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JPH0743176B2 - Heat pump device - Google Patents
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JPH0743176B2 - Heat pump device - Google Patents

Heat pump device

Info

Publication number
JPH0743176B2
JPH0743176B2 JP61130744A JP13074486A JPH0743176B2 JP H0743176 B2 JPH0743176 B2 JP H0743176B2 JP 61130744 A JP61130744 A JP 61130744A JP 13074486 A JP13074486 A JP 13074486A JP H0743176 B2 JPH0743176 B2 JP H0743176B2
Authority
JP
Japan
Prior art keywords
refrigerant
compressor
expansion device
gas
heater
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 - Fee Related
Application number
JP61130744A
Other languages
Japanese (ja)
Other versions
JPS62288451A (en
Inventor
和生 中谷
裕二 向井
茂大 鈴木
雄二 吉田
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP61130744A priority Critical patent/JPH0743176B2/en
Publication of JPS62288451A publication Critical patent/JPS62288451A/en
Publication of JPH0743176B2 publication Critical patent/JPH0743176B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Central Heating Systems (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に関す
るものである。
TECHNICAL FIELD The present invention relates to a heat pump device using a non-azeotropic mixed refrigerant.

従来の技術 従来、非共沸混合冷媒を用いた熱ポンプ装置において、
冷媒精留塔を用いることにより、冷凍サイクルの主回路
の冷媒組成を可変にして、負荷対応の優れたものにする
提案がされている。ここでは、主回路の冷媒の一部を加
熱器で加熱して沸とうさせ、冷媒精留塔内での精留作用
により、貯留器に低沸点冷媒を貯留して主回路を高沸点
冷媒に富んだものとしたり、あるいは貯留器の冷媒を主
回路へ戻すことによって主回路を高沸点冷媒に富んだも
のとすることにより、負荷に対応した能力の出る熱ポン
プ装置となっていた。第3図に冷媒精留塔を用いた熱ポ
ンプ装置の従来例としての我々の先行出願を示す。
Conventional technology Conventionally, in a heat pump device using a non-azeotropic mixed refrigerant,
It has been proposed to use a refrigerant rectification column to make the refrigerant composition of the main circuit of the refrigeration cycle variable so as to be excellent in load handling. Here, a part of the refrigerant in the main circuit is heated by a heater to boil it, and by the rectification action in the refrigerant rectification column, the low boiling point refrigerant is stored in the reservoir and the main circuit becomes the high boiling point refrigerant. The heat pump device has a capacity corresponding to the load by making the main circuit rich in the high boiling point refrigerant by enriching it or by returning the refrigerant in the reservoir to the main circuit. FIG. 3 shows our prior application as a conventional example of a heat pump device using a refrigerant rectification column.

同図において1は圧縮機、2は凝縮器、3は主絞り装
置、4は蒸発器であり、これらを配管接続することによ
り冷凍サイクルの主回路を構成する。圧縮機1の吐出側
には副回路の加熱器5に入る吐出ガスバイパス回路6が
電磁弁7を介して設けられている。また圧縮機1を駆動
するために交流電源8が周波数変換器9を介して供給さ
れている。
In the figure, 1 is a compressor, 2 is a condenser, 3 is a main expansion device, and 4 is an evaporator, and these are connected by piping to form a main circuit of a refrigeration cycle. On the discharge side of the compressor 1, a discharge gas bypass circuit 6 that enters the heater 5 of the sub circuit is provided via a solenoid valve 7. An AC power supply 8 is supplied via a frequency converter 9 to drive the compressor 1.

凝縮器2を出た液冷媒は第1の副絞り装置10によって、
飽和液線以下まで減圧され、加熱器5を通って冷媒精留
塔11の下部に接続されている。冷媒精留塔11には充填材
12が充填されている。冷媒精留塔11の頂部には冷却器13
と貯留器14が配管15によって接続され、更に貯留器14よ
り塔頂に帰還する配管16が接続されている。貯留器14下
部より電磁弁17を介した配管18が、冷媒精留塔11の下部
よりの配管19と合流後、第2の副絞り装置20を通って蒸
発器4に接続されている。冷却器13の冷却源としては圧
縮機1の吸入ガス等を用いている(図示せず)。
The liquid refrigerant discharged from the condenser 2 is supplied by the first sub expansion device 10 to
The pressure is reduced to below the saturated liquid line, and is connected to the lower part of the refrigerant rectification column 11 through the heater 5. A packing material for the refrigerant rectification tower 11
12 filled. At the top of the refrigerant rectification tower 11 is a cooler 13
And a reservoir 14 are connected by a pipe 15, and a pipe 16 for returning from the reservoir 14 to the top of the tower is further connected. A pipe 18 from the lower part of the reservoir 14 via a solenoid valve 17 merges with a pipe 19 from the lower part of the refrigerant rectification column 11, and then is connected to the evaporator 4 through a second auxiliary expansion device 20. As a cooling source of the cooler 13, suction gas of the compressor 1 or the like is used (not shown).

これらの回路には非共沸混合冷媒が任意の組成で封入さ
れているものである。
In these circuits, a non-azeotropic mixed refrigerant is enclosed in an arbitrary composition.

次にかかる熱ポンプ装置の動作について説明する。Next, the operation of the heat pump device will be described.

主冷凍サイクル中を封入した冷媒組成で循環させる場合
には、電磁弁7を閉,電磁弁17を開とする事により、冷
媒精留塔11内を上昇するガス成分がそのまま貯留器14を
通って第2の副絞り装置20から蒸発器4に流入し、冷媒
精留塔11内で精留作用が働かず、封入組成そのままで循
環する。
When circulating the main refrigeration cycle with the enclosed refrigerant composition, the solenoid valve 7 is closed and the solenoid valve 17 is opened so that the gas component rising in the refrigerant rectification column 11 passes through the reservoir 14 as it is. And flows into the evaporator 4 from the second sub-expansion device 20, the rectification action does not work in the refrigerant rectification column 11, and the refrigerant is circulated with the enclosed composition as it is.

次に封入した組成よりも高沸点冷媒の多い組成で循環さ
せる場合について述べる。電磁弁7を開,電磁弁17を閉
とする事により、凝縮器2より分岐された液冷媒は第1
の副絞り装置10によって飽和液線以下にまで減圧され若
干のガス成分を発生して加熱器5に入る。加熱器5によ
り更に分離作用を促進する程度のガス成分を発生して冷
媒精留塔11内に入り上昇してゆく。一方上昇したガスは
冷却器13で凝縮液化して貯留器14に入り、配管16を通っ
て塔頂に還流される。冷媒精留塔11内を上昇するガスと
下降する液とが、充填材12表面で気液接触を行ない熱物
質交換し、より低沸点な冷媒が貯留器14に濃縮し、高沸
点な冷媒は冷媒精留塔11の下部より配管19を通って主サ
イクルに帰還し、結果として主冷凍サイクル側は高沸点
な冷媒に濃縮されるものである。
Next, the case of circulating a composition having a higher boiling point refrigerant than the enclosed composition will be described. By opening the solenoid valve 7 and closing the solenoid valve 17, the liquid refrigerant branched from the condenser 2 is set to the first
It is decompressed to below the saturated liquid line by the sub-throttler 10, and some gas components are generated to enter the heater 5. The heater 5 generates a gas component that further promotes the separation action, and enters the refrigerant rectification column 11 to rise. On the other hand, the rising gas is condensed and liquefied in the cooler 13, enters the reservoir 14, and is returned to the top of the tower through the pipe 16. The gas rising in the refrigerant rectification column 11 and the liquid descending are subjected to heat and mass exchange on the surface of the packing material 12 for gas-liquid contact, the lower boiling point refrigerant is concentrated in the reservoir 14, and the higher boiling point refrigerant is The refrigerant is returned from the lower part of the refrigerant rectification column 11 to the main cycle through the pipe 19, and as a result, the main refrigeration cycle side is concentrated to a high boiling point refrigerant.

一般に、主回路が低沸点成分に富むと能力が増し、高沸
点成分に富むと逆に能力が減少する。本従来例において
は負荷が増す時には、電磁弁17を開,電磁弁7を閉と
し、負荷が減少する時には、逆に電磁弁17を閉,電磁弁
7を開として、前述の如く冷媒組成を可変して負荷に対
応した能力を生じさせるような運転をする。
Generally, when the main circuit is rich in low-boiling components, the capacity is increased, and when high-boiling components are rich, the capacity is decreased. In this conventional example, when the load increases, the solenoid valve 17 is opened and the solenoid valve 7 is closed, and when the load decreases, the solenoid valve 17 is closed and the solenoid valve 7 is opened conversely to change the refrigerant composition as described above. The operation is variable so that the capacity corresponding to the load is generated.

また、周波数変換器9により圧縮機1の回転数を変化さ
せ、主回路の冷媒循環量を変えて能力を制御することも
可能であり、冷媒組成変化の効果と合いまって非常に広
い能力範囲、すなわち、負荷範囲で運転することができ
るものであった。
It is also possible to change the number of revolutions of the compressor 1 by the frequency converter 9 to change the refrigerant circulation amount in the main circuit to control the capacity, and in combination with the effect of the refrigerant composition change, a very wide capacity range. That is, it was able to operate in the load range.

発明が解決しようとする問題点 しかし、このような従来のものでは次のような欠点があ
った。すなわち、非常に負荷の小さい場合、圧縮機1の
回転数を落とし冷媒循環量を下げ、また、電磁弁7,17の
操作により主回路を高沸点成分に富んだ組成として運転
するが、回転数をあまり下げすぎるとモータトルクの減
少によりトルク変動が大となって電流が過剰となりモー
タ損傷につながるため下限があった。また、冷媒組成を
高沸点成分にすることにも限度があり、要求される負荷
よりも大きい能力で運転していることもしばしばあっ
た。そのため、圧縮機のオン,オフ運転等をくりかえし
て対応することもあったため、能力/電力の値(以下EE
R)は低いなどの問題点があった。そこで本発明は、か
かる従来の欠点を改良し、非常に小さい負荷においても
圧縮機のオン,オフ等をしなくてもよい。高負荷対応で
高EERの熱ポンプ装置を提供するものである。
Problems to be Solved by the Invention However, such a conventional device has the following drawbacks. That is, when the load is very small, the number of revolutions of the compressor 1 is reduced to reduce the refrigerant circulation amount, and the main circuit is operated by the composition of the high boiling point components by operating the solenoid valves 7 and 17, but the number of revolutions is high. If the value is too low, there is a lower limit because the motor torque decreases and the torque fluctuations become large, resulting in excessive current and damage to the motor. In addition, there is a limit to the composition of the refrigerant having a high boiling point, and the engine is often operated with a capacity larger than the required load. For this reason, the compressor's on / off operation was sometimes repeated, so the capacity / power value (hereinafter EE
R) had problems such as being low. Therefore, the present invention improves on the above-mentioned conventional drawbacks, and the compressor does not have to be turned on and off even under a very small load. It provides a high EER heat pump device that can handle high loads.

問題点を解決するための手段 上記問題点を解決するための本発明の技術的手段は、冷
媒精留塔の加熱器の加熱源として、圧縮機内に吸入され
て圧縮される途中の冷媒ガスを用いるものである。
Means for Solving the Problems The technical means of the present invention for solving the above problems is, as a heating source of a heater of a refrigerant rectification column, a refrigerant gas that is being sucked into a compressor and is being compressed. It is used.

作用 この技術的手段による作用は次のようになる。Action The action of this technical means is as follows.

すなわち、圧縮機に流入した吸入ガスを圧縮する過程に
おいて、一部、外へ取り出し、冷媒精留塔の加熱源とし
て加熱器に流入させて、副回路に流入してきた冷媒を加
熱することにより、精留作用を行なって冷媒組成を可変
する。また、このガスは凝縮器や蒸発器を通らず、その
まま、再び圧縮機の吸入側へ戻されるため主回路を流れ
る冷媒循環量を減少せしめて能力を減少することができ
る。したがって、冷媒組成と冷媒循環量の両方を可変す
ることにより、能力を幅広く変化させることができるも
のである。
That is, in the process of compressing the suction gas that has flowed into the compressor, a part of the gas is taken out and is allowed to flow into the heater as a heating source for the refrigerant rectification column to heat the refrigerant that has flowed into the sub-circuit. Performs rectification to change the refrigerant composition. Further, since this gas does not pass through the condenser or evaporator and is returned to the suction side of the compressor as it is, the amount of refrigerant circulating through the main circuit can be reduced and the capacity can be reduced. Therefore, the capacity can be widely changed by changing both the refrigerant composition and the refrigerant circulation amount.

実施例 本発明の一実施例を第1図にもとづいて説明する。第1
図において、番号21〜40のそれぞれの構成部品は、従来
例の第2図における番号1〜20と、順にそれぞれ同一の
名称で、同じ機能を持つものであるので説明は省略する
が、異なっているのは、吐出ガスバイパス回路が従来は
圧縮機1を出た後分岐して加熱器5へ向かい、放熱した
後再び主回路へ帰還するようになっていたが本発明の実
施例では圧縮機21のシリンダ内の圧縮途中の吐出ガスを
加熱器25へ向かう吐出ガスバイパス回路26へ導入し、帰
還の戻りガスは圧縮機21の吸入側へ戻して主回路と合流
させるようにしていることである。圧縮機21の内部はお
およそ、第3図の如く成っている。
Embodiment An embodiment of the present invention will be described with reference to FIG. First
In the figure, each of the components numbered 21 to 40 has the same name and the same function as the numbers 1 to 20 in FIG. The discharge gas bypass circuit is conventionally branched from the compressor 1, then branched to the heater 5, and after radiating heat, it is returned to the main circuit again. By introducing the discharge gas in the middle of compression in the cylinder of 21 into the discharge gas bypass circuit 26 toward the heater 25, the return gas of the return is returned to the suction side of the compressor 21 and merged with the main circuit. is there. The inside of the compressor 21 is roughly constructed as shown in FIG.

第3図は空調機等によく用いられているローリングピス
トン型圧縮機の概略図であり、吸入ガス配管41より冷媒
がシリンダ42内に流入し、回転しているピストン43によ
って斜線部内のガスが圧縮されているところを示してい
るが、電磁弁27が開の時には、ピストン43がバイパス孔 44をふさぐまでは、圧縮ガスは吐出ガスバイパス回路26
を流れ前述のように加熱器25を経て吸入側へ戻る。ピス
トン43がバイパス孔44を過ぎると直ちに圧縮を開始し、
所定の圧力になれば吐出回路45を経て主回路へ流出す
る。電磁弁27が閉の時は、バイパス孔44がない時と同様
通常の圧縮過程となる。したがって、電磁弁27を開とす
ることにより、吸入したガスの一部は主回路側へ流れ
ず、常に、吸入ガス配管41→シリンダ42内→バイパス孔
44→吐出ガスバイパス回路26→電磁弁27→加熱器25→吸
入ガス配管41を循環することになり、主回路への循環量
は減少して能力を低下させることができる。
FIG. 3 is a schematic diagram of a rolling piston type compressor often used in an air conditioner or the like, in which the refrigerant flows into the cylinder 42 through the suction gas pipe 41, and the rotating piston 43 causes the gas in the hatched portion to flow. Although the compressed gas is shown, when the solenoid valve 27 is open, the compressed gas is discharged until the piston 43 closes the bypass hole 44.
Flows through the heater 25 and returns to the suction side as described above. As soon as the piston 43 passes the bypass hole 44, compression starts,
When it reaches a predetermined pressure, it flows out to the main circuit through the discharge circuit 45. When the solenoid valve 27 is closed, the normal compression process is performed as when the bypass hole 44 is not provided. Therefore, by opening the solenoid valve 27, a part of the sucked gas does not flow to the main circuit side, and the sucked gas pipe 41 → the cylinder 42 → the bypass hole is always provided.
44 → Discharge gas bypass circuit 26 → Solenoid valve 27 → Heater 25 → Suction gas pipe 41 is circulated, so that the circulation amount to the main circuit is reduced and the capacity can be lowered.

冷媒精留塔31による能力可変とを合わせ考えると、負荷
の大きい場合は、電磁弁27を閉,37を開とすることによ
り、圧縮機21のバイパス孔44は閉じて循環量は大とな
り、しかも、貯留していた低沸点冷媒が主回路へ流入す
るため能力は大となる。逆に負荷の小さい場合は、電磁
弁27を開,37を閉とすることにより、圧縮機21のバイパ
ス孔44が開き、循環量が減少する。しかも、バイパス孔
44より出た吐出ガスが加熱器25へ流入するため、第1の
副絞り装置30よりの冷媒を加熱し、冷媒精留塔31の前述
の動作によって、貯留器34に低沸点冷媒が貯留してい
き、主回路は高沸点成分に富んだ冷媒が多く流れる。
Considering together with the variable capacity of the refrigerant rectification column 31, when the load is large, by closing the solenoid valve 27 and opening 37, the bypass hole 44 of the compressor 21 is closed and the circulation amount becomes large, Moreover, since the low boiling point refrigerant that has been stored flows into the main circuit, the capacity becomes large. On the contrary, when the load is small, by opening the solenoid valve 27 and closing 37, the bypass hole 44 of the compressor 21 is opened and the circulation amount is reduced. Moreover, the bypass hole
Since the discharge gas from 44 flows into the heater 25, the refrigerant from the first auxiliary expansion device 30 is heated, and the low boiling point refrigerant is stored in the reservoir 34 by the above-described operation of the refrigerant rectification column 31. As a result, a large amount of refrigerant rich in high-boiling point flows in the main circuit.

したがって、高沸点成分に富んだ冷媒で、循環量が減少
して、主回路を流れるため、能力はかなり低減させるこ
とができる。しかも、バイパス孔44を通すことにより、
主回路への循環量が減った分相応に電力も低減し、EER
が低下するようなことはないため、従来のような非常に
少ない負荷時でも、圧縮機21をオン,オフするような必
要がなく、EERを高く維持したまま運転することができ
る。また、圧縮機を周波数可変装置で運転することによ
って、さらに広い能力可変が可能となり負荷対応の幅も
さらに広がる。
Therefore, since the refrigerant rich in high-boiling components reduces the circulation amount and flows through the main circuit, the capacity can be considerably reduced. Moreover, by passing the bypass hole 44,
Electricity is reduced correspondingly to the amount of circulation to the main circuit, and EER
Does not decrease, so it is not necessary to turn the compressor 21 on and off even when the load is very small as in the conventional case, and it is possible to operate with EER kept high. In addition, by operating the compressor with a frequency variable device, it is possible to further broaden the capacity and expand the range of load compatibility.

発明の効果 以上の如く本発明は、非共沸混合冷媒を用い、冷媒精留
塔の加熱源として、圧縮機内の圧縮途中の冷媒ガスの一
部を用いたため、EERを低下させることなく広い負荷に
対応した能力を発生させることができる。特に、小さい
負荷の際、従来のような圧縮機のオン,オフ等を行なわ
ず、連続運転できることから、従来にも増してEERの向
上を成しとげることができる。
Effects of the Invention As described above, the present invention uses a non-azeotropic mixed refrigerant, and uses a part of the refrigerant gas in the middle of compression in the compressor as a heating source for the refrigerant rectification column, so that a wide load can be achieved without lowering the EER. Can generate the ability corresponding to. In particular, when the load is small, the compressor can be continuously operated without being turned on and off as in the conventional case, so that the EER can be improved more than ever.

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

第1図は本発明の熱ポンプ装置の一実施例を示す冷媒回
路図、第2図は第1図における圧縮機内部を示す概略
図、第3図は従来例の熱ポンプ装置の冷媒回路図であ
る。 1,21……圧縮機、5,25……加熱器、6,26……吐出ガスバ
イパス回路、7,17,27,37……電磁弁、11,31……冷媒精
留塔、14,34……貯留器、44……バイパス孔。
FIG. 1 is a refrigerant circuit diagram showing an embodiment of the heat pump device of the present invention, FIG. 2 is a schematic diagram showing the inside of the compressor in FIG. 1, and FIG. 3 is a refrigerant circuit diagram of a conventional heat pump device. Is. 1,21 …… Compressor, 5,25 …… Heater, 6,26 …… Discharge gas bypass circuit, 7,17,27,37 …… Solenoid valve, 11,31 …… Refrigerant rectification column, 14, 34 …… reservoir, 44 …… bypass hole.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】非共沸混合冷媒を熱冷媒とし、圧縮機、凝
縮器、主絞り装置、蒸発器等を環状に接続して主回路と
なし、下部を加熱器および第1副絞り装置を介して前記
凝縮器出口に接続し、同じく下部を第2副絞り装置を介
して蒸発器入口と接続した冷媒精留塔を設け、前記精留
分離器の上部と冷却器、貯留器を順に接続して再びその
上部に帰還する回路を設け、前記貯留器の下部を開閉弁
を介して前記第2絞り装置の入口に接続し、前記加熱器
と前記圧縮機のシリンダー内とを開閉弁を介して直接接
続し、前記圧縮機の圧縮途中の冷媒ガスを流入させて前
記第1副絞り装置出口の冷媒と間接的に熱交換し、再
び、前記圧縮機の吸入側に帰還させることを特徴とする
熱ポンプ装置。
1. A non-azeotropic mixed refrigerant is used as a heat refrigerant, and a compressor, a condenser, a main expansion device, an evaporator, etc. are annularly connected to form a main circuit, and a lower part is provided with a heater and a first auxiliary expansion device. A refrigerant rectification column, which is connected to the condenser outlet via the second sub-throttler, is connected to the condenser outlet via the second auxiliary expansion device, and the upper part of the rectification separator is connected to the cooler and the reservoir in order. Then, a circuit for returning to the upper part is provided again, the lower part of the reservoir is connected to the inlet of the second expansion device via an opening / closing valve, and the heater and the inside of the cylinder of the compressor are connected via an opening / closing valve. Direct connection, the refrigerant gas in the middle of compression of the compressor is introduced to indirectly exchange heat with the refrigerant at the outlet of the first auxiliary expansion device, and is returned to the suction side of the compressor again. Heat pump device.
JP61130744A 1986-06-05 1986-06-05 Heat pump device Expired - Fee Related JPH0743176B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61130744A JPH0743176B2 (en) 1986-06-05 1986-06-05 Heat pump device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61130744A JPH0743176B2 (en) 1986-06-05 1986-06-05 Heat pump device

Publications (2)

Publication Number Publication Date
JPS62288451A JPS62288451A (en) 1987-12-15
JPH0743176B2 true JPH0743176B2 (en) 1995-05-15

Family

ID=15041593

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61130744A Expired - Fee Related JPH0743176B2 (en) 1986-06-05 1986-06-05 Heat pump device

Country Status (1)

Country Link
JP (1) JPH0743176B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0239712B2 (en) * 1984-10-25 1990-09-06 Matsushita Electric Ind Co Ltd TEIONSOCHI

Also Published As

Publication number Publication date
JPS62288451A (en) 1987-12-15

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