JP6054269B2 - Refrigeration cycle apparatus and refrigerator using the same - Google Patents

Refrigeration cycle apparatus and refrigerator using the same Download PDF

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JP6054269B2
JP6054269B2 JP2013177471A JP2013177471A JP6054269B2 JP 6054269 B2 JP6054269 B2 JP 6054269B2 JP 2013177471 A JP2013177471 A JP 2013177471A JP 2013177471 A JP2013177471 A JP 2013177471A JP 6054269 B2 JP6054269 B2 JP 6054269B2
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refrigerant
gas
mixer
expansion valve
liquid
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JP2015045467A (en
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研 石川
研 石川
博史 八田
博史 八田
信浩 佐野
信浩 佐野
直樹 西尻
直樹 西尻
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Johnson Controls Hitachi Air Conditioning Technology Hong Kong Ltd
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Description

本発明は、冷凍サイクル装置及びこれを用いた冷凍機に関する。   The present invention relates to a refrigeration cycle apparatus and a refrigerator using the same.

従来技術では、性能向上の一環として、蒸発器の蒸発性能を高めるために、複数の伝熱面への冷媒分配を均一化する手段を講じてきた。また、膨張弁の形状による膨張弁出口の方向性により、蒸発器に至るまでに配管ルートに曲がり部が必要となる場合があり、この曲がり部によって密度差から気液が分離されるため、曲がり部から蒸発器までの直管部の長さについて配慮が必要な場合があった。   In the prior art, as part of the performance improvement, in order to improve the evaporation performance of the evaporator, a means for uniformizing the refrigerant distribution to the plurality of heat transfer surfaces has been taken. Also, depending on the direction of the expansion valve outlet due to the shape of the expansion valve, a bent part may be required in the piping route to reach the evaporator, and gas and liquid are separated from the density difference by this bent part. In some cases, it was necessary to consider the length of the straight pipe section from the section to the evaporator.

これに対して、図4に示すように、各伝熱面に冷媒が分配されるように各伝熱面の入口(膨張弁と蒸発器の間)に分配を促進するための部品(例えばオリフィス)を配置して、気液の混合を促進するものがある。   On the other hand, as shown in FIG. 4, a part (for example, an orifice) for promoting distribution to the inlet (between the expansion valve and the evaporator) of each heat transfer surface so that the refrigerant is distributed to each heat transfer surface ) To promote gas-liquid mixing.

このような従来技術では、圧損により冷媒を減圧気化させて、複数の各伝熱面への冷媒分配を均一化する。従って、圧損を増大させる部品により冷媒の流れにおいて1次側にある膨張弁は、本来必要とする減圧膨張量よりも抑える必要があり、そのため弁のサイズを大きくする必要がある。   In such a conventional technique, the refrigerant is reduced in pressure by pressure loss, and the refrigerant distribution to each of the plurality of heat transfer surfaces is made uniform. Therefore, the expansion valve on the primary side in the flow of the refrigerant due to the component that increases the pressure loss needs to be suppressed more than the originally required decompression expansion amount, and therefore the size of the valve needs to be increased.

近年では、より実質に則した省エネ性の評価として、使用頻度の高い状況となる部分負荷に重きを置いた期間効率の考え方があり、仕様点から部分負荷にかけて効率を上げるために蒸発温度を上げる手段が必要となる。このために従来では、部分負荷で仕様点と比べて伝熱面積が余剰となることにより、冷媒の分配が悪化していた点を改善する必要がある。   In recent years, there has been a concept of period efficiency focusing on the partial load that is frequently used as an evaluation of energy saving more in line with the real situation, and raising the evaporation temperature to increase the efficiency from the specification point to the partial load Means are needed. For this reason, conventionally, it is necessary to improve the point that the distribution of the refrigerant has deteriorated due to the surplus heat transfer area compared to the specification point at the partial load.

また、性能向上のための手段として、蒸発温度を上げるために、蒸発器の伝熱面を増やす傾向にあるが、この場合も同様に、増やした伝熱面を充分に活用するために冷媒の分配に関する配慮が必要となる。   In addition, as a means for improving performance, there is a tendency to increase the heat transfer surface of the evaporator in order to increase the evaporation temperature. In this case as well, in order to fully utilize the increased heat transfer surface, Consideration regarding distribution is required.

効率向上のために蒸発温度を上げる手段として伝熱面を増やす一方で、冷媒の分配が悪化することで伝熱面を増やした効果が充分には得られず、従来の分配では伝熱面積を有効に活用できていなかった。   While increasing the heat transfer surface as a means to increase the evaporation temperature to improve efficiency, the effect of increasing the heat transfer surface cannot be obtained sufficiently due to the deterioration of refrigerant distribution. It was not used effectively.

特許3879032号公報Japanese Patent No. 3879032

本発明は、蒸発器に入る前の冷媒について気液混合を促進することにより、蒸発器伝熱面に均質な冷媒を供給して蒸発器伝熱面を有効に活用し、冷凍サイクル装置の効率を向上させることを課題とする。   The present invention promotes gas-liquid mixing for the refrigerant before entering the evaporator, thereby supplying a homogeneous refrigerant to the evaporator heat transfer surface and effectively utilizing the evaporator heat transfer surface, thereby improving the efficiency of the refrigeration cycle apparatus. It is an object to improve.

本発明の冷凍サイクル装置は、冷媒を圧縮する圧縮機と、前記圧縮機で圧縮された冷媒を凝縮させる凝縮器と、前記凝縮器で凝縮された冷媒を減圧する膨張弁と、前記膨張弁で減圧された気液冷媒を混合する気液混合器と、前記気液混合器で混合された冷媒を蒸発させる蒸発器と、を備え、前記気液混合器は、混合器外径部と、前記混合器外径部内の流路断面全体に形成され流れ方向に沿った複数の冷媒流路とを有し、前記複数の冷媒流路は、流れ方向に沿った複数の穴が点対称に配置されて構成されていることを特徴とする
本発明の冷凍サイクル装置の他の特徴は、冷媒を圧縮する圧縮機と、前記圧縮機で圧縮された冷媒を凝縮させる凝縮器と、前記凝縮器で凝縮された冷媒を減圧する膨張弁と、前記膨張弁で減圧された気液冷媒を混合する気液混合器と、前記気液混合器で混合された冷媒を蒸発させる蒸発器と、を備え、前記気液混合器は、混合器外径部と、前記混合器外径部内の流路断面全体に形成され流れ方向に沿った複数の冷媒流路とを有し、前記複数の冷媒流路は、前記混合器外径部内に配置された十字状の障害物により形成された点対称の4つの冷媒流路により構成されていることにある。
Refrigeration cycle apparatus of the present invention includes a compressor for compressing a refrigerant, a condenser for condensing the refrigerant compressed by the compressor, an expansion valve for decompressing the refrigerant condensed by the condenser, in the expansion valve a gas-liquid mixer for mixing the decompressed liquid refrigerant, and a vaporizer for vaporizing the mixed refrigerant in the gas-liquid mixer, the gas-liquid mixer, a mixer outside diameter, the A plurality of refrigerant flow paths formed in the entire cross section of the flow path in the outer diameter portion of the mixer and extending in the flow direction, and the plurality of refrigerant flow paths are arranged symmetrically with a plurality of holes along the flow direction. It is characterized by being configured .
Other features of the refrigeration cycle apparatus of the present invention include a compressor that compresses the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that depressurizes the refrigerant condensed by the condenser, A gas-liquid mixer that mixes the gas-liquid refrigerant decompressed by the expansion valve; and an evaporator that evaporates the refrigerant mixed in the gas-liquid mixer, the gas-liquid mixer having an outer diameter of the mixer And a plurality of refrigerant channels formed along the flow direction and formed in the entire cross section of the flow channel in the mixer outer diameter portion, and the plurality of refrigerant flow channels are arranged in the mixer outer diameter portion. The point is that it is composed of four point-symmetric refrigerant flow paths formed by cross-shaped obstacles.

本発明の冷凍サイクル装置においては、膨張弁と蒸発器との間に膨張弁で減圧された気相及び液相の冷媒を混合する気液混合器を備えるので、蒸発器に入る前の冷媒について気液混合を促進することにより、蒸発器伝熱面に均質な冷媒を供給して蒸発器伝熱面を有効に活用し、冷凍サイクル装置の効率を向上させることができる。   In the refrigeration cycle apparatus of the present invention, a gas-liquid mixer that mixes the gas-phase and liquid-phase refrigerant decompressed by the expansion valve is provided between the expansion valve and the evaporator. By promoting gas-liquid mixing, it is possible to supply a homogeneous refrigerant to the evaporator heat transfer surface and effectively utilize the evaporator heat transfer surface, thereby improving the efficiency of the refrigeration cycle apparatus.

第1の実施例の説明図Illustration of the first embodiment 第2の実施例の説明図Explanatory drawing of the second embodiment 気液混合器の構造図Structure diagram of gas-liquid mixer 従来方式の説明図Illustration of conventional method 圧縮式冷凍機のサイクル構成図Cycle configuration diagram of compression refrigerator

本実施例の冷凍サイクル装置は、冷媒を圧縮する圧縮機と、圧縮機で圧縮された冷媒を凝縮させる凝縮器と、凝縮器で凝縮された冷媒を減圧する膨張弁と、膨張弁で減圧された気相及び液相の冷媒を混合する気液混合器と、気液混合器で混合された冷媒を蒸発させる蒸発器と、を備える。本実施例の冷凍サイクル装置においては、膨張弁と蒸発器との間に膨張弁で減圧された気液冷媒を混合する気液混合器を備えるので、蒸発器に入る前の冷媒について気液混合を促進することにより、蒸発器伝熱面に均質な冷媒を供給して蒸発器伝熱面を有効に活用し、冷凍サイクル装置の効率を向上させることができる。   The refrigeration cycle apparatus of the present embodiment includes a compressor that compresses refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that decompresses the refrigerant condensed by the condenser, and a pressure that is reduced by the expansion valve. A gas-liquid mixer for mixing the gas-phase and liquid-phase refrigerants, and an evaporator for evaporating the refrigerant mixed in the gas-liquid mixer. In the refrigeration cycle apparatus of the present embodiment, a gas-liquid mixer that mixes the gas-liquid refrigerant decompressed by the expansion valve is provided between the expansion valve and the evaporator. By promoting the above, it is possible to supply a homogeneous refrigerant to the evaporator heat transfer surface and effectively utilize the evaporator heat transfer surface, thereby improving the efficiency of the refrigeration cycle apparatus.

つまり、気液混合器は、仕様点から部分負荷にかけて蒸発器に入る前の冷媒について気液の混合を促進し、蒸発器伝熱面に均質な冷媒を供給することで、伝熱面を偏り無く有効活用することができる。また、部分負荷時に、従来では冷媒供給の偏りにより活用できなかった伝熱面を、蒸発器伝熱面に均質な冷媒を供給することで、充分に活用して部分負荷時の効率を向上させることができる。また、本実施例の混合器は、冷媒流路上に大きな圧損にならない程度の流路内断面形状の変化を付けることで流れを乱して気液の混合を促進するため、減圧膨張による混合促進方法と比べて、膨張弁のサイズを大きくする必要がないのでコスト削減を図ることができる。   In other words, the gas-liquid mixer biases the heat transfer surface by accelerating the gas-liquid mixing of the refrigerant before entering the evaporator from the specified point to the partial load, and supplying a homogeneous refrigerant to the evaporator heat transfer surface. It can be used effectively. Also, at the time of partial load, the heat transfer surface that could not be used conventionally due to the bias of the refrigerant supply is fully utilized by supplying a homogeneous refrigerant to the evaporator heat transfer surface to improve the efficiency at the partial load be able to. In addition, the mixer of this embodiment promotes the mixing of gas and liquid by disturbing the flow by adding a change in the cross-sectional shape in the flow passage so as not to cause a large pressure loss on the refrigerant flow passage. Compared to the method, it is not necessary to increase the size of the expansion valve, so that the cost can be reduced.

本発明を用いる冷凍サイクルについて図5を用いて説明する。本実施例では、圧縮式冷凍機を例にして説明する。一般的な圧縮式冷凍機は、冷媒の蒸発を用いて冷水15を作る蒸発器6、蒸発した冷媒を圧縮する圧縮機7、冷媒を凝縮する凝縮器8、凝縮した冷媒を蒸発器に戻すために圧力を減圧する膨張弁9によって構成される。蒸発器としては、プレート熱交換器や乾式シェルアンドチューブ式を用いることができる。   A refrigeration cycle using the present invention will be described with reference to FIG. In the present embodiment, a description will be given taking a compression refrigerator as an example. A general compression refrigerator includes an evaporator 6 that creates cold water 15 using refrigerant evaporation, a compressor 7 that compresses the evaporated refrigerant, a condenser 8 that condenses the refrigerant, and returns the condensed refrigerant to the evaporator. And an expansion valve 9 for reducing the pressure. As the evaporator, a plate heat exchanger or a dry shell and tube type can be used.

冷媒の流れは以下の通りである。まず、蒸発器6で冷水15の熱を奪い気化した冷媒10は、圧縮機7に吸込まれて圧縮される。圧縮された冷媒11は、凝縮器8に流入し冷却水16によって冷却されて凝縮する。液化した冷媒12は、膨張弁9を経て減圧された冷媒13となり、蒸発器6に戻る。このようにして冷媒が循環して冷凍サイクルが構成される。   The flow of the refrigerant is as follows. First, the refrigerant 10 that has evaporated the vapor of the cold water 15 by the evaporator 6 is sucked into the compressor 7 and compressed. The compressed refrigerant 11 flows into the condenser 8 and is cooled by the cooling water 16 to be condensed. The liquefied refrigerant 12 passes through the expansion valve 9 and becomes a refrigerant 13 whose pressure has been reduced, and returns to the evaporator 6. In this way, the refrigerant circulates to constitute a refrigeration cycle.

本実施の圧縮機冷凍機では、冷凍サイクルを構成する膨張弁9と蒸発器6の間に気液混合器1を配置する。気液混合器1により、蒸発器に入る前の冷媒について気液混合を促進することで、均質流を形成して伝熱面への冷媒分配を良好にすることができ、その結果、蒸発圧力の上昇により性能向上を図ることができる。   In the compressor refrigerator of the present embodiment, the gas-liquid mixer 1 is disposed between the expansion valve 9 and the evaporator 6 constituting the refrigeration cycle. The gas-liquid mixer 1 promotes gas-liquid mixing for the refrigerant before entering the evaporator, thereby forming a homogeneous flow and improving refrigerant distribution to the heat transfer surface. It is possible to improve the performance by increasing.

本発明の第1の実施例について図1を用いて説明する。混合器1は、膨張弁9から蒸発器6に繋がる冷媒流路中に設置される。また、膨張弁9から蒸発器6にかけて曲がり部が存在する場合は、蒸発器6入口につながる直線配管上に配置する。膨張弁9から蒸発器6に繋がる冷媒流路にフランジ継ぎ手部を設け、混合器1をフランジに挟み込むか又はフランジと一体化することで、混合器1を設置する。   A first embodiment of the present invention will be described with reference to FIG. The mixer 1 is installed in a refrigerant flow path that connects the expansion valve 9 to the evaporator 6. Further, when a bent portion exists from the expansion valve 9 to the evaporator 6, it is arranged on a straight pipe connected to the inlet of the evaporator 6. The flange 1 is provided in the refrigerant flow path that connects the expansion valve 9 to the evaporator 6, and the mixer 1 is installed by sandwiching the mixer 1 in the flange or by integrating it with the flange.

混合器1の冷媒流路内断面形状を図3に示す。流路内に多孔混合器を配置することで流れを乱し、密度差によって分離した冷媒の気相と液相が混合される。図3に示す多孔混合器は、流れ方向に沿った複数の穴が空いたもの又は網状のものである。これらの形状は、流路断面において対称な形状を有するので、流路断面全域において偏りなく気液冷媒が攪拌混合される。   FIG. 3 shows a cross-sectional shape in the refrigerant flow path of the mixer 1. By disposing a porous mixer in the flow path, the flow is disturbed, and the gas phase and liquid phase of the refrigerant separated by the density difference are mixed. The porous mixer shown in FIG. 3 is one having a plurality of holes along the flow direction or one having a net shape. Since these shapes have symmetrical shapes in the cross section of the flow path, the gas-liquid refrigerant is stirred and mixed without any deviation in the entire cross section of the flow path.

図3(A)では、異なる大きさの穴(流路)が流路断面全体に対称(点対称)に配置される。流路径が違うこと及びこれらの流路が対象に配置されることにより、流路断面全体により大きな攪拌効果を得ることができる。   In FIG. 3A, holes (channels) of different sizes are arranged symmetrically (point symmetry) over the entire channel cross section. When the channel diameters are different and these channels are arranged on the object, a larger stirring effect can be obtained over the entire channel cross section.

図3(B)では、同様の流路が流路断面全体に点対称に配置される。具体的には、十字状の障害物を配置し、この十字状障害物と混合器外径部との間に4つの流路を形成する。流路断面を対称に4分割することにより、流路断面積を確保しつつ、分割部位において、流れを乱すことで攪拌効果を得ることができる。   In FIG. 3B, similar flow paths are arranged point-symmetrically over the entire flow path cross section. Specifically, a cross-shaped obstacle is arranged, and four flow paths are formed between the cross-shaped obstacle and the mixer outer diameter portion. By dividing the channel cross section symmetrically into four, the stirring effect can be obtained by disturbing the flow at the divided site while ensuring the channel cross-sectional area.

図3(C)では、メッシュ状の混合器網部により流路全体を細分化する。流路全体を細分化することにより、密度差によって起こる偏流を整流化することができる。   In FIG. 3C, the entire flow path is subdivided by a mesh-like mixer network. By subdividing the entire flow path, the drift caused by the density difference can be rectified.

尚、これら図3(A)-(B)に記載の分配器を直列に複数設置することで、より大きな攪拌混合効果を得ることも可能である。   Note that a larger stirring and mixing effect can be obtained by installing a plurality of the distributors shown in FIGS. 3A to 3B in series.

本実施例によれば、蒸発器に入る前の冷媒について気液混合を促進することで均質流を形成し、蒸発器の伝熱面を有効活用し、簡易な構造でサイクルの効率を向上させることができる。   According to the present embodiment, a homogeneous flow is formed by promoting gas-liquid mixing with respect to the refrigerant before entering the evaporator, the heat transfer surface of the evaporator is effectively used, and the efficiency of the cycle is improved with a simple structure. be able to.

本発明の第2の実施例について図2を用いて説明する。膨張弁9を複数(本実施例では2個)用いて蒸発器6に接続する場合の実施例である。膨張弁9の上流側で冷媒流路が並列に複数分割され、分割されたそれぞれの冷媒流路に膨張弁9が配置される。膨張弁9の下流側で、これら複数の冷媒流路が合流した後、気液混合器1に合流する。冷媒は、気液混合器1で気液混合が促進された後、蒸発器6に流入する。冷媒流路の合流により偏った流れが形成されても気液混合器1により、気液混合を促進することで、蒸発器の伝熱面を有効活用し、簡易な構造でサイクルの効率を向上させることができる。   A second embodiment of the present invention will be described with reference to FIG. In this embodiment, a plurality (two in this embodiment) of expansion valves 9 are used and connected to the evaporator 6. A plurality of refrigerant flow paths are divided in parallel on the upstream side of the expansion valve 9, and the expansion valve 9 is disposed in each of the divided refrigerant flow paths. These refrigerant flow paths merge on the downstream side of the expansion valve 9, and then merge with the gas-liquid mixer 1. The refrigerant flows into the evaporator 6 after gas-liquid mixing is promoted in the gas-liquid mixer 1. Even if a biased flow is formed by the confluence of refrigerant flow paths, gas-liquid mixer 1 promotes gas-liquid mixing, effectively using the heat transfer surface of the evaporator and improving cycle efficiency with a simple structure Can be made.

1…混合器
2…混合器外径部
3…混合器多孔部
4…混合器網部
5…オリフィス
6…蒸発器
7…圧縮機
8…凝縮器
9…膨張弁
10…気化冷媒
11…圧縮冷媒
12…液化冷媒
13…減圧冷媒
14…気液混合促進後冷媒
15…冷水
16…冷却水
1 ... Mixer
2… Outer diameter of mixer
3… Mixer perforated part
4 ... Mixer network
5 ... Orifice
6 ... Evaporator
7 ... Compressor
8 ... Condenser
9 ... Expansion valve
10 ... Vaporizing refrigerant
11 ... Compressed refrigerant
12 ... Liquefied refrigerant
13 ... Depressurized refrigerant
14… Refrigerant after gas-liquid mixing promotion
15 ... cold water
16 ... cooling water

Claims (5)

冷媒を圧縮する圧縮機と、前記圧縮機で圧縮された冷媒を凝縮させる凝縮器と、前記凝縮器で凝縮された冷媒を減圧する膨張弁と、前記膨張弁で減圧された気液冷媒を混合する気液混合器と、前記気液混合器で混合された冷媒を蒸発させる蒸発器と、を備え
前記気液混合器は、混合器外径部と、前記混合器外径部内の流路断面全体に形成され流れ方向に沿った複数の冷媒流路とを有し、
前記複数の冷媒流路は、流れ方向に沿った複数の穴が点対称に配置されて構成されていることを特徴とする冷凍サイクル装置。
Mixing a compressor that compresses the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that decompresses the refrigerant condensed by the condenser, and a gas-liquid refrigerant decompressed by the expansion valve A gas-liquid mixer, and an evaporator for evaporating the refrigerant mixed in the gas-liquid mixer ,
The gas-liquid mixer has a mixer outer diameter part, and a plurality of refrigerant flow paths formed in the entire flow path cross section in the mixer outer diameter part along the flow direction,
The refrigeration cycle apparatus, wherein the plurality of refrigerant flow paths are configured such that a plurality of holes along a flow direction are arranged point-symmetrically .
冷媒を圧縮する圧縮機と、前記圧縮機で圧縮された冷媒を凝縮させる凝縮器と、前記凝縮器で凝縮された冷媒を減圧する膨張弁と、前記膨張弁で減圧された気液冷媒を混合する気液混合器と、前記気液混合器で混合された冷媒を蒸発させる蒸発器と、を備え
前記気液混合器は、混合器外径部と、前記混合器外径部内の流路断面全体に形成され流れ方向に沿った複数の冷媒流路とを有し、
前記複数の冷媒流路は、前記混合器外径部内に配置された十字状の障害物により形成された点対称の4つの冷媒流路により構成されていることを特徴とする冷凍サイクル装置。
Mixing a compressor that compresses the refrigerant, a condenser that condenses the refrigerant compressed by the compressor, an expansion valve that decompresses the refrigerant condensed by the condenser, and a gas-liquid refrigerant decompressed by the expansion valve A gas-liquid mixer, and an evaporator for evaporating the refrigerant mixed in the gas-liquid mixer ,
The gas-liquid mixer has a mixer outer diameter part, and a plurality of refrigerant flow paths formed in the entire flow path cross section in the mixer outer diameter part along the flow direction,
The refrigeration cycle apparatus, wherein the plurality of refrigerant flow paths are configured by four point-symmetric refrigerant flow paths formed by cross-shaped obstacles arranged in the outer diameter portion of the mixer .
請求項1に記載の冷凍サイクル装置において、前記複数の冷媒流路は、異なる大きさの穴が点対称に配置されて構成されていることを特徴とする冷凍サイクル装置。2. The refrigeration cycle apparatus according to claim 1, wherein the plurality of refrigerant flow paths are configured such that holes of different sizes are arranged point-symmetrically. 請求項1乃至の何れか一項に記載の冷凍サイクル装置において、前記膨張弁の上流側で並列に形成された複数の冷媒流路を有し、前記複数の冷媒流路のそれぞれに前記膨張弁が配置され、前記膨張弁の下流側で前記複数の冷媒流路が合流し、合流した前記冷媒流路に前記気液混合器が配置される冷凍サイクル装置。 In the refrigeration cycle apparatus according to any one of claims 1 to 3, having a plurality of refrigerant flow paths formed in parallel on the upstream side of the expansion valve, the expansion to each of the plurality of refrigerant flow paths A refrigeration cycle apparatus in which a valve is disposed, the plurality of refrigerant flow paths merge on the downstream side of the expansion valve, and the gas-liquid mixer is disposed in the merged refrigerant flow path. 請求項1乃至4何れか一項に記載の冷凍サイクル装置を備えた冷凍機。 A refrigerator provided with the refrigeration cycle apparatus according to any one of claims 1 to 4 .
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