JPH046857B2 - - Google Patents

Info

Publication number
JPH046857B2
JPH046857B2 JP20137782A JP20137782A JPH046857B2 JP H046857 B2 JPH046857 B2 JP H046857B2 JP 20137782 A JP20137782 A JP 20137782A JP 20137782 A JP20137782 A JP 20137782A JP H046857 B2 JPH046857 B2 JP H046857B2
Authority
JP
Japan
Prior art keywords
refrigerant
liquid
absorption
evaporator
absorber
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
JP20137782A
Other languages
Japanese (ja)
Other versions
JPS5993157A (en
Inventor
Mitsuo Nakano
Keiichi Ootsuka
Kazutaka Nishida
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP20137782A priority Critical patent/JPS5993157A/en
Publication of JPS5993157A publication Critical patent/JPS5993157A/en
Publication of JPH046857B2 publication Critical patent/JPH046857B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ) 発明の技術分野 本発明は吸収冷凍サイクルの放熱側即ち吸収器
及び凝縮器での放熱を温水等被加熱流体を昇温す
る吸収ヒートポンプの改良に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Technical Field of the Invention The present invention relates to an improvement in an absorption heat pump that uses heat radiation from the heat radiation side of an absorption refrigeration cycle, that is, an absorber and a condenser, to raise the temperature of a fluid to be heated, such as hot water.

(ロ) 従来技術とその問題点 吸収器及び凝縮器の放熱作用を利用して被加熱
流体を昇温する吸収ヒートポンプは、駆動エネル
ギー換言すれば発生器への加熱入力に対する被加
熱流体の熱出力比(即ち成績係数)が高く、効率
良く被加熱流体を昇温できる利点を有するもので
あるが、蒸発器へ供給する熱源流体の温度が低く
なり過ぎたり、熱源流体の供給量が不足すると蒸
発器での冷媒気化作用が不十分となり、極端な場
合には蒸発器側の蒸気圧より吸収器側の蒸気圧
(吸収器に散布される吸収液の飽和蒸気圧)の方
が高くなつて冷媒蒸気が吸収器から蒸発器へと移
動し、該蒸発器にて凝縮する現象即ち被加熱流体
から熱源流体への逆放熱現象を生じる問題があ
り、また吸収器に流入する被加熱流体の温度が低
くて逆放熱現象を生じない場合には吸収液の結晶
や冷媒の凍結等を生じる問題がある。このよう
に、従来の此種吸収ヒートポンプにおいては、蒸
発器に供給する熱源流体の温度若しくは流量が低
下し過ぎると安全かつ安定的に被加熱流体を昇温
できないという問題点を有するものであつた。
(b) Prior art and its problems Absorption heat pumps that raise the temperature of the heated fluid by using the heat dissipation effect of the absorber and condenser have drive energy, in other words, the heat output of the heated fluid relative to the heating input to the generator. It has a high ratio (i.e. coefficient of performance) and has the advantage of being able to efficiently raise the temperature of the heated fluid, but if the temperature of the heat source fluid supplied to the evaporator becomes too low or the supply amount of the heat source fluid is insufficient, evaporation will occur. The refrigerant vaporization effect in the absorber becomes insufficient, and in extreme cases, the vapor pressure on the absorber side (saturated vapor pressure of the absorption liquid sprayed in the absorber) becomes higher than the vapor pressure on the evaporator side, causing the refrigerant to evaporate. There is a problem in that steam moves from the absorber to the evaporator and condenses in the evaporator, that is, a reverse heat radiation phenomenon occurs from the heated fluid to the heat source fluid, and the temperature of the heated fluid flowing into the absorber increases. If it is too low to cause a reverse heat dissipation phenomenon, there will be problems such as crystallization of the absorption liquid and freezing of the refrigerant. As described above, conventional absorption heat pumps of this type have the problem that if the temperature or flow rate of the heat source fluid supplied to the evaporator drops too much, the temperature of the heated fluid cannot be raised safely and stably. .

(ハ) 問題点を解決するための手段 本発明は、上記問題点に鑑み、此種吸収ヒート
ポンプにおいて、蒸発器に供給される熱源流体が
設定温度若しくは設定流量以下となつた場合、蒸
発器に収納した熱源管に散布される冷媒液と吸収
器に収納した被加熱管に散布される吸収液が、
夫々冷媒バイパス管及び溶液バイパス管を流れ、
夫々熱源管、被加熱管を側路するように循環せし
める切換え手段を採ることにより、前述の逆放熱
現象或いは吸収液の結晶や冷媒の凍結等の弊害が
生じるのを未然に防止しつつ、発生器から凝縮器
へ流入する冷媒蒸気の熱で該凝縮器において被加
熱流体を安全かつ安定的に昇温できる吸収ヒート
ポンプを提供したものである。
(C) Means for Solving the Problems In view of the above problems, the present invention provides, in this type of absorption heat pump, when the heat source fluid supplied to the evaporator falls below the set temperature or set flow rate, the evaporator is The refrigerant liquid that is sprayed on the stored heat source tubes and the absorption liquid that is sprayed on the heated tubes that are stored in the absorber are
flowing through the refrigerant bypass pipe and the solution bypass pipe, respectively;
By adopting a switching means that circulates the heat source tube and the heated tube in a bypass manner, it is possible to prevent the above-mentioned reverse heat dissipation phenomenon, crystals of the absorption liquid, freezing of the refrigerant, etc., while preventing them from occurring. The present invention provides an absorption heat pump that can safely and stably raise the temperature of a fluid to be heated in the condenser using the heat of refrigerant vapor flowing into the condenser from the condenser.

(ニ) 実施例 図面は本発明の一実施例を示した概略構成図
で、1は燃焼バーナー2を備え、稀液から冷媒を
加熱分離して濃液に再生する発生器、3は発生器
1からの気液を濃液と冷媒蒸気とに分ける分離
器、4は分離器3からの冷媒蒸気を器内に収納し
た被加熱管5内の被加熱流体で冷却して凝縮させ
る凝縮器、6は器内下部に設けた冷媒液溜め7の
冷媒液を気泡ポンプ8により器内に収納した熱源
管9に循環散布して気化させる蒸発器、10は分
離器3からの濃液を器内に収納した被加熱管5に
散布して該管内の被加熱流体で冷却しつつ濃液に
気化冷媒を吸収させる吸収器及び11は溶液熱交
換器で、これらは揚液管12、濃液管13、溶液
ポンプ14を有する稀釈管15、凝縮冷媒液を気
泡ポンプ8内に通した後冷媒分散器16へ導く冷
媒液流下管17、冷媒液溜め7の冷媒液を気泡ポ
ンプ8に導く冷媒液管18、気泡ポンプ8により
冷媒液を冷媒分散器16に送る冷媒液上昇管19
及び冷媒蒸気導管20で接続されて冷媒と吸収液
との循環サイクルを形成するようになつている。
(d) Embodiment The drawing is a schematic configuration diagram showing an embodiment of the present invention, in which 1 is a generator equipped with a combustion burner 2, and 3 is a generator that heats and separates the refrigerant from a dilute liquid and regenerates it into a concentrated liquid. 4 is a separator that separates the gas and liquid from 1 into concentrated liquid and refrigerant vapor; 4 is a condenser that cools and condenses the refrigerant vapor from separator 3 with the heated fluid in the heated tube 5 housed in the container; 6 is an evaporator that circulates and vaporizes the refrigerant liquid in a refrigerant reservoir 7 provided at the lower part of the vessel through a heat source tube 9 housed in the vessel using a bubble pump 8; 11 is a solution heat exchanger, and 11 is a solution heat exchanger, and 11 is a solution heat exchanger. 13. A dilution tube 15 having a solution pump 14; a refrigerant liquid down-flow pipe 17 that passes the condensed refrigerant liquid through the bubble pump 8 and then leads it to the refrigerant distributor 16; a refrigerant liquid that leads the refrigerant liquid in the refrigerant reservoir 7 to the bubble pump 8; pipe 18 , a refrigerant liquid riser pipe 19 that sends the refrigerant liquid to the refrigerant distributor 16 by the bubble pump 8;
and are connected by a refrigerant vapor conduit 20 to form a circulation cycle of refrigerant and absorption liquid.

21は、前記被加熱管5に散布される濃液が該
被加熱管を側路するように、濃液管13から分岐
して吸収器10底部へ接続されている溶液バイパ
ス管で、該管には開閉弁V1が備えてあり、また、
濃液の分岐点から溶液分散器22へ至る途中の濃
液管13にも開閉弁V2が備えてある。23は、
前記気泡ポンプ8により熱源管9に散布される冷
媒液が該熱源管を側路するように、冷媒液溜め7
と溶液溜め24とを接続している冷媒バイパス管
で、該管には開閉弁V3が備えてある。Sは前記
熱源管9に備えた温度検出器(又は流量検出器)
で、該検出器の信号により、熱源流体が設定温度
(又は設定流量)以下であるときは前記開閉弁
V1,V3を開き、開閉弁V2を閉じ、熱源流体が設
定温度より高い(又は設定流量より多い)ときは
逆に前記開閉弁V1,V3を閉じ、開閉弁V2を開く
ように切換え可能となつている。
Reference numeral 21 denotes a solution bypass pipe that is branched from the concentrated liquid pipe 13 and connected to the bottom of the absorber 10 so that the concentrated liquid sprayed onto the heated pipe 5 bypasses the heated pipe. is equipped with an on-off valve V 1 , and
The concentrated liquid pipe 13 on the way from the concentrated liquid branch point to the solution disperser 22 is also provided with an on-off valve V 2 . 23 is
The refrigerant liquid reservoir 7 is arranged so that the refrigerant liquid sprayed onto the heat source pipe 9 by the bubble pump 8 bypasses the heat source pipe.
A refrigerant bypass pipe connects the solution reservoir 24 and the refrigerant bypass pipe, and the pipe is equipped with an on-off valve V3 . S is a temperature detector (or flow rate detector) provided in the heat source tube 9
According to the signal from the detector, when the heat source fluid is below the set temperature (or set flow rate), the on-off valve is activated.
V 1 and V 3 are opened and on-off valve V 2 is closed, and when the heat source fluid is higher than the set temperature (or higher than the set flow rate), the on-off valves V 1 and V 3 are closed and on-off valve V 2 is opened. It is possible to switch as follows.

斯る構成の吸収ヒートポンプにおいては、蒸発
器6へ供給される熱源流体のエネルギーが不足気
味になり、蒸発器6での冷媒気化作用が不十分に
なると、被加熱管5に散布されていた濃液が溶液
バイパス管21を流通すると共に熱源管9に散布
されていた冷媒液が冷媒バイパス管23を流通
し、蒸発器6での冷媒気化作用と吸収器10での
冷媒吸収作用が停止され、被加熱管5内を流通す
る被加熱流体は凝縮器5内で発生器1から分離器
3を経て流入する冷媒蒸気の熱により昇温される
のである。すなわち、吸収器10の被加熱管5に
散布される吸収液の飽和蒸気圧が蒸発器6の冷媒
蒸気圧より高くなり冷媒蒸気が吸収器10側から
蒸発器6側へ移動して該蒸発器の熱源管9に凝縮
する現象言い代えれば被加熱流体の熱が熱源流体
へ放出される所謂逆放熱現象が未然に防止される
よう、冷媒と吸収液との循環サイクルが切換つて
謂わばボイラー運転に移行するものである。
In the absorption heat pump having such a configuration, when the energy of the heat source fluid supplied to the evaporator 6 becomes insufficient and the refrigerant vaporization effect in the evaporator 6 becomes insufficient, the concentrated water that has been sprayed on the heated tubes 5 As the liquid flows through the solution bypass pipe 21, the refrigerant liquid that had been sprayed in the heat source pipe 9 flows through the refrigerant bypass pipe 23, and the refrigerant vaporization action in the evaporator 6 and the refrigerant absorption action in the absorber 10 are stopped. The heated fluid flowing through the heated tube 5 is heated in the condenser 5 by the heat of the refrigerant vapor flowing from the generator 1 through the separator 3. That is, the saturated vapor pressure of the absorption liquid sprayed on the heated tube 5 of the absorber 10 becomes higher than the refrigerant vapor pressure of the evaporator 6, and the refrigerant vapor moves from the absorber 10 side to the evaporator 6 side, and the evaporator In other words, the circulation cycle of the refrigerant and absorption liquid is switched to prevent the phenomenon of condensation in the heat source tube 9, in which the heat of the heated fluid is released to the heat source fluid. This is a transition to

また、熱源流体供給温度が低下し過ぎたり、或
いは供給量が少なすぎる場合に吸収器10に流入
する被加熱流体温度が低くなつてもなお吸収器1
0での冷媒吸収作用を継続すると、蒸発器6及び
吸収器10内圧が低下して冷媒の凍結或いは熱源
流体の凍結延いては吸収液の結晶等の弊害を生じ
る原因となるが、本発明吸収冷凍機においては、
熱源流体の供給温度又は供給量が低下しすぎる前
に吸収器10の冷媒吸収作用と蒸発器6の冷媒気
化作用を停止するので、これら弊害も未然に防止
される。更に、冷媒液溜め7の冷媒液が溶液溜め
24の吸収液に混入されて発生器1に還流される
吸収液濃度がうすくなるので、該発生器内の吸収
液沸騰温度が低くなる結果、所謂ボイラー運転時
に吸収液を昇温するためのエネルギーを節約でき
る利点もある。
In addition, if the heat source fluid supply temperature drops too much or the supply amount is too small, even if the temperature of the heated fluid flowing into the absorber 10 becomes low, the absorber 1
If the refrigerant absorption action continues at 0, the internal pressure of the evaporator 6 and absorber 10 will decrease, causing problems such as freezing of the refrigerant, freezing of the heat source fluid, and crystallization of the absorption liquid. In the refrigerator,
Since the refrigerant absorption action of the absorber 10 and the refrigerant vaporization action of the evaporator 6 are stopped before the supply temperature or supply amount of the heat source fluid drops too much, these disadvantages are also prevented. Furthermore, the refrigerant liquid in the refrigerant liquid reservoir 7 is mixed with the absorbent liquid in the solution reservoir 24, and the concentration of the absorbent liquid returned to the generator 1 becomes diluted, so that the boiling temperature of the absorbent liquid in the generator becomes low, resulting in the so-called Another advantage is that it saves energy needed to heat up the absorption liquid during boiler operation.

尚、冷媒液のバイパス路は、図示したものに限
らず、例えば冷媒液管18と稀釈管15の溶液ポ
ンプ14吸込側とを接続する管(図示せず)や凝
縮冷媒液を直接溶液溜め24に導く管(図示せ
る)或いはこれら管の組み合わせ等で代用しても
良く、また、循環サイクル切換機構も図示したも
のに限らず、例えば前記検出器9と被加熱流体の
吸収器10流入温度を感知する検出器(図示せ
ず)との信号で開閉弁V1,V2及びV3の開閉を切
換えるようにしても良く、或いは開閉弁V1,V2
に代えて三方弁(図示せず)を用いるようにして
も良い。
Note that the bypass path for the refrigerant liquid is not limited to the one shown in the figure, and for example, a pipe (not shown) connecting the refrigerant liquid pipe 18 and the suction side of the solution pump 14 of the dilution tube 15, or a bypass path for directing the condensed refrigerant liquid to the solution reservoir 24. It may be replaced with a pipe (as shown in the figure) or a combination of these pipes, and the circulation cycle switching mechanism is not limited to that shown in the figure. The opening and closing of the on-off valves V 1 , V 2 and V 3 may be switched by a signal from a sensing detector (not shown), or the on-off valves V 1 , V 2 may be switched between opening and closing.
A three-way valve (not shown) may be used instead.

尚亦、図示のように気泡ポンプ8より冷媒液を
揚液する吸収ヒートポンプにあつては、凝縮器4
と蒸発器6との圧力差が小さくなるボイラー運転
時には、気泡ポンプ8の揚液力が低下して冷媒液
の流れが著しく低下する結果、凝縮器4内及び冷
媒液溜め7内に冷媒液が滞留し、循環吸収液が次
第に過濃縮となつて結晶化しやすくなるので、冷
媒バイパス路を設けることが特に有用である。
Furthermore, in the case of an absorption heat pump that pumps refrigerant liquid from a bubble pump 8 as shown in the figure, the condenser 4
During boiler operation, when the pressure difference between the air bubble pump 8 and the evaporator 6 becomes smaller, the liquid pumping power of the bubble pump 8 decreases and the flow of the refrigerant liquid decreases significantly. It is particularly useful to provide a refrigerant bypass path because the circulating absorbent liquid becomes increasingly overconcentrated and tends to crystallize.

一方、斯る構成の吸収ヒートポンプにおいて
は、蒸発器6へ供給される熱源流体のエネルギー
が十分に存するときは、言い代えれば熱源流体の
温度及び流量が設定値より大なるときは、前記検
出器Sの信号により開閉弁V1,V3が閉じられ、
開閉弁V2が開かれ、被加熱流体が吸収器10の
冷媒吸収作用による放熱と凝縮器5の冷媒凝縮作
用による放熱とで昇温される所謂ヒートポンプ運
転が行なわれるのである。尚、熱源流体の設定温
度或いは設定流量は吸収ヒートポンプの仕様に応
じて適宜決められる。前記検出器Sは熱源流体の
温度と流量の両方を感知するものを用いても良
い。
On the other hand, in the absorption heat pump having such a configuration, when there is sufficient energy in the heat source fluid supplied to the evaporator 6, in other words, when the temperature and flow rate of the heat source fluid are higher than the set values, the detector The on-off valves V 1 and V 3 are closed by the signal S,
The on-off valve V2 is opened, and a so-called heat pump operation is performed in which the temperature of the fluid to be heated is raised by heat radiation due to the refrigerant absorption action of the absorber 10 and heat radiation due to the refrigerant condensation action of the condenser 5. Note that the set temperature or set flow rate of the heat source fluid is appropriately determined according to the specifications of the absorption heat pump. The detector S may be one that senses both the temperature and flow rate of the heat source fluid.

尚、吸収液の循環系のいずれかの箇所で結晶を
生じて発生器1での空焚きや溶液ポンプ14のロ
ツク等異常が生じた際には前記開閉弁V1,V2
V3を開いて吸収液の稀釈を行なうことが好まし
い。また吸収ヒートポンプの運転休止に先だつて
前記開閉弁V1,V2,V3を開いて所謂吸収液稀釈
運転を行なうことが望ましい。
In addition, in the event that an abnormality occurs such as dry firing in the generator 1 or locking of the solution pump 14 due to crystal formation in any part of the absorption liquid circulation system, the on-off valves V 1 , V 2 ,
It is preferable to dilute the absorption liquid by opening V3 . Furthermore, it is desirable to open the on-off valves V 1 , V 2 , and V 3 to perform a so-called absorption liquid dilution operation prior to stopping operation of the absorption heat pump.

(ホ) 発明の効果 以上のように、本発明吸収ヒートポンプは、蒸
発器に収納した熱源管内を流通する熱源流体が、
設定温度、設定流量を越え、そのエネルギーが十
分に存するときには効率の良い所謂吸収ヒートポ
ンプ運転を行なつて被加熱流体を昇温し、熱源流
体が設定温度若しくは設定流量以下になると冷媒
液、及び吸収液がそれぞれ冷媒バイパス路、及び
溶液バイパス路を流れるようにして所謂吸収ヒー
トポンプ運転からボイラー運転へ移行せしめるも
のであるから、被加熱流体から熱源流体への逆放
熱現象、或いは冷媒の凍結、吸収液の結晶等の弊
害が生じるのを未然に防止しつつ被加熱流体を安
全かつ安定的に昇温できる効果を奏するものであ
る。
(e) Effects of the invention As described above, in the absorption heat pump of the present invention, the heat source fluid flowing through the heat source tube housed in the evaporator is
When the set temperature and flow rate are exceeded and there is sufficient energy, efficient so-called absorption heat pump operation is performed to raise the temperature of the heated fluid, and when the heat source fluid falls below the set temperature or flow rate, the refrigerant liquid and absorption Since the liquid flows through the refrigerant bypass path and the solution bypass path to transition from so-called absorption heat pump operation to boiler operation, there may be a reverse heat radiation phenomenon from the heated fluid to the heat source fluid, freezing of the refrigerant, or absorption liquid This has the effect of safely and stably raising the temperature of the fluid to be heated while preventing the occurrence of harmful effects such as crystals.

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

図面は本発明の一実施例を示した回路構成概略
説明図である。 1……発生器、4……凝縮器、5……被加熱
管、6……蒸発器、8……気泡ポンプ、9……熱
源管、10……吸収器、11……溶液熱交換器、
21……溶液バイパス管、23……冷媒バイパス
管、S……検出器、V1,V2,V3……開閉弁。
The drawing is a schematic explanatory diagram of a circuit configuration showing an embodiment of the present invention. 1... Generator, 4... Condenser, 5... Heated tube, 6... Evaporator, 8... Bubble pump, 9... Heat source tube, 10... Absorber, 11... Solution heat exchanger ,
21...Solution bypass pipe, 23...Refrigerant bypass pipe, S...Detector, V1 , V2 , V3 ...Opening/closing valve.

Claims (1)

【特許請求の範囲】[Claims] 1 発生器、凝縮器、蒸発器、吸収器及び溶液熱
交換器を配管接続して冷媒と吸収液の循環サイク
ルを形成し、吸収器及び凝縮器に収納した被加熱
管内の被過熱流体を昇温する吸収ヒートポンプに
おいて、吸収器と溶液熱交換器との間の吸収液の
経路に設けられ吸収器の被加熱管を側路する溶液
バイパス路と、蒸発器の冷媒液溜め、あるいは凝
縮器と蒸発器との間の冷媒液の経路に設けられ蒸
発器に収納した熱源管を側路する冷媒バイパス路
と、熱源管内を流通する熱源流体が設定温度若し
くは設定流量以下になつた場合、溶液バイパス路
及び冷媒バイパス路に吸収液及び冷媒液を流す機
構とを備えたことを特徴とする吸収ヒートポン
プ。
1 A generator, condenser, evaporator, absorber, and solution heat exchanger are connected via piping to form a circulation cycle of refrigerant and absorption liquid, and the superheated fluid in the heated pipes housed in the absorber and condenser is elevated. In an absorption heat pump that heats up, there is a solution bypass path that is provided in the absorption liquid path between the absorber and the solution heat exchanger and bypasses the heated tube of the absorber, and a refrigerant liquid reservoir of the evaporator or a condenser. A refrigerant bypass path is provided in the refrigerant liquid path between the evaporator and bypasses the heat source tube housed in the evaporator, and a solution bypass path is provided when the heat source fluid flowing in the heat source tube falls below the set temperature or flow rate. An absorption heat pump characterized by comprising a mechanism for flowing an absorption liquid and a refrigerant liquid into a passage and a refrigerant bypass passage.
JP20137782A 1982-11-16 1982-11-16 Absorption heat pump Granted JPS5993157A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20137782A JPS5993157A (en) 1982-11-16 1982-11-16 Absorption heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20137782A JPS5993157A (en) 1982-11-16 1982-11-16 Absorption heat pump

Publications (2)

Publication Number Publication Date
JPS5993157A JPS5993157A (en) 1984-05-29
JPH046857B2 true JPH046857B2 (en) 1992-02-07

Family

ID=16440059

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20137782A Granted JPS5993157A (en) 1982-11-16 1982-11-16 Absorption heat pump

Country Status (1)

Country Link
JP (1) JPS5993157A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60263057A (en) * 1984-06-11 1985-12-26 株式会社日立製作所 Absorption type cold and hot water machine

Also Published As

Publication number Publication date
JPS5993157A (en) 1984-05-29

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