JPS6119408Y2 - - Google Patents
Info
- Publication number
- JPS6119408Y2 JPS6119408Y2 JP6741682U JP6741682U JPS6119408Y2 JP S6119408 Y2 JPS6119408 Y2 JP S6119408Y2 JP 6741682 U JP6741682 U JP 6741682U JP 6741682 U JP6741682 U JP 6741682U JP S6119408 Y2 JPS6119408 Y2 JP S6119408Y2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- cooling cycle
- generators
- electric heater
- heating means
- 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.)
- Expired
Links
- 238000001816 cooling Methods 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000010521 absorption reaction Methods 0.000 claims description 5
- 238000009792 diffusion process Methods 0.000 claims description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 5
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000003507 refrigerant Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
【考案の詳細な説明】
本考案はアンモニア溶液等を冷媒とし、水素ガ
ス等を不活性ガスとして自然循環により冷却作用
を行なわしめる所謂拡散吸収式冷却装置の改良構
成に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved structure of a so-called diffusion absorption type cooling device that performs cooling by natural circulation using an ammonia solution or the like as a refrigerant and hydrogen gas or the like as an inert gas.
此種拡散吸収式冷却装置に於いてはアンモニア
溶液等を冷媒として用い、発生器に於いて電気ヒ
ータ装置やガスバーナ、石油バーナ等でアンモニ
ア溶液を加熱する事によりアンモニアガスを発生
し該アンモニアガスを凝縮器で液化しその液化ア
ンモニアを蒸発器に導入し水素ガス等の不活性ガ
ス中で蒸発せしめ、その時に生ずる吸熱作用によ
り冷却を行なうものである。このアンモニア溶液
の循環は重力に依存しており、冷却サイクル内の
アンモニア濃溶液と稀溶液の水位差によつて生じ
るものである。従つて冷却能力を増大せしめる事
は即ち冷却装置自体の縦寸法の拡大に結びつく。
従つて上方に開口する所謂チエスト型冷蔵庫等の
様に冷蔵庫本体の縦寸法を大きく出来ない場合に
は必然的に冷却装置の能力を大きくする事が出来
ない欠点が有つた。 In this type of diffusion absorption type cooling device, ammonia solution or the like is used as a refrigerant, and ammonia gas is generated by heating the ammonia solution in a generator with an electric heater device, gas burner, oil burner, etc. The liquefied ammonia is liquefied in a condenser and then introduced into an evaporator where it is evaporated in an inert gas such as hydrogen gas and cooled by the endothermic action that occurs at that time. This circulation of the ammonia solution is dependent on gravity and is caused by the water level difference between the concentrated ammonia solution and the dilute solution in the cooling cycle. Therefore, increasing the cooling capacity leads to an increase in the vertical dimension of the cooling device itself.
Therefore, in cases where the vertical dimension of the refrigerator body cannot be increased, such as a so-called chest-type refrigerator with an upward opening, there is inevitably a drawback that the capacity of the cooling device cannot be increased.
本考案は上記欠点に鑑みて成されたもので、以
下実施例を図面に基づいて説明する。1は例えば
上方に開口する所謂チエスト型冷蔵庫本体で例え
ばその背壁に拡散吸収式冷却装置としての第1の
冷却サイクル2と第2の冷却サイクル3が設けら
れている。第1の冷却サイクル2は冷蔵庫本体1
の外側に設けられる発生器4、精溜器5、凝縮器
6、吸収器7、受液器8、液熱交換器9と、庫内
10側に配設される蒸発器11とから成り、第2
の冷却サイクル3は発生器12、精溜器13、凝
縮器14、吸収器15、受液器16、液熱交換器
17と、庫内10側に配設される蒸発器18とか
ら構成されている。第1の冷却サイクル2と第2
の冷却サイクル3は各々の発生器4,12を背壁
略中央部に於いて近接或いは密接した状態で略左
右対称に設けられる。19は加熱手段としての電
気ヒータ装置であり発生器4と12の相方に熱交
換的に密接して設けられる。20は図示しないガ
スバーナ或いは石油バーナ等の熱を伝達する煙管
であり電気ヒータ装置19同様発生器4と12の
相方に熱交換的に配設される。この煙管20は電
気ヒータ装置19の電源の無い地域等で使用され
る場合に電気ヒータ装置19の代わりに発生器4
及び12を加熱する。これら加熱手段は周囲を発
生器4及び12と共に断熱材21によつて被覆さ
れ、これによつて上記加熱手段から発生した熱の
殆んどが発生器4及び12の加熱に消費されるこ
とになる。これによつて両冷却サイクル2,3内
の冷媒が循環せられて蒸発器11,18によつて
庫内10は蒸発器1個の場合に比して強力に冷却
されることになる。 The present invention has been developed in view of the above-mentioned drawbacks, and embodiments thereof will be described below with reference to the drawings. Reference numeral 1 denotes, for example, a so-called chest-type refrigerator main body that opens upward, and a first cooling cycle 2 and a second cooling cycle 3 as a diffusion-absorption cooling device are provided on the back wall thereof, for example. The first cooling cycle 2 is the refrigerator main body 1
It consists of a generator 4, a rectifier 5, a condenser 6, an absorber 7, a liquid receiver 8, a liquid heat exchanger 9, and an evaporator 11 arranged on the inside 10 side. Second
The cooling cycle 3 is composed of a generator 12, a rectifier 13, a condenser 14, an absorber 15, a liquid receiver 16, a liquid heat exchanger 17, and an evaporator 18 disposed on the inside 10 side. ing. First cooling cycle 2 and second
The cooling cycle 3 is provided approximately laterally symmetrically with the respective generators 4 and 12 located close to or in close contact with each other at approximately the center of the back wall. Reference numeral 19 denotes an electric heater device as a heating means, which is provided in close proximity to the generators 4 and 12 for heat exchange. Reference numeral 20 denotes a smoke pipe for transmitting heat from a gas burner or oil burner (not shown), and like the electric heater device 19, it is disposed on a partner of the generators 4 and 12 for heat exchange. This smoke pipe 20 is used as a generator 4 instead of the electric heater device 19 when used in an area where there is no power source for the electric heater device 19.
and 12 is heated. These heating means, together with the generators 4 and 12, are surrounded by a heat insulating material 21, so that most of the heat generated from the heating means is consumed in heating the generators 4 and 12. Become. As a result, the refrigerant in both cooling cycles 2 and 3 is circulated, and the interior 10 of the refrigerator is cooled more powerfully by the evaporators 11 and 18 than in the case of only one evaporator.
本考案は以上の如く構成した事により冷却サイ
クルの縦寸法を制約される状況下に於いても、縦
寸法を増大させる事なく冷却能力を向上させる事
が出来る。又冷却サイクルも現行の物を用いれば
良く新たに開発する必要が無い。更に電気ヒータ
装置やガスバーナ或いは石油バーナ等の加熱手段
は単一の冷却サイクル分でよいから経済的であ
り、加熱箇所も1箇所に集中するので熱ロスが少
ない。又加熱手段を単一とした事によつて、複数
の冷却サイクルを用いても温度制御が簡単になる
等実用的効果の大なるものである。 By virtue of the configuration of the present invention as described above, even under conditions where the vertical dimension of the cooling cycle is restricted, the cooling capacity can be improved without increasing the vertical dimension. Furthermore, the existing cooling cycle can be used without any need for new development. Furthermore, heating means such as an electric heater device, a gas burner, or an oil burner can be used for a single cooling cycle, which is economical, and since heating is concentrated in one location, there is little heat loss. Furthermore, by using a single heating means, temperature control becomes simple even when using a plurality of cooling cycles, which has great practical effects.
各図は本考案の実施例を示すもので第1図は冷
蔵庫の背面図、第2図は第1図のA−A′線断面
図である。
2……第1冷却サイクル、3……第2冷却サイ
クル、4,12……発生器、19……電気ヒータ
装置、20……煙管。
Each figure shows an embodiment of the present invention, and FIG. 1 is a rear view of the refrigerator, and FIG. 2 is a sectional view taken along the line A-A' in FIG. 1. 2... First cooling cycle, 3... Second cooling cycle, 4, 12... Generator, 19... Electric heater device, 20... Smoke pipe.
Claims (1)
いは密接して並設された2系統の拡散吸収式冷却
サイクルと、前記両発生器の相方に熱伝導的に配
設された加熱手段とから成る拡散吸収式冷却装
置。 A diffusion absorption cooling cycle consisting of two systems of diffusion absorption cooling cycles in which the generators constituting the cooling cycle are arranged close to each other or closely in parallel, and a heating means arranged thermally conductively on the other side of both of the generators. type cooling device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6741682U JPS58169461U (en) | 1982-05-08 | 1982-05-08 | Diffusion absorption cooling device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6741682U JPS58169461U (en) | 1982-05-08 | 1982-05-08 | Diffusion absorption cooling device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58169461U JPS58169461U (en) | 1983-11-11 |
JPS6119408Y2 true JPS6119408Y2 (en) | 1986-06-11 |
Family
ID=30077245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6741682U Granted JPS58169461U (en) | 1982-05-08 | 1982-05-08 | Diffusion absorption cooling device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58169461U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100908501B1 (en) | 2003-03-12 | 2009-07-24 | 주식회사 유일파워텍 | Evaporator Structure for Diffusion Absorption Refrigerator |
-
1982
- 1982-05-08 JP JP6741682U patent/JPS58169461U/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100908501B1 (en) | 2003-03-12 | 2009-07-24 | 주식회사 유일파워텍 | Evaporator Structure for Diffusion Absorption Refrigerator |
Also Published As
Publication number | Publication date |
---|---|
JPS58169461U (en) | 1983-11-11 |
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