JP2775601B2 - Absorption liquid for absorption refrigerator and transfer device for this absorption liquid - Google Patents

Absorption liquid for absorption refrigerator and transfer device for this absorption liquid

Info

Publication number
JP2775601B2
JP2775601B2 JP7187790A JP18779095A JP2775601B2 JP 2775601 B2 JP2775601 B2 JP 2775601B2 JP 7187790 A JP7187790 A JP 7187790A JP 18779095 A JP18779095 A JP 18779095A JP 2775601 B2 JP2775601 B2 JP 2775601B2
Authority
JP
Japan
Prior art keywords
absorption
liquid
absorption liquid
additive
suction
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 - Fee Related
Application number
JP7187790A
Other languages
Japanese (ja)
Other versions
JPH0914783A (en
Inventor
恭敏 庄司
芳明 高谷
明宏 村上
邦彦 中島
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.)
Kawaju Reinetsu Kogyo KK
Kawasaki Motors Ltd
Original Assignee
Kawaju Reinetsu Kogyo KK
Kawasaki Jukogyo KK
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 Kawaju Reinetsu Kogyo KK, Kawasaki Jukogyo KK filed Critical Kawaju Reinetsu Kogyo KK
Priority to JP7187790A priority Critical patent/JP2775601B2/en
Publication of JPH0914783A publication Critical patent/JPH0914783A/en
Application granted granted Critical
Publication of JP2775601B2 publication Critical patent/JP2775601B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

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、吸収冷凍機又は吸収冷
温水機に用いる吸収液、詳しくは、吸収液の一成分とし
て、吸収液より比重が重いフッ素系アルコールを添加す
ることにより、吸収液の水蒸気吸収性能を促進させるよ
うにした吸収冷凍機用又は吸収冷温水機用の吸収液(以
下、単に吸収冷凍機用吸収液という)及び添加剤(吸収
促進剤)を添加した吸収液を添加剤を滞留させることな
く移送する装置に関するものである。
BACKGROUND OF THE INVENTION The present invention, absorption liquid used in the absorption chiller or absorption chiller heater, particularly, as a component of the absorbent, by the specific gravity is added heavy fluorine-based alcohol than the absorption liquid, Absorbing liquid for absorption refrigerator or absorption chiller / heater (hereinafter, simply referred to as absorption liquid for absorption refrigerator) and additive (absorption accelerator) added to promote absorption of water vapor by the absorption liquid. And a device for transferring the additive without retaining the additive.

【0002】[0002]

【従来の技術】図3は一般的な吸収冷凍機を示してい
る。従来、吸収冷凍機において、吸収液にはLiBr水
溶液10が使用されている。また、吸収冷凍機の吸収器
12の冷媒吸収速度(熱貫流率)は吸収冷凍機を構成す
る熱交換器の中でもっとも小さく、最大の伝熱面積を必
要としている。そのため、従来から吸収促進添加剤とし
て、例えば、2−エチルヘキシルアルコール(オクチル
アルコール、沸点187℃)等を添加し、循環使用によ
って熱貫流率を高め、吸収器の小型化を図っている。し
かしながら、オクチルアルコールは、溶液と一緒に吸収
器下部より流出し、溶液熱交換器を介して再生器に向
い、大部分冷媒蒸気とともに凝縮器で凝縮され、蒸発器
に運ばれる。そして、そこで再度冷媒とともに蒸発し、
吸収器に至り、吸収液表面で凝縮し、吸収促進効果を発
揮する。ところが、吸収液と接している界面活性剤は、
吸収液中の高濃度の無機水溶液を抽出しており、それ自
体の粘度が非常に大きくなっている。すなわち、オクチ
ルアルコールは、溶液と接すると高粘度になり、吸収冷
凍機内で滞留が起こりやすいという問題があった。ま
た、界面活性剤が凝縮器に滞留しやすいので、該凝縮器
と吸収器を結ぶバイパス回路を設けている場合もある
が、効率よく、界面活性剤を分離する為には、多量の界
面活性剤が必要となる。これはサイクル効率を低下させ
るとともに、付帯コストも上昇するという欠点がある。
2. Description of the Related Art FIG. 3 shows a general absorption refrigerator. Conventionally, in an absorption refrigerator, a LiBr aqueous solution 10 is used as an absorption liquid. Further, the refrigerant absorption rate (heat transmission rate) of the absorber 12 of the absorption refrigerator is the smallest among the heat exchangers constituting the absorption refrigerator, and requires the largest heat transfer area. Therefore, conventionally, for example, 2-ethylhexyl alcohol (octyl alcohol, boiling point: 187 ° C.) or the like is added as an absorption-promoting additive, thereby increasing the heat transmission coefficient by circulating use, and reducing the size of the absorber. However, octyl alcohol flows out from the lower part of the absorber together with the solution, flows to the regenerator via the solution heat exchanger, is condensed in the condenser together with most of the refrigerant vapor, and is conveyed to the evaporator. And there it evaporates again with the refrigerant,
It reaches the absorber and condenses on the surface of the absorbing liquid, exhibiting an absorption promoting effect. However, the surfactant in contact with the absorbent is
A high-concentration inorganic aqueous solution in the absorbing solution is extracted, and the viscosity of the solution itself is very large. That is, octyl alcohol has a problem that when it comes into contact with a solution, it becomes high in viscosity and easily stays in the absorption refrigerator. In addition, since the surfactant easily stays in the condenser, a bypass circuit connecting the condenser and the absorber may be provided. However, in order to efficiently separate the surfactant, a large amount of surfactant is required. Agent is required. This has the disadvantage that the cycle efficiency is reduced and the incidental costs are also increased.

【0003】一方、吸収器以外の熱交換器である再生器
16、凝縮器18、蒸発器20は、それぞれ沸騰蒸発、
凝縮伝熱、膜蒸発等の伝熱機構のため、装置設計上から
ほぼ限界まで熱貫流率を高めている。したがって、吸収
冷凍機小型化の方途としては、吸収器伝熱面積の縮小が
鍵となっており、吸収促進のための新規添加剤探索、開
発が課題となっている。さらに、吸収促進添加剤には、
比較的比重が軽いアルコール系の有機化合物が多く、そ
の性質(親油性等)からLiBr水溶液には、溶解度分
だけ溶け込み、残りはLiBr水溶液の表面に浮かんで
しまう。そのため再生器内に吸収液を供給する際、吸収
促進剤は吸収液表面に残り、LiBr水溶液だけが供給
されるなど、吸収液の供給方法についても課題がある。
14は吸収液表面の吸収促進剤を示している。
On the other hand, a regenerator 16, a condenser 18, and an evaporator 20, which are heat exchangers other than the absorber, are respectively provided with boiling evaporators,
Due to the heat transfer mechanism such as condensation heat transfer and film evaporation, the heat transmission rate is increased from the device design to almost the limit. Therefore, as a way to reduce the size of the absorption refrigerator, the key is to reduce the heat transfer area of the absorber, and the search and development of new additives for promoting absorption have been a challenge. In addition, absorption enhancing additives include:
There are many alcohol-based organic compounds having a relatively low specific gravity, and due to their properties (lipophilicity, etc.), they are dissolved in the LiBr aqueous solution by the amount corresponding to the solubility, and the remainder floats on the surface of the LiBr aqueous solution. Therefore, when supplying the absorbent into the regenerator, the absorption accelerator remains on the surface of the absorbent, and only the aqueous LiBr solution is supplied.
Reference numeral 14 denotes an absorption accelerator on the surface of the absorbing solution.

【0004】特公昭52−48710号公報には、ブラ
イン水溶液と、このブライン水溶液の吸収率を増加させ
るためのフルオロアルコールとからなる、熱的安定性に
優れ、吸収液の吸収率が増加する吸収剤組成物が記載さ
れている。また、特公平7−6704号公報には、ハロ
ゲン化アルカリを主成分とする水溶液よりなる吸収液
に、吸収促進剤として、2−オクタノール、1−ヘプタ
ノール、2−メチル−1−ヘキサノール、1−ヘキサノ
ール等の沸点が155〜180℃のアルコール系飽和炭
化水素を添加して吸収液の滞留が起こりにくいようにし
た吸収冷凍機の吸収液が記載されている。
Japanese Patent Publication No. 52-48710 discloses an absorbent comprising a brine aqueous solution and a fluoroalcohol for increasing the absorption rate of the brine aqueous solution, which has excellent thermal stability and an increased absorption rate of the absorbing solution. An agent composition is described. Japanese Patent Publication No. 7-6704 discloses that an absorption solution composed of an aqueous solution containing an alkali halide as a main component contains 2-octanol, 1-heptanol, 2-methyl-1-hexanol, 1-hexanol as an absorption promoter. An absorption liquid of an absorption refrigerator in which an alcohol-based saturated hydrocarbon having a boiling point of 155 to 180 ° C. such as hexanol is added so that the retention of the absorption liquid hardly occurs.

【0005】[0005]

【発明が解決しようとする課題】しかし、これらのアル
コール系飽和炭化水素の比重は吸収液の比重より軽いの
で、吸収液の表面に浮き、このため、前述の2−エチル
ヘキシルアルコールの場合と同様に、吸収液と吸収促進
剤とを送液する際、吸収液のみが送液されてしまうとい
う問題がある。すなわち、上記2件の公報に記載された
アルコールとも、吸収液より比重が軽く、冷媒蒸気吸収
後、吸収器の吸収液溜まりでは吸収液の表面に浮かぶた
め(アルコールの分散性の低下)、吸収冷凍機の立ち上
げ時や運転中に、溶液ポンプの吸引力により再生器内に
吸収液を送液する際、吸収液のみが送液されるという問
題がある。それに伴い、長期運転では、吸収液溜まりに
残るアルコール量が増加するため、冷媒蒸気吸収時の吸
収促進効果が減少するという問題がある。さらに、吸収
促進効果を維持するために多量のアルコールを添加・追
加しなければならない。本発明者は、上記の問題点を解
決するために、鋭意研究を重ねた結果、LiBrと水と
を主成分とする吸収液に、フッ素系アルコールを添加す
ることにより、吸収液の水蒸気吸収性能を促進させ、か
つ、フッ素系アルコールが吸収液の表面に浮かび、一部
が吸収液中に沈むことを見い出した。また、本発明者
は、沸点190〜215℃の炭化水素系アルコールを吸
収液に添加することにより、吸収液の水蒸気吸収性能を
促進させることを見い出した。
However, since the specific gravity of these alcohol-based saturated hydrocarbons is lower than the specific gravity of the absorbing solution, they float on the surface of the absorbing solution, and therefore, as in the case of 2-ethylhexyl alcohol described above. When the absorption liquid and the absorption promoter are sent, there is a problem that only the absorption liquid is sent. In other words, the alcohols described in the above two publications have a lower specific gravity than the absorbing liquid, and float on the surface of the absorbing liquid in the absorbing liquid pool of the absorber after absorbing the refrigerant vapor (the dispersibility of the alcohol decreases). When the absorption liquid is sent into the regenerator by the suction force of the solution pump during startup or operation of the refrigerator, there is a problem that only the absorption liquid is sent. Accordingly, in the long-term operation, the amount of alcohol remaining in the absorption liquid reservoir increases, so that there is a problem in that the absorption promotion effect at the time of refrigerant vapor absorption decreases. In addition, a large amount of alcohol must be added or added to maintain the absorption promoting effect. The present inventor has conducted intensive studies in order to solve the above problems, and as a result, by adding a fluorinated alcohol to an absorbing solution mainly composed of LiBr and water, the water absorbing performance of the absorbing solution was It was found that the fluorinated alcohol floated on the surface of the absorbent and a part of the fluoroalcohol sank into the absorbent. In addition, the present inventor has found that by adding a hydrocarbon alcohol having a boiling point of 190 to 215 ° C to the absorbing solution, the water vapor absorbing performance of the absorbing solution is promoted.

【0006】本発明は上記の諸点に鑑み、上記の知見に
基づいてなされたもので、本発明の目的は、吸収冷凍機
用の吸収液の水蒸気吸収性能を促進させ、循環作用によ
って熱貫流率を高め、吸収冷凍機用の吸収器の小型化を
可能とすることにある。本発明の他の目的は、添加剤
(吸収促進剤)を添加した際に、吸収液のみが送液され
ることを防止するとともに、添加剤の滞留を防止するよ
うにした吸収液の移送装置を提供することにある。この
ように、本発明では、フッ素系アルコールのうち吸収液
より比重が重いアルコールを吸収液に添加することによ
り、吸収液を再生器に供給する際、吸収液だけが送液さ
れることを防ぎ、しかも吸収液の水蒸気吸収性能を促進
させることができる。さらに、後述の図2に示すような
装置構造にすることにより、吸収液溜まりから再生器に
供給する吸収液とフッ素系アルコールの分散性が向上で
き、多量のアルコールの添加・追加を必要としないこと
を特徴としている。
The present invention has been made in view of the above-mentioned points, and has been made based on the above findings. It is an object of the present invention to promote the water vapor absorption performance of an absorption liquid for an absorption refrigerator, and to provide a heat transfer coefficient by a circulation action. And the size of the absorber for the absorption refrigerator can be reduced. Another object of the present invention is to provide a device for transferring an absorbing liquid that prevents only the absorbing liquid from being sent when an additive (absorption promoter) is added, and prevents the additive from staying. Is to provide. As described above, in the present invention, when the absorbing liquid is supplied to the regenerator, only the absorbing liquid is prevented from being sent by adding the alcohol having a higher specific gravity than the absorbing liquid to the absorbing liquid. Moreover, the water vapor absorbing performance of the absorbing liquid can be promoted. Furthermore, the dispersibility of the absorbing liquid and the fluorinated alcohol to be supplied to the regenerator from the absorbing liquid pool can be improved by adopting an apparatus structure as shown in FIG. 2 described later, and it is not necessary to add or add a large amount of alcohol. It is characterized by:

【0007】[0007]

【課題を解決するための手段及び作用】上記の目的を達
成するために、本発明の吸収冷凍機用吸収液は、臭化リ
チウムと水とを主成分とするアルカリ性吸収液に、この
アルカリ性吸収液よりも比重が重いフッ素系アルコー
添加してなるように構成されている。フッ素系アルコ
ールとしては、2−(パーフルオロブチル)エタノール
(比重1.590)、2−(パーフルオロヘキシル)エ
タノール、2−(パーフルオロ−3−メチルブチル)エ
タノール、2−(パーフルオロ−5−メチルヘキシル)
エタノール(比重1.762以上)、3−パーフルオロ
ブチル−2−プロペン−1−オール、3−パーフルオロ
ヘキシル−2−プロペン−1−オール、6−(パーフル
オロヘキシル)ヘキサノール、1H,1H,3H−テト
ラフルオロプロパノールからなる群より選ばれた少なく
とも一種類のアルコールが用いられる。
To achieve SUMMARY and effects of the Invention The above object, the absorption chiller absorbing solution of the present invention, the alkaline absorbent solution mainly composed of a lithium bromide and water, the
Specific gravity than the heavier alkaline absorbent solution fluoric alcohol
It is configured to be added. Examples of the fluorinated alcohol include 2- (perfluorobutyl) ethanol (specific gravity 1.590), 2- (perfluorohexyl) ethanol, 2- (perfluoro-3-methylbutyl) ethanol, and 2- (perfluoro-5-ethanol). Methylhexyl)
Ethanol (specific gravity 1.762 or more), 3-perfluorobutyl-2-propen-1-ol, 3-perfluorohexyl-2-propen-1-ol, 6- (perfluorohexyl) hexanol, 1H, 1H, At least one alcohol selected from the group consisting of 3H-tetrafluoropropanol is used.

【0008】これらのアルコールを吸収液に添加する
と、界面撹乱現象を発現するとともに、図1に示すよう
に、これらのアルコール、とくに、フッ素系アルコール
22は希吸収液より比重が大きいので、アルコールの一
部がLiBr水溶液を主成分とする吸収液10中に沈
み、吸収促進剤(添加剤)であるフッ素系アルコール2
2と吸収液10とが一緒に送液される。なお、希吸収液
では比重が重く、濃吸収液では比重が軽いものを選定す
れば、一層好都合である。フッ素系アルコールの添加量
は、0.001〜5重量%、望ましくは0.01〜3重
量%、より望ましくは0.05〜2重量%である。フッ
素系アルコールの添加量がこれらの範囲未満の場合は、
吸収液の表面張力を低下させることが不十分となり、界
面撹乱現象を発現しない傾向があり、一方、これらの範
囲を超える場合は、吸収液の蒸気圧に影響を及ぼし、蒸
気圧を増加させ、吸収液の水蒸気吸収性能を低下させる
傾向がある。
When these alcohols are added to the absorbing solution, an interface disturbance phenomenon is developed, and as shown in FIG. 1, these alcohols, especially the fluorinated alcohol 22, have a higher specific gravity than the dilute absorbing solution. A part of the fluorinated alcohol 2 is settled in the absorbing solution 10 mainly composed of an aqueous solution of LiBr and serves as an absorption accelerator (additive).
2 and the absorbing liquid 10 are sent together. It is more convenient to select a rare absorbing liquid having a high specific gravity and a thick absorbing liquid having a low specific gravity. The addition amount of the fluorinated alcohol is 0.001 to 5% by weight, preferably 0.01 to 3% by weight, and more preferably 0.05 to 2% by weight. When the addition amount of the fluorinated alcohol is less than these ranges,
It becomes insufficient to lower the surface tension of the absorbing solution, and there is a tendency that the interface disturbance phenomenon does not occur.On the other hand, if it exceeds these ranges, it affects the vapor pressure of the absorbing solution and increases the vapor pressure, There is a tendency that the water vapor absorption performance of the absorbent is reduced.

【0009】記の吸収冷凍機用吸収液には、通常、腐
蝕防止剤として水酸化リチウム(LiOH)が添加され
る。
[0009] The upper Symbol absorption refrigerator absorption liquid, usually lithium hydroxide (LiOH) is added as a corrosion inhibitor.

【0010】図2は、本発明の吸収冷凍機用吸収液の移
送装置の一実施例を示している。なお、図2は、図1に
おける吸収器の底部まわりの詳細図である。本発明の移
送装置は、吸収冷凍機用吸収液を循環する溶液ポンプ3
0の吸引管32を、吸収冷凍機の吸収器12の底部を貫
通して上端の吸引口34が吸収液10中に位置するよう
に配設し、吸収器12内の底部近傍に位置する吸引管3
2に、主として吸収液より比重が重い添加剤(吸収促進
剤)を吸引して添加剤の滞留を防止するための添加剤
(吸収促進剤)吸引孔36を設け、吸引管32上端の吸
引口34の面積S と、添加剤吸引孔36の全面積S
との比S /S が、添加剤に対する吸収液の液組成比
の範囲から、19〜99999の範囲となるようにし、
沈降してきた添加剤を主として前記添加剤吸引孔から吸
引し、吸引管の上端の吸引口から主として添加剤より比
重が軽い吸収液を吸引し、吸収液中への添加剤の分散性
を向上させるように構成されている。この場合、添加剤
吸引孔36から主として添加剤が吸引されるので、吸収
液より比重が重い添加剤の滞留を防ぐことができる。吸
収器内における吸引管32の高さの上限hは、吸収液
溜まりの吸収液表面までの高さHより低ければよく、
下限hは、吸収液溜まり底部より高ければ、特に問題
はない。また、吸引管32の形状は円筒型でもよく角筒
型でもよく、特に限定されない。上記のように、吸引管
32上端の吸引口34の面積Sと、添加剤吸引孔36
の全面積Sとの比n=S/Sを、19〜9999
9の範囲とする。すなわち、nは吸収液とフッ素系アル
コールの液組成比の範囲であればよい。 n=S:S=99.999:0.001 n=S:S=95:5 (吸収液を100とした場合) すなわち、19<S/S<99999の範囲とな
り、望ましくは最小で、より望ましくは最大である。ま
た、添加剤吸引孔36の形状、個数は特に限定されない
が、添加剤吸引孔36を同一高さで複数個設けることが
望ましい。
FIG. 2 shows an embodiment of the absorption liquid transfer device for an absorption refrigerator according to the present invention. FIG. 2 is a detailed view around the bottom of the absorber in FIG. The transfer device of the present invention comprises a solution pump 3 for circulating an absorption liquid for an absorption refrigerator.
The suction pipe 32 is disposed so as to penetrate the bottom of the absorber 12 of the absorption refrigerator so that the suction port 34 at the upper end is located in the absorption liquid 10, and the suction is located near the bottom in the absorber 12. Tube 3
2, the additive (absorption enhancer) suction holes 36 to prevent stagnation of the additive was aspirated from the primarily absorbing liquid specific gravity additive (absorption enhancer) is provided, intake of the suction tube 32 the upper end
The area S A of引口34, the total area S B of the additive suction holes 36
The ratio S A / S B is, the liquid composition ratio of the absorption liquid to additives and
From the range of 19 to 99999,
Additives have settled mainly sucked from the additive suction holes, the ratio mainly of additives from the suction port of the upper end of the suction pipe
The absorption liquid having a light weight is sucked, and the dispersibility of the additive in the absorption liquid is improved. In this case, since the additive is mainly sucked from the additive suction hole 36, the absorption is performed.
The stagnation of the additive having a higher specific gravity than the liquid can be prevented. The upper limit h 1 of the height of the suction pipe 32 in the absorber vessel may be lower than the height H 1 to the absorption liquid surface of the reservoir absorption liquid,
The lower limit h 2, if higher than the bottom reservoir absorbing fluid, there is no particular problem. In addition, the shape of the suction tube 32 may be a cylindrical shape or a square tube shape, and is not particularly limited. As described above, the area S A of the suction port 34 at the upper end of the suction tube 32 and the additive suction hole 36
The ratio n = S A / S B of the total area S B of 19 to 9999
9 range. That is, n may be in the range of the liquid composition ratio between the absorbing liquid and the fluorinated alcohol. n = S A : S B = 99.999: 0.001 n = S A : S B = 95: 5 (assuming that the absorption liquid is 100) That is, the range of 19 <S A / S B <99999 is satisfied. Desirably the minimum, more desirably the maximum. The shape and number of the additive suction holes 36 are not particularly limited, but it is desirable to provide a plurality of additive suction holes 36 at the same height.

【0011】[0011]

【実施例】以下、本発明を実施例及び比較例に基づいて
さらに詳細に説明するが、本発明は下記実施例に何ら限
定されるものではなく、適宜変更して実施することが可
能なものである。 比較例1 LiBrを64重量%含有する水溶液を調製し、この水
溶液に2−エチルヘキシルアルコール(オクチルアルコ
ール)を0.10重量%を添加して試料吸収液を調製
し、水蒸気吸収量を測定した。結果を表1に示す。な
お、表1では、水蒸気吸収量を吸収量比で表わし、実施
例と比較しやすいように、比較例1における値を1.0
0として表示している。
EXAMPLES Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples. However, the present invention is not limited to the following Examples and can be carried out with appropriate modifications. It is. Comparative Example 1 An aqueous solution containing 64 % by weight of LiBr was prepared, and 0.10% by weight of 2-ethylhexyl alcohol (octyl alcohol) was added to this aqueous solution to prepare a sample absorbing solution, and the water vapor absorption was measured. Table 1 shows the results. In Table 1, the water vapor absorption amount is represented by an absorption amount ratio, and the value in Comparative Example 1 is set to 1.0 to facilitate comparison with the embodiment.
It is displayed as 0.

【0012】[0012]

【表1】 [Table 1]

【0013】実施例1、2 LiBrを64重量%含有する水溶液を調製した。この
水溶液に表1に示すようにフッ素系アルコール又は/及
び炭化水素系アルコールを添加し、試料吸収液を調製
し、各試料吸収液の水蒸気吸収量を測定した。測定評価
結果を表1に示す。表1から、LiBr水溶液にフッ素
系アルコールを添加した吸収液は、水蒸気吸収性能を促
進させることがわかる。
Examples 1 and 2 An aqueous solution containing 64 % by weight of LiBr was prepared. As shown in Table 1, a fluorine-based alcohol and / or a hydrocarbon-based alcohol was added to this aqueous solution to prepare sample absorbing solutions, and the amount of water vapor absorption of each sample absorbing solution was measured. Table 1 shows the evaluation results. From Table 1, the absorption solution obtained by adding a fluorine-based alcohol in aqueous LiBr solution is found to promote water vapor absorption performance.

【0014】[0014]

【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1) LiBrと水とを主成分とする吸収液に、吸収
促進剤(添加剤)としてこの吸収液よりも比重が重いフ
ッ素系アルコールを添加することにより、界面撹乱現象
を発現し、吸収液の水蒸気吸収性能を促進させ、循環作
用によって熱貫流率を高め、吸収冷凍機用の吸収器の小
型化を可能とする。 (2) 吸収液に吸収促進剤として吸収液よりも比重が
重いフッ素系アルコールを添加する場合は、吸収促進剤
の一部が吸収液中に沈み、吸収液供給の際に、吸収促進
剤が吸収液の表面に残ることにより、LiBr水溶液だ
けが供給されることを防止することができる。 (3) 本発明の吸収液の移送装置では、添加剤吸引孔
から主として吸収液より比重が重い添加剤(吸収促進
剤)が吸引されるので、添加剤(吸収促進剤)を添加し
た際に、添加剤より比重が軽い吸収液のみが送液される
ことを防止することができるとともに、添加剤の滞留を
防止することができ、吸収液中への添加剤の分散性が向
上する。
As described above, the present invention has the following effects. (1) By adding a fluorinated alcohol having a higher specific gravity than the absorption liquid as an absorption accelerator (additive) to an absorption liquid containing LiBr and water as main components, an interface disturbance phenomenon is developed and the absorption liquid Promotes the water vapor absorption performance, increases the heat transmission rate by the circulation function, and makes it possible to reduce the size of the absorber for the absorption refrigerator. (2) When a fluorine-based alcohol having a higher specific gravity than the absorption liquid is added to the absorption liquid as an absorption promoter, a part of the absorption promoter sinks in the absorption liquid, and the absorption promoter is supplied when the absorption liquid is supplied. By remaining on the surface of the absorbing liquid, it is possible to prevent the supply of only the LiBr aqueous solution. (3) In the absorption liquid transfer device of the present invention, the additive (absorption accelerator) having a higher specific gravity than the absorption liquid is mainly sucked from the additive suction hole, so that when the additive (absorption accelerator) is added, In addition, it is possible to prevent only the absorbing liquid having a specific gravity lower than that of the additive from being sent, prevent the additive from staying therein, and improve the dispersibility of the additive in the absorbing liquid.

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

【図1】本発明の吸収冷凍機用吸収液を用いた場合を示
す吸収冷凍機の一例を示す系統図である。
FIG. 1 is a system diagram showing an example of an absorption refrigerator showing a case where the absorption liquid for an absorption refrigerator of the present invention is used.

【図2】図1における吸収器底部まわりを示す拡大詳細
図である。
FIG. 2 is an enlarged detail view showing the area around the bottom of the absorber in FIG. 1;

【図3】従来の吸収冷凍機用吸収液を用いた場合を示す
吸収冷凍機の系統図である。
FIG. 3 is a system diagram of an absorption refrigerator showing a case where a conventional absorption liquid for an absorption refrigerator is used.

【符号の説明】[Explanation of symbols]

10 吸収液 12 吸収器 14 吸収促進剤 16 再生器 18 凝縮器 20 蒸発器 22 フッ素系アルコール(吸収促進剤、添加剤) 30 溶液ポンプ 32 吸引管 34 吸引口 36 添加剤吸引孔 DESCRIPTION OF SYMBOLS 10 Absorbent liquid 12 Absorber 14 Absorption promoter 16 Regenerator 18 Condenser 20 Evaporator 22 Fluorinated alcohol (absorption promoter, additive) 30 Solution pump 32 Suction pipe 34 Suction port 36 Additive suction hole

───────────────────────────────────────────────────── フロントページの続き (72)発明者 村上 明宏 兵庫県明石市川崎町1番1号 川崎重工 業株式会社 明石工場内 (72)発明者 中島 邦彦 滋賀県草津市青地町1000番地 川重冷熱 工業株式会社 本社工場内 (56)参考文献 特開 昭49−101949(JP,A) 特開 平1−184371(JP,A) 特開 昭58−219938(JP,A) 特公 昭52−48710(JP,B2) ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Akihiro Murakami 1-1, Kawasaki-cho, Akashi-shi, Hyogo Kawasaki Heavy Industries, Ltd. Akashi Plant (72) Inventor Kunihiko Nakajima 1000, Aoji-cho, Kusatsu-shi, Shiga (56) References JP-A-49-101949 (JP, A) JP-A-1-184371 (JP, A) JP-A-58-219938 (JP, A) JP-B-52-48710 (JP, B2)

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 臭化リチウムと水とを主成分とするアル
カリ性吸収液に、このアルカリ性吸収液よりも比重が重
いフッ素系アルコールを添加してなることを特徴とする
吸収冷凍機用吸収液。
1. An absorption liquid for an absorption refrigerator, wherein a fluorine-based alcohol having a higher specific gravity than the alkaline absorption liquid is added to an alkaline absorption liquid containing lithium bromide and water as main components.
【請求項2】 フッ素系アルコールが、2−(パーフル
オロブチル)エタノール、2−(パーフルオロヘキシ
ル)エタノール、2−(パーフルオロ−3−メチルブチ
ル)エタノール、2−(パーフルオロ−5−メチルヘキ
シル)エタノール、3−パーフルオロブチル−2−プロ
ペン−1−オール、3−パーフルオロヘキシル−2−プ
ロペン−1−オール、6−(パーフルオロヘキシル)ヘ
キサノール、1H,1H,3H−テトラフルオロプロパ
ノールからなる群より選ばれた少なくとも一種類のアル
コールである請求項1記載の吸収冷凍機用吸収液。
2. The fluorinated alcohol is 2- (perfluorobutyl) ethanol, 2- (perfluorohexyl) ethanol, 2- (perfluoro-3-methylbutyl) ethanol, or 2- (perfluoro-5-methylhexyl). ) From ethanol, 3-perfluorobutyl-2-propen-1-ol, 3-perfluorohexyl-2-propen-1-ol, 6- (perfluorohexyl) hexanol, 1H, 1H, 3H-tetrafluoropropanol 2. The absorption liquid for an absorption refrigerator according to claim 1, wherein the absorption liquid is at least one alcohol selected from the group consisting of:
【請求項3】 フッ素系アルコールの添加量が、0.0
01〜5重量%である請求項1又は2記載の吸収冷凍機
用吸収液。
3. The amount of the fluorine-based alcohol added is 0.0
3. The absorption liquid for an absorption refrigerator according to claim 1, wherein the amount is from 01 to 5% by weight.
【請求項4】 腐蝕防止剤として水酸化リチウムを添加
してなる請求項1〜3のいずれかに記載の吸収冷凍機用
吸収液。
4. The absorption liquid for an absorption refrigerator according to claim 1, wherein lithium hydroxide is added as a corrosion inhibitor.
【請求項5】 吸収冷凍機用吸収液を循環する溶液ポン
プの吸引管を、吸収冷凍機の吸収器底部を貫通して上端
の吸引口が吸収液中に位置するように配設し、吸収器内
の底部近傍に位置する吸引管に、主として吸収液より比
重が重い添加剤を吸引して添加剤の滞留を防止するため
の添加剤吸引孔を設け、吸引管上端の吸引口面積S
と、添加剤吸引孔の全面積S との比S /S が、
添加剤に対する吸収液の液組成比の範囲から、19〜9
9999の範囲となるようにし、沈降してきた添加剤を
主として前記添加剤吸引孔から吸引し、吸引管の上端の
吸引口から主として添加剤より比重が軽い吸収液を吸引
し、吸収液中への添加剤の分散性を向上させるようにし
たことを特徴とする吸収冷凍機用吸収液の移送装置。
5. A solution pump for circulating an absorption liquid for an absorption refrigerator.
Through the bottom of the absorber of the absorption refrigerator
Is arranged so that the suction port of
The suction tube located near the bottom of theRatio than absorption liquid
HeavyTo prevent additives from staying by sucking additives
The additive suction hole ofSuction port area S at top of suction tube
A And the total area S of the additive suction holes B Ratio S A / S B But,
From the range of the liquid composition ratio of the absorbing solution to the additive, from 19 to 9
In the range of 9999,Additives that have settled
Suction is mainly performed from the additive suction hole, and the upper end of the suction tube is
Mainly from the suction portLighter specific gravity than additiveAspirate absorbing liquid
And improve the dispersibility of the additive in the absorbing solution.
An absorption liquid transfer device for an absorption refrigerator.
【請求項6】 添加剤吸引孔を同一高さで複数個設けた
請求項5記載の吸収冷凍機用吸収液の移送装置。
6. The absorption liquid transfer device for an absorption refrigerator according to claim 5, wherein a plurality of additive suction holes are provided at the same height.
JP7187790A 1995-06-30 1995-06-30 Absorption liquid for absorption refrigerator and transfer device for this absorption liquid Expired - Fee Related JP2775601B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7187790A JP2775601B2 (en) 1995-06-30 1995-06-30 Absorption liquid for absorption refrigerator and transfer device for this absorption liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7187790A JP2775601B2 (en) 1995-06-30 1995-06-30 Absorption liquid for absorption refrigerator and transfer device for this absorption liquid

Publications (2)

Publication Number Publication Date
JPH0914783A JPH0914783A (en) 1997-01-17
JP2775601B2 true JP2775601B2 (en) 1998-07-16

Family

ID=16212275

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7187790A Expired - Fee Related JP2775601B2 (en) 1995-06-30 1995-06-30 Absorption liquid for absorption refrigerator and transfer device for this absorption liquid

Country Status (1)

Country Link
JP (1) JP2775601B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5427327B2 (en) * 2008-01-30 2014-02-26 三菱マテリアル株式会社 Method for absorbing perfluoroalkanesulfonyl fluoride

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5223413B2 (en) * 1973-02-01 1977-06-24
JPS5248710A (en) * 1975-10-14 1977-04-19 Fujio Hisashi Rotary engine
JPS57121854U (en) * 1981-01-23 1982-07-29
JPS57137950U (en) * 1981-02-18 1982-08-28
JPS58219938A (en) * 1982-06-17 1983-12-21 Mitsubishi Heavy Ind Ltd Absorbent for absorbing type heat pump
JPH0663671B2 (en) * 1987-01-30 1994-08-22 株式会社日立製作所 Absorption refrigerator and its absorbing liquid
JPH076704B2 (en) * 1988-01-20 1995-01-30 矢崎総業株式会社 Absorption refrigerator absorption liquid
JPH02294383A (en) * 1989-05-08 1990-12-05 Hitachi Ltd Absorbing solution of absorption refrigerator

Also Published As

Publication number Publication date
JPH0914783A (en) 1997-01-17

Similar Documents

Publication Publication Date Title
JPH09512332A (en) Absorption cooling device and method
JP2775601B2 (en) Absorption liquid for absorption refrigerator and transfer device for this absorption liquid
JPS59501750A (en) Water-based absorbent for absorption cycle heat pumps
CN106839795B (en) A kind of efficient foam metal steam condenser handled through hydrophobicity
CN105953623A (en) Multi-branch phase change heat transfer system
CN202133188U (en) Semi-hot pipe type water source heat pump system
CN207755952U (en) Tungsten reaction kettle device for recovering tail gas
CN216745533U (en) Condensing system
JP2008267667A (en) Absorbent for absorption chiller/heater and absorption chiller/heater
CN210751315U (en) Air source multiple-effect vacuum evaporation system applied to cutting fluid concentration
CN203561254U (en) Two-phase flow power heat pipe device
JP4852958B2 (en) Organic solvent recovery system
CN102230691B (en) Half heat pipe type water source heat pump system
JPH0559165U (en) Absorption chiller / heater
CN220559944U (en) Cleaning device
CN212457501U (en) Straight-through type two-class heat pump
JPH11257797A (en) Absorber for absorption type refrigerator
JP2002130858A (en) Absorption refrigerating machine
CN210295029U (en) Temperature control device of machine room server
CN206219559U (en) A kind of wine brewing cooling device
JPH076704B2 (en) Absorption refrigerator absorption liquid
JPS58210440A (en) Heat pipe type solar heat water heater
JPH0325258A (en) Air cooled absorption type cold and hot water supplier
JP2668063B2 (en) Absorbent composition for absorption air conditioner
JP3241498B2 (en) Absorption refrigerator

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090501

Year of fee payment: 11

LAPS Cancellation because of no payment of annual fees
S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313117

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R370 Written measure of declining of transfer procedure

Free format text: JAPANESE INTERMEDIATE CODE: R370