JPS6023264B2 - Air-cooled absorption refrigerator that removes absorbed heat using absorption liquid as a heat medium - Google Patents
Air-cooled absorption refrigerator that removes absorbed heat using absorption liquid as a heat mediumInfo
- Publication number
- JPS6023264B2 JPS6023264B2 JP3207778A JP3207778A JPS6023264B2 JP S6023264 B2 JPS6023264 B2 JP S6023264B2 JP 3207778 A JP3207778 A JP 3207778A JP 3207778 A JP3207778 A JP 3207778A JP S6023264 B2 JPS6023264 B2 JP S6023264B2
- Authority
- JP
- Japan
- Prior art keywords
- absorption liquid
- absorption
- heat
- air
- liquid
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
この発明は吸収液を熱媒体として吸収熱を除去する空冷
式吸収冷凍機に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an air-cooled absorption refrigerator that removes absorbed heat using an absorption liquid as a heat medium.
従来の吸収冷凍機においては、吸収器の管群の管外面を
流下している高濃度の吸収液は、蒸発器で蒸発した袷煤
蒸気を吸収する際に濃度が下り、吸収熱を発生する。In conventional absorption refrigerators, the highly concentrated absorption liquid flowing down the outer surface of the absorber tube group decreases in concentration as it absorbs the soot vapor evaporated in the evaporator, generating absorption heat. .
そのため吸収液の冷却は吸収器管群の管内に冷却塔など
からの冷却水を蒸発による不足量を外部から補充しつつ
流して行っている。しかし、この様な従来方式は水資源
に乏しかったり、水質が汚れていたりなどの冷却水の得
難い地域には不向きである。Therefore, the absorption liquid is cooled by flowing cooling water from a cooling tower or the like into the tubes of the absorber tube group while replenishing the insufficient amount due to evaporation from the outside. However, such conventional methods are not suitable for areas where cooling water is difficult to obtain, such as where water resources are scarce or the water quality is dirty.
この発明はこのような従来の水冷方式によることなく、
吸収器からその上位の吸収液の散布装置に至る吸収液循
環系に吸収液空冷部を設け、その吸収液循環量の一部を
分流させる管路に再生器を設け、再生器で熱媒体により
加熱濃縮された吸収液を前記吸収液循環系に戻すと共に
その再生器で蒸発分離した冷煤を冷煤凝縮空冷部を通し
冷却凝縮した冷煤液を蒸発器からその上位の冷煤液の散
布装置に至る冷嬢液循環系に戻すことにより、冷却水を
用いる凝縮器を省略し「冷却水の代りに吸収液自身を熱
媒体として吸収熱を大気に放熱して吸収液の冷却を容易
にすることができ、しかも吸収器における吸収液の濃度
を所定値に保つことができるようにしたものである。This invention does not rely on such conventional water cooling method,
An absorption liquid air-cooling section is installed in the absorption liquid circulation system from the absorber to the upper absorption liquid dispersion device, and a regenerator is installed in the pipe line that diverts a part of the absorption liquid circulation amount. The heated and concentrated absorption liquid is returned to the absorption liquid circulation system, and the cold soot that has been evaporated and separated in the regenerator is cooled and condensed through the cold soot condensation air cooling section. By returning the cooling liquid to the cooling liquid circulation system leading to the equipment, the condenser that uses cooling water can be omitted, and the absorption liquid itself can be used as a heat medium instead of cooling water to radiate absorbed heat to the atmosphere, making it easier to cool the absorption liquid. In addition, the concentration of the absorption liquid in the absorber can be maintained at a predetermined value.
以下図面に示す実施例により本発明を説明する。The present invention will be explained below with reference to embodiments shown in the drawings.
図面は本発明の構造系統図を示したものであって、中空
胴体よりなる密閉容器1内の胴体のほぼ全長にわたって
設けた受皿2に溜った例えば水などの冷嬢液は管路4に
設けた冷嬢ポンプ3で、管路4を経て散布装置16に至
り受皿2の上位にある蒸発器6の管群の管外面に散布さ
れ、その管内に管路5から流入してこれを流通し管路1
7に流出する冷水を冷煤の気化熱で冷却させく冷凍効果
をあらわす。The drawing shows a structural system diagram of the present invention, in which a refrigerating liquid such as water accumulated in a saucer 2 provided over almost the entire length of the body in a closed container 1 made of a hollow body is provided in a conduit 4. The refrigeration pump 3 passes through the pipe 4 to the spraying device 16, where it is sprayed onto the outer surface of the tubes of the evaporator 6 located above the receiver tray 2, and flows into the pipe from the pipe 5 to be distributed. Conduit 1
7 shows the refrigeration effect in which the cold water flowing out is cooled by the heat of vaporization of the cold soot.
この冷水は冷房、冷凍、その他の用途に供されるものと
なる。即ち冷媒液自らは蒸発器内の圧力に相当する蒸発
温度で蒸発する。このような蒸発作用を行なう機造にす
るため蒸発器6は高度の真空に保たれる密閉容器1内に
談薄される。密度容器1の下部には臭化リチウム水溶液
などの吸収液の溜り7が設けてあり、これにより吸収液
は管略18に排出され、管路18に設けた吸収液ポンプ
8で冷却器則ち吸収液空冷部9を通り、管路19を経て
溜り7の上位の所要の間隔を保って複数段に形成した多
数通孔を有するトレー状の吸収器11の上方空間に設け
た散布装置1川こ至り散布されるようにしてある。This cold water is used for cooling, freezing, and other purposes. That is, the refrigerant liquid itself evaporates at an evaporation temperature corresponding to the pressure within the evaporator. In order to provide a mechanism for performing such an evaporation action, the evaporator 6 is placed in a closed container 1 that is maintained at a high degree of vacuum. At the bottom of the density container 1, there is provided a reservoir 7 for an absorbing liquid such as an aqueous lithium bromide solution, and the absorbing liquid is discharged into a pipe 18. The absorption liquid passes through the air cooling section 9, passes through the pipe line 19, and is disposed in the space above the tray-shaped absorber 11, which has a large number of through holes formed in multiple stages at a required interval above the reservoir 7. It is made to be distributed widely.
従って前述した蒸発器6よりの冷煤蒸気を吸収すること
ができる。本発明では、まず吸収液の循環量を増加する
。そして吸収器11において袷煤蒸気の吸収中に冷却水
での冷却が行なわれない代りに、吸収熱により自らの温
度が上昇するのであるが、その循環量を増加しているた
めに、その温度上昇を微小に留めるようにしているので
ある。吸収液の冷却は吸収液空冷部9のごとき冷却器を
用い大気による空冷で行なってから、これを散布装置1
川こ戻す。一方、吸収液溜り7の吸収液の一部は吸収液
ポンプ8で、管路18からの分汁皮管路に流入し制御弁
をもつ流量加減装置12で流量を加減し熱交換器13を
経て再生器14に供給し、ここで熱源21や外部からの
熱媒体で吸収液を加熱沸騰させる。発生する冷煤蒸気は
従釆方式は凝縮器で冷却水を用い冷却液化するのである
が、本発明では冷媒蒸気を管路22を通し大気による空
冷凝縮器即ち冷煤凝縮空冷部15で冷却液化し、管路2
3から蒸発器6の下位の受皿2などから適宜袷煤液循環
系統に戻せばよい。前記再生器14で吸収液自らは濃度
が上昇し、管路24を通り熱交換器13を経て再生器1
4に送られる吸収液に熱を与え溜り7の上方の空間など
適宜吸収液循環系統に戻り、吸収液循環系統の濃度を維
持する。Therefore, the cold soot vapor from the evaporator 6 described above can be absorbed. In the present invention, first, the circulation amount of the absorption liquid is increased. While the absorber 11 is absorbing the soot vapor, it is not cooled with cooling water, but its own temperature rises due to the absorbed heat. This is to keep the increase to a minimum. The absorption liquid is cooled by atmospheric air using a cooler such as the absorption liquid air cooling section 9, and then transferred to the spraying device 1.
Bring back the river. On the other hand, a part of the absorption liquid in the absorption liquid reservoir 7 flows into the separation skin pipe line from the pipe line 18 by the absorption liquid pump 8, and the flow rate is adjusted by the flow rate adjustment device 12 having a control valve, and the heat exchanger 13 is controlled. The absorption liquid is then supplied to the regenerator 14, where the absorption liquid is heated and boiled using the heat source 21 or a heat medium from the outside. In the conventional method, the generated cold soot vapor is cooled and liquefied in a condenser using cooling water, but in the present invention, the refrigerant vapor is passed through a pipe 22 and cooled and liquefied in an air-cooled condenser, that is, a cold soot condensing air cooling section 15. and pipe 2
3 to the saucer 2 below the evaporator 6, etc., to the soot liquid circulation system as appropriate. The absorption liquid itself increases in concentration in the regenerator 14, passes through the pipe line 24, passes through the heat exchanger 13, and then returns to the regenerator 1.
Heat is applied to the absorption liquid sent to the absorption liquid circulation system 4, and the absorption liquid is returned to the absorption liquid circulation system as appropriate, such as in the space above the reservoir 7, to maintain the concentration of the absorption liquid circulation system.
尚、上述のように吸収液を吸収器11で冷却する必要が
ないため、吸収器11では専ら吸収液と冷媒蒸気の良好
な気液接触を期待すればよく、本実施例ではトレー状の
ごとき充填棚を例示したが、このほかに断面円形、角形
その他任意形状でハニカム状に形成した気液接触用のプ
ラスチック充填物を吸収器に充填するようにしてもよい
。As mentioned above, since there is no need to cool the absorption liquid in the absorber 11, it is only necessary to expect good gas-liquid contact between the absorption liquid and the refrigerant vapor in the absorber 11. Although a filling shelf is shown as an example, the absorber may be filled with a plastic filling for gas-liquid contact formed in a honeycomb shape with a circular cross section, a square cross section, or any other arbitrary shape.
前記実施例についての説明から明らかであるように、本
発明の構成によれば、吸収器での吸収液の流量を増加し
、冷媒蒸気の吸収時に発生する吸収熱の上昇を極力抑え
、温度上昇した吸収液は吸収液循環系に設けた吸収液空
冷部で大気に放熱して冷却して散布装置に戻すようにし
たから、従釆方式のように冷却水を全く使用しないでよ
いので、冷却水の得難い地域での使用に最適である。又
、再生器で吸収液循環量の一部を濃縮して吸収液循環系
に戻すようにしたから、吸収器における吸収液の濃度を
所定値に保つことができるので、吸収能力を低下させる
おそれもない。更に、再生器で熱媒体によって加熱され
蒸発分離した冷媒は冷媒凝縮空冷部で大気に放熱して冷
却液化して、蒸発器からその上位の散布装置に至る袷煤
液循環系に戻すようにしたから、従釆の凝縮器での冷却
水による冷却方式と異り冷却水が全く不要である。As is clear from the description of the above embodiments, according to the configuration of the present invention, the flow rate of the absorption liquid in the absorber is increased, the rise in absorption heat generated when refrigerant vapor is absorbed is suppressed as much as possible, and the temperature rise is The absorbed liquid is cooled by radiating heat to the atmosphere in the absorption liquid air-cooling section installed in the absorption liquid circulation system, and then returned to the spraying equipment.Therefore, there is no need to use cooling water at all as in the conventional method, so cooling is possible. Ideal for use in areas where water is difficult to obtain. In addition, since a part of the circulating amount of absorption liquid is concentrated in the regenerator and returned to the absorption liquid circulation system, the concentration of absorption liquid in the absorber can be maintained at a predetermined value, which eliminates the risk of reducing the absorption capacity. Nor. Furthermore, the refrigerant that is heated by the heat medium and evaporated and separated in the regenerator is cooled and liquefied by radiating heat to the atmosphere in the refrigerant condensing air cooling section, and is returned to the soot liquid circulation system from the evaporator to the dispersion equipment above it. Therefore, unlike the cooling method using cooling water in the secondary condenser, no cooling water is required.
図面は本発明の一実施例を示す構造系統図である。
1・・…・密閉容器、2・・・・・・受皿、3・・・・
・・冷嬢ポンプ、4,5,17,18,19,20,2
2,23, 24・・・・・・管路、6・・・・・・蒸
発器、7・・・・・・溜り、8…・・・吸収液ポンプ、
9……吸収液空冷部、10,16・・・・・・散布装置
、11・・…・吸収器、12・・・…流量加減装置、1
3・・・・・・熱交換器、14・…・・再生器、15・
・・・・・冷煤凝縮空冷部、21・・・・・・熱源。The drawing is a structural system diagram showing one embodiment of the present invention. 1...Airtight container, 2...Saucer, 3...
... Refrigerated pump, 4, 5, 17, 18, 19, 20, 2
2, 23, 24... Pipeline, 6... Evaporator, 7... Reservoir, 8... Absorbent pump,
9... Absorption liquid air cooling section, 10, 16... Spraying device, 11... Absorber, 12... Flow rate adjustment device, 1
3... Heat exchanger, 14... Regenerator, 15...
... Cold soot condensation air cooling section, 21 ... Heat source.
Claims (1)
媒蒸気吸収時に発生する吸収熱で温度上昇した吸収液を
大気に放熱して冷却するための吸収液空冷部を吸収器か
ら散布装置に至る吸収液循環系に設けたことを特徴とす
る吸収液を熱媒体として吸収熱を除去する空冷式吸収冷
凍機。 2 前記吸収器に蒸発器から発生する冷媒蒸気を能率よ
く吸収するよう気液接触面積を大ならしめるごとく構成
した充填物を充填してある特許請求の範囲第1項に記載
の吸収液を熱媒体として吸収熱を除去する空冷式吸収冷
凍機。 3 前記吸収液空冷部を外面にフインを有する管群で配
列し、管内に吸収液を流し管外に大気を通して吸収液を
冷却し温度を低下させるようにした特許請求の範囲第1
項若しくは第2項記載の吸収液を熱媒体として吸収熱を
除去する空冷式吸収冷凍機。 4 吸収器で流過する吸収液を増量し、蒸発器からの冷
媒蒸気吸収時に発生する吸収熱で温度上昇した吸収液を
大気に放熱して冷却するための吸収液空冷部を吸収器か
ら散布装置に至る吸収液循環系に設け、その循環系に吸
収液循環量の一部を分流せしめる分岐管路を設け、これ
に吸収液の濃度を上げて所定値に保つよう再生器を設け
ると共にその再生器で濃縮した吸収液を前記吸収液循環
系に戻すようにしたことを特徴とする吸収液を熱媒体と
して吸収熱を除去する空冷式吸収冷凍機。 5 前記再生器で加熱媒体により加熱され蒸発分離した
冷媒を大気に放熱して冷却液化するための冷媒凝縮空冷
部を経て蒸発器から散布装置に至る冷媒液循環系に戻す
ようにしてある特許請求の範囲第4項に記載の吸収液を
熱媒体として吸収熱を除去する空冷式吸収冷凍機。[Scope of Claims] 1. Absorption liquid air cooling for increasing the amount of absorption liquid flowing through the absorber and cooling the absorption liquid whose temperature has risen due to absorption heat generated during absorption of refrigerant vapor from the evaporator by radiating heat to the atmosphere. An air-cooled absorption refrigerator that removes absorbed heat using an absorption liquid as a heat medium, characterized in that a part is provided in an absorption liquid circulation system from an absorber to a dispersion device. 2. The absorption liquid according to claim 1 is filled with a filler configured to increase the gas-liquid contact area so as to efficiently absorb the refrigerant vapor generated from the evaporator. Air-cooled absorption refrigerator that removes absorbed heat as a medium. 3. The absorption liquid air-cooling section is arranged in a group of tubes having fins on the outer surface, and the absorption liquid is flowed inside the tubes and air is passed outside the tubes to cool the absorption liquid and lower the temperature.
An air-cooled absorption refrigerator that removes absorbed heat using the absorption liquid described in item 1 or 2 as a heat medium. 4 Increase the amount of absorption liquid flowing through the absorber, and distribute the absorption liquid air-cooling section from the absorber to cool the absorption liquid, whose temperature has risen due to absorption heat generated when absorbing refrigerant vapor from the evaporator, by releasing heat to the atmosphere. A branch pipe is installed in the absorption liquid circulation system leading to the device, and a branch pipe is provided to divert a part of the circulation amount of the absorption liquid to the circulation system. An air-cooled absorption refrigerator that removes absorption heat using the absorption liquid as a heat medium, characterized in that the absorption liquid concentrated in the regenerator is returned to the absorption liquid circulation system. 5. A patent claim in which the refrigerant heated by the heating medium and evaporated and separated in the regenerator is returned to the refrigerant liquid circulation system from the evaporator to the dispersion device through a refrigerant condensing air cooling section for radiating heat to the atmosphere and cooling and liquefying the refrigerant. An air-cooled absorption refrigerator that removes absorbed heat using the absorption liquid according to item 4 as a heat medium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3207778A JPS6023264B2 (en) | 1978-03-20 | 1978-03-20 | Air-cooled absorption refrigerator that removes absorbed heat using absorption liquid as a heat medium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3207778A JPS6023264B2 (en) | 1978-03-20 | 1978-03-20 | Air-cooled absorption refrigerator that removes absorbed heat using absorption liquid as a heat medium |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS54124359A JPS54124359A (en) | 1979-09-27 |
JPS6023264B2 true JPS6023264B2 (en) | 1985-06-06 |
Family
ID=12348808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3207778A Expired JPS6023264B2 (en) | 1978-03-20 | 1978-03-20 | Air-cooled absorption refrigerator that removes absorbed heat using absorption liquid as a heat medium |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6023264B2 (en) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4715574B2 (en) * | 2006-03-20 | 2011-07-06 | ダイキン工業株式会社 | Absorption refrigeration system |
JP4572860B2 (en) * | 2006-03-31 | 2010-11-04 | ダイキン工業株式会社 | Absorption refrigeration system |
JP2007278570A (en) * | 2006-04-05 | 2007-10-25 | Daikin Ind Ltd | Air-cooled absorption type refrigerating device |
JP4887872B2 (en) * | 2006-04-05 | 2012-02-29 | ダイキン工業株式会社 | Absorption refrigeration system |
JP4887871B2 (en) * | 2006-04-05 | 2012-02-29 | ダイキン工業株式会社 | Absorption refrigeration system |
JP4986666B2 (en) * | 2007-03-22 | 2012-07-25 | 大阪瓦斯株式会社 | Absorption refrigerator |
JP2008232573A (en) * | 2007-03-22 | 2008-10-02 | Osaka Gas Co Ltd | Absorption refrigerating machine |
JP5217264B2 (en) * | 2007-06-19 | 2013-06-19 | ダイキン工業株式会社 | Waste heat driven absorption refrigeration system |
JP2009052811A (en) * | 2007-08-28 | 2009-03-12 | Daikin Ind Ltd | Exhaust heat drive-type absorption refrigerating device |
JP2009058181A (en) * | 2007-08-31 | 2009-03-19 | Daikin Ind Ltd | Absorption type refrigerating apparatus |
JP5018376B2 (en) * | 2007-09-28 | 2012-09-05 | ダイキン工業株式会社 | Refrigeration system |
JP5098547B2 (en) * | 2007-10-03 | 2012-12-12 | ダイキン工業株式会社 | Absorption refrigeration system |
JP5092668B2 (en) * | 2007-10-10 | 2012-12-05 | ダイキン工業株式会社 | Absorption refrigeration system |
JP5098561B2 (en) * | 2007-10-15 | 2012-12-12 | ダイキン工業株式会社 | Absorption refrigeration system |
JP5092677B2 (en) * | 2007-10-18 | 2012-12-05 | ダイキン工業株式会社 | Absorption refrigeration system |
JP5244230B2 (en) * | 2008-06-09 | 2013-07-24 | コンセジョ スペリオール デ インベスティガショネス シエンティフィカス | Absorber, absorber-evaporator assembly for absorber, and lithium bromide-water absorber incorporating said absorber and absorber-evaporator assembly |
-
1978
- 1978-03-20 JP JP3207778A patent/JPS6023264B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS54124359A (en) | 1979-09-27 |
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