JPS5993157A - Absorption heat pump - Google Patents

Absorption heat pump

Info

Publication number
JPS5993157A
JPS5993157A JP20137782A JP20137782A JPS5993157A JP S5993157 A JPS5993157 A JP S5993157A JP 20137782 A JP20137782 A JP 20137782A JP 20137782 A JP20137782 A JP 20137782A JP S5993157 A JPS5993157 A JP S5993157A
Authority
JP
Japan
Prior art keywords
refrigerant
heat source
absorption
liquid
heated
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.)
Granted
Application number
JP20137782A
Other languages
Japanese (ja)
Other versions
JPH046857B2 (en
Inventor
三男 中野
大塚 慶一
西田 一孝
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Electric Co Ltd
Sanyo Denki 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 Tokyo Sanyo Electric Co Ltd, Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo 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)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (イ)発明の技術分野 本発明は吸収冷凍ザ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1−る吸収ヒート
ポンプの改良に門−1ろ。
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 on the heat radiation side of an absorption/refrigeration cycle, that is, in an absorber and a condenser, to raise the temperature of a heated fluid such as hot water. -1ro.

(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(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−甲が不足
1−ると蒸発器での冷媒気化作用が不十分どなり、極ψ
;M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(
なっ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J−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間(1αがある
。このように、従来の此種吸収ヒートポンプにお(・で
は、蒸発器に供給する熱源流体の温度若しくけ流量が低
下し過ぎろと安全かつ安定的に被加熱流体を昇温できな
いと(・5問題点を有するものであった。
(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 are driven by energy output, 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 is efficient (it has the advantage of being able to raise the temperature of the heated fluid, but the temperature of the heat source fluid supplied to the evaporator may become too low or the supply of heat source fluid may be insufficient). 1-, the refrigerant vaporization effect in the evaporator is insufficient and the pole ψ
; In the case of
As a result, the refrigerant vapor moves from the absorber to the evaporator, causing a phenomenon of condensation in the evaporator, that is, a reverse heat radiation phenomenon from the heated fluid to the heat source fluid. When the temperature of the heating fluid is low and reverse heat radiation does not occur, crystallization of the absorption liquid and freezing of the refrigerant occur (1α). If the temperature of the heat source fluid supplied to the device or the flow rate of the heat source fluid decreases too much, the temperature of the heated fluid cannot be raised safely and stably (5 problems).

(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、+lt挿吸収ヒートポン
プにおいて、蒸発器に供給される熱源流体が設定温度若
1〜(は設定流量以下とl、仁つlこ1橢含、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、夫々熱源管、被加熱管
を4ft、!回路するように循環せしめろ切換え手段を
採ることにより、前iボ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-mentioned problems, the present invention provides a +lt absorption heat pump in which the heat source fluid supplied to the evaporator is at a set temperature of 1 to 1 (where l is below the set flow rate). The refrigerant liquid that is sprayed on the heat source tubes housed in the evaporator and the absorption liquid that is sprayed on the heated tubes housed in the absorber connect the heat source tubes and the heated tubes in a 4ft circuit, respectively. By adopting this circulation switching means, the refrigerant flowing from the generator to the condenser can be prevented from occurring, such as the reverse heat dissipation phenomenon described above or the crystallization of the absorption liquid and freezing of the refrigerant. 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 steam.

に)実施例 図面は本発明の一実施例を示した概略措成ジ1で、(1
)は燃焼バーナー(2)を備え、稀液から冷illを加
熱外!’lfしてWjl!l液に再生する発生器、(3
)は発生器(1)からθ)気ン(蜀を41′〜液と冷媒
蒸気とに分しする分離器、「4)は分離器(3)からの
冷媒蒸気を器内に収納1.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(1入濃液
管(13)、溶液ポンプ(14)を有する稀液管(15
)、凝縮伶媒液を包、泡ポンプ(8)内に通した後冷媒
分散器(1日)へ導(冷媒液流下管(1η、冷媒液溜め
(刀の冷媒液を気泡ポンプ(8)に導(冷媒液管(18
)、気泡ポンプ(8)により冷媒液を冷媒分散器(It
’、IK送る冷媒液−上昇前0!′I)及び冷媒蒸気導
管(2t11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っている。
(1) Embodiment drawings are schematic diagrams showing one embodiment of the present invention.
) is equipped with a combustion burner ( 2 ) and heats cold ill from dilute liquid outside! 'lf and wjl! Generator for regenerating liquid, (3
) is a separator that separates θ) air from the generator (1) into liquid and refrigerant vapor. The condenser (6) cools and condenses the fluid to be heated in the heated tube (5), and the condenser (6) cools and condenses the fluid in the heated tube (5). The evaporator (10) distributes the concentrated liquid from the separator (3) to the heated tube (5) housed in the vessel to vaporize it by circulating it into the heat source tube (9). The absorber (11) is a solution heat exchanger that absorbs vaporized refrigerant into a concentrated liquid while being cooled by a heating fluid. Liquid pipe (15
), the condensed refrigerant liquid is passed through the bubble pump (8), and then guided to the refrigerant distributor (1 day) (the refrigerant liquid down pipe (1η), the refrigerant liquid is passed through the bubble pump (8) (Refrigerant liquid pipe (18)
), the bubble pump (8) transfers the refrigerant liquid to the refrigerant disperser (It
', Refrigerant liquid sent by IK - 0 before rising! 'I) and the refrigerant vapor conduit (2t11) to form a circulation cycle of refrigerant and absorption liquid.

(21)は、前記被加熱管(5)に11(布さ)L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・\接続さ第1ている溶ソ
f叉バイパス管で、導管には開閉弁(■、)が備えCあ
り、また、メ、゛4液の分岐点から溶液分散器(肋へ至
る途中の濃液管(13)にも開閉弁(■、)が備えであ
る。(2:(l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(2イ)とを接続してい
る冷媒バイパス管で、導管には開閉弁(■3)が備えで
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(■、)、(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(■1)、(■3)を閉じ、開閉
弁(V2)を開くよ51/C切換え可能となっている。
(21) is branched from the concentrated liquid pipe (13) and placed at the bottom of the absorber (10) so that the concentrated liquid flowing into the heated pipe (5) bypasses the heated pipe.・\The first molten pipe is connected to the bypass pipe, and the conduit is equipped with an on-off valve (■,). The concentrated liquid pipe (13) is also equipped with an on-off valve (■,). This is a refrigerant bypass pipe that connects the refrigerant liquid reservoir (7) and the solution reservoir (2a) so that the refrigerant reservoir (7) and the solution reservoir (2a) are connected to each other, and the conduit is equipped with an on-off valve (■3). (S) is the heat source pipe (9) Temperature detector (
or a flow rate detector), when the heat source fluid is below the set temperature (or set flow rate) according to the signal of the detector, the on-off valves (■,), (v3) are opened and the on-off valve (v2) is closed. ,
The heat source fluid is higher than the set temperature (or higher than the set flow rate)
At this time, the switching valve 51/C can be switched to close the on-off valves (1) and (3) and open the on-off valve (V2).

斯る構成の吸収ヒートポンプにおいては、蒸発器(Gl
へ供給されろ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c液が溶液バイパス管(2
1)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(2禿を流通し、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
+1され、被加熱管(5)内を?iir、浦する被加熱
流体は凝縮器(5)内で発生器(,1)から分+号!#
器(3)を経て流入する冷媒蒸気の熱により!1渦され
るのである。
In an absorption heat pump with such a configuration, the evaporator (Gl
The energy of the heat source fluid supplied to the
When the refrigerant vaporization effect in the evaporator (6) becomes insufficient, the c liquid that has been sprayed on the heated tube (5) flows into the solution bypass tube (2).
The refrigerant liquid that had been distributed through the heat source pipe (9) while flowing through the refrigerant bypass pipe (2) passes through the refrigerant bypass pipe (2) and undergoes refrigerant vaporization in the evaporator (6) and refrigerant absorption in the absorber (10). is stopped, and the heated fluid flowing inside the heated tube (5) is heated from the generator (,1) in the condenser (5).
Due to the heat of the refrigerant vapor flowing through the container (3)! One vortex is created.

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)の冷媒蒸気用より
高くなり冷媒蒸気が吸収器(1(1)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ろ所
謂逆放熱現象が未然に防止されろよう、冷媒と吸収液と
の循環サイクルが切換っ°(M’Jわばボイラー運転に
移行するものである。
That is, the saturated vapor pressure of the absorption liquid sprayed onto the heated pipe (5) of the absorber (10) is higher than that of the refrigerant vapor of the evaporator (6), and the refrigerant vapor evaporates from the absorber (1 (1) side). Vessel (6
) side and condenses in the heat source tube (9) of the evaporator.In other words, the heat of the heated fluid is released to the heat source fluid, so that the so-called reverse heat radiation phenomenon can be prevented. The circulation cycle is switched (M'J, in other words, shifts to boiler operation).

また、熱源流体供給温度が低下12過ぎたり、或いは供
給■°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(なってもlrお吸収5flO+での
冷媒吸収作用を継続すると、蒸発器(6)及び吸収器0
0)白玉が低下して冷媒の凍結成いは熱源流体の凍結延
い℃は吸収液の結晶等の弊害を生じる原因となるが、本
発明吸収冷凍四においては、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F発器(6)の冷媒気化作用を停止−[るので、これ
ら弊害も未然に防止される。
In addition, if the heat source fluid supply temperature drops too much or the supply ■° is too small, the temperature of the heated fluid flowing into the absorber (10) is low (even if the temperature of the heated fluid flowing into the absorber (10) is low, the refrigerant absorption effect at lr absorption 5flO+ continues. Then, the evaporator (6) and absorber 0
0) When the white beads drop and the refrigerant freezes, the heat source fluid freezes and extends.Celsius can cause adverse effects such as crystallization of the absorption liquid, but in absorption refrigeration 4 of the present invention, the supply temperature or Since the refrigerant absorption action of the absorber (10) and the refrigerant vaporization action of the F generator (6) are stopped before the amount decreases too much, these adverse effects are also prevented.

更に、冷p%液溜め(7)の冷媒液が溶液調め(24)
の吸収液に混入さ旧て発生器(1)にσ流される吸収液
濃度が5す(/、C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別器
するためのエネルギーを節約できろ利点もある。
Furthermore, the refrigerant liquid in the cold p% liquid reservoir (7) is prepared as a solution (24).
Since the concentration of the absorption liquid mixed in the absorption liquid and flowing into the generator (1) is 5/C, the boiling temperature of the absorption liquid in the generator becomes lower, and as a result, when the boiler is operated, the absorption liquid It also has the advantage of saving energy for separate equipment.

尚、冷媒液のバイパス路は、図示しブ、−ものに限1っ
ず、例えば冷媒液管(国と稲液管(151(7)σf液
ポンプ(141吸込側とを接続1−る管(図示せず)や
、・憂シ縮冷媒液ケ直吸溶液溜め(24)に導(管(図
示せず)或いOよこれも管の組み合わせ等で代用しても
良く、よフ、二、循J1i ’リ−fクルtjlJ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(I O+oIL人温度を感知″[
る検出器(図示せず)との1d号で開閉弁(V、)、(
V2)及び(V、 ) 0) 1jil閉を切換えるよ
うにしても良(、或いは開閉弁(V、)、(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 refrigerant liquid bypass path is not limited to those shown in the figure, but includes, for example, a refrigerant liquid pipe (151 (7)) and a pipe connecting the σf liquid pump (141 suction side). (not shown), - The condensed refrigerant liquid is led directly to the suction solution reservoir (24) (pipe (not shown), or O. This may also be replaced by a combination of pipes, etc. 2. The circulation mechanism is not limited to the one shown, for example, the detector (9) and the absorber for the heated fluid (I O+OIL detects human temperature).
On-off valve (V, ), (
V2) and (V, ) 0) 1jil close may be switched (or a three-way valve (not shown) may be used in place of the on-off valves (V, ) and (v2).

尚亦、図示のように気泡ポンプ(8)より冷媒液を揚液
1−る吸収ヒートポンプにk〉ってけ1.%+iF縮に
:朝4)と蒸発器(6)との圧力差が小さく7.「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(力内に冷媒液が7111留し、循環吸
収液が次第に過濃縮となっ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11テに有用である。
In addition, as shown in the figure, transfer the refrigerant liquid from the bubble pump (8) to an absorption heat pump that pumps liquid 1. %+iF contraction: Morning 4) and evaporator (6) pressure difference is small 7. When the boiler is operated, the pumping power of the bubble pump (8) decreases and the flow of the refrigerant drops significantly, resulting in 7111 points of refrigerant remaining in the condenser (4) and the refrigerant reservoir The circulating absorption liquid gradually becomes overconcentrated and tends to crystallize.
Providing a refrigerant bypass path is useful in 11 cases.

一方、斯る構成の吸収ヒートポンプにおいては。On the other hand, in an absorption heat pump having such a configuration.

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
が設定値より犬なるときは、前記検出器(S)の信号に
より開閉弁(V、)、(■3)が閉じられ、開閉弁(V
、)が開かれ、被加il(流体が吸収器(10)の冷媒
吸収作用による放熱と凝縮器(5)の冷媒吸収作用によ
る放熱とで昇温されろ所謂ヒートポンプ運転が行なわれ
るのである。1)“6.熱源流体の設定湿度或いは設定
温情は吸収ヒ l・ポンプの仕様に応じて適宜法められ
ろ。前記イへ小器(Sl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。
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 on-off valve ( V, ), (■3) are closed, and the on-off valve (V
, ) are opened and the temperature of the applied fluid (fluid is raised by the heat radiated by the refrigerant absorption action of the absorber (10) and the heat radiated by the refrigerant absorption action of the condenser (5), so-called heat pump operation is performed. 1) 6. The set humidity or temperature of the heat source fluid should be determined as appropriate according to the specifications of the absorption pump. You may also use

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(1イ)σ)ロック
等異常が生じた際には前記開閉弁(V、)、(■2)、
(■リ 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って前記開閉
弁(V、)、(V2)、(V3)を開いて所141ff
吸収液稀釈運転を行なうことが望ましい。
In addition, if an abnormality occurs such as dry firing in the generator (1) or locking of the solution pump (1a) due to crystal formation in any part of the absorption liquid circulation system, the on-off valves (V, ), (■2),
(■ It is preferable to dilute the absorption liquid by opening 141ff.) Also, before stopping the operation of the absorption heat pump, open the on-off valves (V, ), (V2), and (V3).
It is desirable to perform an absorption liquid dilution operation.

(ホ)発明の効果 以−ヒのように、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
定流ボ: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って被加
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1.Cろと熱源管に散布される冷媒液が肢管を側
路すると共に被加熱管に散布される吸収液が肢管を側路
するように冷媒と吸収液の循環ザイクルを切換えて所謂
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−\の逆数熱
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 in (H) above, the absorption heat pump of the present invention is effective when the heat source fluid flowing in the heat source tube housed in the evaporator exceeds the set temperature and set flow rate and has sufficient energy. The temperature of the heated fluid is raised by performing efficient so-called absorption heat pump operation, and the heat source fluid is lowered to below the set temperature or set flow rate.1. A so-called absorption heat pump is created by switching the circulation cycle of the refrigerant and absorption liquid so that the refrigerant liquid sprayed on the C filter and the heat source tube bypasses the limb pipes, and the absorption liquid sprayed on the heated tube bypasses the limb pipes. Since it allows the transition from operation to boiler operation, it is possible to transfer the heated fluid while preventing adverse effects such as the reciprocal thermal phenomenon from the heated fluid to the heat source fluid, freezing of the refrigerant, and crystallization of the absorption liquid. This has the effect of raising the temperature safely and stably.

【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、θ0)・・・吸収
器、 (団・・・溶液熱父換器、 (21)・・・溶6
にバイパス管、 (23)・・・冷媒バイパス管、 (
S)・・・検出器、(■、)、(v2)、(■、)・・
・開閉プp。 出願人 三洋1E4jJ株式会社 外1名代理人 弁理
士  佐 野 静 夫
The drawing is a schematic explanatory diagram of a circuit configuration showing one embodiment of the present invention.
It is. (1)...generator, (4)...condenser, (5)
... Heated tube, (6) ... Evaporator, (8) ...
Bubble pump, (9)... Heat source tube, θ0)... Absorber, (Group... Solution heat exchanger, (21)... Melt 6
bypass pipe, (23)...refrigerant bypass pipe, (
S)...Detector, (■,), (v2), (■,)...
・Opening/closing. Applicant Sanyo 1E4JJ Co., Ltd. and 1 other agent Patent attorney Shizuo Sano

Claims (1)

【特許請求の範囲】[Claims] (11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11g液の循環ザイクルを形
成し、吸収器及び凝縮器に収納した被加熱管内の被加熱
流体を昇温する吸収ヒートポンプにおいて、前記被加熱
管に散布される吸収液が該被加熱管を側路する溶液バイ
パス路な設けろと共に蒸発器に収納した熱源管に散布さ
れる冷媒液が該熱源管を側路する冷媒バイパス路を設け
、前記熱源管内を流通する熱源流体が設定温度若しくは
設定流量以下となった場合、溶液バイパス路及び冷媒バ
イパス路を介して冷媒と吸収液の循環ザイクルを切換え
る磯構を備えたことを特徴とする吸収ヒートポンプ。
(The 11 generator, condenser, evaporator, absorber, and solution heat exchanger are connected via piping to form a circulation cycle of refrigerant and absorbed 11 g liquid, and the heated fluid in the heated tubes housed in the absorber and condenser is In an absorption heat pump that raises the temperature of a heat source tube, a solution bypass path is provided so that the absorption liquid sprayed on the heated tube bypasses the heated tube, and the refrigerant liquid sprayed on the heat source tube housed in the evaporator flows through the heat source tube. A refrigerant bypass path is provided to bypass the heat source, and when the heat source fluid flowing in the heat source tube becomes lower than a set temperature or a set flow rate, the circulation cycle of the refrigerant and absorption liquid is switched via the solution bypass path and the refrigerant bypass path. An absorption heat pump characterized by having a structure.
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 true JPS5993157A (en) 1984-05-29
JPH046857B2 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)

Cited By (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

Cited By (2)

* 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
JPH0414262B2 (en) * 1984-06-11 1992-03-12 Hitachi Ltd

Also Published As

Publication number Publication date
JPH046857B2 (en) 1992-02-07

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