JPH0118115B2 - - Google Patents

Info

Publication number
JPH0118115B2
JPH0118115B2 JP56074739A JP7473981A JPH0118115B2 JP H0118115 B2 JPH0118115 B2 JP H0118115B2 JP 56074739 A JP56074739 A JP 56074739A JP 7473981 A JP7473981 A JP 7473981A JP H0118115 B2 JPH0118115 B2 JP H0118115B2
Authority
JP
Japan
Prior art keywords
lithium bromide
temperature
aqueous solution
crystallization temperature
cooling
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
Application number
JP56074739A
Other languages
Japanese (ja)
Other versions
JPS57190634A (en
Inventor
Yasumasa Oochi
Seiichi Ito
Masaji Ootoshi
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
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 Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP56074739A priority Critical patent/JPS57190634A/en
Priority to SE8203089A priority patent/SE8203089L/en
Priority to IT83388/82A priority patent/IT1165786B/en
Priority to GB08214444A priority patent/GB2103641B/en
Priority to DE3218744A priority patent/DE3218744A1/en
Priority to FR8208723A priority patent/FR2505861B1/en
Publication of JPS57190634A publication Critical patent/JPS57190634A/en
Publication of JPH0118115B2 publication Critical patent/JPH0118115B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)
  • Gas Separation By Absorption (AREA)

Description

【発明の詳細な説明】 本発明は、吸収式の空調装置あるいは給湯装置
に用いる吸収剤の組成改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improving the composition of an absorbent used in an absorption type air conditioner or water heater.

従来一般に、水を熱運搬媒とする場合、吸収剤
として臭化リチウムが用いられ、実際の運転に際
しては臭化リチウム水溶液として使用されるが、
その水溶液の臭化リチウム濃度は62重量%程度で
あり、それ以上に濃度を上げることはむずかしか
つた。なぜなら、臭化リチウムの62重量%水溶液
の晶析温度は約40℃であり、これ以上に濃度を上
げて晶析温度を上昇させると、空調装置や給湯装
置の運転休止時はもちろん運転中においても臭化
リチウムが晶析し、装置の動作不良などのトラブ
ルが発生するからである。そして、従来のように
62重量%程度の臭化リチウム水溶液を使用した場
合、熱運搬媒を水とすると、冷房の際蒸発器内に
おいて、温度が5〜7℃程度、蒸気圧が6mmHg
程度となるから、吸収器内においては、蒸気圧が
6mmHg程度になるように温度を40℃程度に維持
する必要があつた。吸収器内の温度を40℃程度に
しようとすると、吸収に伴う発熱を除去するのに
どうしても空冷ではむずかしく、そのため、冷房
に際して水冷方式を採用せねばならず、クーリン
グタワーが必要になるとともに、設備維持管理が
困難であるという欠点があつた。また、暖房や給
湯に際して、外気を熱源とすることが不可能で、
例えば温泉や高温廃水等の高温熱源が必要で、利
用地域に限定を受ける欠点があつた。
Conventionally, when water is used as a heat transfer medium, lithium bromide is generally used as an absorbent, and in actual operation it is used as an aqueous solution of lithium bromide.
The concentration of lithium bromide in the aqueous solution was approximately 62% by weight, and it was difficult to increase the concentration beyond that. This is because the crystallization temperature of a 62% by weight aqueous solution of lithium bromide is approximately 40°C, and if the crystallization temperature is increased by increasing the concentration higher than this, the This is because lithium bromide crystallizes, causing problems such as equipment malfunction. And as usual
When using a 62% by weight aqueous lithium bromide solution and using water as the heat transfer medium, the temperature in the evaporator during cooling will be approximately 5-7℃ and the vapor pressure will be 6mmHg.
Therefore, it was necessary to maintain the temperature within the absorber at approximately 40°C so that the vapor pressure would be approximately 6 mmHg. If you try to keep the temperature inside the absorber at around 40℃, it is difficult to remove the heat generated by absorption with air cooling, so a water cooling system must be used for cooling, which requires a cooling tower and requires equipment maintenance. The drawback was that it was difficult to manage. In addition, it is impossible to use outside air as a heat source for heating or hot water supply.
For example, it requires a high-temperature heat source such as a hot spring or high-temperature wastewater, and has the disadvantage of being limited to specific areas.

さらに詳述すると、一般に、吸収器内の温度を
45℃程度にすれば、空冷による冷房が可能であ
り、かつ、40℃では困難であつた外気を熱源とす
るヒートポンプ暖房も可能であると言われている
が、そのためには、臭化リチウム水溶液の濃度を
65重量%程度にして、吸収能力を高める必要があ
る。しかし、そのように濃度を上げると晶析温度
が上昇するのは前述の通りであり、単に臭化リチ
ウムのみを含む水溶液では、空冷による冷房や、
外気を熱源とする暖房あるいは給湯を実用的に行
うことはとうてい不可能であつた。
More specifically, in general, the temperature inside the absorber is
It is said that if the temperature is set to around 45°C, air cooling is possible, and heat pump heating using outside air as the heat source, which was difficult at 40°C, is also possible. concentration of
It is necessary to increase the absorption capacity by setting the content to about 65% by weight. However, as mentioned above, increasing the concentration increases the crystallization temperature, and in an aqueous solution containing only lithium bromide, cooling by air cooling,
It was virtually impossible to use outside air as a heat source for heating or hot water supply.

他方、臭化リチウムに臭化亜鉛を添加して、そ
の混合物の水溶液の晶析温度を臭化リチウム水溶
液よりも低下させることが提案されているが、実
際上、最高で18℃程度しか晶析温度を低下させる
ことができず、温暖地域での空冷による冷房、寒
冷地域での外気を熱源とする暖房や給湯には適用
できない欠点があつた。
On the other hand, it has been proposed to add zinc bromide to lithium bromide to lower the crystallization temperature of the aqueous solution of the mixture compared to that of the lithium bromide aqueous solution, but in reality, crystallization only occurs at a maximum of about 18°C. It had the disadvantage that it could not lower the temperature and could not be applied to air conditioning in warm regions, or to heating or hot water supply in cold regions using outside air as a heat source.

本発明の目的は、上記実情に鑑みて、臭化リチ
ウムと同じ程度の吸収能力を持ち、水溶液の晶析
温度が、62重量%程度の臭化リチウム水溶液の晶
析温度よりも10℃程度以上低くなり、かつ、必要
に応じて30℃程度以上も低くできる吸収剤を提供
し、温暖地や寒冷地いかんにかかわらず広範な地
域において、冷房の際の吸収器の空冷下、あるい
は、吸収器用水冷設備の大巾な小型化、並びに、
暖房や給湯の際の外気を熱源とするヒートポンプ
を可能にする点にある。
In view of the above circumstances, it is an object of the present invention to have an absorption capacity similar to that of lithium bromide, and a crystallization temperature of an aqueous solution that is approximately 10°C higher than the crystallization temperature of an approximately 62% by weight aqueous lithium bromide solution. We provide an absorbent that can lower the temperature by as much as 30℃ or more if necessary, and can be used under air cooling of absorbers during air conditioning or for use in absorbers in a wide range of regions, regardless of whether it is warm or cold. Significant miniaturization of water cooling equipment, and
Its purpose is to enable heat pumps that use outside air as a heat source for heating and hot water supply.

本発明による吸収剤の特徴組成は、臭化リチウ
ムに対して塩化亜鉛を乾燥重量比で10%ないし
200%添加したことにあり、このような臭化リチ
ウムと塩化亜鉛の混合物の水溶液を吸収剤として
吸収式空調装置や給湯装置に使用することによつ
て、従来の62重量%程度の臭化リチウム水溶液に
比して晶析温度を10℃程度ないし33℃程度低下で
き、換言すれば、溶質濃度を上げて、吸収器の温
度を高くでき、もつて、冷房に際しての空冷化や
水冷設備の大巾な小型化、並びに、外気を熱源と
しての暖房や給湯を実用的に行えるようになつ
た。
The characteristic composition of the absorbent according to the present invention is that the dry weight ratio of zinc chloride to lithium bromide is 10% or more.
By using this aqueous solution of a mixture of lithium bromide and zinc chloride as an absorbent in absorption type air conditioners and water heaters, it is possible to reduce the amount of lithium bromide from the conventional 62% by weight. The crystallization temperature can be lowered by about 10 to 33 degrees Celsius compared to an aqueous solution.In other words, the solute concentration can be increased and the temperature of the absorber can be raised, making it possible to use air cooling or water cooling equipment for cooling. It has become much more compact and has become practical for heating and hot water supply using outside air as a heat source.

さらに説明すると、吸収剤として臭化リチウム
を用いた場合、これに吸湿性の無機物を混入して
も吸収能力が低下しないことは知られているが、
その混合物の水溶液は、臭化リチウムのみの水溶
液よりも晶析温度が上昇するものと一般に認識さ
れている。ところが、本発明者達が、臭化リチウ
ムをベースとして、これに種々の吸湿性無機物を
混入して、各種の実験を試みたところ、特定の割
合で混入された塩化亜鉛に限り、62重量%程度の
臭化リチウム水溶液に比して晶析温度が十分に低
下する事実を新しく知るに至つたのであり、その
確認実験の結果を以下に示す。
To explain further, it is known that when lithium bromide is used as an absorbent, the absorption capacity does not decrease even if a hygroscopic inorganic substance is mixed into it.
It is generally recognized that an aqueous solution of the mixture will have a higher crystallization temperature than an aqueous solution of lithium bromide alone. However, when the present inventors tried various experiments using lithium bromide as a base and mixed various hygroscopic inorganic substances into it, only zinc chloride mixed in a specific proportion was found to be 62% by weight. We have newly learned that the crystallization temperature is sufficiently lower than that of an aqueous solution of lithium bromide, and the results of an experiment to confirm this are shown below.

〔実験 1〕 濃度65%の臭化リチウム水溶液に塩化亜鉛を各
種添加量で混入した多数の試料を調製し、それら
試料夫々の晶析温度を調べて、塩化亜鉛添加量
(=ZnCl2/65%aq.LiBr+Zncl2×100wt%)と晶析温度 との関係を調べたところ、第1図に示す結果が得
られた。
[Experiment 1] A large number of samples were prepared by mixing various amounts of zinc chloride into an aqueous solution of lithium bromide with a concentration of 65 % . %aq.LiBr+Zncl 2 ×100wt%) and crystallization temperature, the results shown in FIG. 1 were obtained.

そして、第1図に示す結果から、臭化リチウム
に対する塩化亜鉛の乾燥重量比(=Zncl2/LiBr× 100wt%)と晶析温度の相関を算出したところ、
第3図に示す結果が得られた。
From the results shown in Figure 1, we calculated the correlation between the dry weight ratio of zinc chloride to lithium bromide (=Zncl 2 /LiBr x 100wt%) and the crystallization temperature.
The results shown in FIG. 3 were obtained.

この実験結果から、臭化リチウムに対して塩化
亜鉛を乾燥重量比で10%ないし200%添加すると、
晶析温度が10℃以上低下し、15%ないし130%添
加すると20℃以上の晶析温度降下が生じることが
判る。そして、この事は、空冷による冷房、外気
を熱源とする暖房や給湯等が可能であることを示
している。
From this experimental result, when zinc chloride is added in a dry weight ratio of 10% to 200% to lithium bromide,
It can be seen that the crystallization temperature decreases by 10°C or more, and when 15% to 130% is added, the crystallization temperature decreases by 20°C or more. This fact indicates that air cooling, heating using outside air as a heat source, hot water supply, etc. are possible.

〔実験 2〕 臭化リチウムに対してほぼ等重量の塩化亜鉛を
混入した混合物を調整し、この混合物の水溶液濃
度(重量%)を種々変更したものにつき、それぞ
れ、蒸気圧を温度との関係を調べたところ、第2
図に示す結果が得られた。
[Experiment 2] A mixture of lithium bromide and zinc chloride in an approximately equal weight was prepared, and the relationship between vapor pressure and temperature was determined for each mixture with various aqueous solution concentrations (wt%). Upon investigation, the second
The results shown in the figure were obtained.

この実験結果から臭化リチウムと塩化亜鉛の混
合物の濃度を例えば78重量%にすると、蒸気圧が
6mmHgでも晶析を生じず、その時の水溶液温度
はほぼ55℃にもなることが判つた。この事は、吸
収器の温度を45℃以上に、つまり、空冷による冷
房、外気を熱源とする暖房や給湯が可能な吸収器
温度にできることを示している。
From the results of this experiment, it was found that when the concentration of the mixture of lithium bromide and zinc chloride was set to 78% by weight, for example, no crystallization occurred even at a vapor pressure of 6 mmHg, and the aqueous solution temperature at that time reached approximately 55°C. This shows that the temperature of the absorber can be raised to 45°C or higher, which is a temperature that allows air cooling, heating using outside air as a heat source, and hot water supply.

〔実験 3〕 臭化リチウムに対する塩化亜鉛の乾燥重量比が
晶析温度に及ぼす影響と、臭化リチウムに対する
臭化亜鉛の乾燥重量比が晶析温度に及ぼす影響に
ついて、比較実験したところ、第4図に示す結果
を得た。
[Experiment 3] A comparative experiment was conducted to examine the effect of the dry weight ratio of zinc chloride to lithium bromide on the crystallization temperature and the effect of the dry weight ratio of zinc bromide to lithium bromide on the crystallization temperature. The results shown in the figure were obtained.

この実験結果から、従来提案されている臭化亜
鉛添加では最高で18℃程度しか晶析温度が低下し
ないが、本発明の場合には最高40℃程度もの大巾
な晶析温度低下が可能であり、性能的に顕著な差
が認められた。
From this experimental result, the conventionally proposed addition of zinc bromide reduces the crystallization temperature by only about 18°C at most, but in the case of the present invention, it is possible to reduce the crystallization temperature by a wide range of about 40°C. There was a significant difference in performance.

なお、本発明の吸収剤は、冷房あるいは暖房専
用、冷暖房兼用、あるいは、給湯設備を組込んだ
もの等の各種吸収式空調装置に利用でき、また、
給湯装置にも利用できる。
The absorbent of the present invention can be used in various absorption type air conditioners, such as those exclusively for cooling or heating, those for both cooling and heating, or those incorporating hot water supply equipment.
It can also be used for water heaters.

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

第1図は、臭化リチウム水溶液に対する塩化亜
鉛添加量と、その混合物水溶液の晶析温度の相関
を調べた実験結果を示すグラフである。第2図
は、臭化リチウムと塩化亜鉛の定量混合物の水溶
液濃度変化、その水溶液の蒸気圧と温度の相関を
調べた実験結果を示すグラフである。第3図は、
第1図の実験結果に基いて、臭化リチウムに対す
る塩化亜鉛の乾燥重量比と晶析温度の相関を算出
した結果を示すグラフである。第4図は、塩化亜
鉛を添加した場合と、臭化亜鉛を添加した場合
に、臭化リチウムと添加物の混合水溶液の晶析温
度がいかに低下するかを比較した実験の結果を示
すグラフである。
FIG. 1 is a graph showing the results of an experiment in which the correlation between the amount of zinc chloride added to an aqueous lithium bromide solution and the crystallization temperature of an aqueous solution of the mixture was investigated. FIG. 2 is a graph showing the results of an experiment in which the correlation between the change in concentration of an aqueous solution of a quantitative mixture of lithium bromide and zinc chloride, and the vapor pressure and temperature of the aqueous solution was investigated. Figure 3 shows
2 is a graph showing the results of calculating the correlation between the dry weight ratio of zinc chloride to lithium bromide and the crystallization temperature based on the experimental results shown in FIG. 1. Figure 4 is a graph showing the results of an experiment comparing how the crystallization temperature of a mixed aqueous solution of lithium bromide and additives decreases when zinc chloride is added and when zinc bromide is added. be.

Claims (1)

【特許請求の範囲】[Claims] 1 臭化リチウムに対して塩化亜鉛を乾燥重量比
で10%ないし200%添加してある事を特徴とする
空調装置あるいは給湯装置用吸収剤。
1. An absorbent for air conditioners or water heaters, characterized in that zinc chloride is added in a dry weight ratio of 10% to 200% relative to lithium bromide.
JP56074739A 1981-05-18 1981-05-18 Adsorbent for air conditioning apparatus or hot water supply system Granted JPS57190634A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP56074739A JPS57190634A (en) 1981-05-18 1981-05-18 Adsorbent for air conditioning apparatus or hot water supply system
SE8203089A SE8203089L (en) 1981-05-18 1982-05-17 ABSORPTION COMPOSITION FOR AIR CONDITIONING OR HEATING WATER
IT83388/82A IT1165786B (en) 1981-05-18 1982-05-17 ABSORBENT COMPOSITION FOR AIR CONDITIONERS OR HOT WATER SUPPLIERS
GB08214444A GB2103641B (en) 1981-05-18 1982-05-18 Absorbent composition for air-cinditioners or water heaters
DE3218744A DE3218744A1 (en) 1981-05-18 1982-05-18 COMPOSITION OF AN ABSORBENT FOR ABSORPTION AIR CONDITIONING AND HOT WATER SUPPLY SYSTEMS
FR8208723A FR2505861B1 (en) 1981-05-18 1982-05-18 ABSORBENT COMPOSITION FOR AIR CONDITIONING OR PROVIDING HOT WATER

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56074739A JPS57190634A (en) 1981-05-18 1981-05-18 Adsorbent for air conditioning apparatus or hot water supply system

Publications (2)

Publication Number Publication Date
JPS57190634A JPS57190634A (en) 1982-11-24
JPH0118115B2 true JPH0118115B2 (en) 1989-04-04

Family

ID=13555904

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56074739A Granted JPS57190634A (en) 1981-05-18 1981-05-18 Adsorbent for air conditioning apparatus or hot water supply system

Country Status (1)

Country Link
JP (1) JPS57190634A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6164781A (en) * 1984-09-06 1986-04-03 Osaka Gas Co Ltd Absorbent for air-conditioning or hot-water supply equipment

Also Published As

Publication number Publication date
JPS57190634A (en) 1982-11-24

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