JP2759367B2 - Refrigerant system in absorption heat pump air conditioner - Google Patents
Refrigerant system in absorption heat pump air conditionerInfo
- Publication number
- JP2759367B2 JP2759367B2 JP1340183A JP34018389A JP2759367B2 JP 2759367 B2 JP2759367 B2 JP 2759367B2 JP 1340183 A JP1340183 A JP 1340183A JP 34018389 A JP34018389 A JP 34018389A JP 2759367 B2 JP2759367 B2 JP 2759367B2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- path
- absorber
- valve
- refrigerant
- 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 - Lifetime
Links
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- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は吸収式ヒートポンプ冷暖房装置に於ける冷媒
系統に関するものである。Description: TECHNICAL FIELD The present invention relates to a refrigerant system in an absorption heat pump cooling and heating device.
(従来の技術) 吸収式サイクルは各種冷温水装置に於いて広く実用に
供されているが、ヒートポンプ冷暖房装置、特に空冷式
ヒートポンプ冷暖房装置としては殆ど実用化されていな
い。この吸収式サイクルを用いて空冷式ヒートポンプ冷
暖房装置を構成する場合、冷房運転に於いては蒸発器か
ら吸熱するので、室内側熱交換器を蒸発器として動作さ
せれば良く、この点に関しては室内側熱交換器への冷媒
配管は2管で良いが、暖房運転に於いては凝縮器と吸収
器の両方に於いて発生する熱を放熱するので、通常考え
られる構成では、室内側熱交換器はこれらの動作をさせ
る2つの熱交換器が必要となり、従って室内側熱交換器
への冷媒配管は4管が必要となり、結局室内側熱交換器
への冷媒配管は四管式となってしまう。(Prior Art) Absorption-type cycles are widely used in various types of cooling / heating water devices, but are hardly practically used as heat pump cooling / heating devices, particularly air-cooling heat pump cooling / heating devices. When an air-cooled heat pump air conditioner is configured using this absorption cycle, heat is absorbed from the evaporator during the cooling operation, so that the indoor heat exchanger may be operated as an evaporator. The refrigerant pipe to the inner heat exchanger may be two pipes. However, in the heating operation, heat generated in both the condenser and the absorber is radiated. Requires two heat exchangers to perform these operations, and therefore requires four pipes for the refrigerant pipe to the indoor heat exchanger, and eventually the refrigerant pipe to the indoor heat exchanger becomes a four-pipe type. .
(発明が解決しようとする課題) 四管式の冷媒配管では、配管、施工が煩雑となり、所
要スペースも大きくなってしまうという課題がある。(Problems to be Solved by the Invention) In a four-tube refrigerant pipe, there is a problem that piping and construction become complicated and a required space becomes large.
本発明は以上の課題を解決することを目的とするもの
である。An object of the present invention is to solve the above problems.
(課題を解決するための手段) 上記の課題を解決するための本発明の構成を、その実
施例を表わした図につき説明すると、本発明の吸収式ヒ
ートポンプ冷暖房装置に於ける冷媒系統は、室内熱交換
器1と室外熱交換器2を設け、該室内熱交換器1と室外
熱交換器2の一端側の夫々を四方弁3の各選択口3a,3b
に接続すると共に、室内熱交換器1の他端側に膨張弁4a
と逆止弁5aの並列経路6aの一端側を、そして室外熱交換
器2の他端側に膨張弁4bと開閉弁5bの並列経路6bの一端
側を接続し、これらの並列経路6a,6bの他端側を相互に
接続すると共に、吸収サイクルを構成する再生器7から
の高圧冷媒蒸気経路8及び吸収器9に至る低圧冷媒蒸気
経路10の夫々を前記四方弁3の各共通口3i,3oに接続
し、前記吸収器9との熱交換部11を設けた吸収器放熱経
路12を構成して、その上流側を前記並列経路6bの他端側
に接続すると共に、下流側を三方弁13の共通口13cに接
続し、該三方弁13の一方の選択口13aを前記室外熱交換
器2の一端側に接続すると共に、他方の選択口13bを逆
止弁14を経て前記室内熱交換器1の一端側に接続し、ま
た吸収器放熱経路12に於いて、吸収器9との熱交換部11
の上流側に冷媒タンク15と、この冷媒タンク15からの経
路を共通口16cに接続した三方弁16とを設け、該三方弁1
6の一方の選択口16aは前記熱交換部11側に接続すると共
に、他方の線他口16bは吸収式サイクルを構成する溶液
タンク17に逆止弁18を介して接続して冷媒量調節機構19
を構成したものである。(Means for Solving the Problems) The structure of the present invention for solving the above problems will be described with reference to the drawings showing the embodiments. The refrigerant system in the absorption heat pump cooling and heating apparatus of the present invention is an indoor type. A heat exchanger 1 and an outdoor heat exchanger 2 are provided, and one end of each of the indoor heat exchanger 1 and the outdoor heat exchanger 2 is connected to each of the selection ports 3a and 3b of the four-way valve 3.
And an expansion valve 4a at the other end of the indoor heat exchanger 1.
And one end of the parallel path 6a of the check valve 5a, and one end of the parallel path 6b of the expansion valve 4b and the on-off valve 5b to the other end of the outdoor heat exchanger 2. These parallel paths 6a, 6b Are connected to each other, and the high-pressure refrigerant vapor path 8 from the regenerator 7 and the low-pressure refrigerant vapor path 10 to the absorber 9 constituting the absorption cycle are connected to the common ports 3i, 3o, an absorber heat-dissipating path 12 provided with a heat exchange section 11 with the absorber 9 is connected, the upstream side is connected to the other end of the parallel path 6b, and the downstream side is a three-way valve. 13, the one-way selection port 13a of the three-way valve 13 is connected to one end of the outdoor heat exchanger 2, and the other selection port 13b is connected to the indoor heat exchange through a check valve 14. Connected to one end of the absorber 1, and a heat exchange section 11 with the absorber 9 in the absorber radiation path 12.
A refrigerant tank 15 and a three-way valve 16 having a path from the refrigerant tank 15 connected to a common port 16c are provided upstream of the three-way valve 1.
6, one selection port 16a is connected to the heat exchange unit 11 side, and the other wire port 16b is connected to a solution tank 17 constituting an absorption cycle via a check valve 18 to control the refrigerant amount. 19
It is what constituted.
(作用及び実施例) 次に、上記の本発明の作用を、実施例に対応する第1
図、第2図を参照して説明する。尚、第2図が本発明の
全体構成に対応する実施例を示す系統図であり、第1図
は冷房、暖房及び除霜運転を説明するために、全体構成
から冷媒量調節機構19に係る構成を便宜的に省略した系
統図である。(Operation and Example) Next, the operation of the present invention described above will be described with reference to the first example corresponding to the example.
This will be described with reference to FIGS. FIG. 2 is a system diagram showing an embodiment corresponding to the entire configuration of the present invention, and FIG. 1 is a diagram showing a cooling amount adjusting mechanism 19 for explaining cooling, heating and defrosting operations. It is the system diagram which omitted the structure for convenience.
まず、冷房を行う場合には、第1図(a)に示すよう
に、四方弁3は共通口3iを選択口3bを介して室外熱交換
器2と連通させると共に、共通口3oを選択口3aを介して
室内熱交換器1と連通させる。一方、図中ハッチングで
示したように、吸収器放熱経路12の三方弁13は、共通口
13cと選択口13aを連通させ、また開閉弁5bは開とするよ
うに操作する。First, when performing cooling, as shown in FIG. 1 (a), the four-way valve 3 allows the common port 3i to communicate with the outdoor heat exchanger 2 via the selection port 3b, and connects the common port 3o to the selection port. It communicates with the indoor heat exchanger 1 via 3a. On the other hand, as indicated by hatching in the figure, the three-way valve 13 of the absorber heat release path 12 has a common port.
The selection port 13a communicates with the selection port 13c, and the on-off valve 5b is operated to be opened.
しかして再生器7に於いて適宜の加熱源により加熱さ
れて発生した高温高圧の冷媒蒸気は、高圧冷媒蒸気経路
8を通り、四方弁3を経て室外熱交換器2に至り、ここ
で外気に放熱して凝縮する。次いで冷媒は開閉弁5bを経
て室内側との経路20bを流れ、室内機R内の膨張弁4aを
経て減圧されて室内熱交換器1に至る。そして冷媒は該
室内熱交換器1に於いて蒸発して室内の熱を奪い、室内
の冷房を行うことができる。このようにして室内の熱を
奪った低圧の冷媒蒸気は、室内側との経路20aを流れ、
四方弁3を経て低圧蒸気経路10に還流し、再生器7から
吸収器9に至る濃溶液経路21の濃溶液と合流して吸収器
9に至り、ここで濃溶液に吸収された後に溶液タンク17
に流入し、次いで希溶液経路22を経て再生器7に還流す
る。Thus, the high-temperature and high-pressure refrigerant vapor generated by being heated by an appropriate heating source in the regenerator 7 passes through the high-pressure refrigerant vapor path 8, reaches the outdoor heat exchanger 2 through the four-way valve 3, and is converted to outside air. Radiates and condenses. Next, the refrigerant flows through the path 20b to the indoor side via the on-off valve 5b, is decompressed via the expansion valve 4a in the indoor unit R, and reaches the indoor heat exchanger 1. Then, the refrigerant evaporates in the indoor heat exchanger 1 to remove indoor heat and cool the room. In this way, the low-pressure refrigerant vapor that robbed the indoor heat flows through the path 20a with the indoor side,
After returning to the low-pressure steam path 10 through the four-way valve 3, the concentrated solution in the concentrated solution path 21 from the regenerator 7 to the absorber 9 merges with the concentrated solution to reach the absorber 9, where the solution is absorbed by the concentrated solution, 17
And then return to the regenerator 7 via the dilute solution path 22.
一方、吸収器放熱経路12を流れる冷媒は熱交換部11に
於いて、吸収器9で発生する吸収熱を奪って蒸発し、三
方弁13から経路24を経て前記再生器7からの冷媒蒸気と
合流して室外熱交換器2に至り、ここで凝縮して放熱さ
れる。こうして、室外熱交換器2から開閉弁5bを経て並
列経路6bの他端側に至った冷媒は、一部が吸収器放熱経
路12に分岐して流入し、循環する。On the other hand, the refrigerant flowing through the absorber radiation path 12 takes away the absorption heat generated in the absorber 9 and evaporates in the heat exchange section 11, and passes through the three-way valve 13 through the path 24 to the refrigerant vapor from the regenerator 7. It merges and reaches the outdoor heat exchanger 2, where it is condensed and radiated. In this manner, the refrigerant that has reached the other end of the parallel path 6b from the outdoor heat exchanger 2 via the on-off valve 5b is partially branched into the absorber radiation path 12, flows in, and circulates.
以上の如くして、室内熱交換器1を蒸発器として動作
させると共に、室外熱交換器2に、再生器7からの冷媒
蒸気と吸収器9で発生する熱を奪った冷媒蒸気を合流さ
せて流入して凝縮器として動作させるので、この室外熱
交換器2は吸収器9の冷却用放熱手段を兼用し、こうし
て吸収式サイクルを利用した冷房を行うことができる。As described above, the indoor heat exchanger 1 is operated as an evaporator, and the refrigerant vapor from the regenerator 7 and the refrigerant vapor deprived of heat generated in the absorber 9 are combined with the outdoor heat exchanger 2. Since the outdoor heat exchanger 2 flows and operates as a condenser, the outdoor heat exchanger 2 also serves as a cooling radiator for the absorber 9, and thus can perform cooling using an absorption cycle.
次に暖房を行う場合には、第1図(b)に示すよう
に、四方弁3は共通口3oを選択口3bを介して室外熱交換
器2と連通させると共に、共通口3iを選択口3aを介して
室内燃交換器1と連通させる。一方、前述と同様に図中
ハッチングで示したように、吸収器放熱経路12の三方弁
13は、共通口13cと選択口13bを連通させ、また開閉弁5b
は閉とするように操作する。Next, when heating is performed, as shown in FIG. 1 (b), the four-way valve 3 connects the common port 3o to the outdoor heat exchanger 2 through the selection port 3b, and connects the common port 3i to the selection port. It communicates with the internal combustion exchanger 1 via 3a. On the other hand, as indicated by hatching in the figure, the three-way valve
13 communicates the common port 13c with the selection port 13b, and also includes an on-off valve 5b.
Is operated to be closed.
しかして再生器7に於いて発生した高温高圧の冷媒蒸
気は高圧冷媒蒸気経路8を通り、四方弁3を経て室内側
との経路20aを流れて、室内熱交換器1に至り、ここで
室内に放熱して凝縮し、暖房に供される。次いで冷媒は
逆止弁5aを経て室内側との経路20bを流れ、一部は吸収
器放熱経路12に流入すると共に残りは膨張弁4bを経て減
圧されて室外熱交換器2に至る。そして冷媒は該室外熱
交換器2に於いて蒸発して外気の熱を奪う。そして外気
の熱を奪った低圧の冷媒蒸気は、前述の冷房運転と同様
に四方弁3を経て低圧蒸気経路10を通り、冷房運転と同
様に再生器7から吸収器9に至る濃溶液経路21の濃溶液
と合流して吸収器9に至り、該濃溶液に吸収された後に
溶液タンク17に流入し、次いで希溶液経路22を経て再生
器7に還流する。Thus, the high-temperature and high-pressure refrigerant vapor generated in the regenerator 7 passes through the high-pressure refrigerant vapor path 8, flows through the four-way valve 3 and the path 20a with the indoor side, and reaches the indoor heat exchanger 1, where the indoor heat exchanger 1 The heat is released and condensed, and is provided for heating. Next, the refrigerant flows through the path 20b to the indoor side via the check valve 5a, a part of the refrigerant flows into the absorber radiation path 12, and the rest is decompressed through the expansion valve 4b and reaches the outdoor heat exchanger 2. Then, the refrigerant evaporates in the outdoor heat exchanger 2 and takes heat of the outside air. The low-pressure refrigerant vapor from which the heat of the outside air has been removed passes through the low-pressure steam path 10 via the four-way valve 3 as in the above-described cooling operation, and the concentrated solution path 21 from the regenerator 7 to the absorber 9 as in the cooling operation. And flows into the solution tank 17 after being absorbed by the concentrated solution, and then returns to the regenerator 7 via the dilute solution path 22.
一方、前述した通り、室内側との経路20bから吸収器
放熱経路12に流入した冷媒は熱交換部11に於いて、吸収
器9で発生する吸収熱を奪って蒸発し、三方弁13を経て
放熱経路25を流れ、逆止弁14を経て室内側との経路20a
に至り、前記高圧蒸気経路8から四方弁3を経て流入し
た高温高圧の冷媒蒸気と合流して室内熱交換器1に至
り、ここで放熱して室内の暖房に供される。On the other hand, as described above, the refrigerant flowing into the absorber radiation path 12 from the path 20b to the indoor side takes away the heat of absorption generated in the absorber 9 and evaporates in the heat exchange section 11, and passes through the three-way valve 13. Flowing through the heat radiation path 25, and passing through the check valve 14 to the indoor side 20a
, And merges with the high-temperature and high-pressure refrigerant vapor flowing in from the high-pressure vapor path 8 via the four-way valve 3 to reach the indoor heat exchanger 1 where heat is released and used for heating the room.
このように、再生器7からの冷媒蒸気と、吸収器9で
発生する熱を奪った冷媒蒸気を合流させて室内熱交換器
1に供給して凝縮器として動作させると共に、室外熱交
換器2を蒸発器として動作させることにより吸収式サイ
クルを利用したヒートポンプ暖房を行うことができる。As described above, the refrigerant vapor from the regenerator 7 and the refrigerant vapor deprived of heat generated in the absorber 9 are combined and supplied to the indoor heat exchanger 1 to operate as a condenser, and to operate as a condenser. By operating as an evaporator, heat pump heating using an absorption cycle can be performed.
以上の説明から明らかなように、本発明に於いては冷
房運転は勿論のこと暖房運転に於いても室内熱交換器1
への経路、即ち室内側との経路20a,20bは一対で良く、
従って室内熱交換器1への配管は二管式として構成する
ことができる。As is clear from the above description, in the present invention, the indoor heat exchanger 1 is used not only in the cooling operation but also in the heating operation.
Path, that is, the path 20a, 20b with the indoor side may be a pair,
Therefore, the pipe to the indoor heat exchanger 1 can be configured as a two-pipe type.
以上の暖房運転に於いて、室外熱交換器2に霜が発生
した場合には、開閉弁5を開とする。しかして、室内側
との経路20aを経て室内熱交換器1に至った冷媒蒸気
は、ここで一部放熱し、凝縮しながら室内側との経路20
bを経て、その一部が開閉弁5bを経て室外熱交換器2に
流れ込む。そして冷媒蒸気は、ここで凝縮し、この際の
放熱によりそれまで蒸発器として動作していた室外熱交
換器2の霜を溶かし、除去することができる。該室外熱
交換器2に於いて凝縮した冷媒は、次いで四方弁3から
低圧蒸気経路10を経て吸収式サイクルに還流する。一
方、前述した通り、室内側との経路20bから吸収器放熱
経路12に流入した冷媒は前述の暖房運転と同様に熱交換
部11に於いて、吸収器9で発生する吸収熱を奪って蒸発
し、三方弁13を経て放熱経路25を流れ、逆止弁14を経て
室内側との経路20aに至り、前記高圧蒸気経路8から四
方弁3を経て流入した高温高圧の冷媒蒸気と合流して室
内熱交換器1に至り、ここで放熱して室内の暖房に供さ
れる。In the above heating operation, when frost occurs in the outdoor heat exchanger 2, the on-off valve 5 is opened. Thus, the refrigerant vapor reaching the indoor heat exchanger 1 via the path 20a to the indoor side is partially radiated here, and condensed while passing through the path 20a to the indoor side.
After b, a part of it flows into the outdoor heat exchanger 2 via the on-off valve 5b. The refrigerant vapor is condensed here, and the heat released at this time can melt and remove the frost of the outdoor heat exchanger 2 which has been operating as an evaporator. The refrigerant condensed in the outdoor heat exchanger 2 then returns from the four-way valve 3 through the low-pressure steam path 10 to the absorption cycle. On the other hand, as described above, the refrigerant that has flowed into the absorber radiation path 12 from the path 20b to the indoor side takes away the absorption heat generated in the absorber 9 and evaporates in the heat exchange unit 11 in the same manner as in the above-described heating operation. Then, it flows through the heat radiation path 25 through the three-way valve 13, reaches the path 20 a with the indoor side through the check valve 14, and merges with the high-temperature and high-pressure refrigerant vapor flowing from the high-pressure vapor path 8 through the four-way valve 3. The heat reaches the indoor heat exchanger 1, where the heat is released and the indoor heat exchanger 1 is heated.
以上の冷房、暖房又は除霜運転に於いて、吸収器放熱
経路12を流れる冷媒の量の、全体量に対しての割合は、
本発明に係る冷媒量調節機構19により調節して適切に維
持することができる。In the above cooling, heating or defrosting operation, the ratio of the amount of the refrigerant flowing through the absorber radiation path 12 to the total amount is:
It can be adjusted and maintained appropriately by the refrigerant amount adjusting mechanism 19 according to the present invention.
即ち、暖房運転を表わした第2図(a)の状態に於い
て、吸収器放熱経路12に流入する冷媒量が過多となる場
合には、かかる冷媒量の過多に対応する冷媒タンク15内
の液面の上昇を液面計26によって検出して三方弁16を制
御し、第2図(b)に示すように共通口16cと選択口16b
を連通状態として、吸収器放熱経路12に流入した冷媒を
逆止弁18を設けた返送経路27を経て、溶液タンク17側に
返送すると共に、このようにして過多を解消した場合に
は、三方弁16を制御して再び第2図(a)に示す状態に
戻し、このようにして冷媒タンク15の液面を一定に制御
することにより、吸収器放熱経路12を流れる冷媒の量
の、全体量に対しての割合を適切に維持することができ
る。That is, in the state of FIG. 2A showing the heating operation, when the amount of the refrigerant flowing into the absorber radiation path 12 becomes excessive, the refrigerant in the refrigerant tank 15 corresponding to the excessive amount of the refrigerant. The three-way valve 16 is controlled by detecting the rise of the liquid level by the liquid level gauge 26, and the common port 16c and the selection port 16b are controlled as shown in FIG.
And the refrigerant flowing into the absorber heat radiation path 12 is returned to the solution tank 17 via the return path 27 provided with the check valve 18, and if the excess is eliminated in this way, a three-way By controlling the valve 16 again to return to the state shown in FIG. 2 (a) and controlling the liquid level of the refrigerant tank 15 to a constant level in this manner, the total amount of refrigerant flowing through the absorber radiation path 12 is reduced. The ratio to the amount can be appropriately maintained.
以上に詳細に説明した本発明は、適宜の冷媒、吸収剤
を用いた吸収式サイクルに適用することができ、以上の
説明に於ける希溶液とは冷媒が多く含まれている状態の
溶液、濃溶液とは冷媒の少ない溶液を表わすものであ
る。The present invention described in detail above can be applied to an appropriate refrigerant, an absorption cycle using an absorbent, and the dilute solution in the above description is a solution containing a large amount of refrigerant, A concentrated solution refers to a solution containing less refrigerant.
尚、図中の符号28は減圧手段、23,29はポンプ、30は
溶液熱交換器である。In the figure, reference numeral 28 denotes a pressure reducing means, 23 and 29 denote pumps, and 30 denotes a solution heat exchanger.
(発明の効果) 本発明は以上の通り、冷房運転に於いては蒸発器とし
て動作させる室内熱交換器を、暖房運転に於いては再生
器からの冷媒蒸気と、吸収器で発生する熱を奪った冷媒
とを合流させて供給して、凝縮器として動作させるの
で、冷房運転は勿論のこと暖房運転に於いても室内熱交
換器への経路、即ち室内側との経路は一対で良く、従っ
て該室内熱交換器への配管を二管式として構成すること
ができると共に、暖房を行いながらの除霜運転も可能で
あるという効果がある。更に、本発明では、以上の各運
転において、吸収器放熱経路を流れる冷媒の量の、全体
量に対する割合を、冷媒量調節機構により適切に維持す
ることができるという効果がある。(Effect of the Invention) As described above, the present invention provides an indoor heat exchanger that operates as an evaporator in the cooling operation, and a refrigerant vapor from the regenerator and the heat generated in the absorber in the heating operation. Since the taken refrigerant is combined and supplied and operated as a condenser, the path to the indoor heat exchanger in the heating operation as well as the cooling operation, that is, the path to the indoor side may be a pair, Therefore, there is an effect that the pipe to the indoor heat exchanger can be configured as a two-pipe type, and a defrosting operation while heating is also possible. Further, in the present invention, in each of the above operations, there is an effect that the ratio of the amount of the refrigerant flowing through the absorber radiation path to the total amount can be appropriately maintained by the refrigerant amount adjusting mechanism.
第1図(a)、(b)、(c)は本発明の全体構成の実
施例を、全体構成中、冷媒量調節機構の部分を便宜的に
省略した構成、動作を冷房運転、暖房運転、除霜運転に
於いて説明した系統図、第2図(a)、(b)は本発明
の全体構成の実施例を冷媒量の調節動作に於いて説明し
た系統図である。 符号1……室内熱交換器、2……室外熱交換器、3……
四方弁、4a,4b……膨張弁、5a,14,18……逆止弁、5b…
…開閉弁、6a,6b……並列経路、7……再生器、8……
高圧冷媒蒸気経路、9……吸収器、10……低圧冷媒蒸気
経路、11……熱交換部、12……吸収器放熱経路、13,16
……三方弁、15……冷媒タンク、17……溶液タンク、19
……冷媒量調節機構、20a,20b……室内側との経路、21
……濃溶液経路、22……希溶液経路、24……経路、25…
…放熱経路、23,29……ポンプ、26……液面計、27……
返送経路、28……減圧手段、30……溶液熱交換器。1 (a), 1 (b) and 1 (c) show an embodiment of the entire configuration of the present invention, in which the configuration of the entire configuration is omitted for convenience of the refrigerant amount adjusting mechanism, and the operation is a cooling operation and a heating operation. 2 (a) and 2 (b) are system diagrams illustrating an embodiment of the overall configuration of the present invention in the operation of adjusting the amount of refrigerant. Symbol 1 ... indoor heat exchanger, 2 ... outdoor heat exchanger, 3 ...
Four-way valve, 4a, 4b …… Expansion valve, 5a, 14, 18 …… Check valve, 5b…
... On-off valve, 6a, 6b ... Parallel path, 7 ... Regenerator, 8 ...
High-pressure refrigerant vapor path, 9: absorber, 10: low-pressure refrigerant vapor path, 11: heat exchange unit, 12: absorber radiation path, 13, 16
... three-way valve, 15 ... refrigerant tank, 17 ... solution tank, 19
…… Refrigerant amount adjustment mechanism, 20a, 20b …… Route to indoor side, 21
… Concentrated solution route, 22… dilute solution route, 24… route, 25…
… Radiation path, 23,29… pump, 26 …… level gauge, 27 ……
Return path, 28 ... decompression means, 30 ... solution heat exchanger.
Claims (1)
内熱交換器と室外熱交換器の一端側の夫々を四方弁の各
選択口に接続すると共に、室内熱交換器の他端側に膨張
弁と逆止弁の並列経路の一端側を、そして室外熱交換器
の他端側に膨張弁と開閉弁の並列経路の一端側を接続
し、これらの並列経路の他端側を相互に接続すると共
に、吸収サイクルを構成する再生器からの高圧冷媒蒸気
経路及び吸収器に至る低圧冷媒蒸気経路の夫々を前記四
方弁の各共通口に接続し、前記吸収器との熱交換部を設
けた吸収器放熱経路を構成して、その上流側を前記並列
経路の他端側に接続すると共に、下流側を三方弁の共通
口に接続し、該三方弁の一方の選択口を前記室外熱交換
器の一端側に接続すると共に、他方の選択口を逆止弁を
経て前記室内熱交換器の一端側に接続し、前記吸収器放
熱経路に於いて、吸収器との熱交換部の上流側に冷媒タ
ンクと、この冷媒タンクからの経路を共通口に接続した
三方弁とを設け、該三方弁の一方の選択口は前記熱交換
部側に接続すると共に、他方の選択口は吸収式サイクル
を構成する溶液タンクに逆止弁を介して接続して冷媒量
調節機構を構成したことを特徴とする吸収式ヒートポン
プ冷暖房装置に於ける冷媒系統An indoor heat exchanger and an outdoor heat exchanger are provided. One end of each of the indoor heat exchanger and the outdoor heat exchanger is connected to each selection port of a four-way valve. One end of the parallel path of the expansion valve and the check valve is connected to one end, and one end of the parallel path of the expansion valve and the on-off valve is connected to the other end of the outdoor heat exchanger. And a high-pressure refrigerant vapor path from the regenerator constituting the absorption cycle and a low-pressure refrigerant vapor path leading to the absorber are connected to respective common ports of the four-way valve, and heat exchange with the absorber is performed. A part of the absorber radiation path is configured, the upstream side is connected to the other end side of the parallel path, the downstream side is connected to a common port of the three-way valve, and one selection port of the three-way valve is connected. One end of the outdoor heat exchanger is connected to the other end of the indoor heat exchanger via a check valve. A refrigerant tank upstream of a heat exchange part with the absorber in the heat radiation path of the absorber, and a three-way valve connected to a common port from the refrigerant tank; One selection port of the valve is connected to the heat exchange section side, and the other selection port is connected to a solution tank constituting an absorption cycle via a check valve to constitute a refrigerant amount adjusting mechanism. System in absorption type heat pump air conditioner
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1340183A JP2759367B2 (en) | 1989-12-28 | 1989-12-28 | Refrigerant system in absorption heat pump air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1340183A JP2759367B2 (en) | 1989-12-28 | 1989-12-28 | Refrigerant system in absorption heat pump air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03199871A JPH03199871A (en) | 1991-08-30 |
| JP2759367B2 true JP2759367B2 (en) | 1998-05-28 |
Family
ID=18334515
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1340183A Expired - Lifetime JP2759367B2 (en) | 1989-12-28 | 1989-12-28 | Refrigerant system in absorption heat pump air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2759367B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103604249B (en) * | 2013-11-12 | 2016-06-15 | 清华大学 | A kind of energy tower type absorption-type cold-hot water dispenser group |
| CN111023619B (en) * | 2019-11-13 | 2021-07-20 | 吴巧魁 | Green heat pump refrigerating and heating device and method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57166455A (en) * | 1981-04-06 | 1982-10-13 | Daikin Ind Ltd | Absorption type refrigerating plant |
-
1989
- 1989-12-28 JP JP1340183A patent/JP2759367B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03199871A (en) | 1991-08-30 |
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