JPS63231149A - Adsorption type refrigeration cycle - Google Patents
Adsorption type refrigeration cycleInfo
- Publication number
- JPS63231149A JPS63231149A JP6100887A JP6100887A JPS63231149A JP S63231149 A JPS63231149 A JP S63231149A JP 6100887 A JP6100887 A JP 6100887A JP 6100887 A JP6100887 A JP 6100887A JP S63231149 A JPS63231149 A JP S63231149A
- Authority
- JP
- Japan
- Prior art keywords
- refrigeration cycle
- adsorbent
- container
- heat
- water
- 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
Links
- 238000005057 refrigeration Methods 0.000 title claims description 17
- 238000001179 sorption measurement Methods 0.000 title claims description 16
- 239000003463 adsorbent Substances 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 239000000741 silica gel Substances 0.000 claims description 3
- 229910002027 silica gel Inorganic materials 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- 239000003507 refrigerant Substances 0.000 description 15
- 238000010438 heat treatment Methods 0.000 description 7
- 238000001816 cooling Methods 0.000 description 6
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 6
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 230000005855 radiation Effects 0.000 description 4
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は吸着式冷凍サイクルに係り、特にO′C以下の
冷熱源を得るのに好適な吸着式冷凍サイクルに関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an adsorption refrigeration cycle, and particularly to an adsorption refrigeration cycle suitable for obtaining a cold source below O'C.
放熱手段を設は内部にゼオライト等の吸着剤を充填した
容器に水を冷媒として封入した冷凍サイクルを連結した
ものがある。この吸着式冷凍サイクルは、ゼオライト等
の吸着された水蒸気を加熱装置によって蒸発させ、蒸発
に伴なう水の冷却で冷熱源を得て冷却に利用する吸着式
冷凍サイクルがある。Some devices are equipped with heat dissipation means and are connected to a refrigeration cycle in which water is sealed as a refrigerant to a container filled with an adsorbent such as zeolite. This adsorption type refrigeration cycle includes an adsorption type refrigeration cycle in which water vapor adsorbed on zeolite or the like is evaporated by a heating device, and a cold heat source is obtained by cooling the water accompanying the evaporation, which is used for cooling.
その−例を太陽熱を熱源とした第2図により説明する。An example of this will be explained with reference to FIG. 2 in which solar heat is used as a heat source.
17はゼオライト等の吸着剤を収納した容器であり、実
線矢印12の如く太陽熱を吸収したり破線矢印13の如
く夜間の天空放射により放熱する。該吸着剤収納容器1
7は放熱器14が接続されてさらに該放熱器14の他端
は水容器15が接続され、該水容器15内には熱交換器
16が設置されている。Reference numeral 17 denotes a container containing an adsorbent such as zeolite, which absorbs solar heat as shown by the solid arrow 12 and radiates heat by sky radiation at night as shown by the broken arrow 13. The adsorbent storage container 1
A radiator 14 is connected to 7, and a water container 15 is connected to the other end of the radiator 14, and a heat exchanger 16 is installed in the water container 15.
18は放熱器14を放熱するためのファンである。上述
の構成における密閉系の水吸着式冷凍サイクルにおいて
放熱器14からの放熱を加熱源として利用する場合には
吸着剤収納容器17を加熱して吸着剤中の水分を水蒸気
として分離せしめ、放熱器14において水蒸気の凝縮潜
熱を放出させて加熱能力を得て水にして水容器15に収
納させる。熱交換器16から冷却熱源を得る場合には、
水分を分離した吸着剤に水容器15内の水を水蒸気とし
て吸着せしめ、蒸発潜熱により冷却された水を冷熱源と
して熱交換器16で冷却能力を得ることができる。これ
を繰り返すことにより間欠的に加熱能力、冷却能力を発
生させることができる。18 is a fan for radiating heat from the radiator 14. When the heat radiation from the radiator 14 is used as a heating source in the closed water adsorption refrigeration cycle having the above configuration, the adsorbent storage container 17 is heated to separate the moisture in the adsorbent as water vapor, and the radiator 14 is heated. In step 14, the latent heat of condensation of water vapor is released to obtain heating ability, which is converted into water and stored in a water container 15. When obtaining a cooling heat source from the heat exchanger 16,
The water in the water container 15 is adsorbed as water vapor by the adsorbent from which water has been separated, and the heat exchanger 16 can obtain a cooling capacity by using the water cooled by the latent heat of vaporization as a cold heat source. By repeating this, heating capacity and cooling capacity can be generated intermittently.
尚、この種の吸着式冷凍サイクルは1982年発行第4
6巻第7号「化学工業」の第23頁〜第25頁に論じら
れている。This type of adsorption refrigeration cycle was published in 1982, No. 4.
Discussed in Vol. 6, No. 7, "Chemical Industry", pages 23 to 25.
上記従来技術は、水を冷媒として利用しているために0
℃以下の冷熱源が必要な食品の冷凍や製氷に際しては、
水の凝固温度が0℃であるために冷媒である水が固化し
てしまい0℃以下の冷熱源を得ることができないという
問題があった。The above conventional technology uses water as a refrigerant, so
When freezing food or making ice that requires a cold source below ℃,
Since the solidification temperature of water is 0°C, there is a problem in that the water as a refrigerant solidifies, making it impossible to obtain a cold source at temperatures below 0°C.
本発明の目的は、0℃以下の冷熱源が得られる吸着式冷
凍サイクルを提供することにある。An object of the present invention is to provide an adsorption refrigeration cycle that can provide a cold source at temperatures below 0°C.
上記目的は、内部に吸着剤を充填した容器と、この容器
に逆止弁を介して連結された凝縮器と、上記凝縮器に連
結された液溜部と、上記液溜部に連結された開閉弁と、
上記開閉弁に連結された減圧装置と、上記減圧装置に連
結された蒸発器とからなり、上記容器にヒーターを設け
るとともに、上記容器内にフロン系ガスの冷媒を封入す
ることにより達成される。The above purpose includes a container filled with an adsorbent inside, a condenser connected to the container via a check valve, a liquid reservoir connected to the condenser, and a liquid reservoir connected to the liquid reservoir. An on-off valve,
It consists of a pressure reducing device connected to the on-off valve and an evaporator connected to the pressure reducing device, and is achieved by providing a heater in the container and sealing a fluorocarbon gas refrigerant in the container.
容器内に封入されたフロン系ガスの凝固温度は0℃以下
であるから、蒸発器は0℃以下の冷熱を発生することが
できる。Since the solidification temperature of the fluorocarbon gas sealed in the container is 0°C or lower, the evaporator can generate cold heat at 0°C or lower.
以下、本発明の一実施例を第1図により説明する。第1
図は本発明の吸着式冷凍サイクルの構成図である。1は
吸着材収納容器でシリカゲル等の吸着剤1aが充填され
ている。この吸着剤収納容器1には放熱手段2と加熱手
段3とが具備されている。吸着剤収納容器1にはガス冷
媒送出パイプ4が逆止弁5を介して接続されており、凝
縮用放熱器6を有する液溜め部7と連結されている。上
記液溜め部7の下部には開閉弁8を介して減圧機構9が
接続されている。該減圧機構9の他端には蒸発器10が
接続されている。該蒸発器10の他端は逆止弁11を介
して吸着剤収納容器1に連結されている。12は蒸発器
10を含めた冷熱源利用系である。An embodiment of the present invention will be described below with reference to FIG. 1st
The figure is a block diagram of the adsorption refrigeration cycle of the present invention. 1 is an adsorbent storage container filled with an adsorbent 1a such as silica gel. This adsorbent storage container 1 is equipped with a heat radiation means 2 and a heating means 3. A gas refrigerant delivery pipe 4 is connected to the adsorbent storage container 1 via a check valve 5, and is connected to a liquid reservoir 7 having a condensing radiator 6. A pressure reducing mechanism 9 is connected to the lower part of the liquid reservoir 7 via an on-off valve 8. An evaporator 10 is connected to the other end of the pressure reducing mechanism 9. The other end of the evaporator 10 is connected to the adsorbent storage container 1 via a check valve 11. 12 is a cold heat source utilization system including the evaporator 10.
上述の如き吸着式冷凍サイクルは、冷凍サイクル内にフ
ロン系等の冷媒を封入し、開閉弁8を閉じ加熱−!AA
s2容器1を30℃〜40℃に加熱すると、吸着剤1a
に吸着していたフロン系ガス冷媒は加熱され高圧ガス冷
媒となって容器1から凝縮用放熱器6に放出される。凝
縮用放熱器6では高圧ガス冷媒が、凝縮潜熱を放出する
ことによって液化する。液化した冷媒は液溜部7内に貯
溜する。しかる後、加熱装置3で容器1を加熱すること
を停止させ冷熱源利用系12と連係させて開閉弁8を開
にすると減圧機構9を通過した高圧液冷発器10内の低
温低圧液冷媒は蒸発潜熱により冷熱源利用系12を冷却
し低圧ガス冷媒となり容器1内の吸着剤1aに放熱手段
2に吸着熱を放出しながら吸着される。これを間欠的に
繰り返すことにより冷熱源利用系12を連続して冷却す
ることが可能になる。なお、吸着剤収納容器1.凝縮用
放熱系6.液溜め部7、減圧機構9等を2セツトとし、
1個の蒸発器10に具備させれば連続的に冷却作用を持
続できることは言うまでもない。In the adsorption type refrigeration cycle as described above, a refrigerant such as fluorocarbon is sealed in the refrigeration cycle, and the on-off valve 8 is closed to heat the cycle. A.A.
When the s2 container 1 is heated to 30°C to 40°C, the adsorbent 1a
The fluorocarbon-based gas refrigerant adsorbed on the container 1 is heated and becomes a high-pressure gas refrigerant, which is discharged from the container 1 to the condensing radiator 6. In the condensing heat radiator 6, the high-pressure gas refrigerant liquefies by releasing latent heat of condensation. The liquefied refrigerant is stored in the liquid reservoir 7. Thereafter, when the heating device 3 stops heating the container 1 and the on-off valve 8 is opened in conjunction with the cold source utilization system 12, the low-temperature, low-pressure liquid refrigerant in the high-pressure liquid refrigerator 10 that has passed through the pressure reduction mechanism 9 is removed. The latent heat of vaporization cools the cold heat source utilization system 12 and becomes a low-pressure gas refrigerant, which is adsorbed by the adsorbent 1a in the container 1 while releasing heat of adsorption to the heat radiating means 2. By repeating this intermittently, it becomes possible to continuously cool the cold heat source utilization system 12. In addition, adsorbent storage container 1. Heat dissipation system for condensation 6. There are two sets of liquid reservoir 7, pressure reducing mechanism 9, etc.
It goes without saying that if one evaporator 10 is equipped, the cooling effect can be maintained continuously.
尚、フロン系冷媒ガスが吸着するための吸着剤の穴径は
、例えば冷蔵庫に使用されているフロン12冷媒ガスの
分子径が5オングストロ一ム程度であるから1本実施例
を冷蔵庫に使用する場合は穴径が13オングストロ一ム
程度のシリカゲル系吸着剤が適している。The hole diameter of the adsorbent for adsorbing the fluorocarbon-based refrigerant gas is, for example, because the molecular diameter of the fluorocarbon 12 refrigerant gas used in refrigerators is approximately 5 angstroms, so this embodiment is used for refrigerators. In this case, a silica gel adsorbent with a hole diameter of about 13 angstroms is suitable.
本発明によれば、吸着式冷凍サイクルにフロン系冷媒ガ
スを使用したので0℃以下の冷熱源を得ることができる
効果がある。According to the present invention, since a fluorocarbon-based refrigerant gas is used in the adsorption type refrigeration cycle, it is possible to obtain a cold heat source of 0° C. or lower.
第1図は本発明の一実施例を備えた吸着式冷凍サイクル
の構成図、第2図は従来の水吸着式冷凍サイクルの構成
図である。FIG. 1 is a block diagram of an adsorption type refrigeration cycle equipped with an embodiment of the present invention, and FIG. 2 is a block diagram of a conventional water adsorption type refrigeration cycle.
1・・・フロン吸着材収納容器、2・・・放熱手段、3
・・・II熱手段、6・・・凝縮用放熱系、7・・・液
溜め部。1... Freon adsorbent storage container, 2... Heat dissipation means, 3
...II heat means, 6... condensing heat radiation system, 7... liquid reservoir section.
8・・・開閉弁、9・・・減圧機構、IO・・・然発器
、11・・・冷熱源利用系、14・・・放熱器、15・
・・水容器、16・・・熱交換器、17・・・水分吸着
剤収納容器。8... Opening/closing valve, 9... Pressure reduction mechanism, IO... Natural generator, 11... Cold heat source utilization system, 14... Heat radiator, 15...
...Water container, 16...Heat exchanger, 17...Moisture adsorbent storage container.
′t−1121 1・70〉吸着材1又納容器 6 凝椙用v!!L!。't-1121 1.70〉Adsorbent 1-fold storage container 6. For condensation v! ! L! .
Claims (1)
を介して連結された凝縮器と、上記凝縮器に連結された
液溜め部と、上記液溜め部に連結された開閉弁と、上記
開閉弁に連結された減圧装置と、上記減圧装置に連結さ
れた蒸発器とからなり、上記容器にヒータを設けるとと
もに、上記容器内にフロン系ガスの冷媒を封入したこと
を特徴とする吸着式冷凍サイクル。 2、上記吸着剤をシリカゲル系吸着剤としたことを特徴
とする特許請求の範囲第1項記載の吸着式冷凍サイクル
。[Claims] 1. A container filled with an adsorbent, a condenser connected to the container via a check valve, a liquid reservoir connected to the condenser, and a liquid reservoir It consists of an on-off valve connected to the on-off valve, a pressure reducing device connected to the on-off valve, and an evaporator connected to the pressure reducing device. An adsorption refrigeration cycle characterized by the fact that it is sealed. 2. The adsorption type refrigeration cycle according to claim 1, wherein the adsorbent is a silica gel-based adsorbent.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6100887A JPS63231149A (en) | 1987-03-18 | 1987-03-18 | Adsorption type refrigeration cycle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6100887A JPS63231149A (en) | 1987-03-18 | 1987-03-18 | Adsorption type refrigeration cycle |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63231149A true JPS63231149A (en) | 1988-09-27 |
Family
ID=13158879
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6100887A Pending JPS63231149A (en) | 1987-03-18 | 1987-03-18 | Adsorption type refrigeration cycle |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63231149A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04124566A (en) * | 1990-09-14 | 1992-04-24 | Matsushita Electric Ind Co Ltd | Heat transfer device |
JP2012083015A (en) * | 2010-10-08 | 2012-04-26 | Fuji Silysia Chemical Ltd | Adsorption heat pump |
-
1987
- 1987-03-18 JP JP6100887A patent/JPS63231149A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04124566A (en) * | 1990-09-14 | 1992-04-24 | Matsushita Electric Ind Co Ltd | Heat transfer device |
JP2012083015A (en) * | 2010-10-08 | 2012-04-26 | Fuji Silysia Chemical Ltd | Adsorption heat pump |
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