JPH0481708B2 - - Google Patents
Info
- Publication number
- JPH0481708B2 JPH0481708B2 JP62309015A JP30901587A JPH0481708B2 JP H0481708 B2 JPH0481708 B2 JP H0481708B2 JP 62309015 A JP62309015 A JP 62309015A JP 30901587 A JP30901587 A JP 30901587A JP H0481708 B2 JPH0481708 B2 JP H0481708B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- main
- separator
- heat exchanger
- side heat
- 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
- 239000003507 refrigerant Substances 0.000 claims description 61
- 238000009835 boiling Methods 0.000 description 21
- 238000010438 heat treatment Methods 0.000 description 21
- 238000005057 refrigeration Methods 0.000 description 16
- 238000001816 cooling Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000000945 filler Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、非共沸混合冷媒を用いた熱ポンプ装
置の冷凍サイクルに関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a refrigeration cycle for a heat pump device using a non-azeotropic mixed refrigerant.
従来の技術
非共沸混合冷媒を用いた熱ポンプ装置は、冷凍
サイクル内部を循環する冷媒組成を可変すること
により能力制御や性能改善を行うことができ、
我々の先行発明になる特願昭60−116109号公報記
載のの熱ポンプ装置を、暖冷房装置として適用し
た第2図の実施例をもつて以下に説明する。Conventional technology A heat pump device using a non-azeotropic mixed refrigerant can control capacity and improve performance by varying the composition of the refrigerant circulating inside the refrigeration cycle.
The heat pump device described in Japanese Patent Application No. 116109/1988, which is our prior invention, will be described below with reference to an embodiment shown in FIG. 2 in which it is applied as a heating/cooling device.
第2図において、1は圧縮機、2は四方弁、3
は暖房運転時凝縮器として作用する負荷側熱交換
器、4は絞り装置、5は暖房運転時蒸発器として
作用する熱源側熱交換器、6はアキユームレー
タ、7は暖冷房切換時に常に絞り装置4の入口側
が凝縮器出口側に位置する如く冷媒流路を構成す
るための逆止弁群であり、順次接続配管すること
により通常暖房運転時は実線矢印の如く主冷凍サ
イクルを構成している。次に8は精留器であり、
内部には充填材9を充填すると共に、底部には加
熱源1を設けている。本実施例では加熱源10
は、電磁弁11を介した分岐吐出ガス配管12か
ら構成されており、四方弁2の吐出側に接続され
ている。また精留器8の頂部は、冷却源13を設
けた低沸点冷媒循環回路が構成されており、一部
が貯留される様になつている。ここで冷却源11
は別設の冷却装置や、特に暖房低負荷時のみ精留
器8を運転させる場合には蒸発器として作用する
熱源側熱交換器5の入口又は出口配管や低温の外
気で冷却する如く構成してもよい。さらに精留器
8の底部は電磁弁14を介した配管15により、
絞り装置4と並列に凝縮器出口側に接続されてお
り、絞り装置4の上流側で圧力損失のほとんどな
い位置に再び配管16により精留器8の底部と接
続されている。電磁弁14は加熱源10が停止し
た状態で配管15,16を通じた冷媒の微少な流
動を閉止させるためのものである。 In Fig. 2, 1 is a compressor, 2 is a four-way valve, and 3 is a compressor.
is a load side heat exchanger that acts as a condenser during heating operation, 4 is a throttle device, 5 is a heat source side heat exchanger that acts as an evaporator during heating operation, 6 is an accumulator, and 7 is a throttle that is always used when switching between heating and cooling. This is a check valve group for configuring a refrigerant flow path so that the inlet side of the device 4 is located on the condenser outlet side, and by connecting piping in sequence, a main refrigeration cycle is configured as shown by the solid line arrow during normal heating operation. There is. Next, 8 is a rectifier,
The inside is filled with a filler 9, and a heating source 1 is provided at the bottom. In this embodiment, the heating source 10
consists of a branch discharge gas pipe 12 via a solenoid valve 11, and is connected to the discharge side of the four-way valve 2. Further, the top of the rectifier 8 constitutes a low boiling point refrigerant circulation circuit provided with a cooling source 13, in which a portion of the refrigerant is stored. Here cooling source 11
If the rectifier 8 is to be operated only during low heating load, it is configured to be cooled by a separate cooling device, the inlet or outlet piping of the heat source side heat exchanger 5 that acts as an evaporator, or low-temperature outside air. It's okay. Furthermore, the bottom of the rectifier 8 is connected to a pipe 15 via a solenoid valve 14.
It is connected to the outlet side of the condenser in parallel with the throttle device 4, and is again connected to the bottom of the rectifier 8 by a pipe 16 at a position upstream of the throttle device 4 where there is almost no pressure loss. The solenoid valve 14 is for closing the minute flow of refrigerant through the pipes 15 and 16 when the heating source 10 is stopped.
かかる構成になるヒートポンプ装置において、
特に暖房運転時の負荷に対する能力制御の様態を
以下に説明する。非共沸混合冷媒を封入した第2
図のヒートポンプ装置において、通常暖房運転時
は、電磁弁11及び14を閉止しておくと、加熱
源10は起動しないばかりか、精留器8は配管1
6により連通した単なる過剰冷媒の液留めとして
存在し、主冷凍サイクルには封入した非共沸混合
冷媒とほぼ同等濃度の冷媒が循環し、暖房運転が
行なわれるものである。 In a heat pump device having such a configuration,
In particular, the mode of capacity control for the load during heating operation will be explained below. A second chamber containing a non-azeotropic mixed refrigerant
In the heat pump device shown in the figure, if the solenoid valves 11 and 14 are closed during normal heating operation, not only will the heating source 10 not start, but the rectifier 8 will
The main refrigeration cycle is a refrigerant with approximately the same concentration as the non-azeotropic mixed refrigerant sealed in the main refrigeration cycle, and a heating operation is performed.
次に外気温が上昇し低負荷暖房運転を行う場合
には、電磁弁11及び14を開放すると、分岐吐
出ガス配管12を経由して流入する圧縮機1の高
温吐出ガスにより加熱源10が起動され、精留器
8の底部に貯つた液冷媒の内、主に低沸点冷媒が
蒸発せられ、頂部の冷却源13を介した低沸点冷
媒循環回路から流下してくる液状の混合冷媒と充
填材9を介して向流接触し、精留器8の頂部では
低沸点冷媒が、底部では高沸点冷媒が濃縮され
る。ここで電磁弁14は開放されており、配管1
5、16と共に主冷凍サイクルが、精留器8の底
部の高沸点冷媒循環回路を構成することとなり、
主冷凍サイクル中の混合冷媒が電磁弁14を経由
して精留器8の底部に流入し、逆に底部に濃縮さ
れた高沸点冷媒は主冷凍サイクル中を低圧まで循
環する冷媒に誘引されて流出するため、主冷凍サ
イクルを循環する冷媒は、徐々に高沸点冷媒の濃
度が増大するものである。この作用態様は第2図
の破線矢印で示されている。従つて高沸点成分が
多くなる程ガス比容積が増大するため、圧縮機1
での冷媒循環量が減少して、能力低減が実現され
るものである。 Next, when the outside temperature rises and low-load heating operation is performed, when the solenoid valves 11 and 14 are opened, the heating source 10 is activated by the high temperature discharge gas of the compressor 1 flowing in via the branch discharge gas pipe 12. Of the liquid refrigerant stored at the bottom of the rectifier 8, mainly the low boiling point refrigerant is evaporated and charged with the liquid mixed refrigerant flowing down from the low boiling point refrigerant circulation circuit via the cooling source 13 at the top. Countercurrent contact occurs through the material 9, and the low-boiling refrigerant is concentrated at the top of the rectifier 8, and the high-boiling refrigerant is concentrated at the bottom. Here, the solenoid valve 14 is open, and the pipe 1
The main refrigeration cycle together with 5 and 16 constitutes a high boiling point refrigerant circulation circuit at the bottom of the rectifier 8,
The mixed refrigerant in the main refrigeration cycle flows into the bottom of the rectifier 8 via the solenoid valve 14, and conversely, the high boiling point refrigerant concentrated at the bottom is attracted by the refrigerant circulating in the main refrigeration cycle to a low pressure. Due to the outflow, the refrigerant circulating through the main refrigeration cycle has a progressively increasing concentration of high boiling refrigerant. This mode of action is indicated by the dashed arrow in FIG. Therefore, as the amount of high boiling point components increases, the gas specific volume increases.
This reduces the amount of refrigerant circulated in the engine and reduces the capacity.
発明が解決しようとする問題点
上記比較例の如き熱ポンプ装置において、基本
的に冷媒の組成可変は可能となるものの、たとえ
ば以下の如き不具合点を生じる。精留作用は主冷
凍サイクルから配管15を通して供給される冷媒
中の低沸点冷媒を精留器8の頂部に循環し、底部
で濃縮される高沸点冷媒は配管16を通して主冷
凍サイクル中の冷媒と混合するものであるが、配
管15,16の分岐流量は基本的に配管抵抗によ
つて決るため主冷凍サイクル中の絞り装置4の開
度調節によつて大いに左右され所望の分離性能が
得られない等の不具合点を生じる。Problems to be Solved by the Invention Although it is basically possible to change the composition of the refrigerant in the heat pump device as in the above comparative example, the following problems occur, for example. The rectifying action circulates the low boiling point refrigerant in the refrigerant supplied from the main refrigeration cycle through the pipe 15 to the top of the rectifier 8, and the high boiling point refrigerant concentrated at the bottom is exchanged with the refrigerant in the main refrigeration cycle through the pipe 16. However, since the branch flow rate of the pipes 15 and 16 is basically determined by the pipe resistance, it is greatly influenced by the opening degree adjustment of the throttling device 4 in the main refrigeration cycle, and the desired separation performance cannot be obtained. This may cause problems such as no
また配管15,16と主冷凍サイクルとの接続
のし方によつては、精留器8の底部で循環された
高沸点冷媒が誘引されず、新たな冷媒の供給がな
いため精留作用が停止する等の不具合点があるも
のであつた。 Also, depending on how the pipes 15 and 16 are connected to the main refrigeration cycle, the high boiling point refrigerant circulated at the bottom of the rectifier 8 is not attracted, and no new refrigerant is supplied, resulting in a rectification effect. It had some problems such as stopping.
本発明はかかる非共沸混合冷媒を用いた熱ポン
プ装置において、精留作用の確実性を増し、組成
の制御性を向上するための冷凍サイクルの改良に
関するものである。 The present invention relates to an improvement of a refrigeration cycle in a heat pump device using such a non-azeotropic mixed refrigerant in order to increase the reliability of the rectification action and improve the controllability of the composition.
問題点を解決するための手段
本発明になる熱ポンプ装置は、非共沸混合冷媒
の組成可変手段として精留作用を行う分離器を用
い、分離器下部を主サイクル回路の主絞り装置を
バイパスとして、凝縮器出口および絞り装置を介
して蒸発器入口と接続し、分離器上部に冷却器・
貯留器を連結した循環回路を構成し、確実な精留
作用を実現するものである。Means for Solving the Problems The heat pump device according to the present invention uses a separator that performs a rectifying action as a means for varying the composition of a non-azeotropic mixed refrigerant, and the lower part of the separator bypasses the main throttling device of the main cycle circuit. The condenser outlet is connected to the evaporator inlet through a throttling device, and a cooler/cooler is installed at the top of the separator.
A circulation circuit is constructed in which reservoirs are connected to achieve reliable rectification.
作 用
かかる冷凍サイクル上の構成を採用することに
より、分離器側への分岐流量は分離器と蒸発器入
口の間に介した絞り装置の配管抵抗によつてほぼ
規定されるため、主サイクル回路の主絞り装置の
開度調節によつても大きく変動せず確実な精留作
用が実現され、分離器で濃縮された冷媒はそのま
ま絞り装置を介して低圧配管となる蒸発器入口に
流出するためすみやかな組成可変が保証されるも
のである。Effect By adopting such a configuration on the refrigeration cycle, the branched flow rate to the separator side is almost determined by the piping resistance of the throttling device interposed between the separator and the evaporator inlet, so the main cycle circuit Even by adjusting the opening of the main throttling device, a reliable rectification effect is achieved without large fluctuations, and the refrigerant concentrated in the separator directly flows through the throttling device to the evaporator inlet, which becomes the low-pressure pipe. This ensures rapid compositional variation.
実施例
本発明になる熱ポンプ装置の実施例を、冷暖房
装置に適用した第1図の実施例をもつて説明す
る。Embodiment An embodiment of the heat pump device according to the present invention will be explained using the embodiment shown in FIG. 1, which is applied to an air-conditioning device.
第1図においては、圧縮機31、四方弁32、
負荷側熱交換器33、主絞り装置34、熱源側熱
交換器35等を還状に接続し、主サイクル回路を
構成している。また主絞り装置34のバイパスと
して絞り装置36,37、逆止弁38,39、充
填材40を充填した分離器41、貯留器42等を
連結した副サイクル回路を構成し、分離器41の
下部には加熱器43、上部には冷却器44を配置
し、本実施例では加熱器43の加熱用熱源として
圧縮機31からの吐出ガスを、電磁弁45を介し
てバイパス回路46から導くことによつて構成し
ている。また冷却器44の冷却用熱源としては、
圧縮機31の吸入ガスを用いてもよいし(図示せ
ず)、低温の外気で冷却する如く構成してもよく、
冷凍サイクル内部には非共沸混合冷媒が封入され
ている。 In FIG. 1, a compressor 31, a four-way valve 32,
The load side heat exchanger 33, the main throttle device 34, the heat source side heat exchanger 35, etc. are connected in a circular manner to form a main cycle circuit. Also, as a bypass of the main throttle device 34, a sub-cycle circuit is constructed in which throttle devices 36, 37, check valves 38, 39, a separator 41 filled with a filler 40, a reservoir 42, etc. are connected. A heater 43 is disposed at the top, and a cooler 44 is disposed at the top. In this embodiment, the discharge gas from the compressor 31 is used as a heat source for heating the heater 43 and is led from a bypass circuit 46 via a solenoid valve 45. It is structured accordingly. In addition, as a cooling heat source for the cooler 44,
The suction gas of the compressor 31 may be used (not shown), or the cooling may be performed using low-temperature outside air.
A non-azeotropic mixed refrigerant is sealed inside the refrigeration cycle.
かかる熱ポンプ装置の作用態様を暖房運転時を
中心に説明すると、高能力を得るためには、主サ
イクル回路を循環する冷媒組成として低沸点冷媒
を多く循環させることが知られており、電磁弁4
5を閉止することにより、封入した非共沸混合冷
媒とほぼ等しい組成の混合冷媒が、主には圧縮機
31→四方弁32→負荷側熱交換器33→主絞り
装置34→熱源側熱交換器35→四方弁32→圧
縮機31の順に循環し、一部は凝縮器となる負荷
側熱交換器33からバイパスして、逆止弁38→
分離器41下部→絞り装置37→熱源側熱交換器
35と循環し余剰冷媒は貯留器42で貯留される
ことになるため、低沸点冷媒を含んだ混合冷媒に
より、凝縮器となる負荷側熱交換器33において
高暖房能力を出力することが可能となる。 The mode of operation of such a heat pump device will be explained with a focus on heating operation. In order to obtain high capacity, it is known that a large amount of low boiling point refrigerant is circulated in the main cycle circuit as a refrigerant composition. 4
By closing 5, a mixed refrigerant having almost the same composition as the enclosed non-azeotropic mixed refrigerant is mainly transferred to the compressor 31 → four-way valve 32 → load side heat exchanger 33 → main throttle device 34 → heat source side heat exchange It circulates in the order of container 35 → four-way valve 32 → compressor 31, and a part bypasses from load-side heat exchanger 33, which serves as a condenser, and circulates through check valve 38 →
The surplus refrigerant circulates from the lower part of the separator 41 to the throttling device 37 to the heat source side heat exchanger 35 and is stored in the reservoir 42, so the mixed refrigerant containing the low boiling point refrigerant absorbs heat from the load side, which becomes the condenser. It becomes possible to output high heating capacity in the exchanger 33.
一方能力を低減させる場合には、電磁弁45を
開放すると、圧縮機31からの吐出ガスの一部は
バイパス回路46を経由して加熱器43内を流れ
るため、副サイクル回路を循環していた一部の混
合冷媒を加熱することになる。このとき非共沸混
合冷媒の性質として、より揮発性の高い低沸点冷
媒が気化され、分離器41内を上昇し、冷却器4
4により凝縮液化され、貯留器42内の余剰冷媒
と混合し、一部は分離器41内を流下還流してく
る。ここで分離器41内部においては上昇するガ
ス冷媒と流下する液冷媒が微少な流速状態の中で
充填材40により気液接触が促進され、いわゆる
精留作用により貯留器42中では低沸点冷媒が濃
縮され、高沸点冷媒は分離器41の下部に連結さ
れた絞り装置37を経由して低圧配管となる熱源
側熱交換器35に流出し主サイクル回路は高沸点
冷媒の濃度が高まることによつて、負荷側熱交換
器33において低暖房能力を実現することが可能
となるものである。 On the other hand, when reducing the capacity, when the solenoid valve 45 is opened, a part of the gas discharged from the compressor 31 flows through the heater 43 via the bypass circuit 46, so that it is circulated through the sub-cycle circuit. This will heat some of the mixed refrigerant. At this time, due to the nature of the non-azeotropic mixed refrigerant, the more volatile low-boiling refrigerant is vaporized, rises in the separator 41, and rises in the cooler 4.
4, the refrigerant is condensed and liquefied, mixed with the surplus refrigerant in the reservoir 42, and a part of the refrigerant flows down and refluxes in the separator 41. Here, inside the separator 41, gas-liquid contact between the ascending gas refrigerant and the descending liquid refrigerant is promoted by the filler 40 in a state of minute flow velocity, and the low boiling point refrigerant is The concentrated high-boiling refrigerant flows through the throttle device 37 connected to the lower part of the separator 41 to the heat source side heat exchanger 35, which is a low-pressure pipe, and the main cycle circuit is closed due to the increased concentration of the high-boiling refrigerant. Therefore, it becomes possible to realize low heating capacity in the load side heat exchanger 33.
なお冷房運転時は四方弁32を切換えることに
より、主には圧縮機31→四方弁32→熱源側熱
交換器35→主絞り装置34→負荷側熱交換器3
3→四方弁32→圧縮機31の順に循環し、一部
は凝縮器となる熱源側熱交換器35からバイパス
して、逆止弁39→分離器41下部→絞り装置3
6→負荷側熱交換器33と循環し、精留作用によ
る冷媒組成の可変手段は暖房運転時と同じであ
る。すなわち絞り装置36,37及び逆止弁3
8,39は、本実施例では分離器41を高圧に位
置させ凝縮器として作用する熱交換器からの高圧
液冷媒を分離器41内に供給し、加熱器43での
気化を促進するためのものであり、場合によつて
別の絞り装置を介して接続した分離器41を中間
圧に位置させて、その絞り装置の減圧により低沸
点冷媒を気化させるようにしてもよい。 During cooling operation, by switching the four-way valve 32, the main flow is as follows: compressor 31 → four-way valve 32 → heat source side heat exchanger 35 → main throttling device 34 → load side heat exchanger 3
It circulates in the order of 3 → four-way valve 32 → compressor 31, and part of it bypasses from the heat source side heat exchanger 35, which serves as a condenser, and goes through the check valve 39 → the lower part of the separator 41 → the throttle device 3.
6→Load-side heat exchanger 33 and the means for varying the refrigerant composition by rectification are the same as in the heating operation. That is, the throttle devices 36, 37 and the check valve 3
8 and 39 are for supplying high pressure liquid refrigerant from a heat exchanger that positions the separator 41 at high pressure and acting as a condenser into the separator 41 and promoting vaporization in the heater 43 in this embodiment. If necessary, the separator 41 connected via another throttling device may be located at an intermediate pressure, and the low boiling point refrigerant may be vaporized by the pressure reduction of the throttling device.
本実施例では、熱ポンプ装置の組成可変手段と
して精留作用を働かせる時に、分離器上部に配置
した貯留器中に低沸点冷媒を濃縮させる場合に、
分離器中での精留作用の確実性を増し、主サイク
ル回路の主絞り装置の開度調節によらず分離器側
への分岐流量の変動を押えるために、主絞り装置
をバイパスして凝縮器出口と接続された分離器を
再び蒸発器入口と絞り装置を介して接続するもの
であり、もちろんその他の加熱源や冷却源と組合
せることは本発明の範囲に含まれるものである。 In this embodiment, when a rectification effect is used as a composition variable means of a heat pump device, when a low boiling point refrigerant is concentrated in a reservoir placed at the upper part of a separator,
In order to increase the reliability of the rectifying action in the separator and suppress fluctuations in the branch flow rate to the separator side without adjusting the opening of the main throttle device in the main cycle circuit, the main throttle device is bypassed for condensation. The separator connected to the outlet of the evaporator is again connected to the inlet of the evaporator via a throttling device, and of course it is within the scope of the present invention to combine it with other sources of heating or cooling.
発明の効果
本発明になる熱ポンプ装置は、非共沸混合冷媒
を用い主サイクル回路の主絞り装置をバイパスし
て凝縮器出口及び絞り装置を介して蒸発器入口と
接続された分離器、分離器上部の循環回路に設け
た冷却器・貯留器等からなる副サイクル回路を構
成し高圧または中間圧の位置に配置した分離器に
おける精留作用により分離器上部の貯留器に低沸
点冷媒を濃縮することにより主サイクル回路中の
冷媒組成を可変する如く構成したものであるか
ら、主サイクル回路の組成の制御性が高まり、ひ
いては能力制御や性能改善を保証することが可能
となるものである。Effects of the Invention The heat pump device of the present invention uses a non-azeotropic mixed refrigerant and bypasses the main throttling device of the main cycle circuit, and connects the condenser outlet and the evaporator inlet via the throttling device. The sub-cycle circuit consists of a cooler, a storage device, etc. installed in the circulation circuit at the top of the separator, and the low boiling point refrigerant is concentrated in the storage device at the top of the separator by rectification in the separator placed at a high pressure or intermediate pressure position. By doing so, the composition of the refrigerant in the main cycle circuit can be varied, thereby increasing the controllability of the composition of the main cycle circuit, thereby making it possible to guarantee capacity control and performance improvement.
第1図は本発明の一実施例における熱ポンプ装
置の原理図、第2図は非共沸混合冷媒を用いた熱
ポンプ装置の比較例の原理図である。
31……圧縮機、33……負荷側熱交換器、3
4……主絞り装置、35……熱源側熱交換器、3
6,37……絞り装置、38,39……逆止弁、
41……分離器、42……貯留器。
FIG. 1 is a principle diagram of a heat pump device according to an embodiment of the present invention, and FIG. 2 is a principle diagram of a comparative example of a heat pump device using a non-azeotropic mixed refrigerant. 31...Compressor, 33...Load side heat exchanger, 3
4... Main throttling device, 35... Heat source side heat exchanger, 3
6, 37... throttle device, 38, 39... check valve,
41... Separator, 42... Reservoir.
Claims (1)
装置、熱源側熱交換器を環状接続して主サイクル
回路を構成し、前記主絞り装置をバイパスして凝
縮器となる熱交換器出口と接続された分離器下部
を、再び蒸発器となる熱交換器入口と絞り装置を
介して接続し、前記分離器上部に冷却器・貯留器
を連結した循環回路を構成し、非共沸混合冷媒を
封入したことを特徴とする熱ポンプ装置。1 At least a compressor, a load-side heat exchanger, a main throttle device, and a heat source-side heat exchanger are connected in a ring to form a main cycle circuit, and the main cycle circuit is connected to the outlet of a heat exchanger that bypasses the main throttle device and becomes a condenser. The lower part of the separated separator is connected again to the inlet of the heat exchanger, which becomes an evaporator, via a throttle device, and a circulation circuit is constructed in which a cooler and a storage device are connected to the upper part of the separator, and the non-azeotropic mixed refrigerant is A heat pump device characterized by being enclosed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62309015A JPS63153367A (en) | 1987-12-07 | 1987-12-07 | Heat pump device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62309015A JPS63153367A (en) | 1987-12-07 | 1987-12-07 | Heat pump device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63153367A JPS63153367A (en) | 1988-06-25 |
| JPH0481708B2 true JPH0481708B2 (en) | 1992-12-24 |
Family
ID=17987856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62309015A Granted JPS63153367A (en) | 1987-12-07 | 1987-12-07 | Heat pump device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63153367A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5062275A (en) * | 1989-03-09 | 1991-11-05 | Nippondenso Co., Ltd. | Automotive air conditioner |
| JP2001153480A (en) * | 1999-11-26 | 2001-06-08 | Daikin Ind Ltd | Refrigeration equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59197762A (en) * | 1983-04-22 | 1984-11-09 | 三菱電機株式会社 | refrigeration cycle |
-
1987
- 1987-12-07 JP JP62309015A patent/JPS63153367A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63153367A (en) | 1988-06-25 |
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