JP5927633B2 - Air conditioner - Google Patents

Air conditioner Download PDF

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JP5927633B2
JP5927633B2 JP2012244492A JP2012244492A JP5927633B2 JP 5927633 B2 JP5927633 B2 JP 5927633B2 JP 2012244492 A JP2012244492 A JP 2012244492A JP 2012244492 A JP2012244492 A JP 2012244492A JP 5927633 B2 JP5927633 B2 JP 5927633B2
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refrigerant
lubricating oil
accumulator
compressor
oil
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JP2014092339A (en
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横関 敦彦
敦彦 横関
中山 進
進 中山
坪江 宏明
宏明 坪江
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Johnson Controls Hitachi Air Conditioning Technology Hong Kong Ltd
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Johnson Controls Hitachi Air Conditioning Technology Hong Kong Ltd
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Application filed by Johnson Controls Hitachi Air Conditioning Technology Hong Kong Ltd filed Critical Johnson Controls Hitachi Air Conditioning Technology Hong Kong Ltd
Priority to JP2012244492A priority Critical patent/JP5927633B2/en
Priority to CN201310544957.8A priority patent/CN103808070B/en
Priority to ES13191783.3T priority patent/ES2661868T3/en
Priority to EP13191783.3A priority patent/EP2728279B1/en
Priority to CN201610757973.9A priority patent/CN106382768B/en
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    • 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
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • 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
    • F25B31/00Compressor arrangements
    • F25B31/002Lubrication
    • F25B31/004Lubrication oil recirculating arrangements
    • 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
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/006Accumulators
    • 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
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/006Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant containing more than one component
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/12Inflammable refrigerants
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/16Lubrication

Description

本発明は、空気調和機に関する。   The present invention relates to an air conditioner.

空気調和機の冷媒としてHFC系冷媒を用い、冷凍機油として冷媒と相溶性のあるエーテル油を用いる技術は知られている(特許文献1)。また、HFC系冷媒であるR32は、圧縮機の吐出温度が従来の冷媒R410Aよりも10〜15℃高くなるため、吐出温度を抑制すべく、圧縮機入口の冷媒かわき度を0.65以上かつ0.85以下にする技術も知られている(特許文献2)。   A technique using an HFC-based refrigerant as a refrigerant of an air conditioner and using an ether oil compatible with the refrigerant as a refrigerating machine oil is known (Patent Document 1). Further, R32, which is an HFC-based refrigerant, has a compressor discharge temperature of 10 to 15 ° C. higher than that of the conventional refrigerant R410A. Therefore, in order to suppress the discharge temperature, the refrigerant inlet degree at the compressor inlet is 0.65 or more and There is also known a technique of making the value 0.85 or less (Patent Document 2).

特開平11−325620号公報JP-A-11-325620 特許第3956589号公報Japanese Patent No. 3956589

HFC系冷媒であるR32は、温暖化係数GWP(Global Warming Potentia)の値が低いため、環境に優しい冷媒として期待されている。しかし、冷媒R32と潤滑油との混合特性に着目すると、潤滑油の混合率が少ない場合に相溶性が低下して、潤滑油と液冷媒との二層に分離する領域がある。   R32, which is an HFC-based refrigerant, is expected as an environmentally friendly refrigerant because it has a low global warming potential GWP (Global Warming Potentia). However, paying attention to the mixing characteristics of the refrigerant R32 and the lubricating oil, there is a region where the compatibility is lowered and the lubricating oil and the liquid refrigerant are separated into two layers when the mixing ratio of the lubricating oil is small.

また、冷媒R32は、圧縮機入口側の冷媒かわき度を従来の冷媒であるR410Aよりも小さくなるように制御する。したがって、R32を用いる場合、圧縮機入口側に設けられたアキュムレータ内の液冷媒と潤滑油との混合液の潤滑油混合率が小さくなる。このため、アキュムレータ内で液冷媒と潤滑油とが二層分離しやすくなって、圧縮機へ潤滑油が戻りにくくなる。これによって、圧縮機内の潤滑油が不足して、潤滑不良などが発生し、信頼性が低下する。   Further, the refrigerant R32 controls the refrigerant inlet side refrigerant degree to be smaller than that of the conventional refrigerant R410A. Therefore, when R32 is used, the lubricating oil mixing ratio of the liquid mixture of the liquid refrigerant and the lubricating oil in the accumulator provided on the compressor inlet side becomes small. For this reason, the liquid refrigerant and the lubricating oil are easily separated into two layers in the accumulator, and the lubricating oil is difficult to return to the compressor. As a result, the lubricating oil in the compressor becomes insufficient, causing poor lubrication and the reliability is lowered.

従って、本発明の目的は、液冷媒と潤滑油とが二層に分離するのを抑制し、潤滑不足の発生を低減できるようにした空気調和機を提供することにある。   Accordingly, an object of the present invention is to provide an air conditioner that can prevent liquid refrigerant and lubricating oil from separating into two layers and reduce the occurrence of insufficient lubrication.

上記課題を解決すべく、本発明に係る空気調和機は、室内機と室外機を配管を介して接続し、冷媒を循環させる空気調和機において、冷媒として、R32単独の冷媒またはR32を所定の質量パーセント以上含む混合冷媒を使用し、室外機の有する圧縮機には、液冷媒と潤滑油の二層分離が生じないように所定値以上の潤滑油が混合した冷媒を供給する、ようになっている。   In order to solve the above-described problems, an air conditioner according to the present invention connects an indoor unit and an outdoor unit through a pipe and circulates the refrigerant. A mixed refrigerant containing at least mass percent is used, and the compressor of the outdoor unit is supplied with a refrigerant mixed with a lubricating oil of a predetermined value or more so that two-layer separation between the liquid refrigerant and the lubricating oil does not occur. ing.

室外機は、圧縮機と、該圧縮機の吐出側に接続され、圧縮機から吐出された冷媒中の油を分離して回収する油分離器と、圧縮機の流入側に接続され、冷媒から液冷媒を分離して蓄積し、ガス冷媒を圧縮機に供給するためのアキュムレータと、油分離器で分離した潤滑油をアキュムレータに戻すことで、アキュムレータ内に蓄積される液冷媒と潤滑油との混合液における潤滑油混合率を所定値以上に調整するための供給油量調整部と、を備えてもよい。   The outdoor unit is connected to a compressor and a discharge side of the compressor, and is connected to an oil separator that separates and recovers oil in the refrigerant discharged from the compressor. The liquid refrigerant is separated and accumulated, and the accumulator for supplying the gas refrigerant to the compressor and the lubricating oil separated by the oil separator are returned to the accumulator, so that the liquid refrigerant and the lubricating oil accumulated in the accumulator And a supply oil amount adjusting unit for adjusting the lubricating oil mixing ratio in the mixed liquid to a predetermined value or more.

本発明によれば、液冷媒と潤滑油の二層分離の発生を抑制することができ、潤滑不足を低減して信頼性を高めることができる。   According to the present invention, occurrence of two-layer separation between the liquid refrigerant and the lubricating oil can be suppressed, and insufficient lubrication can be reduced to increase reliability.

空気調和機の回路構成図である。It is a circuit block diagram of an air conditioner. アキュムレータの縦断面図である。It is a longitudinal cross-sectional view of an accumulator. 冷媒R32と潤滑油の混合特性を示す図である。It is a figure which shows the mixing characteristic of refrigerant | coolant R32 and lubricating oil.

以下、図面に基づいて、本発明の実施の形態を説明する。本実施形態では、以下に詳述するように、HFC系冷媒であるR32を少なくとも所定の質量パーセント以上含む冷媒を用いる場合において、所定値以上の潤滑油が混合した冷媒を圧縮機に供給する。詳しくは、圧縮機の流入側に接続されるアキュムレータに蓄積される混合液(液冷媒と潤滑油との混合液)において、潤滑油の混合率を所定値以上に調整する。アキュムレータ内の混合液における潤滑油の混合率を調整するために、圧縮機の吐出側に接続された油分離器で分離された潤滑油をアキュムレータ内に所定の条件を満たすようにして戻す。ここで、本実施形態では、R32を70質量パーセント以上含む混合冷媒を使用する。R32の比率が70質量パーセント以上になると、GWPの値、吸入湿り、油との相溶性などの特性がR32と同等になるためである。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. In this embodiment, as will be described in detail below, when a refrigerant containing at least a predetermined mass percent of R32, which is an HFC refrigerant, is used, a refrigerant mixed with a lubricating oil of a predetermined value or more is supplied to the compressor. Specifically, in the mixed liquid (mixed liquid of liquid refrigerant and lubricating oil) accumulated in the accumulator connected to the inflow side of the compressor, the mixing ratio of the lubricating oil is adjusted to a predetermined value or more. In order to adjust the mixing ratio of the lubricating oil in the mixed liquid in the accumulator, the lubricating oil separated by the oil separator connected to the discharge side of the compressor is returned to the accumulator so as to satisfy a predetermined condition. Here, in this embodiment, a mixed refrigerant containing 70 mass% or more of R32 is used. This is because, when the ratio of R32 is 70 mass percent or more, characteristics such as GWP value, wetness of suction, compatibility with oil, and the like become equivalent to R32.

本実施形態によれば、アキュムレータ内の冷媒R32と潤滑油との混合液における潤滑油の混合率を調整することで、アキュムレータ内において液冷媒と潤滑油とが二層分離するのを抑制することができる。この結果、アキュムレータから圧縮機に供給される冷媒中に含まれる潤滑油の量を増加させて、圧縮機内で潤滑油が不足する事態の発生を低減でき、圧縮機および空気調和機の信頼性を向上することができる。   According to this embodiment, the liquid refrigerant and the lubricating oil are prevented from being separated into two layers in the accumulator by adjusting the mixing ratio of the lubricating oil in the mixed liquid of the refrigerant R32 and the lubricating oil in the accumulator. Can do. As a result, the amount of lubricating oil contained in the refrigerant supplied from the accumulator to the compressor can be increased, reducing the occurrence of a shortage of lubricating oil in the compressor, and improving the reliability of the compressor and the air conditioner. Can be improved.

図1〜図3を用いて実施例を説明する。図1は、本実施例に係る空気調和機1の冷凍サイクルの構成例を示す。   Embodiments will be described with reference to FIGS. FIG. 1 shows a configuration example of a refrigeration cycle of an air conditioner 1 according to the present embodiment.

空気調和機1の有する冷凍サイクルは、少なくとも一つの室外機100と、少なくとも一つの室内機200とを備える。図1では、複数の室内機200A,200Bを示すが、特に区別しない場合は、室内機200と呼ぶ。図1では、一つの室外機100と2つの室内機200とを接続する例を示すが、これに限らず、2つ以上の室外機100と3つ以上の室内機200とを接続する構成でもよい。   The refrigeration cycle of the air conditioner 1 includes at least one outdoor unit 100 and at least one indoor unit 200. In FIG. 1, a plurality of indoor units 200 </ b> A and 200 </ b> B are shown. Although FIG. 1 shows an example in which one outdoor unit 100 and two indoor units 200 are connected, the present invention is not limited to this, and a configuration in which two or more outdoor units 100 and three or more indoor units 200 are connected is also possible. Good.

室外機100は、例えば、室外熱交換器101、室外ファン102、室外膨張弁103、圧縮機104、アキュムレータ105、オイルセパレータ106、返油キャピラリ107、四方弁108、過冷却熱交換器109、過冷却バイパス膨張弁110および各配管112〜117を含んで構成されている。   The outdoor unit 100 includes, for example, an outdoor heat exchanger 101, an outdoor fan 102, an outdoor expansion valve 103, a compressor 104, an accumulator 105, an oil separator 106, an oil return capillary 107, a four-way valve 108, a supercooling heat exchanger 109, The cooling bypass expansion valve 110 and the pipes 112 to 117 are included.

室内機200は、例えば、室内熱交換器201、室内ファン202、室内膨張弁203を含んで構成されている。室外機100と室内機200とは、液配管121とガス配管302で接続されている。   The indoor unit 200 includes, for example, an indoor heat exchanger 201, an indoor fan 202, and an indoor expansion valve 203. The outdoor unit 100 and the indoor unit 200 are connected by a liquid pipe 121 and a gas pipe 302.

ここで、本実施例では、R32だけから構成される冷媒、または、R32を70質量パーセント以上含む混合冷媒を使用する。次に動作を説明する。   Here, in the present embodiment, a refrigerant composed of only R32 or a mixed refrigerant containing R32 in an amount of 70% by mass or more is used. Next, the operation will be described.

圧縮機104は、例えばクランクケースと、クランクケース内に設けられる圧縮機本体(いずれも図示せず)とを備え、クランクケースの底部側には潤滑油が蓄積される。圧縮機本体による圧縮動作中に、クランクケース内の潤滑油がポンプ作用で吸い上げられて、潤滑の必要な箇所に供給される。潤滑油の一部は、冷媒と一緒に吐出配管112に吐出される。   The compressor 104 includes, for example, a crankcase and a compressor main body (both not shown) provided in the crankcase, and lubricating oil is accumulated on the bottom side of the crankcase. During the compression operation by the compressor main body, the lubricating oil in the crankcase is sucked up by a pump action and supplied to a portion requiring lubrication. A part of the lubricating oil is discharged to the discharge pipe 112 together with the refrigerant.

圧縮機104には、アキュムレータ105から配管117を介して、低圧ガス状の冷媒が流入する。圧縮機104は冷媒を圧縮することで、高温で高圧のガス状冷媒を吐出口から吐出する。圧縮機104の吐出口から配管112内に吐出された高圧ガス状の冷媒は、配管112を介して「油分離器」としてのオイルセパレータ106に流入する。圧縮機104から吐出される高温で高圧のガス状冷媒には、潤滑油が混じっている。   A low-pressure gaseous refrigerant flows into the compressor 104 through the pipe 117 from the accumulator 105. The compressor 104 compresses the refrigerant to discharge a high-temperature and high-pressure gaseous refrigerant from the discharge port. The high-pressure gaseous refrigerant discharged from the discharge port of the compressor 104 into the pipe 112 flows into the oil separator 106 as an “oil separator” through the pipe 112. Lubricating oil is mixed in the high-temperature and high-pressure gaseous refrigerant discharged from the compressor 104.

オイルセパレータ106は、高圧ガス状の冷媒に含まれる潤滑油を回収し、回収した潤滑油を返油キャピラリ107および配管116を介してアキュムレータ105に戻す。配管116は、四方弁108の圧縮機流入口側のポートとアキュムレータ105の流入口を接続するための管路である。「供給油量調整部」の例である返油キャピラリ107は、オイルセパレータ106からアキュムレータ105に戻される潤滑油の流量および圧力を調整するための装置である。   The oil separator 106 collects the lubricating oil contained in the high-pressure gaseous refrigerant and returns the collected lubricating oil to the accumulator 105 through the oil return capillary 107 and the pipe 116. The pipe 116 is a pipe line for connecting the port on the compressor inlet side of the four-way valve 108 and the inlet of the accumulator 105. An oil return capillary 107 as an example of a “supply oil amount adjusting unit” is a device for adjusting the flow rate and pressure of lubricating oil returned from the oil separator 106 to the accumulator 105.

四方弁108は、高圧ガス状の冷媒を室外熱交換器101に導くか、それとも室外機200内の室内熱交換器201に導くかを切り替えるための方向切替弁である。四方弁108は、冷房運転時には、図1中の矢印線Cの方向に高圧ガス状の冷媒を流す。高圧ガス状の冷媒は、四方弁108の室外熱交換器側ポートと室外熱交換器101の入口側とを接続する配管113を介して、凝縮器として働く室外熱交換器101に流入する。   The four-way valve 108 is a direction switching valve for switching whether the high-pressure gaseous refrigerant is led to the outdoor heat exchanger 101 or the indoor heat exchanger 201 in the outdoor unit 200. The four-way valve 108 allows a high-pressure gaseous refrigerant to flow in the direction of the arrow C in FIG. The high-pressure gaseous refrigerant flows into the outdoor heat exchanger 101 that functions as a condenser via a pipe 113 that connects the outdoor heat exchanger side port of the four-way valve 108 and the inlet side of the outdoor heat exchanger 101.

高温高圧のガス状冷媒は、室外熱交換器101を通過する間に、室外ファン102によって送られた室外空気と熱交換して凝縮し、高温高圧の液状冷媒(液冷媒)となる。高温で高圧の液冷媒は、室外熱交換器101の出口側に接続された配管114を介して、室外膨張弁103に流入する。室外膨張弁103から流れ出た低圧の液冷媒は分岐し、その一部の液冷媒は過冷却バイパス膨張弁110に流入する。他の液冷媒は、過冷却熱交換器109を介してさらに冷却されて、配管301に流れ込む。配管301は、室外機100の熱交換器101と室内機200の熱交換器201とを接続する配管である。   While passing through the outdoor heat exchanger 101, the high-temperature and high-pressure gaseous refrigerant is condensed by exchanging heat with outdoor air sent by the outdoor fan 102 to become a high-temperature and high-pressure liquid refrigerant (liquid refrigerant). The high-temperature and high-pressure liquid refrigerant flows into the outdoor expansion valve 103 via the pipe 114 connected to the outlet side of the outdoor heat exchanger 101. The low-pressure liquid refrigerant flowing out of the outdoor expansion valve 103 branches, and a part of the liquid refrigerant flows into the supercooling bypass expansion valve 110. The other liquid refrigerant is further cooled via the supercooling heat exchanger 109 and flows into the pipe 301. The pipe 301 is a pipe that connects the heat exchanger 101 of the outdoor unit 100 and the heat exchanger 201 of the indoor unit 200.

過冷却バイパス膨張弁110へ流れ込んだ液冷媒は、過冷却バイパス膨張弁110で減圧されて、過冷却熱交換器109に流入する。過冷却熱交換器109に流入した液冷媒は、過冷却熱交換器109を通過する間に、他の液冷媒と熱交換して蒸発し、低圧ガス状の冷媒となる。低圧ガス状の冷媒は、配管116に接続される戻し管路115を介して、アキュムレータ105に流れ込む。   The liquid refrigerant flowing into the supercooling bypass expansion valve 110 is decompressed by the supercooling bypass expansion valve 110 and flows into the supercooling heat exchanger 109. The liquid refrigerant that has flowed into the supercooling heat exchanger 109 evaporates by exchanging heat with other liquid refrigerant while passing through the supercooling heat exchanger 109 to become a low-pressure gaseous refrigerant. The low-pressure gaseous refrigerant flows into the accumulator 105 via a return pipe line 115 connected to the pipe 116.

室内機200へ送られた低圧の液冷媒は、室内膨張弁203で減圧されて、室内熱交換器201に流入する。室内熱交換器201に流入した低圧の液冷媒は、室内熱交換器201を通過する間に室内ファン202によって送られた室内空気と熱交換して蒸発し、ガス状の冷媒(ガス冷媒)となる。   The low-pressure liquid refrigerant sent to the indoor unit 200 is decompressed by the indoor expansion valve 203 and flows into the indoor heat exchanger 201. The low-pressure liquid refrigerant that has flowed into the indoor heat exchanger 201 evaporates by exchanging heat with the indoor air sent by the indoor fan 202 while passing through the indoor heat exchanger 201, and a gaseous refrigerant (gas refrigerant). Become.

低圧の液冷媒が室内熱交換器201内で気化するときに、室内の空気が冷却されて、室内が冷房される。室内熱交換器201から流れ出たガス冷媒は、ガス配管302を介して室外機100に送られる。   When the low-pressure liquid refrigerant is vaporized in the indoor heat exchanger 201, the indoor air is cooled and the room is cooled. The gas refrigerant flowing out from the indoor heat exchanger 201 is sent to the outdoor unit 100 via the gas pipe 302.

室外機100に入ったガス冷媒は、四方弁108および配管116を通って、アキュムレータ105に流入する。アキュムレータ105は、蒸発しなかった液冷媒を蓄積することで、液冷媒が圧縮機104に流入するのを阻止する。圧縮機104が液冷媒を圧縮すると、圧縮機104の部品が破損等する可能性があるためである。   The gas refrigerant that has entered the outdoor unit 100 flows into the accumulator 105 through the four-way valve 108 and the pipe 116. The accumulator 105 prevents the liquid refrigerant from flowing into the compressor 104 by accumulating the liquid refrigerant that has not evaporated. This is because if the compressor 104 compresses the liquid refrigerant, parts of the compressor 104 may be damaged.

アキュムレータ105には、ガス状の冷媒、液冷媒、オイルセパレータ106から戻される潤滑油が流入する。アキュムレータ105内でガス冷媒と潤滑油とは混合し、圧縮機104に送られる。液冷媒は、アキュムレータ105に滞留する。   A gaseous refrigerant, liquid refrigerant, and lubricating oil returned from the oil separator 106 flow into the accumulator 105. The gas refrigerant and lubricating oil are mixed in the accumulator 105 and sent to the compressor 104. The liquid refrigerant stays in the accumulator 105.

暖房運転時の動作を説明する。暖房運転時の冷媒の流れを矢印線Hで示す。圧縮機104から吐出した高温高圧のガス冷媒は、オイルセパレータ106で潤滑油が分離された後、四方弁108を通ってガス配管302へ送られる。オイルセパレータ106で分離された潤滑油は、返油キャピラリ107を通ってアキュムレータ105へ送られる。   The operation during heating operation will be described. The flow of the refrigerant during the heating operation is indicated by an arrow line H. The high-temperature and high-pressure gas refrigerant discharged from the compressor 104 is sent to the gas pipe 302 through the four-way valve 108 after the lubricating oil is separated by the oil separator 106. The lubricating oil separated by the oil separator 106 is sent to the accumulator 105 through the oil return capillary 107.

室外機100からの高温高圧のガス冷媒は、ガス配管302を介して室内機200へ送られる。室内機200へ入った高温のガス冷媒は、室内熱交換器201内を流れる間に、室内ファン202によって送られた室内空気と熱交換して凝縮し、液冷媒となる。液冷媒は、室内膨張弁203を通って室内機200から出る。室内熱交換器200で高温高圧のガス冷媒と室内空気が熱交換することによって、暖房が行われる。   The high-temperature and high-pressure gas refrigerant from the outdoor unit 100 is sent to the indoor unit 200 via the gas pipe 302. While flowing through the indoor heat exchanger 201, the high-temperature gas refrigerant that has entered the indoor unit 200 exchanges heat with the indoor air sent by the indoor fan 202 and becomes liquid refrigerant. The liquid refrigerant exits the indoor unit 200 through the indoor expansion valve 203. Heating is performed by heat exchange between the high-temperature and high-pressure gas refrigerant and room air in the indoor heat exchanger 200.

室内機200を出た液冷媒は、液配管301を介して室外機100へ流れる。室外機100へ入った液冷媒は室外膨張弁103を通過後、2つに分岐する。一部の液冷媒は過冷却バイパス膨張弁110へ流れ、配管115,116を介してアキュムレータ105に送られる。   The liquid refrigerant that has exited the indoor unit 200 flows to the outdoor unit 100 via the liquid pipe 301. The liquid refrigerant that has entered the outdoor unit 100 passes through the outdoor expansion valve 103 and then branches into two. A part of the liquid refrigerant flows to the supercooling bypass expansion valve 110 and is sent to the accumulator 105 via the pipes 115 and 116.

他の液冷媒は室外膨張弁103で減圧された後、室外熱交換器101に流入する。室外熱交換器101に流入した液冷媒は、室外熱交換器101を流れる間に、室外ファン102によって送られた室外空気と熱交換して蒸発し、ガス冷媒になる。ガス冷媒は、四方弁108を通り、配管116を介してアキュムレータ105に流入する。アキュムレータ105には、上述の通り、ガス冷媒と潤滑油が流入して混合し、潤滑油の溶け込んだガス冷媒が圧縮機104に送られる。   The other liquid refrigerant is decompressed by the outdoor expansion valve 103 and then flows into the outdoor heat exchanger 101. The liquid refrigerant that has flowed into the outdoor heat exchanger 101 evaporates by exchanging heat with outdoor air sent by the outdoor fan 102 while flowing through the outdoor heat exchanger 101, and becomes a gas refrigerant. The gas refrigerant passes through the four-way valve 108 and flows into the accumulator 105 through the pipe 116. As described above, the gas refrigerant and the lubricating oil flow into the accumulator 105 and mix, and the gas refrigerant in which the lubricating oil is dissolved is sent to the compressor 104.

図2は、図1の冷凍サイクルの室外機100に示すアキュムレータ105を示すものである。   FIG. 2 shows the accumulator 105 shown in the outdoor unit 100 of the refrigeration cycle of FIG.

アキュムレータ105内には、導入用の配管116(導入管)と導出用の配管117(導出管)とが挿入されて取り付けられている。導入管116は、ガス冷媒および/または潤滑油をアキュムレータ105内に導入するための配管である。   In the accumulator 105, an introduction pipe 116 (introduction pipe) and a lead-out pipe 117 (outlet pipe) are inserted and attached. The introduction pipe 116 is a pipe for introducing a gas refrigerant and / or lubricating oil into the accumulator 105.

導出管117は、先端側が略U字状となっており、アキュムレータ105から潤滑油の混合したガス冷媒を圧縮機104に送るための配管である。導出管117は、そのU字状の湾曲部がアキュムレータ105の底部側に位置するようにして取り付けられる。これにより、導出管117のU字状湾曲部は、アキュムレータ105に蓄積された液冷媒に浸される。   The lead-out pipe 117 has a substantially U shape at the tip side, and is a pipe for sending a gas refrigerant mixed with lubricating oil from the accumulator 105 to the compressor 104. The lead-out tube 117 is attached so that the U-shaped curved portion is positioned on the bottom side of the accumulator 105. As a result, the U-shaped curved portion of the outlet pipe 117 is immersed in the liquid refrigerant accumulated in the accumulator 105.

導出管117のU字状湾曲部には、第1の液戻し口121Aが形成されている。さらに、導出管117には、第1の液戻し口121Aよりも上側に位置して、第2の液戻し口121Bが形成されている。導出管117の上側には、アキュムレータ105内の上側に位置して、導出管117内の圧力を調整するための均圧穴122が形成されている。   A first liquid return port 121 </ b> A is formed in the U-shaped curved portion of the outlet pipe 117. Further, the outlet pipe 117 is formed with a second liquid return port 121B located above the first liquid return port 121A. A pressure equalizing hole 122 for adjusting the pressure in the outlet pipe 117 is formed on the upper side of the outlet pipe 117 and is positioned on the upper side in the accumulator 105.

導入管116からアキュムレータ105内に流入した冷媒と潤滑油は、液とガスとに分離する。ガス冷媒は、導出管117を介して圧縮機104に送られる。ガス冷媒の流通により、第1の液戻し口121Aから導出管117内に液が吸い込まれて、所定の液混合率でアキュムレータ105から圧縮機104へ送られる。   The refrigerant and lubricating oil flowing into the accumulator 105 from the introduction pipe 116 are separated into liquid and gas. The gas refrigerant is sent to the compressor 104 through the outlet pipe 117. Due to the circulation of the gas refrigerant, the liquid is sucked into the outlet pipe 117 from the first liquid return port 121A and is sent from the accumulator 105 to the compressor 104 at a predetermined liquid mixing ratio.

アキュムレータ105の液面が第2の液戻し口121Bよりも上に位置すると、第2の液戻し口121Bからも液が吸い込まれて、液混合率が増加する。液混合率は、2つの液戻し口121A,121Bの穴径と、均圧穴122の穴径とによって調整される。   When the liquid level of the accumulator 105 is positioned above the second liquid return port 121B, the liquid is also sucked from the second liquid return port 121B, and the liquid mixing rate increases. The liquid mixing ratio is adjusted by the hole diameters of the two liquid return ports 121A and 121B and the hole diameter of the pressure equalizing hole 122.

ここで、本実施例では、冷媒を従来のR410Aから温暖化係数のより小さいR32に変更している。R32を冷媒として用いると、圧縮機104の吐出温度が10〜15℃高くなる。本実施例では、吐出温度の上昇を抑制するために、圧縮機104の入り口かわき度を従来よりも小さく設定する。   Here, in this embodiment, the refrigerant is changed from the conventional R410A to R32 having a smaller warming coefficient. When R32 is used as a refrigerant, the discharge temperature of the compressor 104 increases by 10 to 15 ° C. In the present embodiment, in order to suppress an increase in the discharge temperature, the entrance degree of the compressor 104 is set to be smaller than that in the prior art.

そのために、本実施例のアキュムレータ105は、液冷媒を従来冷媒R410Aより多く蓄積する。アキュムレータ105が従来よりも多くの液冷媒を蓄積すると、アキュムレータ105内の下部に溜まる混合液における潤滑油混合率が小さくなる。   Therefore, the accumulator 105 of the present embodiment accumulates more liquid refrigerant than the conventional refrigerant R410A. When the accumulator 105 accumulates more liquid refrigerant than before, the lubricating oil mixing ratio in the mixed liquid that accumulates in the lower part of the accumulator 105 decreases.

図3は、冷媒としてR32を用いた場合の、冷媒と潤滑油の混合特性を示す。冷媒R32において、潤滑油の混合比率が40%以下になると、低温域で液冷媒と潤滑油との二層分離域が現れる。つまり、アキュムレータ105の下側に液冷媒が溜まり、液冷媒の層の上に潤滑油の層ができる。   FIG. 3 shows the mixing characteristics of refrigerant and lubricating oil when R32 is used as the refrigerant. In the refrigerant R32, when the mixing ratio of the lubricating oil is 40% or less, a two-layer separation region of the liquid refrigerant and the lubricating oil appears in the low temperature region. That is, the liquid refrigerant is accumulated below the accumulator 105, and a lubricating oil layer is formed on the liquid refrigerant layer.

二層分離域の条件が成立すると、アキュムレータ105の下側で混合液が液冷媒と潤滑油とに分離する。潤滑油の密度が液冷媒の密度よりも小さければ、潤滑油が上側に浮くことになる。潤滑油が液冷媒の上側に浮くと、第1の液戻し口121Aから導出管117内に潤滑油が吸い込まれなくなり、圧縮機104に供給される潤滑油の量が低下する。圧縮機104に送られる潤滑油の量が少なくなると、潤滑不良などの問題を生じて信頼性が低下する可能性がある。   When the condition of the two-layer separation zone is satisfied, the mixed liquid is separated into the liquid refrigerant and the lubricating oil below the accumulator 105. If the density of the lubricating oil is smaller than the density of the liquid refrigerant, the lubricating oil will float upward. When the lubricating oil floats above the liquid refrigerant, the lubricating oil is not sucked into the outlet pipe 117 from the first liquid return port 121A, and the amount of lubricating oil supplied to the compressor 104 decreases. If the amount of lubricating oil sent to the compressor 104 decreases, problems such as poor lubrication may occur and reliability may decrease.

そこで、本実施例では、オイルセパレータ106で回収した潤滑油が所定量以上、アキュムレータ105に戻るように、返油キャピラリ107の形状(管路面積、管路長など)を設定する。その調整方法を以下に示す。   Therefore, in this embodiment, the shape (pipe area, pipe length, etc.) of the oil return capillary 107 is set so that the lubricating oil recovered by the oil separator 106 returns to the accumulator 105 by a predetermined amount or more. The adjustment method is shown below.

アキュムレータ105から圧縮機104へ流れる液比率をR(=(冷媒液流量+潤滑油流量)/(冷媒全流量)、アキュムレータ105内の液冷媒と潤滑油との混合液の二層分離限界(混合液の溶解域と分離域との境界)の潤滑油混合率をn(=潤滑油量/冷媒液量)、返油キャピラリ107を流れる潤滑油返油率x(=潤滑油流量/冷媒全流量)、オイルセパレータ106から冷凍サイクルへ流れる潤滑油循環率y(=潤滑油流量/冷媒全流量)とする。   The ratio of the liquid flowing from the accumulator 105 to the compressor 104 is R (= (refrigerant liquid flow rate + lubricating oil flow rate) / (refrigerant total flow rate), and the two-layer separation limit of the mixed liquid of the liquid refrigerant and the lubricating oil in the accumulator 105 (mixing) The lubricating oil mixing rate in the liquid dissolution zone and the separation zone) is n (= lubricating oil amount / refrigerant liquid amount), and the lubricating oil return rate x (= lubricating oil flow rate / refrigerant total flow rate) flowing through the oil return capillary 107. ), And the lubricating oil circulation rate y (= lubricating oil flow rate / refrigerant total flow rate) flowing from the oil separator 106 to the refrigeration cycle.

返油キャピラリ107を流れる潤滑油返油率xは、下記(1)式で求められる。
x≧n×R−y・・・(1)
The lubricating oil return rate x flowing through the return oil capillary 107 is obtained by the following equation (1).
x ≧ n × R−y (1)

図3に示す特性の場合、潤滑油の混合比率を40%(n=0.4)以上、好ましくは50%(n=0.5)以上にすれば、二層分離の発生を抑制できると考えられる。そこで、上記の(2)式は、
x≧0.5×R−y・・・(2)
となる。
In the case of the characteristics shown in FIG. 3, if the mixing ratio of the lubricating oil is 40% (n = 0.4) or more, preferably 50% (n = 0.5) or more, the occurrence of two-layer separation can be suppressed. Conceivable. Therefore, the above equation (2) is
x ≧ 0.5 × R−y (2)
It becomes.

なお、アキュムレータ105から圧縮機104に流れる液比率Rは、アキュムレータ105の導出管117の液戻し口121A、121Bの穴径と均圧穴122の穴径とによって調整される。また、オイルセパレータ106から冷凍サイクルへ流れる潤滑油循環率yは、圧縮機104とオイルセパレータ106の特性によって決まる。   The ratio R of the liquid flowing from the accumulator 105 to the compressor 104 is adjusted by the hole diameters of the liquid return ports 121A and 121B of the outlet pipe 117 of the accumulator 105 and the hole diameter of the pressure equalizing hole 122. The lubricating oil circulation rate y flowing from the oil separator 106 to the refrigeration cycle is determined by the characteristics of the compressor 104 and the oil separator 106.

このように冷媒としてR32を使用すると、アキュムレータ105に蓄積する液冷媒量を増加させる必要があり、その結果、潤滑油混合率が低下する。しかし、本実施例では、オイルセパレータ106で回収した潤滑油を、従来よりも多くアキュムレータ105に戻すため、アキュムレータ105内の潤滑油混合率を所定値(40%以上、好ましくは50%以上)に高めることができる。したがって、本実施例によれば、アキュムレータ105内で二層分離域の発生条件が成立するのを阻止して、液冷媒と潤滑油が分離するのを抑制し、圧縮機104に十分な潤滑油を送り込むことができる。   Thus, when R32 is used as the refrigerant, it is necessary to increase the amount of liquid refrigerant accumulated in the accumulator 105, and as a result, the lubricating oil mixing ratio is lowered. However, in this embodiment, since the lubricating oil recovered by the oil separator 106 is returned to the accumulator 105 more than before, the lubricating oil mixing ratio in the accumulator 105 is set to a predetermined value (40% or more, preferably 50% or more). Can be increased. Therefore, according to the present embodiment, it is possible to prevent the generation condition of the two-layer separation zone in the accumulator 105 from being satisfied, thereby suppressing the separation of the liquid refrigerant and the lubricating oil, and sufficient lubricating oil for the compressor 104. Can be sent in.

なお、本発明は、上述した実施例に限定されない。当業者であれば、本発明の範囲内で、種々の追加や変更等を行うことができる。例えば、オイルセパレータからアキュムレータに潤滑油を戻す手段は、返油キャピラリに限定されず、他の手段を用いてもよい。また、本発明は、例えば「空気調和機に使用される室外機であって、冷媒として、R32単独の冷媒またはR32を所定の質量パーセント以上含む混合冷媒を使用し、圧縮機には、液冷媒と潤滑油の二層分離が生じないように所定値以上の潤滑油が混合した冷媒を供給する、空気調和機用の室外機。」として表現することもできる。   In addition, this invention is not limited to the Example mentioned above. A person skilled in the art can make various additions and changes within the scope of the present invention. For example, the means for returning the lubricating oil from the oil separator to the accumulator is not limited to the oil return capillary, and other means may be used. Further, the present invention provides, for example, “an outdoor unit used in an air conditioner, wherein R32 alone or a mixed refrigerant containing R32 in a predetermined mass percentage or more is used as the refrigerant, and the compressor is a liquid refrigerant. It can also be expressed as an outdoor unit for an air conditioner that supplies a refrigerant mixed with a lubricating oil of a predetermined value or more so that two-layer separation between the lubricating oil and the lubricating oil does not occur.

1:空気調和機、100:室外機、101:室外熱交換器、103:室外膨張弁、104:圧縮機、105:アキュムレータ、106:オイルセパレータ、107:返油キャピラリ、108:四方弁、109:過冷却熱交換器   1: air conditioner, 100: outdoor unit, 101: outdoor heat exchanger, 103: outdoor expansion valve, 104: compressor, 105: accumulator, 106: oil separator, 107: oil return capillary, 108: four-way valve, 109 : Supercooling heat exchanger

Claims (4)

室内機と室外機を配管を介して接続し、冷媒を循環させる空気調和機において、
前記冷媒として、R32単独の冷媒またはR32を所定の質量パーセント以上含む混合冷媒を使用し、
前記室外機の有する圧縮機には、液冷媒と潤滑油の二層分離が生じないように所定値以上の潤滑油が混合した冷媒を供給する、
空気調和機。
In an air conditioner that connects an indoor unit and an outdoor unit via a pipe and circulates a refrigerant,
As the refrigerant, R32 single refrigerant or a mixed refrigerant containing R32 in a predetermined mass percent or more,
The compressor of the outdoor unit is supplied with a refrigerant mixed with a lubricating oil of a predetermined value or more so that two-layer separation between the liquid refrigerant and the lubricating oil does not occur.
Air conditioner.
前記室外機は、
前記圧縮機と、
該圧縮機の吐出側に接続され、前記圧縮機から吐出された冷媒中の油を分離して回収する油分離器と、
前記圧縮機の流入側に接続され、冷媒から液冷媒を分離して蓄積し、ガス冷媒を前記圧縮機に供給するためのアキュムレータと、
前記油分離器で分離した潤滑油を前記アキュムレータに戻すことで、前記アキュムレータ内に蓄積される液冷媒と潤滑油との混合液における潤滑油混合率を前記所定値以上に調整するための供給油量調整部と、
を備える請求項1に記載の空気調和機。
The outdoor unit is
The compressor;
An oil separator connected to the discharge side of the compressor and separating and recovering oil in the refrigerant discharged from the compressor;
An accumulator connected to the inflow side of the compressor, separating and storing liquid refrigerant from the refrigerant, and supplying gas refrigerant to the compressor;
Supply oil for adjusting the lubricating oil mixing ratio in the mixed liquid of the liquid refrigerant and lubricating oil accumulated in the accumulator to the predetermined value or more by returning the lubricating oil separated by the oil separator to the accumulator An amount adjustment unit;
An air conditioner according to claim 1.
前記供給油量調整部により前記油分離器から前記アキュムレータに戻される潤滑油の返油率をx(x=潤滑油流量/冷媒全流量)、
前記アキュムレータから前記圧縮機に流れる混合液の比率をR(R=(液冷媒流量+潤滑油流量)/冷媒全流量)、
前記アキュムレータ内の液冷媒と潤滑油との混合液が二層に分離する限界の潤滑油混合率をn(n=潤滑油量/液冷媒量)、
前記油分離器から冷凍サイクル流れる潤滑油の循環率をy(y=潤滑油流量/冷媒全流量)としたとき、x≧n・R−yが成立する、
請求項2に記載の空気調和機。
X (x = lubricant oil flow rate / refrigerant total flow rate), the return rate of the lubricating oil returned from the oil separator to the accumulator by the supply oil amount adjustment unit,
The ratio of the mixed liquid flowing from the accumulator to the compressor is R (R = (liquid refrigerant flow rate + lubricant oil flow rate) / refrigerant total flow rate),
N (n = lubricating oil amount / liquid refrigerant amount), the limit lubricating oil mixing ratio at which the mixed liquid of the liquid refrigerant and lubricating oil in the accumulator is separated into two layers,
When the circulation ratio of the lubricating oil flowing from the oil separator to a refrigeration cycle was y (y = lubricating oil flow rate / coolant total flow), x ≧ n · R- y is satisfied,
The air conditioner according to claim 2.
前記nの値を0.4以上に設定する、
請求項3に記載の空気調和機。
The value of n is set to 0.4 or more,
The air conditioner according to claim 3.
JP2012244492A 2012-11-06 2012-11-06 Air conditioner Active JP5927633B2 (en)

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