JPH07269994A - Cooling system - Google Patents

Cooling system

Info

Publication number
JPH07269994A
JPH07269994A JP6063101A JP6310194A JPH07269994A JP H07269994 A JPH07269994 A JP H07269994A JP 6063101 A JP6063101 A JP 6063101A JP 6310194 A JP6310194 A JP 6310194A JP H07269994 A JPH07269994 A JP H07269994A
Authority
JP
Japan
Prior art keywords
refrigerant
oxygen
cooling system
composition
absorbing agent
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
JP6063101A
Other languages
Japanese (ja)
Inventor
Yoshiaki Inoue
義彰 井上
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.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP6063101A priority Critical patent/JPH07269994A/en
Publication of JPH07269994A publication Critical patent/JPH07269994A/en
Pending legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Gas Separation By Absorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To prevent substitute fluorocarbon, reduction in cooling function or corrosion of metal of a device by a method wherein oxygen absorbing agent is arranged in a circulating system of a cooling system. CONSTITUTION:In a refrigerator having a freezing device operated under a cycle of compression and liquefaction of refrigerant and expansion gasification, an oxygen absorbing agent storing part 5 is arranged at a pocket part where it is out of a refrigerant compressor 1 so as to arranged the oxygen absorbing agent. The oxygen absorbing agent to be applied is composed of oxygen, moisture, carbonic acid gas and absorbing composition of organic material. More practically, the agent is composed of composition including organic material having non-saturated coupling, and composition including alkali metal or oxide of alkaline earth metal can be added. With such an arrangement as above, decomposition of the substitute fluorocarbon of the refrigerant is prevented. Even if a small amount of decomposition of the substitute fluorocarbon is present, the decomposed product is absorbed into the oxygen absorbing agent 5 and the substitute fluorocarbon can be used as refrigerant without making any corrosion of metallic material of the freezing device.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はフロンを冷媒とする冷却
システムに関しく、詳しくは、家庭用の冷蔵庫、冷凍
庫、ルームクーラー、カークーラー等の冷却機器さらに
は産業用冷蔵庫、冷凍庫等に採用して、冷媒に代替フロ
ン類を用いても分解することがなく安定的に長期運転が
可能な冷却システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling system using chlorofluorocarbon as a refrigerant, and more specifically, it is used in refrigerators for home use, refrigerators, room coolers, car coolers and the like, as well as industrial refrigerators and freezers. In addition, the present invention relates to a cooling system which can be stably operated for a long period of time without decomposing even if alternative CFCs are used as a refrigerant.

【0002】[0002]

【従来の技術】家庭用、産業用の冷凍、冷蔵機器には、
冷媒の圧縮液化−膨張ガス化サイクルによる冷却システ
ムが採用されている。この冷却システムには、安定な冷
媒として従来から特定フロンが好適に使用されてきた。
2. Description of the Related Art Household and industrial refrigeration and refrigeration equipment is
A cooling system using a compression liquefaction-expansion gasification cycle of a refrigerant has been adopted. In the cooling system, a specific CFC has been conventionally suitably used as a stable refrigerant.

【0003】しかしながら、特定フロンはオゾン層破壊
物質として1995年中には全廃される。このため、特
定フロンに替えて指定フロン又は代替フロンなどの代替
フロン類の使用が進められているが、代替フロン類は特
定フロンに比べて分解し易いために、冷媒に用いた場
合、冷凍装置や冷却装置の金属材料の腐食や真空度の低
下による熱効率の低下の原因になる。
However, specific CFCs are completely abolished in 1995 as ozone depleting substances. For this reason, alternative CFCs such as designated CFCs or alternative CFCs are being used in place of CFCs, but CFCs are more likely to decompose than CFCs. It also causes corrosion of the metal material of the cooling device and a decrease in the degree of vacuum, resulting in a decrease in thermal efficiency.

【0004】フロン類は本来吸湿性であり、冷媒に伴わ
れて水分が冷却システム中に混入することは好ましくな
く、従来から、冷却システム系内に活性炭や水分吸収剤
を配して水分の除去が行われている。しかし、代替フロ
ン類の場合には、冷却システム系内の単に水分の除去だ
けでは十分でなく、系内に持ち込まれたりリークしたり
してくる微量酸素によって代替フロン類が容易に分解す
るため、さらには圧縮機の潤滑油の分解を促進するた
め、代替フロン類の使用には冷蔵・冷凍機器の冷却機能
と耐用性に問題があった。
Fluorocarbons are inherently hygroscopic, and it is not preferable that water is mixed with the refrigerant into the cooling system. Conventionally, activated carbon or a water absorbent is arranged in the cooling system to remove water. Is being done. However, in the case of alternative CFCs, simply removing water in the cooling system is not sufficient, and the alternative CFCs are easily decomposed by trace oxygen introduced into the system or leaking, Furthermore, the use of alternative CFCs has a problem in the cooling function and durability of refrigerating / refrigerating equipment because it accelerates the decomposition of the lubricating oil of the compressor.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、冷却
システム系内における代替フロン類の分解を防止するこ
とにより、冷却機能低下や装置金属の腐食を防止し、代
替フロン類を使用する冷蔵・冷凍機器の上記問題を解決
することにある。
SUMMARY OF THE INVENTION An object of the present invention is to prevent decomposition of alternative CFCs in a cooling system system, thereby preventing deterioration of cooling function and corrosion of apparatus metal, and refrigeration using alternative CFCs. -To solve the above problems of refrigeration equipment.

【0006】[0006]

【課題を解決するための手段】本発明者らは上記の問題
点に鑑み数々の検討を実施したところ、代替フロン類を
冷媒とする冷却システムの冷媒循環系に酸素吸収剤を配
し、酸素、さらには水分、炭酸ガスおよび有機物をトラ
ップすることにより、容易に上記課題の解決できること
を見いだし、本発明を完成させた。
Means for Solving the Problems The inventors of the present invention have made various investigations in view of the above-mentioned problems. As a result, an oxygen absorbent is arranged in a refrigerant circulation system of a cooling system using alternative CFCs as a refrigerant, and Furthermore, they have found that the above problems can be easily solved by trapping water, carbon dioxide gas and organic matter, and have completed the present invention.

【0007】すなわち、本発明は、冷媒の圧縮液化と膨
張ガス化のサイクルによるフロンを冷媒とする冷却シス
テムの冷媒循環系に酸素吸収剤を配することを特徴とす
る冷却システムに関する発明である。さらには、冷媒の
循環系に配する酸素吸収剤が酸素、水分、炭酸ガスおよ
び有機物を吸収する組成物よりなる冷却システムに関す
る発明である。より詳しくは、冷媒の循環系に配する酸
素吸収剤が不飽和結合を有する有機化合物を含む組成物
よりなる冷却システムに関する発明である。
That is, the present invention is an invention relating to a cooling system characterized by arranging an oxygen absorbent in a refrigerant circulation system of a cooling system using Freon as a refrigerant by a cycle of compression liquefaction and expansion gasification of the refrigerant. Furthermore, the present invention relates to a cooling system in which the oxygen absorbent arranged in the circulation system of the refrigerant comprises a composition that absorbs oxygen, moisture, carbon dioxide gas and organic matter. More specifically, the invention relates to a cooling system including a composition in which an oxygen absorbent arranged in a circulation system of a refrigerant contains an organic compound having an unsaturated bond.

【0008】本発明に係る冷却システムでは、まず冷媒
のフロンが圧縮機で圧縮され、圧縮された冷媒は放熱器
で放熱して凝縮液化し、次いで液化した冷媒は膨張器で
断熱膨張、気化して温度が低下し、冷却した冷媒が冷却
器で熱交換して外部から熱を奪い冷却する。熱交換を終
えた冷媒ガスは再び圧縮機に戻され、圧縮液化−膨張ガ
ス化の冷却サイクルが繰り返される。
In the cooling system according to the present invention, first, the CFC of the refrigerant is compressed by the compressor, the compressed refrigerant radiates heat by the radiator and is condensed and liquefied, and then the liquefied refrigerant is adiabatically expanded and vaporized by the expander. As a result, the cooled refrigerant exchanges heat with the cooler to take heat from the outside and cool. The refrigerant gas that has completed the heat exchange is returned to the compressor again, and the cooling cycle of compression liquefaction-expansion gasification is repeated.

【0009】本発明においては、酸素吸収剤が上記の冷
却システムの冷媒循環系に配されるが、その配置個所は
酸素吸収剤が吸収機能を発揮できるところであれば特に
限定されず、冷媒フロンが気体状で酸素吸収剤に接触で
きる個所が好ましい。例えば、気体状の冷媒を圧縮器で
圧縮した個所、または冷媒が放熱器で放熱して凝縮して
いる個所、液状冷媒を真空下で気化している個所が挙げ
られ、いずれにしても冷媒が気体状で酸素吸収剤に効率
的に接触できることが好ましい。
In the present invention, the oxygen absorbent is arranged in the refrigerant circulation system of the above cooling system, but the arrangement position is not particularly limited as long as the oxygen absorbent can exhibit the absorbing function, and the refrigerant CFC is A location that can contact the oxygen absorbent in a gaseous state is preferable. For example, a location where a gaseous refrigerant is compressed by a compressor, or a location where the refrigerant radiates heat in a radiator to condense, a location where a liquid refrigerant is vaporized under vacuum, and in any case the refrigerant is It is preferable that the oxygen can be efficiently contacted with the oxygen absorbent in a gaseous state.

【0010】本発明に冷媒のフロンとしては、指定フロ
ンや代替フロンなどの代替フロン類を用いることができ
る。指定フロンの代表例としては、HCFC−22、H
CFC−123、HCFC−124、HCFC−141
B、HCFC−142B、HCFC−225CA、HC
FC−225CD等が挙げられ、代替フロンの代表例と
しては、HFC−125、HFC−134A、HFC−
152A等が挙げられる。
As the CFC of the refrigerant in the present invention, alternative CFCs such as designated CFCs and CFC alternatives can be used. Typical examples of designated CFCs are HCFC-22 and H
CFC-123, HCFC-124, HCFC-141
B, HCFC-142B, HCFC-225CA, HC
FC-225CD and the like, and typical examples of CFC alternatives include HFC-125, HFC-134A, and HFC-.
152A etc. are mentioned.

【0011】本発明に係る酸素吸収剤は、水分が実質的
非存在下で酸素を吸収することができるものであり、さ
らには水分、炭酸ガスおよび有機物を吸収することがで
きることがより好ましい。本発明に用いられる酸素吸収
剤は、酸素、水分、炭酸ガスおよび有機物を吸収する組
成物からなる。具体的には、不飽和結合を有する有機物
を含む組成物(A)からなるものであり、さらにアルカ
リ金属又はアルカリ土類金属の酸化物を含む組成物
(B)を加えることができる。
The oxygen absorbent according to the present invention is capable of absorbing oxygen in the substantial absence of water, and more preferably capable of absorbing water, carbon dioxide gas and organic substances. The oxygen absorbent used in the present invention is composed of a composition that absorbs oxygen, moisture, carbon dioxide gas and organic matter. Specifically, it is composed of the composition (A) containing an organic material having an unsaturated bond, and the composition (B) containing an oxide of an alkali metal or an alkaline earth metal can be further added.

【0012】不飽和結合を有する有機物を含む組成物
(A)は、主剤の不飽和結合を有する有機物の他に酸化
促進物質、塩基性物質および吸着剤よりなるものであ
る。不飽和結合を有する有機物としては、不飽和脂肪酸
化合物および/または不飽和基を有する鎖状炭化水素重
合物が用いられる。
The composition (A) containing an organic compound having an unsaturated bond is composed of an oxidation promoting substance, a basic substance and an adsorbent in addition to the organic compound having an unsaturated bond as the main ingredient. As the organic compound having an unsaturated bond, an unsaturated fatty acid compound and / or a chain hydrocarbon polymer having an unsaturated group is used.

【0013】ここで用いる不飽和脂肪酸化合物とは、炭
素数が10以上で炭素原子間の二重結合一つ以上を有す
る不飽和脂肪酸、該不飽和脂肪酸のエステル、該不飽和
脂肪酸エステルを含有する油脂類、該不飽和脂肪酸の塩
などである。炭素数が10以上で炭素原子間の二重結合
一つ以上を有する不飽和脂肪酸としては、例えばオレイ
ン酸、リノール酸、リノレン酸、アラキドン酸、パリナ
リン酸、ダイマー酸、リチノレイン酸またはリシノール
酸などが挙げられ、不飽和脂肪酸化合物として、これら
の不飽和脂肪酸、不飽和脂肪酸のエステル、不飽和脂肪
酸エステル類を含有する油脂、不飽和脂肪酸の金属塩な
どが挙げられる。
The unsaturated fatty acid compound used herein includes an unsaturated fatty acid having 10 or more carbon atoms and at least one double bond between carbon atoms, an ester of the unsaturated fatty acid, and an unsaturated fatty acid ester. Oils and fats, salts of the unsaturated fatty acids, and the like. Examples of the unsaturated fatty acid having 10 or more carbon atoms and one or more double bonds between carbon atoms include, for example, oleic acid, linoleic acid, linolenic acid, arachidonic acid, parinaric acid, dimer acid, ricinoleic acid or ricinoleic acid. Examples of the unsaturated fatty acid compound include unsaturated fatty acids, esters of unsaturated fatty acids, fats and oils containing unsaturated fatty acid esters, metal salts of unsaturated fatty acids, and the like.

【0014】不飽和基を有する鎖状炭化水素重合物と
は、炭素数が10以上で炭素原子間の二重結合一つ以上
を有する鎖状炭化水素重合物およびその誘導体である。
該誘導体としては、例えば、水酸基、ホルミル基等の置
換基を有する化合物であってもよい。炭素数が10以上
で炭素原子間の二重結合一つ以上を有する鎖状炭化水素
重合物としては、ブタジエン、イソプレン、1,3−ペ
ンタジエンなどで例示される鎖状不飽和炭化水素の重合
体を用いることができ、重合体としてオリゴマーであっ
てもよい。
The chain hydrocarbon polymer having an unsaturated group is a chain hydrocarbon polymer having 10 or more carbon atoms and one or more double bonds between carbon atoms, and derivatives thereof.
The derivative may be, for example, a compound having a substituent such as a hydroxyl group or a formyl group. Examples of the chain hydrocarbon polymer having 10 or more carbon atoms and one or more double bonds between carbon atoms include chain unsaturated hydrocarbon polymers exemplified by butadiene, isoprene, and 1,3-pentadiene. Can be used, and the polymer may be an oligomer.

【0015】不飽和結合を有する有機物は酸素吸収反応
の主剤となるものであり、好ましくは主剤として、不飽
和脂肪酸の遷移金属塩または不飽和脂肪酸の遷移金属塩
と不飽和脂肪酸の混合物、もしくはこれら混合に不飽和
基を有する炭化水素重合物を加えたものが用いられる。
上記の不飽和脂肪酸化合物および鎖状炭化水素重合物は
不純物が混入していても差し支えない。
The organic compound having an unsaturated bond serves as a main agent for the oxygen absorption reaction, and preferably, the main agent is a transition metal salt of an unsaturated fatty acid or a mixture of a transition metal salt of an unsaturated fatty acid and an unsaturated fatty acid, or these. A mixture obtained by adding a hydrocarbon polymer having an unsaturated group to the mixture is used.
The unsaturated fatty acid compound and the chain hydrocarbon polymer may be mixed with impurities.

【0016】酸化促進物質は、主剤による酸素吸収反応
の役割を果たす物質である。酸化促進物質としては、
鉄、コバルト、クロム、銅、ニッケルなどの遷移金属の
化合物が用いられ、上記遷移金属の炭酸塩、硫酸塩、硝
酸塩などの無機酸塩、飽和脂肪酸塩、不飽和脂肪酸塩な
どの有機酸塩、アミン錯体などが用いられる。酸化促進
物質は、主剤と均一に混合することが望ましく、主剤の
不飽和脂肪酸の遷移金属塩として加えることが好まし
い。
The oxidation-promoting substance is a substance which plays a role in the oxygen absorption reaction by the main agent. As an oxidation promoter,
Compounds of transition metals such as iron, cobalt, chromium, copper and nickel are used, and inorganic acid salts such as carbonates, sulfates and nitrates of the above transition metals, saturated fatty acid salts, organic acid salts such as unsaturated fatty acid salts, An amine complex or the like is used. It is desirable that the oxidation promoting substance is uniformly mixed with the main agent, and it is preferable to add it as a transition metal salt of unsaturated fatty acid of the main agent.

【0017】ここにいう塩基性物質とは、塩基性物質と
して酸性物質を吸収することができる物質をいい、主剤
の酸素吸収により生成する酸性物質のみならず酸性物質
を補足する役割を果たすものであればよい。塩基性物質
としては、目的を達成するものであれば特に限定されな
いが、好ましくはアルカリ金属またはアルカリ土類金属
の酸化物、水酸化物、炭酸塩、有機酸塩並びに有機アミ
ン類が挙げられる。
The basic substance referred to here is a substance capable of absorbing an acidic substance as a basic substance, and plays a role of supplementing not only the acidic substance generated by the oxygen absorption of the main ingredient but also the acidic substance. I wish I had it. The basic substance is not particularly limited as long as it achieves the purpose, but preferably includes alkali metal or alkaline earth metal oxides, hydroxides, carbonates, organic acid salts and organic amines.

【0018】吸着物質は、主剤を担持して、酸素との接
触面積を増し、酸素吸収速度を増大させる担体の役割を
果たし、かつ、水分を吸収できる物質であり、さらには
酸性物質をできるものが好ましい。吸着物質の好ましい
具体例として、シリカゲル、活性炭、ゼオライト、活性
白土などが用いられる。
The adsorbing substance is a substance that supports the main agent, increases the contact area with oxygen, plays the role of a carrier for increasing the oxygen absorption rate, and is capable of absorbing water, and further can be an acidic substance. Is preferred. Silica gel, activated carbon, zeolite, activated clay and the like are used as preferable specific examples of the adsorbent.

【0019】組成物(A)の各成分の比率は、特に限定
しないが、不飽和有機化合物の主剤100重量部に対し
て、酸化促進物質は0.01〜10重量部、塩基性物質
は1〜1000重量部、吸着物質は10〜1000重量
部からなることが好ましい。
The proportion of each component of the composition (A) is not particularly limited, but 0.01 to 10 parts by weight of the oxidation promoting substance and 1 part of the basic substance with respect to 100 parts by weight of the main component of the unsaturated organic compound. ˜1000 parts by weight, and the adsorbing material preferably comprises 10 to 1000 parts by weight.

【0020】組成物(A)としては、上記各成分が混合
され、液状物質は吸着物質に担持させることが好まし
い。組成物(A)の混合物は顆粒状、錠剤状、シート状
などにすることができ、その形状特に限定されない。
As the composition (A), it is preferable that the above-mentioned respective components are mixed and the liquid substance is supported on the adsorbent substance. The mixture of the composition (A) can be in the form of granules, tablets, sheets, etc., and its shape is not particularly limited.

【0021】組成物(A)は、通常、通気性包装材料に
包装した包装体とし、酸素吸収剤として用いられる。ま
た、層状に充填した顆粒状または錠剤状の組成物(A)
を冷却システム系内に配置して冷媒のフロンを通過させ
ることができる。包装体の通気性包装材料としては、例
えば、紙、不織布、微多孔膜などの通気性材料、または
これらに穴開きのプラスチックフィルムなどの基材を積
層した積層が用いられる。
The composition (A) is usually packaged in a breathable packaging material and used as an oxygen absorbent. Also, a granular or tablet composition (A) packed in layers
Can be placed in the cooling system to allow the refrigerant CFCs to pass through. As the breathable packaging material of the package, for example, breathable materials such as paper, non-woven fabric, and microporous membrane, or a laminate in which a base material such as a perforated plastic film is laminated is used.

【0022】アルカリ金属又はアルカリ土類金属の酸化
物を含む組成物(B)は、水分、炭酸ガスおよび有機物
を吸収させるための組成物である。具体的には、水分と
炭酸ガスを吸収する物質としては固形アルカリ金属の酸
化物やアルカリ金属の水酸化物をアルカリ土類酸化物に
含浸した物質が用いられる。また、有機物を吸収させる
物質として吸着剤が用いられ、具体例としては、シリカ
ゲル、活性炭、ゼオライト、活性白土などが挙げら、真
空処理又は100℃以上で熱処理して用いることが好ま
しい。上記の組成物(B)は、組成物(A)と混合物と
して用いることができるが、組成物(B)のみを別の包
装体として組成物(A)の包装体と共に配置することが
できる。
The composition (B) containing an oxide of an alkali metal or an alkaline earth metal is a composition for absorbing water, carbon dioxide gas and organic matter. Specifically, as the substance that absorbs water and carbon dioxide, a substance obtained by impregnating an alkaline earth oxide with a solid alkali metal oxide or an alkali metal hydroxide is used. Further, an adsorbent is used as a substance that absorbs organic substances, and specific examples thereof include silica gel, activated carbon, zeolite, activated clay and the like, which are preferably used after vacuum treatment or heat treatment at 100 ° C. or higher. The composition (B) can be used as a mixture with the composition (A), but only the composition (B) can be arranged as a separate package together with the package of the composition (A).

【0023】本発明の冷却システムにおいては、液化し
た冷媒の気化場所は、真空度600mmHg以下好まし
くは500mmHg以下の真空、0℃以下の温度に維持
することが望ましい。また、本発明の冷却システムの系
内の酸素分圧は1mmHg以下、水分分圧は1mmHg
以下に維持される。
In the cooling system of the present invention, it is desirable that the liquefied refrigerant is vaporized at a vacuum degree of 600 mmHg or less, preferably 500 mmHg or less and a temperature of 0 ° C. or less. The oxygen partial pressure in the cooling system of the present invention is 1 mmHg or less, and the water partial pressure is 1 mmHg.
Maintained below.

【0024】[0024]

【実施例】本発明を実施例に基づいて説明する。本発明
はこの実施例に拘束を受けるものでない。 実施例1〜実施例10 実施例では図1の冷媒の圧縮液化−膨張ガス化サイクル
による冷凍装置を備えた冷蔵庫において、冷媒の圧縮機
3を出た箇所に図2のごときポケット部に酸素吸収剤の
収納部を設け、酸素吸収剤を配置した。
EXAMPLES The present invention will be described based on examples. The present invention is not bound by this embodiment. Example 1 to Example 10 In Examples, in a refrigerator equipped with a refrigerating apparatus by the compression liquefaction-expansion gasification cycle of the refrigerant shown in FIG. 1, oxygen is absorbed in a pocket portion as shown in FIG. An agent storage was provided and an oxygen absorber was placed.

【0025】酸素吸収剤として、次の組成物(A)およ
び組成物(B)を、それぞれ、開孔ポリエチレンフィル
ム内張の通気性紙袋(70×70mm)に充填し、酸素
吸収剤包装体として用いた。 組成物(A):大豆油脂肪酸1gに、ナフテン酸コバル
ト0.2gを溶かし珪土5gに含浸させた後、消石灰
0.1gを被覆して顆粒とし、この顆粒状組成物と顆粒
状酸化カルシウム2.5gを混合して組成物(A)を調
製した。 組成物(B):200℃、10mmHgの雰囲気下で1
時間熱処理して炭酸ガスを除去した活性炭10gと、生
石灰5gに苛生ソーダ水溶液(50%)1gを含浸させ
たソーダライムとを混合して組成物(B)を調製した。
As the oxygen absorbent, the following composition (A) and composition (B) were filled in an air-permeable paper bag (70 × 70 mm) lined with an open polyethylene film to form an oxygen absorbent package. Using. Composition (A): 0.2 g of cobalt naphthenate was dissolved in 1 g of soybean oil fatty acid to impregnate 5 g of silica, and then 0.1 g of slaked lime was coated to form granules. The granular composition and granular calcium oxide Composition (A) was prepared by mixing 2.5 g. Composition (B): 1 at 200 ° C. in an atmosphere of 10 mmHg
Composition (B) was prepared by mixing 10 g of activated carbon from which carbon dioxide was removed by heat treatment for a period of time and 5 g of quick lime with soda lime impregnated with 1 g of an aqueous sodium hydroxide solution (50%).

【0026】実施例1〜実施例10において、それぞ
れ、冷媒の種類を変え、酸素吸収剤を配置した冷蔵庫を
連続可動させた。冷凍装置の冷媒の保有量は約1.2kg
であり、装置主要部の配管には圧力配管用炭素鋼管を用
いた。1年間可動後の冷却システム系の酸素分圧および
水分分圧、冷媒中の水分量、並びに、冷凍装置の腐食指
標として、配管内壁の変色状況を表1に示す。比較例と
して、酸素吸収剤の替わりに、合成ゼオライト(200
℃で乾燥)21gを用いた場合の結果を表1に併記す
る。なお、使用した冷媒のオゾン破壊係数と使用前の水
分含有量を表2に示す。
In each of Examples 1 to 10, the type of the refrigerant was changed, and the refrigerator in which the oxygen absorbent was placed was continuously moved. Refrigerator has about 1.2kg of refrigerant
A carbon steel pipe for pressure piping was used for the piping of the main part of the device. Table 1 shows the discolored state of the inner wall of the pipe as the oxygen partial pressure and the water partial pressure of the cooling system after being operated for one year, the amount of water in the refrigerant, and the corrosion index of the refrigeration system. As a comparative example, a synthetic zeolite (200
The results when 21 g (dried at ℃) are used are also shown in Table 1. Table 2 shows the ozone depletion potential of the used refrigerant and the water content before use.

【0027】表1の実施例に示すごとく、本発明に係る
酸素吸収剤を用いることにより、系内の酸素および水分
の分圧が低下し、これがため冷媒の分解が防止され、腐
食の前徴である配管の変色は全く認められなかった。一
方、酸素吸収剤に代えて合成ゼオライトを用いた比較例
では、十分水分分圧が低下しなかっただけでなく、酸素
が除去されないために、冷媒の分解が認められ、配管に
は著しい変色が認められ腐食が始まっていた。
As shown in the examples of Table 1, by using the oxygen absorbent according to the present invention, the partial pressure of oxygen and water in the system is lowered, which prevents the decomposition of the refrigerant and causes the precursor of corrosion. No discoloration of the pipe was observed. On the other hand, in the comparative example using the synthetic zeolite instead of the oxygen absorbent, not only was the water partial pressure not sufficiently lowered, but because oxygen was not removed, the decomposition of the refrigerant was observed, and significant discoloration of the piping It was recognized and corrosion had started.

【0028】[0028]

【表1】 [Table 1]

【0029】[0029]

【表2】 [Table 2]

【0030】[0030]

【発明の効果】本発明によれば、系内に持ち込まれる又
はリークしてくる酸素および水分が冷媒循環系に配した
酸素吸収剤にトラップされることにより、冷媒の代替フ
ロン類の分解が防止される。たとえ、代替フロン類の分
解が微量あったとしても、分解生成物が酸素吸収剤に吸
収され、冷凍能力の低下や冷凍装置の金属材料の腐食を
招くことなく、代替フロン類が容易に冷媒として使用で
きる。
EFFECTS OF THE INVENTION According to the present invention, oxygen and water introduced or leaked into the system are trapped by the oxygen absorbent arranged in the refrigerant circulation system to prevent decomposition of CFC substitutes for the refrigerant. To be done. Even if there is a slight amount of decomposition of the CFC substitutes, the decomposition products are absorbed by the oxygen absorbent, and the CFC substitutes are easily converted into a refrigerant without reducing the refrigeration capacity or corroding the metal material of the refrigeration system. Can be used.

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

【図1】 冷媒の圧縮液化−膨張ガス化サイクルによる
冷却システム
FIG. 1 Cooling system by compression liquefaction-expansion gasification cycle of refrigerant

【図2】 酸素吸収剤の配置場所[Fig.2] Location of oxygen absorber

【符号の説明】[Explanation of symbols]

1 圧縮機 2 放熱器 3 膨張弁 4 冷却器 5 酸素吸収剤の配置場所 51 酸素吸収剤 1 Compressor 2 Radiator 3 Expansion valve 4 Cooler 5 Placement of oxygen absorbent 51 Oxygen absorbent

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 冷媒の圧縮液化と膨張ガス化のサイクル
によるフロンを冷媒とする冷却システムの冷媒の循環系
に酸素吸収剤を配することを特徴とする冷却システム。
1. A cooling system, wherein an oxygen absorbent is arranged in a refrigerant circulation system of a cooling system which uses Freon as a refrigerant by a cycle of compression liquefaction and expansion gasification of the refrigerant.
【請求項2】 酸素吸収剤が酸素、水分、炭酸ガスおよ
び有機物を吸収する組成物よりなることを特徴とする請
求項1の冷却システム。
2. The cooling system according to claim 1, wherein the oxygen absorbent is a composition that absorbs oxygen, moisture, carbon dioxide gas and organic matter.
【請求項3】 酸素吸収剤が不飽和結合を有する有機化
合物を含む組成物よりなることを特徴とする請求項1ま
たは請求項2の冷却システム。
3. The cooling system according to claim 1, wherein the oxygen absorbent is a composition containing an organic compound having an unsaturated bond.
JP6063101A 1994-03-31 1994-03-31 Cooling system Pending JPH07269994A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6063101A JPH07269994A (en) 1994-03-31 1994-03-31 Cooling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6063101A JPH07269994A (en) 1994-03-31 1994-03-31 Cooling system

Publications (1)

Publication Number Publication Date
JPH07269994A true JPH07269994A (en) 1995-10-20

Family

ID=13219574

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6063101A Pending JPH07269994A (en) 1994-03-31 1994-03-31 Cooling system

Country Status (1)

Country Link
JP (1) JPH07269994A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5718119A (en) * 1995-07-28 1998-02-17 Matsushita Electric Industrial Co., Ltd. Refrigeration system and method of installing same
US5813240A (en) * 1995-11-14 1998-09-29 Matsushita Electric Industrial Co., Ltd. Method for constructing a refrigerating cycle including a process of removing oxygen
EP1041347A2 (en) 1999-04-01 2000-10-04 Matsushita Electric Industrial Co., Ltd. Connecting apparatus for installing air conditioner
EP1067340A2 (en) 1999-07-05 2001-01-10 Matsushita Electric Industrial Co., Ltd. Replacing gas collecting trap for an air conditioner
JP2006162081A (en) * 2004-12-02 2006-06-22 Hitachi Ltd Refrigerating cycle device
JP2007315663A (en) * 2006-05-25 2007-12-06 Sanden Corp Refrigeration system
JP2008267680A (en) * 2007-04-19 2008-11-06 Sanden Corp Refrigerating circuit
JP2019184236A (en) * 2016-12-13 2019-10-24 ダイキン工業株式会社 Heat transfer device and heat transfer method using the same

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5718119A (en) * 1995-07-28 1998-02-17 Matsushita Electric Industrial Co., Ltd. Refrigeration system and method of installing same
US5842349A (en) * 1995-07-28 1998-12-01 Matsushita Electric Industrial Co., Ltd. Refrigeration system and method of installing same
US5813240A (en) * 1995-11-14 1998-09-29 Matsushita Electric Industrial Co., Ltd. Method for constructing a refrigerating cycle including a process of removing oxygen
EP1041347A2 (en) 1999-04-01 2000-10-04 Matsushita Electric Industrial Co., Ltd. Connecting apparatus for installing air conditioner
EP1067340A2 (en) 1999-07-05 2001-01-10 Matsushita Electric Industrial Co., Ltd. Replacing gas collecting trap for an air conditioner
JP2006162081A (en) * 2004-12-02 2006-06-22 Hitachi Ltd Refrigerating cycle device
JP2007315663A (en) * 2006-05-25 2007-12-06 Sanden Corp Refrigeration system
JP2008267680A (en) * 2007-04-19 2008-11-06 Sanden Corp Refrigerating circuit
WO2008133201A1 (en) * 2007-04-19 2008-11-06 Sanden Corporation Refrigeration circuit
JP2019184236A (en) * 2016-12-13 2019-10-24 ダイキン工業株式会社 Heat transfer device and heat transfer method using the same

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