JPH03199864A - Adsorption type refrigerator by circulation of adsorbent - Google Patents
Adsorption type refrigerator by circulation of adsorbentInfo
- Publication number
- JPH03199864A JPH03199864A JP34232089A JP34232089A JPH03199864A JP H03199864 A JPH03199864 A JP H03199864A JP 34232089 A JP34232089 A JP 34232089A JP 34232089 A JP34232089 A JP 34232089A JP H03199864 A JPH03199864 A JP H03199864A
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- cylinder
- path
- adsorption
- pressure side
- 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
- 239000003463 adsorbent Substances 0.000 title claims abstract description 132
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 40
- 238000003795 desorption Methods 0.000 claims abstract description 15
- 238000005057 refrigeration Methods 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 4
- 230000000717 retained effect Effects 0.000 claims 1
- 230000009471 action Effects 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 230000000694 effects Effects 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 239000004020 conductor Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は吸着剤を循環移動させる方式の吸着剤冷凍機に
係り、詳しくは、吸着剤を上昇させかつ自然落下させる
ことによって吸着剤を循環させ、もって効率的な冷凍サ
イクルを行わせるようにした吸着剤循環による吸着式冷
凍機に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an adsorbent refrigerator that circulates and moves an adsorbent. This invention relates to an adsorption refrigerator that uses adsorbent circulation to perform an efficient refrigeration cycle.
(従来の技術)
近時、吸着式冷凍において吸着式冷凍機が、装置コスト
やランニングコストの面から見直され、それに係る発明
、考案が種々発表されている。(Prior Art) Recently, in adsorption refrigeration, adsorption refrigerators have been reviewed from the viewpoint of equipment costs and running costs, and various inventions and ideas related thereto have been announced.
一般に吸着式冷凍機は、シリカゲル、ゼオライト等の固
体吸着剤が水、アルコール等の冷媒との間で脱着、吸着
を繰り返し吸着時に発生する冷媒の気化熱を利用して冷
水を取り出し、室内の冷房等に利用するものである。In general, adsorption refrigerators use a solid adsorbent such as silica gel or zeolite to repeatedly desorb and adsorb a refrigerant such as water or alcohol, and use the heat of vaporization of the refrigerant generated during adsorption to extract cold water and cool the room. It is used for such purposes.
その作動原理を第3図を用いて説明すると、(31)は
吸着剤充填管で、伝熱管の周囲に固体吸着剤を付設して
いる。一方、(32)は伝熱管で、該管の周囲にはフィ
ンが設けられている。そして、この2種類の管(31)
、 (32)はそれぞれ熱交換器を形成しており、吸
着剤充填管(31)gjでは吸着剤を加熱及び冷却し、
伝熱管(32)側では冷媒を冷却して凝縮したり、冷水
を取り出したりするようになっておりこれらは冷媒であ
る水と共に通常、円筒の真空容器(33)中に収められ
ている。The operating principle will be explained using FIG. 3. (31) is an adsorbent-filled tube, and a solid adsorbent is attached around the heat transfer tube. On the other hand, (32) is a heat transfer tube, and fins are provided around the tube. And these two types of tubes (31)
, (32) each form a heat exchanger, and the adsorbent filling pipe (31)gj heats and cools the adsorbent,
On the heat transfer tube (32) side, the refrigerant is cooled and condensed, and cold water is taken out, and these are usually housed in a cylindrical vacuum container (33) together with the refrigerant water.
そして、脱着作用は、吸着剤充填管(31)に温水を流
し、吸着剤を加熱することにより行われ、これにより吸
着剤が吸着していた冷媒は、水蒸気となって伝熱管(3
2)近辺に浮遊し、このとき伝熱管(32)に冷却水を
流すと、前記水蒸気は伝熱管(32)付近で熱が奪われ
凝縮して水になり、伝熱管(32)に付着する。The desorption action is carried out by heating the adsorbent by flowing hot water through the adsorbent-filled tube (31). As a result, the refrigerant adsorbed by the adsorbent turns into water vapor, and the refrigerant is turned into water vapor.
2) Floating nearby, and at this time, when cooling water is flowed through the heat exchanger tube (32), the water vapor loses heat near the heat exchanger tube (32), condenses and becomes water, and adheres to the heat exchanger tube (32). .
一方、吸着作用は、吸着剤充填管(31)に冷却水を流
し、吸着剤を冷却する。これによって吸着剤は前記の伝
熱管(32)に付着の水を吸着し、水蒸気に変え、その
とき、発生する気化熱が伝熱管(32)を冷却する。従
って、このとき伝熱管(32)に流れている水は冷却さ
れ、この冷却された水が冷房等に利用される。On the other hand, for the adsorption action, cooling water is flowed through the adsorbent filling pipe (31) to cool the adsorbent. As a result, the adsorbent adsorbs the water adhering to the heat transfer tube (32) and converts it into water vapor, and the heat of vaporization generated at this time cools the heat transfer tube (32). Therefore, the water flowing through the heat exchanger tubes (32) at this time is cooled, and this cooled water is used for air conditioning and the like.
以上が一般的な吸着式冷凍機の原理であるが、実際には
上記の伝熱管(32)は凝縮器と蒸発器とに分かれて構
成されるものが多い。しかし、何れにしても上述のよう
に吸着剤は固定されていて、加熱、冷却を交互に繰り返
し、脱着及び吸着を行うようになっている。The above is the principle of a general adsorption refrigerator, but in reality, the heat exchanger tube (32) is often divided into a condenser and an evaporator. However, in any case, the adsorbent is fixed as described above, and heating and cooling are repeated alternately to perform desorption and adsorption.
(発明が解決しようとする課題)
ところで、上述の如きこれまでの吸着式冷凍では、何れ
も吸着剤を特定の個所で位置せしめたまま加熱したり冷
却したりするため、吸着剤用の熱交換器には切り替え装
置が不可欠であった。そして切り替えても直ちに熱交換
器の温度が変化するものでもなく、その間に時間的にロ
スやエネルギーのロスが生じていた。(Problem to be Solved by the Invention) By the way, in the conventional adsorption refrigeration systems as described above, the adsorbent is heated or cooled while being positioned at a specific location. A switching device was essential for the vessel. Even when switching, the temperature of the heat exchanger does not change immediately, and a loss of time and energy occurs during the switching.
そこで本発明者等はこれらの問題を解決するために吸着
剤を循環させるという全く新規方式の吸着式冷凍機をさ
きに開示した。(特願平112324号参照)
この冷凍機の構成は第2図に示すようなもので、スクリ
ューコンベヤ(26)を介して、上方に設けられた脱着
側回転ドラム(21)に入った吸着剤(25)がこの回
転ドラム(21)内に設けられた脱着測用熱交換器(2
2)により加熱され、凝縮器(28)に対して冷媒を脱
着し、さらに案内通路(27)を自然落下して下方に設
けられた吸着側回転ドラム(21)’に入り、ここで吸
着用熱交換器(22)’によって冷却されて蒸発器(3
0)から冷媒を吸着するという循環をくり返すものであ
る。Therefore, in order to solve these problems, the present inventors have previously disclosed a completely new type of adsorption refrigerator that circulates the adsorbent. (Refer to Japanese Patent Application No. 112324) The structure of this refrigerator is as shown in Fig. 2, in which the adsorbent enters the desorption rotating drum (21) provided above via a screw conveyor (26). (25) is a desorption measurement heat exchanger (2) installed in this rotating drum (21).
2), the refrigerant is desorbed from the condenser (28), and then naturally falls through the guide passage (27) and enters the suction side rotating drum (21)' provided below, where it is used for adsorption. The heat exchanger (22)' cools the evaporator (3).
The cycle of adsorbing refrigerant from 0) is repeated.
従って、吸脱着作用の切り替えは不要で、両作用共並行
して連続的に行われ、このため時間的ロスやエネルギー
ロスの生じない優れた吸着式冷凍機の構成が可能となる
。Therefore, there is no need to switch between adsorption and desorption operations, and both operations are performed in parallel and continuously, making it possible to construct an excellent adsorption refrigerator that does not cause time loss or energy loss.
しかし安定した冷凍出力を得るためにはこのままでは不
都合で例えば、上記冷凍機において脱着側回転ドラム(
21)の周囲は冷媒の脱着により高圧となり、他方吸着
側回転ドラム(21)’の周囲は吸着により低圧となる
が、上記の目的のためには両者の飽和蒸気圧力差を一定
に保つ必要がある。However, in order to obtain stable refrigeration output, this is inconvenient as it is, and for example, in the above-mentioned refrigerator, the rotating drum on the desorption side (
The area around the rotating drum (21)' becomes high pressure due to refrigerant desorption, while the area around the adsorption side rotating drum (21)' becomes low pressure due to adsorption, but for the above purpose, it is necessary to keep the saturated vapor pressure difference between the two constant. be.
これに対処するため前記案内通路(27)に蒸気弁やオ
リフィス(29)等を付設しなければならない。To cope with this, it is necessary to provide a steam valve, an orifice (29), etc. to the guide passage (27).
さらにこれとは別に、熱交換器を用意し、脱着側回転ド
ラム(21)に入る吸着剤と吸着側回転ドラム(21)
’に入る吸着剤との間で熱交換を行わせる等、成績係数
(COP)を向上させるための通例の手段も併用されね
ばならない。Furthermore, apart from this, a heat exchanger is prepared, and the adsorbent entering the desorption side rotating drum (21) and the adsorption side rotating drum (21) are prepared.
Customary measures to improve the coefficient of performance (COP) must also be used, such as heat exchange with the adsorbent entering the sorbent.
また、各回転ドラム(21) 、 (21)’のための
モータ(M)が夫々必要で、このため装置全体が大形化
するf頃向があった。Further, a motor (M) is required for each of the rotating drums (21) and (21)', which tends to increase the size of the entire device.
本発明はかかる実状に鑑みて、吸着剤循環方式の利点を
生かし、それをさらに小型化、簡略化すると共に、前記
オリフィスや熱交換器等を併設しなくても充分なc、
o、 pが得られる更に改善された吸着剤循環による吸
着式冷凍機を提供することを目的とするものである。In view of the above circumstances, the present invention utilizes the advantages of the adsorbent circulation system, further downsizing and simplifying it, and also provides sufficient c.
It is an object of the present invention to provide an adsorption refrigerator using improved adsorbent circulation that can obtain o and p.
(課題を解決するための手段)
即ち、上記目的に適合する本発明に係る吸着剤循環によ
る吸着式冷凍機の特徴は、容器内において吸着剤を上方
へ搬送する手段を中心に配し、周囲に吸着剤の自然落下
通路を設けて吸着剤の循環一
経路を形成すると共に、該循環経路の上方側を高圧側に
、一方下方側を低圧側に形成せしめたことにある。(Means for Solving the Problems) That is, the feature of the adsorption refrigerator using adsorbent circulation according to the present invention, which is suitable for the above-mentioned purpose, is that the means for transporting the adsorbent upward in the container is arranged at the center, and the A natural fall passage for the adsorbent is provided at the top to form a circulation path for the adsorbent, and the upper side of the circulation path is formed as a high pressure side, while the lower side is formed as a low pressure side.
ここで前記高圧側及び低圧側の形成は吸着剤循環経路の
上部吸着剤に対して吸着剤加熱手段を、一方吸着剤循環
経路の下部吸着剤に対して吸着剤冷却手段を夫々配設し
、かつ前記循環経路の上方に凝縮器、下方に蒸発器を夫
々配置することにより夫々形成される。Here, the formation of the high-pressure side and the low-pressure side is achieved by providing an adsorbent heating means for the upper adsorbent in the adsorbent circulation path, and an adsorbent cooling means for the lower adsorbent in the adsorbent circulation path, respectively, A condenser is disposed above the circulation path, and an evaporator is disposed below the circulation path.
また吸着剤循環経路の上部吸着剤と下部吸着剤の間に、
脱着を終了して下降する吸着剤と吸着を終了して上昇す
る吸着剤とが伝熱面を介して熱交換する熱交換部分を設
けることにより本発明をさらに効果的なものとすること
ができる。Also, between the upper and lower adsorbents in the adsorbent circulation path,
The present invention can be made more effective by providing a heat exchange portion where the adsorbent that descends after completing desorption and the adsorbent that ascends after completing adsorption exchange heat via a heat transfer surface. .
(作用)
上記の提出によって、吸着剤は搬送手段を介して上昇し
た後、その周囲に落下するという循環をくり返すが、そ
の間循環経路の上部では吸着剤が加熱されて、冷媒が脱
着され、一方循環経路の下部では吸着剤が冷却されて冷
媒が吸着される。そして、吸着剤の上方に配された凝縮
器において脱着冷媒が冷却され、ここで液状に凝縮する
。次いでこの液冷媒はトラップ配管等によって吸着剤の
下方に配された蒸発器に送られ、ここで前記の理由によ
り吸着剤に吸着される。このとき、気化熱が奪われて利
用側に冷熱が供給されるのは通常の冷凍機と同様である
。(Function) According to the above submission, the adsorbent rises through the conveyance means and then falls around it, repeating the cycle, during which time the adsorbent is heated in the upper part of the circulation path and the refrigerant is desorbed. On the other hand, in the lower part of the circulation path, the adsorbent is cooled and the refrigerant is adsorbed. The desorption refrigerant is then cooled in a condenser placed above the adsorbent, where it is condensed into a liquid state. Next, this liquid refrigerant is sent to an evaporator placed below the adsorbent through a trap pipe or the like, where it is adsorbed by the adsorbent for the reasons mentioned above. At this time, the heat of vaporization is taken away and cold energy is supplied to the user side, similar to a normal refrigerator.
ところで本発明に係る冷凍機は上部に凝縮器、下部に蒸
発器が配置されて、この間に吸着剤循環機能が介在され
ている。従って吸着剤自身の粒子層によって高圧側と低
圧側とは夫々密閉され、両者の飽和蒸気圧力差が保たれ
て、安定した冷凍出力が得られる。By the way, in the refrigerator according to the present invention, a condenser is disposed in the upper part and an evaporator is disposed in the lower part, and an adsorbent circulation function is interposed between the condenser and the evaporator. Therefore, the high-pressure side and the low-pressure side are each sealed by the particle layer of the adsorbent itself, and the saturated vapor pressure difference between the two is maintained, resulting in a stable refrigeration output.
またこの配置関係により、高圧側の押圧力は降下通路に
在る吸着剤の移動を促し、吸着剤の循環をスムーズなも
のとする。Further, due to this arrangement, the pressing force on the high pressure side promotes the movement of the adsorbent in the descending passage, thereby making the circulation of the adsorbent smooth.
一方、吸着剤の循環経路の上部吸着剤と下部吸着剤の間
に前記の如き熱交換部分を設けることによってこの部分
を下降する加熱された吸着剤と同部分を上昇する冷却さ
れた吸着剤との間で輸送手段の壁面を介して熱交換がな
され、脱着作用に入る前の吸着剤が予熱され吸着作用に
入る前の吸着剤が予冷されて、c、o、pの顕著な向上
を得ることができる。On the other hand, by providing a heat exchange section as described above between the upper adsorbent and the lower adsorbent in the adsorbent circulation path, heated adsorbent descends through this section and cooled adsorbent ascends through the same section. Heat exchange takes place between them through the walls of the transport vehicle, preheating the adsorbent before entering the desorption action and precooling the adsorbent before entering the adsorption action, resulting in significant improvements in c, o, and p. be able to.
(実施例) 以下、図面にもとづいて本発明に実施例を説明する。(Example) Embodiments of the present invention will be described below based on the drawings.
第1図は本発明に係る吸着剤循環方式吸着式冷凍機の構
造を示す部分上面図(イ)及び側面図(ロ)である。FIG. 1 is a partial top view (A) and a side view (B) showing the structure of an adsorption refrigerating machine with adsorbent circulation according to the present invention.
同図において、(1)は伝熱性素材で繭形状に形成され
た真空容器であって、上部に凝縮器(21,下部に蒸発
器(3)が設けられ、この両者の間に吸着剤(4)が充
填されている。(5)はこの充填された吸着剤(4)に
内包された上下に開口部を有する円筒であって伝熱性素
材で形成され、内部には下端から上端にわたって、スク
リューコンベアあるいはコイルスプリング等の吸着剤搬
送手段(6)が配設されている。In the figure, (1) is a vacuum container formed in a cocoon shape with a heat conductive material, and a condenser (21) is provided at the top, an evaporator (3) is provided at the bottom, and an adsorbent (3) is provided between the two. 4) is filled in. (5) is a cylinder with openings at the top and bottom that is enclosed in the filled adsorbent (4), and is made of a heat conductive material. An adsorbent conveying means (6) such as a screw conveyor or a coil spring is provided.
(7)はこの搬送手段(6)を駆動するモータである。(7) is a motor that drives this conveyance means (6).
なお吸着剤(4)は、真空容器(11内周に張り渡した
金網(8)によって蒸発器(3)への落下が防止されて
いる。Note that the adsorbent (4) is prevented from falling into the evaporator (3) by a wire mesh (8) stretched around the inner periphery of the vacuum container (11).
また前記@縮器(2)には下方に傾斜したフィン(9A
)と、該フィン(9A)に対向した傾斜板αΦが設けら
れ、一方蒸発器(3)にはフィン(9B)が設けられて
いる。そして前記傾斜板00)と真空容器(1)内壁と
で凝縮器(2)内部に冷媒貯溜部0υが形成され、該冷
媒貯溜部0Dと蒸発器(3)上部とがトラップ配管(2
)によって連結されている。In addition, the compressor (2) has downwardly inclined fins (9A
) and an inclined plate αΦ facing the fin (9A), while the evaporator (3) is provided with a fin (9B). A refrigerant reservoir 0υ is formed inside the condenser (2) by the inclined plate 00) and the inner wall of the vacuum container (1), and the refrigerant reservoir 0D and the upper part of the evaporator (3) are connected to the trap pipe (2).
) are connected by.
さらに通常の吸着式冷凍機と同様、所定量の冷媒が上記
真空容器(1)内に封入されている。Furthermore, like a normal adsorption refrigerator, a predetermined amount of refrigerant is sealed in the vacuum container (1).
一方、(13A)〜(130)は前記真空容器(1)の
外周に周設されたチューブであって、凝縮器(2)及び
吸着剤(41m環経路における上部軸吸着剤(4八)、
下部吸着剤(4C)及び蒸発器(3)に夫々該当して設
けられ、いずれも入口04)から出口a勃に向かって後
記する所定の熱媒が流れ、各部分の加熱や冷却等がなさ
れる。On the other hand, (13A) to (130) are tubes installed around the outer periphery of the vacuum container (1), including a condenser (2) and adsorbents (an upper shaft adsorbent (48) in the 41m ring path);
They are provided corresponding to the lower adsorbent (4C) and the evaporator (3), respectively, and in both cases, a predetermined heat medium (described later) flows from the inlet 04) toward the outlet a, heating and cooling each part. Ru.
また、前記上部吸着剤(4A)と下部吸着剤(4C)と
の間にはチューブの周設されていない部分が設けられて
、後記する吸着剤(4)同志の熱交換部分(4B)0
を形成している。In addition, a portion where the tube is not circumferentially provided is provided between the upper adsorbent (4A) and the lower adsorbent (4C), and a heat exchange portion (4B) between the adsorbent (4) to be described later. is formed.
以上が本発明にかかる吸着式冷凍機の構成の概略である
が、次にこの吸着式冷凍機の作用について以下説明する
。The above is an outline of the structure of the adsorption refrigerator according to the present invention. Next, the operation of this adsorption refrigerator will be explained below.
モータ(7)を駆動すると前記搬送手段(6)が回転し
、これによって吸着剤(4)は、円筒(5)内を上昇し
、円筒(5)上端に至り周辺に拡がって円筒(5)外周
と真空容器fil内周との間に構成された通路叫を金鋼
(8)部分まで落下し、再び円筒(5)内に入って上昇
するという循環をくり返す。When the motor (7) is driven, the conveying means (6) rotates, whereby the adsorbent (4) rises inside the cylinder (5), reaches the upper end of the cylinder (5), spreads around the cylinder (5) It falls through the passage formed between the outer periphery and the inner periphery of the vacuum container to the metal steel (8), enters the cylinder (5) again, and rises, repeating the cycle.
同時にこの間、凝縮器(2)に周設したチューブ(13
八)に冷却水を供給し、上部報吸着剤(4A)に周設し
たチューブ(13B)に熱源を供給し、下部吸着剤(4
C)に周設したチューブ(13C)に冷却水を供給し、
蒸発器(3)に周設したチューブ(130)に冷水を供
給する。At the same time, during this period, the tube (13
8), a heat source is supplied to the tube (13B) surrounding the upper adsorbent (4A), and a heat source is supplied to the tube (13B) surrounding the upper adsorbent (4A).
Supply cooling water to the tube (13C) installed around C),
Cold water is supplied to a tube (130) surrounding the evaporator (3).
すると上部吸着剤(4A)は加熱されて肌着作用が生じ
、凝縮器(2)に向かって水蒸気が放出される。Then, the upper adsorbent (4A) is heated and an undercoat effect occurs, and water vapor is released toward the condenser (2).
この水蒸気は、凝縮器(2)の中で冷却され、フィン(
9八)に水滴として付着後、前記冷媒貯溜部ODに蓄え
られ、トラップ配管α乃を介して蒸発器(3)に送られ
る。一方冷媒を脱着した後の吸着剤(4)は通路00を
落下して下部吸着剤(4C)となり、ここで冷却される
。この結果、下部吸着剤(4C)の側では吸着作用が生
じて蒸発器(3)の中の冷媒は吸着剤(4)に吸着され
、蒸発器(3)に冷熱が発生する。この冷熱がチューブ
(130)を流れる冷水によって蒸発器(3)から利用
側に供給されるのは通常の場合と同様である。This water vapor is cooled in the condenser (2) and the fins (
98), the refrigerant is stored in the refrigerant reservoir OD and sent to the evaporator (3) via the trap pipe α. On the other hand, the adsorbent (4) after desorbing the refrigerant falls down the passage 00 and becomes a lower adsorbent (4C), where it is cooled. As a result, an adsorption effect occurs on the lower adsorbent (4C) side, the refrigerant in the evaporator (3) is adsorbed by the adsorbent (4), and cold heat is generated in the evaporator (3). As in the normal case, this cold heat is supplied from the evaporator (3) to the user side by means of cold water flowing through the tube (130).
勿論、上記の各作用は、吸着剤(4)が循環することに
より連続して生じており、このためロスのない冷凍運転
が可能になるのは言う迄もない。Of course, the above-mentioned effects occur continuously as the adsorbent (4) circulates, and it goes without saying that loss-free refrigeration operation is therefore possible.
さらに、前記のように吸着剤(4)を中間に配し、上方
に凝縮器(2)、下方に蒸発器(3)が配置されている
ため、吸着剤(4)の上方が高圧側、下方が低圧側とな
り、通路αOを落下する吸着剤(4)を上方から押圧す
ることができ、下降する吸着剤が滞留することなく円滑
な循環が可能となる。Furthermore, as mentioned above, since the adsorbent (4) is placed in the middle, the condenser (2) is placed above and the evaporator (3) is placed below, the upper side of the adsorbent (4) is the high pressure side, The lower side is the low pressure side, and the adsorbent (4) falling down the passage αO can be pressed from above, allowing smooth circulation of the descending adsorbent without stagnation.
また、縦方向に構成された吸着剤粒子層、下降しながら
絶えず輸送装置の上方からの後続粒子によって補給され
、殆ど一定層厚みが維持される。In addition, the longitudinally structured adsorbent particle layer is continuously replenished while descending by subsequent particles from above the transport device, so that an almost constant layer thickness is maintained.
1
2
これにより上下の圧力差を保つ役割りをさせることも本
発明に係る吸着式冷凍機の特徴である。1 2 Another feature of the adsorption refrigerator according to the present invention is that it serves to maintain the pressure difference between the upper and lower sides.
一方、吸着剤(4)の循環経路中、上部吸着剤(4A)
と下部吸着剤(4C)の間に設けられた熱媒のチューブ
が周設されていない部分、即ち熱交換部分(4B)は円
筒【5)の中を上昇する吸着剤(4)とその周囲の通路
α0を落下する吸着剤(4)とが円筒(5)を介して互
いに熱交換する部分である。前者は冷却された後の吸着
剤(4)であり、これに対して後者は加熱された後の吸
着剤(4)であって、この両者が対向することにより上
昇する吸着剤(4)は加熱され、下降する吸着剤(4)
は冷却される。周知のように脱着作用に入る前の吸着剤
(4)を予熱し、吸着作用に入る前の吸着剤(4)を予
冷することで、吸着式冷凍サイクルのc、 o、 pは
向上する。上記の熱交換部分は、このための作用効果を
具備したものであり、従来のように同目的のためにさら
に熱交換器を付設する必要はない。On the other hand, in the circulation path of the adsorbent (4), the upper adsorbent (4A)
The heat exchanger section (4B), which is provided between the lower adsorbent (4C) and the part where the heating medium tube is not circumferential, is the part between the adsorbent (4) rising in the cylinder [5] and its surroundings. This is the part where the adsorbent (4) falling through the passage α0 exchanges heat with each other via the cylinder (5). The former is the adsorbent (4) after being cooled, whereas the latter is the adsorbent (4) after being heated, and the adsorbent (4) rising when these two face each other is Heated and descending adsorbent (4)
is cooled. As is well known, c, o, and p of an adsorption refrigeration cycle can be improved by preheating the adsorbent (4) before entering the desorption action and precooling the adsorbent (4) before entering the adsorption action. The heat exchange section described above has the function and effect for this purpose, and there is no need to provide an additional heat exchanger for the same purpose as in the conventional case.
なお、最後に本発明は以上の実施例に拘泥されるもので
ないことは勿論である。例えば真空容器(1)に周設し
たチューブ(13A)〜(130)等は、既知の加熱手
段、冷却手段に適宜変更可能なことは言う迄もない。Finally, it goes without saying that the present invention is not limited to the above embodiments. For example, it goes without saying that the tubes (13A) to (130) provided around the vacuum container (1) can be changed to known heating means and cooling means as appropriate.
(発明の効果)
本発明は以上のように吸着剤を搬送手段によって上昇せ
しめ、その周囲に吸着剤の自然落下通路を設けると共に
、吸着剤の上方に高圧側、吸着剤の下方に低圧側を形成
して吸着剤循環による構造の簡素な吸着式冷凍機を構成
するものである。(Effects of the Invention) As described above, the present invention raises the adsorbent by means of a conveyance means, provides a natural fall path for the adsorbent around it, and has a high pressure side above the adsorbent and a low pressure side below the adsorbent. This constitutes an adsorption refrigerator with a simple structure based on adsorbent circulation.
この他に以下のような特徴を有する。In addition, it has the following characteristics.
即ち前記上方の高圧側と、下方の低圧側との間に吸着剤
の集合体が介在して両者の飽和蒸気圧力差を保っている
ため、あえてこのための隔壁やその他の機構、あるいは
オリフィス等を付設する必要がない。In other words, an aggregate of adsorbents is interposed between the upper high-pressure side and the lower low-pressure side to maintain the saturated vapor pressure difference between the two, so a partition wall or other mechanism, or orifice, etc. There is no need to attach.
また吸着剤同志の対向流による熱交換部分を上部吸着剤
と下部吸着剤の間に設けることで脱着前の吸着剤が予熱
され、吸着前の吸着剤が予冷されるため、熱交換器を付
設しなくても良好な成績係数を得ることができる。In addition, by providing a heat exchange section between the upper adsorbent and the lower adsorbent through counterflow of adsorbents, the adsorbent before desorption is preheated and the adsorbent before adsorption is precooled, so a heat exchanger is installed. You can get a good coefficient of performance even if you don't.
3
4
さらに本発明の如く構成することによって、吸着剤の循
環に係る駆動装置は一基だけで良く、装置全体を小型、
かつ簡略な構成にすることができ、性能的には勿論、実
用的にも一層すぐれた吸着剤循環による吸着式冷凍機と
なる。3 4 Furthermore, by configuring as in the present invention, only one drive device is required for circulating the adsorbent, making the entire device compact and compact.
Moreover, the structure can be simplified, and an adsorption refrigerator with adsorbent circulation that is superior not only in terms of performance but also in practical terms can be obtained.
第1図は本発明吸着剤循環による吸着式冷凍機の部分上
面図及び側面図、第2図、第3図は従来の吸着式冷凍機
の側面図である。
(1)・・・真空容器、
(2)・・・凝縮器、
(3)・・・蒸発器、
(4)・・・吸着剤、
(4A)・・・上部吸着剤、
(4B〉・・・熱交換部分、
(4C)・・・下部吸着剤、
(6)・・・搬送手段、
(13A)〜(13D)・・・チューブ、αO・・・通
路。
5FIG. 1 is a partial top view and side view of an adsorption refrigerator using adsorbent circulation according to the present invention, and FIGS. 2 and 3 are side views of a conventional adsorption refrigerator. (1)...Vacuum container, (2)...Condenser, (3)...Evaporator, (4)...Adsorbent, (4A)...Upper adsorbent, (4B>・... Heat exchange part, (4C) ... Lower adsorbent, (6) ... Conveying means, (13A) - (13D) ... Tube, αO ... Passage. 5
Claims (1)
に配し、周囲に吸着剤の自然落下通路を設けて吸着剤の
循環経路を形成して、該循環サイクルと共に冷凍サイク
ルを形成せしめたことを特徴とする吸着剤循環による吸
着式冷凍機。 2、吸着剤循環経路の上方に高圧側の吸着剤加熱手段と
凝縮器を、一方、下方に低圧側の吸着剤冷却手段と蒸発
器を夫々配設し、両者の蒸気圧力差を吸着剤粒子層で保
持したことを特徴とする請求項1記載の吸着剤循環によ
る吸着式冷凍機。 3、吸着剤循環経路の上部吸着剤と下部吸着剤の間に、
脱着を終了して下降する吸着剤と吸着を終了して上昇す
る吸着剤とが伝熱壁面を介して熱交換する熱交換部分を
搬送通路と兼ねそなえたことを特徴とする請求項2記載
の吸着剤循環による吸着式冷凍機。[Claims] 1. A means for transporting the adsorbent upward is arranged at the center in the container, and a natural fall passage for the adsorbent is provided around the container to form a circulation path for the adsorbent, and the circulation cycle is An adsorption refrigerator using adsorbent circulation, which is characterized by forming a refrigeration cycle. 2. A high-pressure side adsorbent heating means and a condenser are arranged above the adsorbent circulation path, while a low-pressure side adsorbent cooling means and an evaporator are arranged below, and the vapor pressure difference between the two is used to calculate the adsorbent particles. The adsorption refrigerator according to claim 1, characterized in that the adsorbent is retained in layers. 3. Between the upper and lower adsorbents in the adsorbent circulation path,
3. A heat exchange section in which the adsorbent that descends after completing desorption and the adsorbent that ascends after completing adsorption exchange heat through a heat transfer wall surface also serves as a conveyance path. Adsorption refrigerator using adsorbent circulation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34232089A JPH0765819B2 (en) | 1989-12-28 | 1989-12-28 | Adsorption refrigerator with circulation of adsorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34232089A JPH0765819B2 (en) | 1989-12-28 | 1989-12-28 | Adsorption refrigerator with circulation of adsorbent |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03199864A true JPH03199864A (en) | 1991-08-30 |
JPH0765819B2 JPH0765819B2 (en) | 1995-07-19 |
Family
ID=18352816
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34232089A Expired - Fee Related JPH0765819B2 (en) | 1989-12-28 | 1989-12-28 | Adsorption refrigerator with circulation of adsorbent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0765819B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5421173A (en) * | 1992-11-03 | 1995-06-06 | Samsung Electronics Co., Ltd. | Absorption heating and cooling device |
EP0702199A1 (en) | 1994-09-19 | 1996-03-20 | Nippondenso Co., Ltd. | Adsorptive type refrigeration apparatus |
EP1645819A1 (en) * | 2004-10-08 | 2006-04-12 | Viessmann Werke GmbH & Co KG | Vacuum sorption device |
JP2012021712A (en) * | 2010-07-15 | 2012-02-02 | Fujitsu Ltd | Adsorption type heat pump |
JP2012247171A (en) * | 2011-05-31 | 2012-12-13 | Ricoh Co Ltd | Chemical heat pump and heat recovery method |
CN111801537A (en) * | 2018-03-07 | 2020-10-20 | 依诺森公司 | Adsorption heat pump |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5024815B2 (en) * | 2006-11-21 | 2012-09-12 | 独立行政法人産業技術総合研究所 | Adsorbent particle circulation type refrigerator |
-
1989
- 1989-12-28 JP JP34232089A patent/JPH0765819B2/en not_active Expired - Fee Related
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5421173A (en) * | 1992-11-03 | 1995-06-06 | Samsung Electronics Co., Ltd. | Absorption heating and cooling device |
US5542267A (en) * | 1992-11-03 | 1996-08-06 | Samsung Electronics Co., Ltd. | Absorption heating and cooling device |
EP0702199A1 (en) | 1994-09-19 | 1996-03-20 | Nippondenso Co., Ltd. | Adsorptive type refrigeration apparatus |
US5619866A (en) * | 1994-09-19 | 1997-04-15 | Nippondenso Co., Ltd. | Adsorptive type refrigeration apparatus |
EP1645819A1 (en) * | 2004-10-08 | 2006-04-12 | Viessmann Werke GmbH & Co KG | Vacuum sorption device |
JP2012021712A (en) * | 2010-07-15 | 2012-02-02 | Fujitsu Ltd | Adsorption type heat pump |
JP2012247171A (en) * | 2011-05-31 | 2012-12-13 | Ricoh Co Ltd | Chemical heat pump and heat recovery method |
CN111801537A (en) * | 2018-03-07 | 2020-10-20 | 依诺森公司 | Adsorption heat pump |
JP2021521409A (en) * | 2018-03-07 | 2021-08-26 | エネシオン インコーポレイテッド | Adsorption base heat pump |
CN115183501A (en) * | 2018-03-07 | 2022-10-14 | 依诺森公司 | Adsorption heat pump |
JP2023026674A (en) * | 2018-03-07 | 2023-02-24 | エネシオン インコーポレイテッド | Adsorption-based heat pump and method of water desalination |
US11619426B2 (en) | 2018-03-07 | 2023-04-04 | Enersion Inc. | Adsorption-based heat pump |
Also Published As
Publication number | Publication date |
---|---|
JPH0765819B2 (en) | 1995-07-19 |
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