JP2646516B2 - Absorption type air-cooled heat pump air conditioner - Google Patents

Absorption type air-cooled heat pump air conditioner

Info

Publication number
JP2646516B2
JP2646516B2 JP7330689A JP7330689A JP2646516B2 JP 2646516 B2 JP2646516 B2 JP 2646516B2 JP 7330689 A JP7330689 A JP 7330689A JP 7330689 A JP7330689 A JP 7330689A JP 2646516 B2 JP2646516 B2 JP 2646516B2
Authority
JP
Japan
Prior art keywords
way valve
heat exchanger
path
heat
valve
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
Application number
JP7330689A
Other languages
Japanese (ja)
Other versions
JPH02251066A (en
Inventor
茂吉 黒沢
武 横山
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 Gas Co Ltd
Original Assignee
Tokyo Gas 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 Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP7330689A priority Critical patent/JP2646516B2/en
Publication of JPH02251066A publication Critical patent/JPH02251066A/en
Application granted granted Critical
Publication of JP2646516B2 publication Critical patent/JP2646516B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2315/00Sorption refrigeration cycles or details thereof
    • F25B2315/006Reversible sorption cycles

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は吸収式空冷ヒートポンプ冷暖房装置に関する
ものである。
Description: TECHNICAL FIELD The present invention relates to an absorption type air-cooled heat pump air conditioner.

(従来の技術及び発明の目的) 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、特に空冷ヒ
ートポンプ冷暖房装置としては殆んど実用化されていな
い。
(Prior Art and Object of the Invention) Although the absorption cycle is widely used in various cooling and heating water apparatuses, it has hardly been practically used as a heat pump cooling and heating apparatus, particularly as an air cooling heat pump cooling and heating apparatus.

本発明は冷房及び暖房運転の切り替えを、少ない構成
要素で行えるようにすることにより、吸収式空冷ヒート
ポンプ冷暖房装置の実用化を図ることを目的とするもの
である。
An object of the present invention is to achieve practical use of an absorption-type air-cooled heat pump cooling / heating device by enabling switching between cooling and heating operations with a small number of components.

(発明の構成) 本発明の構成を実施例に対応する第1図及び第2図を
参照して説明すると、本発明は、室内側及び室外側に設
置する熱交換部I,Oの夫々に、第1並びに第2の熱交換
器1i,1o;2i,2oを設け、該第1の熱交換器1i,1oは、夫々
の一端側を三方弁3の各選択口4i,4oに接続すると共
に、他端側を夫々逆止弁5i,5oを介して合流させ、また
第2の熱交換器2i,2oは、夫々の一端側を膨張弁6i,6o
開閉弁7i,7oの並列経路を介して第1の四方弁8の各選
択口9i,9oに接続すると共に、夫々の他端側を第2の四
方弁10の各選択口11i,11oに接続し、再生器12からの高
温冷媒蒸気経路13を前記三方弁3の共通入口14に接続す
ると共に、第1の熱交換器1i,1oの合流部15と前記第1
の四方弁8の共通入口16間に冷媒経路17を構成し、また
該第1の四方弁8の共通出口18を前記再生器12に至る希
溶液経路19に接続すると共に、該再生器12からの濃溶液
経路20を気液混合器21を介して前記第2の四方弁10の共
通入口22に接続し、該第2の四方弁10の共通出口23から
前記気液混合器21間に冷媒蒸気経路24を構成したもので
ある。
(Configuration of the Invention) The configuration of the present invention will be described with reference to FIGS. 1 and 2 corresponding to the embodiment. The present invention is applied to each of the heat exchange units I and O installed on the indoor side and the outdoor side. , First and second heat exchangers 1 i , 1 o ; 2 i , 2 o , each of the first heat exchangers 1 i , 1 o having one end connected to each of the selection ports of the three-way valve 3. 4 i , 4 o , the other ends are joined via check valves 5 i , 5 o , respectively, and the second heat exchangers 2 i , 2 o are each connected at one end to an expansion valve. 6 i, 6 o-off valve 7 i, 7 o while connected to the selected port 9 i, 9 o of the first four-way valve 8 through the parallel paths of the other end of the respective second four-way valve 10 are connected to the respective selection ports 11 i , 11 o , the high-temperature refrigerant vapor path 13 from the regenerator 12 is connected to the common inlet 14 of the three-way valve 3, and the first heat exchanger 1 i , 1 o Merging part 15 and the first
A refrigerant path 17 is formed between the common inlets 16 of the four-way valves 8, and a common outlet 18 of the first four-way valve 8 is connected to a dilute solution path 19 leading to the regenerator 12. Is connected to a common inlet 22 of the second four-way valve 10 via a gas-liquid mixer 21, and a refrigerant is provided between the common outlet 23 of the second four-way valve 10 and the gas-liquid mixer 21. This constitutes the steam path 24.

(作用及び実施例) 以上の構成に於いて、暖房を行う場合には、第1図に
示すように、三方弁3は共通入口14を選択口4iを介して
室内側の第1の熱交換器1iと連通させるように切替える
と共に、第1の四方弁8は共通入口16及び共通出口18
を、夫々選択口9o,9iを介して室外側の第2の熱交換器2
o及び室内側の第2の熱交換器2iと連通させるように切
り替え、また、第2の四方弁10は共通入口22及び共通出
口23を夫々選択口11i,11oを介して第2の熱交換器2i,2o
と連通させるように切り替える。そして室内側の第2の
熱交換器2iに対応する開閉弁7iは開とすると共に、室外
側の第2の熱交換器2oに対応する開閉弁7oは閉となる。
In (Advantageous embodiments) above configuration, when performing the heating, as shown in FIG. 1, the three-way valve 3 is first heat the indoor side through the selected port 4 i a common inlet 14 The first four-way valve 8 is switched so as to communicate with the exchanger 1 i, and the common inlet 16 and the common outlet 18 are connected.
Through the selection ports 9 o and 9 i , respectively.
Switching o and so as to communicate with the second heat exchanger 2 i of the indoor side, also, a second four-way valve 10 through the common inlet 22 and common outlet 23 respectively select port 11 i, 11 o the second Heat exchanger 2 i , 2 o
Switch to communicate with. And with the on-off valve 7 i corresponding to the second heat exchanger 2 i of the indoor side is open, on-off valve 7 o corresponding to the second heat exchanger 2 o of the outdoor side is closed.

しかして、再生器12に於いて加熱源25により加熱され
て発生した高温の冷媒蒸気は、高温冷媒蒸気経路13を通
り、三方弁3を経て室内側の第1の熱交換器1iに至り、
ここで室内には放熱して暖房に供すると共に、自体は温
度が低下し、凝縮する。次いで冷媒は、逆止弁5iを経て
合流部15に至り、ここから冷媒経路17を通って第1の四
方弁8の共通入口16に至る。ここから冷媒は選択口9o
通り、そして膨張弁6oを経て減圧されて室外側の第2の
熱交換器2oに至り、ここで蒸発して外気の熱を奪う。こ
うして外気の熱を奪った冷媒蒸気は第2の四方弁10の選
択口11oから共通出口23を通り、冷媒蒸気経路24を経て
気液混合器21に至る。
Thus, the high-temperature refrigerant vapor generated by being heated by the heating source 25 in the regenerator 12 passes through the high-temperature refrigerant vapor path 13, passes through the three-way valve 3, and reaches the first heat exchanger 1 i on the indoor side. ,
Here, heat is radiated into the room and used for heating, and the temperature of the room itself decreases and condenses. Next, the refrigerant reaches the junction 15 through the check valve 5 i, and from there, passes through the refrigerant path 17 to the common inlet 16 of the first four-way valve 8. The refrigerant from here through selection port 9 o, and is depressurized through the expansion valve 6 o reaches the second heat exchanger 2 o of the outdoor side, take the outside air heat evaporates here. The refrigerant vapor thus robbed of the heat of the outside air passes through the common outlet 23 from the selection port 11 o of the second four-way valve 10 and reaches the gas-liquid mixer 21 via the refrigerant vapor path 24.

一方、該気液混合器21には再生器12から濃溶液経路20
を経て濃溶液が供給されており、冷媒蒸気は該濃溶液と
混合状態で、気液混合器21から第2の四方弁10の共通入
口22及び選択口11iを経て室内側の第2の熱交換器2i
至る。このように第2の熱交換器2iに至った混合状態の
濃溶液と冷媒蒸気は、ここで室内側に放熱しながら吸収
反応して希溶液となる。しかして希溶液は、該熱交換器
2iから、開状態の開閉弁7iを通り、第1の四方弁8の選
択口9i、共通出口18から、希溶液経路19を経て再生器21
に還流する。
On the other hand, the gas-liquid mixer 21 is supplied from the regenerator 12 to the concentrated solution path 20.
Menstrual is supplied with the concentrated solution, the refrigerant vapor in admixture with the concentrated solution, from the gas-liquid mixer 21 second indoor side through the common inlet 22 and selected ports 11 i of the second four-way valve 10 It reaches the heat exchanger 2 i. Thus concentrated solution and refrigerant vapor mixed state that led to the second heat exchanger 2 i is a dilute solution by absorbing reaction while radiating heat where the indoor side. The dilute solution is then transferred to the heat exchanger
From 2 i, through the on-off valve 7 i in an open state, select port 9 i of the first four-way valve 8, the common outlet 18, regenerator through a dilute solution path 19 21
Reflux.

以上の動作に於いては、室内側の熱交換部Iの第1,第
2の熱交換器1i,2iが、夫々吸収式サイクルの凝縮器、
吸収器として動作して系内の熱を室内側に放熱すると共
に、室外側の熱交換部Oの第2の熱交換器2oが蒸発器と
して動作して外気の熱を系内に奪い、こうしてヒートポ
ンプ動作の暖房を行うことができる。
In the above operation, the first and second heat exchangers 1 i and 2 i of the indoor-side heat exchange section I are respectively a condenser of an absorption cycle,
It operates as an absorber to dissipate the heat inside the system to the indoor side, and the second heat exchanger 2 o of the heat exchange unit O outside the room operates as an evaporator to take the heat of the outside air into the system, In this way, heating by the heat pump operation can be performed.

以上の暖房運転に於いて、外気温度の低下により第2
の熱交換器2oに霜が発生した場合には、それまで閉状態
の開閉弁7oを開とする。
In the above heating operation, the second
If the frost is generated in the heat exchanger 2 o, the switch valve 7 o the closed state to the open before.

かかる状態に於いては、前述したように三方弁3から
室内側の第1の熱交換器1iに至った高温冷媒は、該第1
の熱交換器1iに於いても若干放熱し、一部凝縮しながら
該熱交換器1iを素通りし、そして膨張弁6oをバイアス
し、開閉弁7oを経て室外側の第2の熱交換器2oに至り、
ここで放熱して凝縮し、かかる放熱により霜を溶かし、
除去することができる。従って、暖房運転に於ける適宜
時点に開閉弁7oを開とすることにより、前述の動作によ
り必要に応じての除霜を行うことができる。
Is In this state, the high-temperature refrigerant that has reached the three-way valve 3 as described above to the first heat exchanger 1 i of the indoor side, first
The heat exchanger 1 i also slightly dissipates heat, partially condenses, passes through the heat exchanger 1 i , biases the expansion valve 6 o , and passes through the on-off valve 7 o to the second outdoor side. Heat exchanger 2 o ,
Here heat is dissipated and condensed, and the heat dissipates frost,
Can be removed. Therefore, by the on-off valve 7 o open the appropriate time in the heating operation, it is possible to perform defrosting as needed by the above-described operation.

以上の除霜動作に於いては、前述した通り高温冷媒蒸
気の一部が室内側の第1の熱交換器1iで若干放熱すると
共に、室内側の第2の熱交換器2iは、濃溶液経路20を介
して再生器12から入る熱や吸収熱により暖房可能な温度
に維持されるので、暖房を継続することができる。
In the above defrosting operation, as described above, a part of the high-temperature refrigerant vapor radiates slightly in the first heat exchanger 1 i on the indoor side, and the second heat exchanger 2 i on the indoor side Heating is maintained at a temperature at which heating can be performed by heat or absorption heat from the regenerator 12 via the concentrated solution path 20, so that heating can be continued.

次に、冷房を行う場合には、第2図に示すように、三
方弁3は共通入口14を選択口4oを介して室外側の第1の
熱交換器1oと連通させるように切替えると共に、第1の
四方弁8は共通入口16及び共通出口18を、夫々選択口
9i,9oを介して室内側の第2の熱交換器2i及び室外側の
第2の熱交換器2oと連通させるように切り替え、また、
第2の四方弁10は共通入口22及び共通出口23を夫々選択
口11o,11iを介して第2の熱交換器2o,2iと連通させるよ
うに切り替える。そして室外側の第2の熱交換器2oに対
応する開閉弁7oは開とすると共に、室内側の第2の熱交
換器2iに対応する開閉弁7iは閉とする。
Then, in the case of cooling, as shown in FIG. 2, the three-way valve 3 is switched so as to communicate with the first heat exchanger 1 o of the outdoor side through the selected port 4 o a common inlet 14 At the same time, the first four-way valve 8 has a common inlet 16 and a common outlet 18,
9 i, the switching so as to communicate with the second heat exchanger 2 o of the second heat exchanger 2 i and the outdoor side of the indoor side through the 9 o, also,
The second four-way valve 10 is switched so as to pass the second heat exchanger 2 o, 2 i and the communication through the common inlet 22 and common outlet 23 respectively select port 11 o, 11 i. The opening and closing valve 7 o corresponding to the outdoor side of the second heat exchanger 2 o with the opening, closing valve 7 i corresponding to the second heat exchanger 2 i of the indoor side is closed.

以上のように切り替えると、冷媒及び溶液は第2図中
の仮想線で示すように流れ、室外側の熱交換部Oの第1,
第2の熱交換器1o,2oが、夫々吸収式サイクルの凝縮
器、吸収器として動作して系内の熱を室外側に放熱する
と共に、室内側の熱交換部Iの第2の熱交換器2iが蒸発
器として動作して室内の熱を系内に奪い、こうして冷房
を行うことができる。
When switched as described above, the refrigerant and the solution flow as indicated by the phantom lines in FIG.
The second heat exchangers 1 o and 2 o operate as condensers and absorbers in the absorption cycle, respectively, to radiate heat in the system to the outside of the room, and to perform second heat exchange in the indoor-side heat exchange unit I. heat exchanger 2 i operates as an evaporator depriving indoor heat in the system, thus it is possible to perform cooling.

以上の構成に於いて、気液混合器21は、濃溶液側をキ
ャピラリ・チューブ等の減圧手段26により減圧して容器
内で冷媒蒸気と混合させる構成等とする他、濃溶液を駆
動流とし、冷媒蒸気を二次流とするエゼクタで構成する
こともでき、後者の場合には圧力差を有効に利用して、
前記吸収動作を昇圧した条件の基で行うことができるよ
うになり、この場合には吸収式サイクルの濃度差を大と
したり、吸収温度を高くすることができ、空冷ヒートポ
ンプとして最適な吸収式サイクルを行わせることができ
る。
In the above configuration, the gas-liquid mixer 21 has a configuration in which the concentrated solution side is decompressed by the decompression means 26 such as a capillary tube and mixed with the refrigerant vapor in the container, and the like, and the concentrated solution is used as a driving flow. It can also be configured with an ejector that uses refrigerant vapor as a secondary flow, and in the latter case, effectively utilizing the pressure difference,
The absorption operation can be performed under the condition of increased pressure. In this case, the concentration difference of the absorption cycle can be increased, and the absorption temperature can be increased. Can be performed.

以上の本発明は、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、濃溶液は
冷媒の少ない状態の溶液を表わすものである。尚、図中
符号27はポンプ、28は溶液熱交換器を示すものである。
The present invention can be applied to an absorption cycle using an appropriate refrigerant and an absorbent.The dilute solution in the above description is a solution containing a large amount of refrigerant, and a concentrated solution is a refrigerant. It represents a solution in a state with a small amount. In the figure, reference numeral 27 denotes a pump, and 28 denotes a solution heat exchanger.

(発明の効果) 本発明は以上の通り、室内側及び室外側に設置する熱
交換部の夫々に、第1並びに第2の熱交換器を設けると
共に、これらを四方弁と三方弁により切り替えて、前記
第1の熱交換器のいずれか一方側を凝縮器として動作さ
せると共に、第2の熱交換器の夫々を蒸発器または吸収
器として交互に動作させることにより、吸収式サイクル
を利用した空冷ヒートポンプ冷暖房装置を構成すること
ができるという効果がある。
(Effect of the Invention) As described above, the present invention provides the first and second heat exchangers in the heat exchange units installed on the indoor side and the outdoor side, respectively, and switches these by the four-way valve and the three-way valve. By operating either one side of the first heat exchanger as a condenser and alternately operating each of the second heat exchangers as an evaporator or an absorber, air cooling using an absorption cycle is performed. There is an effect that a heat pump cooling / heating device can be configured.

殊に本発明は、交互に吸収器として動作させるために
比較的大きな伝熱面積を必要とする第2の熱交換器の双
方を、冷暖房運転にかかわらず常時使用するようにした
ので、熱交換部のスペース効率が良いという効果があ
る。
In particular, the present invention uses both of the second heat exchangers, which require a relatively large heat transfer area to operate alternately as absorbers, at all times regardless of the cooling and heating operation. There is an effect that the space efficiency of the section is good.

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

第1図及び第2図は、夫々暖房運転、冷房運転を表わし
た本発明の実施例に対応する系統説明図である。 符号1i,1o……第1の熱交換器、2i,2o……第2の熱交換
器、3……三方弁、4i,4o,9i,9o,11i,11o……選択口、5
i,5o……逆止弁、6i,6o……膨張弁、7i,7o……開閉弁、
8,10……四方弁、12……高温冷媒蒸気経路、14,16,22…
…共通入口、15……合流部、17……冷媒経路、18,23…
…共通出口、19……希溶液経路、20……濃溶液経路、21
……気液混合器、24……冷媒蒸気経路、25……加熱源、
26……減圧手段、27……ポンプ、28……溶液熱交換器。
FIG. 1 and FIG. 2 are system explanatory diagrams showing a heating operation and a cooling operation, respectively, corresponding to the embodiment of the present invention. Symbols 1 i , 1 o ... first heat exchanger, 2 i , 2 o ... second heat exchanger, 3 ... three-way valve, 4 i , 4 o , 9 i , 9 o , 11 i , 11 o ...... Selection port, 5
i , 5 o ... check valve, 6 i , 6 o ... expansion valve, 7 i , 7 o ... on-off valve,
8,10 …… Four-way valve, 12… High-temperature refrigerant vapor path, 14,16,22…
… Common entrance, 15… Merge, 17 …… Refrigerant path, 18,23…
... Common outlet, 19 ... Dilute solution path, 20 ... Concentrated solution path, 21
... gas-liquid mixer, 24 ... refrigerant vapor path, 25 ... heating source,
26 ... decompression means, 27 ... pump, 28 ... solution heat exchanger.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】室内側及び室外側に設置する熱交換部の夫
々に、第1並びに第2の熱交換器を設け、該第1の熱交
換器は、夫々の一端側を三方弁の各選択口に接続すると
共に、他端側を夫々逆止弁を介して合流させ、また第2
の熱交換器は、夫々の一端側を膨張弁と開閉弁の並列経
路を介して第1の四方弁の各選択口に接続すると共に、
夫々の他端側を第2の四方弁の各選択口に接続し、再生
器からの高温冷媒蒸気経路を前記三方弁の共通入口に接
続すると共に、第1の熱交換器の合流部と前記第1の四
方弁の共通入口間に冷媒経路を構成し、また該第1の四
方弁の共通出口を前記再生器に至る希溶液経路に接続す
ると共に、該再生器からの濃溶液経路を気液混合器を介
して前記第2の四方弁の共通入口に接続し、該第2の四
方弁の共通出口から前記気液混合器間に冷媒蒸気経路を
構成したことを特徴とする吸収式空冷ヒートポンプ冷暖
房装置
A first and a second heat exchanger are provided in each of a heat exchange section installed on the indoor side and an outdoor side, and the first heat exchanger has one end side of each of three-way valves. Connected to the selection port, and the other end is joined via a check valve.
The heat exchanger has one end connected to each selection port of the first four-way valve via a parallel path of the expansion valve and the on-off valve,
The other end of each is connected to each selection port of the second four-way valve, the high-temperature refrigerant vapor path from the regenerator is connected to the common inlet of the three-way valve, and the junction of the first heat exchanger and the A refrigerant path is formed between the common inlets of the first four-way valve, the common outlet of the first four-way valve is connected to a dilute solution path leading to the regenerator, and a concentrated solution path from the regenerator is connected to a gas path. An absorption type air cooling, wherein the refrigerant is connected to a common inlet of the second four-way valve via a liquid mixer, and a refrigerant vapor path is formed between the common outlet of the second four-way valve and the gas-liquid mixer. Heat pump air conditioner
【請求項2】第1項記載の気液混合器は、濃溶液を駆動
流とし、冷媒蒸気を二次流とするエゼクタで構成したこ
とを特徴とする吸収式ヒートポンプ冷暖房装置
2. An absorption type heat pump cooling and heating apparatus according to claim 1, wherein said gas-liquid mixer comprises an ejector using a concentrated solution as a driving flow and a refrigerant vapor as a secondary flow.
JP7330689A 1989-03-25 1989-03-25 Absorption type air-cooled heat pump air conditioner Expired - Lifetime JP2646516B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7330689A JP2646516B2 (en) 1989-03-25 1989-03-25 Absorption type air-cooled heat pump air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7330689A JP2646516B2 (en) 1989-03-25 1989-03-25 Absorption type air-cooled heat pump air conditioner

Publications (2)

Publication Number Publication Date
JPH02251066A JPH02251066A (en) 1990-10-08
JP2646516B2 true JP2646516B2 (en) 1997-08-27

Family

ID=13514347

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7330689A Expired - Lifetime JP2646516B2 (en) 1989-03-25 1989-03-25 Absorption type air-cooled heat pump air conditioner

Country Status (1)

Country Link
JP (1) JP2646516B2 (en)

Also Published As

Publication number Publication date
JPH02251066A (en) 1990-10-08

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