat transfer between alternately working adsorbers and device |
| JP2011524968A (en) * | 2008-06-19 | 2011-09-08 | ゾルテッヒ アーゲー | Method and apparatus for performing heat transfer between adsorbers operating alternately |
| KR20170048400A (en) * | 2014-09-02 | 2017-05-08 | 네덜란제 오르가니자티에 포오르 토에게파스트-나투우르베텐샤펠리즈크 온데르조에크 테엔오 | System and method for thermochemical storage of energy |
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| A300 | Application deemed to be withdrawn because no request for examination was validly filed |
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