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JP2010032104A - Air conditioner - Google Patents

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JP2010032104A
JP2010032104A JP2008194269A JP2008194269A JP2010032104A JP 2010032104 A JP2010032104 A JP 2010032104A JP 2008194269 A JP2008194269 A JP 2008194269A JP 2008194269 A JP2008194269 A JP 2008194269A JP 2010032104 A JP2010032104 A JP 2010032104A
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refrigerant
gas
heat exchanger
indoor heat
indoor
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Kenji Nagoshi
健二 名越
Shoji Takaku
昭二 高久
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Hitachi Global Life Solutions Inc
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Hitachi Appliances Inc
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Abstract

<P>PROBLEM TO BE SOLVED: To prevent increase of pressure loss and degradation of heat exchanging performance in a heat exchange passage of a heat exchanger, and to improve cooling performance of an air conditioner. <P>SOLUTION: In this air conditioner composed of an indoor unit installed in an air-conditioned room, and an outdoor unit installed outdoors, a flow rate adjustment valve is disposed on a bypass circuit connecting a gas-liquid separator disposed on the way of an indoor heat exchange passage and an outlet of the indoor heat exchanger, temperature sensors are respectively disposed near the outlet of the indoor heat exchanger and at a suction side of a compressor, and the bypass flow rate of the refrigerant is adjusted to be optimum to improve performance. By applying this constitution, the cooling performance of the air conditioner can be improved. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、熱交換器の熱交換路での圧力損失増加や熱交換性能の低下を防止する空気調和機に関する。   The present invention relates to an air conditioner that prevents an increase in pressure loss and a decrease in heat exchange performance in a heat exchange path of a heat exchanger.

近年、地球温暖化など深刻な環境問題を受け、地球環境保護の観点からCO2削減が求められている。一般家庭のエネルギー消費量の中で大きなウエイトを占める空調機においても、省エネルギー化が大きな課題となっており、高性能化の要求は非常に高い。そのため、これまでに様々な空調機の高性能化のための研究開発がなされてきた。そのような背景に対し、冷媒の気相と液相を分離するための気液分離器を冷凍サイクルの中に適切かつ効果的に配置することで、空調機全体の高性能化を狙うことを本発明の指針とした。この気液分離器を使用した空気調和機の発明としては、蒸発器として機能する熱交換器の熱交換路の途中に、冷媒を気液分離する気液分離器を設置し、さらに気液分離器により分離された気相冷媒を、蒸発器として機能する熱交換器の出口と四方弁とを接続する管路に流入させるバイパス管を設置することにより、蒸発器としての性能向上化を図るものがある(例えば、特許文献1参照)。特許文献1によると、蒸発器として機能する熱交換器のうち、気液分離器より上流側において熱交換により気液混合状態となった冷媒は、気液分離器により一旦気相分が取り除かれ、液相分が多い状態で下流側の熱交換器において熱交換されるため、管内冷媒の流速が高速度とならず圧力損失の増加が抑制されることで、蒸発器としての性能向上に繋がるとしている。また、蒸発器を凝縮器として使用する場合において、冷媒がバイパス管を逆流して気液分離器に戻らないように、バイパス管に逆止弁を設置している。 In recent years, in response to serious environmental problems such as global warming, CO 2 reduction is required from the viewpoint of protecting the global environment. Even in air conditioners that occupy a large weight in the energy consumption of ordinary households, energy saving is a major issue, and the demand for higher performance is very high. Therefore, research and development for improving the performance of various air conditioners has been made so far. Against such a background, we aim to improve the overall performance of air conditioners by appropriately and effectively arranging gas-liquid separators for separating the gas phase and liquid phase of the refrigerant in the refrigeration cycle. It was used as a guide for the present invention. As an invention of an air conditioner using this gas-liquid separator, a gas-liquid separator that gas-liquid separates the refrigerant is installed in the middle of the heat exchange path of the heat exchanger that functions as an evaporator, and further the gas-liquid separation By installing a bypass pipe that allows the gas-phase refrigerant separated by the evaporator to flow into the conduit connecting the outlet of the heat exchanger that functions as an evaporator and the four-way valve, the performance of the evaporator is improved. (For example, refer to Patent Document 1). According to Patent Document 1, among the heat exchangers functioning as an evaporator, the gas-liquid mixed state of the refrigerant that has been in a gas-liquid mixed state by heat exchange upstream of the gas-liquid separator is once removed by the gas-liquid separator. Since heat is exchanged in the heat exchanger on the downstream side with a large amount of liquid phase, the flow rate of the refrigerant in the pipe does not become high, and the increase in pressure loss is suppressed, leading to improved performance as an evaporator. It is said. In addition, when the evaporator is used as a condenser, a check valve is provided in the bypass pipe so that the refrigerant does not flow back through the bypass pipe and return to the gas-liquid separator.

特開2002−372323号公報JP 2002-372323 A

上述した冷凍サイクルにおいては、気液分離器に対する液戻りを防ぐために逆止弁を設置しているが、弁の開閉しかできないという点では、冷媒循環量や冷媒状態が変わった場合の工夫がなされておらず、運転条件によっては液ガス混合でバイパスしてしまう場合や、ガスバイパス量が十分に確保することができなくなると共に各冷媒流路に分流する時に分流割合のアンバランスが生じ、性能が悪化する可能性がある。   In the refrigeration cycle described above, a check valve is installed to prevent liquid return to the gas-liquid separator. However, in the point that the valve can only be opened and closed, a contrivance is made when the refrigerant circulation amount or refrigerant state changes. However, depending on the operating conditions, when bypassing with liquid gas mixing, or when the amount of gas bypass cannot be secured sufficiently, and when the flow is divided into each refrigerant flow path, an unbalance of the flow dividing ratio occurs, and the performance is reduced. It can get worse.

請求項1の発明は、圧縮機,四方弁,室外熱交換器,膨張弁,室外送風装置等を具備する室外機と、室内熱交換器,室内送風装置,除湿運転時に使用する除湿弁等を具備する室内機と、前記室内機の前記室内熱交換器と前記室外機内部に設けた前記膨張弁に至る内部に冷媒を循環させる接続配管により構成され、前記室内熱交換器と前記室外機と前記接続配管を各々接続し冷媒配管経路を構成し、内部で冷媒を循環させ、冷房運転や暖房運転を行うことのできる空気調和機において、冷房運転時、前記室内熱交換器の熱交換路の途中の冷媒を気液分離する気液分離器を除湿弁の下流側に配し、前記気液分離器で分離された気相の冷媒を前記室内熱交換器の出口管路に流入させるバイパス配管を配し、前記バイパス管には流量調整弁を設置し、前記室内熱交換器の出口管路近傍、および圧縮機吸込み側に、それぞれ熱交冷媒温度検知センサおよび圧縮機吸込み冷媒温度検知センサを設けたことを特徴とする空気調和機とする。   The invention of claim 1 includes an outdoor unit including a compressor, a four-way valve, an outdoor heat exchanger, an expansion valve, an outdoor air blower, etc., an indoor heat exchanger, an indoor air blower, a dehumidifying valve used during dehumidifying operation, and the like. An indoor unit comprising: an indoor heat exchanger of the indoor unit; and a connection pipe that circulates a refrigerant to an interior of the outdoor unit that reaches the expansion valve. The indoor heat exchanger and the outdoor unit Each of the connection pipes is connected to form a refrigerant pipe path, and the refrigerant is circulated inside the air conditioner capable of performing a cooling operation or a heating operation. During the cooling operation, the heat exchange path of the indoor heat exchanger A bypass pipe that arranges a gas-liquid separator that separates the refrigerant in the middle on the downstream side of the dehumidification valve, and causes the gas-phase refrigerant separated by the gas-liquid separator to flow into the outlet pipe of the indoor heat exchanger The flow adjustment valve is installed in the bypass pipe, Outlet conduit near the serial indoor heat exchanger, and the compressor suction side, the air conditioner being characterized in that each provided a coolant temperature sensor suction heat exchange refrigerant temperature sensor and compressor.

請求項2の発明は、請求項1において、冷房運転時の冷媒の流れ方向で気液分離を作用させた場合、前記熱交冷媒温度検知センサおよび前記圧縮機吸込み冷媒温度検知センサにより得られる熱交冷媒温度および圧縮機吸込み冷媒温度が、「熱交冷媒温度<圧縮機吸込み冷媒温度」となるように、前記流量調整弁の絞りを調整することを特徴とする。   According to a second aspect of the present invention, in the first aspect, when gas-liquid separation is applied in the flow direction of the refrigerant during the cooling operation, the heat obtained by the heat exchange refrigerant temperature detection sensor and the compressor suction refrigerant temperature detection sensor. The throttle of the flow rate adjusting valve is adjusted so that the refrigerant temperature and the compressor suction refrigerant temperature satisfy “heat exchange refrigerant temperature <compressor suction refrigerant temperature”.

請求項3の発明は、請求項1又は2において、冷房運転時の冷媒の流れ方向で気液分離を作用させた場合、前記気液分離器に接続する配管を
(流入配管の断面積)≒(ガス冷媒流出配管の断面積)+(液冷媒流出配管の断面積)
(ガス冷媒流出配管の断面積)<(液冷媒流出配管の断面積)
の条件を満たす気液分離器を有することを特徴とする。
When the gas-liquid separation is applied in the flow direction of the refrigerant during the cooling operation, the pipe connected to the gas-liquid separator is (the cross-sectional area of the inflow pipe) ≈ (Cross sectional area of gas refrigerant outflow pipe) + (Cross sectional area of liquid refrigerant outflow pipe)
(Cross sectional area of gas refrigerant outflow pipe) <(Cross sectional area of liquid refrigerant outflow pipe)
It has the gas-liquid separator which satisfy | fills these conditions.

請求項4の発明は、請求項1乃至3の何れかにおいて、前記気液分離器の下流側に位置する前記室内熱交換器について、前記室内送風装置からの風速分布に応じて、前記室内熱交換器の各熱交配管Lの長さを、「風速が大の位置のL1<風速が小の位置のL2」と設定したことを特徴とする。   A fourth aspect of the present invention provides the indoor heat exchanger according to any one of the first to third aspects, wherein the indoor heat exchanger is positioned on the downstream side of the gas-liquid separator according to a wind speed distribution from the indoor blower. The length of each heat exchange pipe L of the exchanger is set as “L1 at a position where the wind speed is large <L2 where the wind speed is small”.

請求項5の発明は、請求項1乃至3の何れかにおいて、前記気液分離器の下流側に位置する前記室内熱交換器について、前記室内送風装置からの風速分布に応じて、前記室内熱交換器の各冷媒流路配管の太さDを、「風速が小の位置のD1<風速が大の位置のD2」と設定したことを特徴とする。   A fifth aspect of the present invention provides the indoor heat exchanger according to any one of the first to third aspects, wherein the indoor heat exchanger is positioned on the downstream side of the gas-liquid separator according to a wind speed distribution from the indoor blower. The thickness D of each refrigerant passage pipe of the exchanger is set as “D1 at a position where the wind speed is low <D2 where the wind speed is high”.

請求項6の発明は、請求項1乃至5において、前記気液分離器は円柱の形状を成し、その内径を35mm以上にしたことを特徴とする。   A sixth aspect of the present invention is characterized in that, in any of the first to fifth aspects, the gas-liquid separator has a cylindrical shape and an inner diameter of 35 mm or more.

本発明に係る請求項1の効果は、圧縮機,四方弁,室外熱交換器,膨張弁,室外送風装置等を具備する室外機と、室内熱交換器,室内送風装置,除湿運転時に使用する除湿弁等を具備する室内機と、前記室内機の前記室内熱交換器と前記室外機内部に設けた前記膨張弁に至る内部に冷媒を循環させる接続配管により構成され、前記室内熱交換器と前記室外機と前記接続配管を各々接続し冷媒配管経路を構成し、内部で冷媒を循環させ、冷房運転や暖房運転を行うことのできる空気調和機において、冷房運転時、前記室内熱交換器の熱交換路の途中の冷媒を気液分離する気液分離器を前記室内熱交換器の途中経路に設けた除湿弁の下流側に配し、前記気液分離器で分離された気相の冷媒を前記室内熱交換器の出口管路に流入させるバイパス配管を配し、前記バイパス管には流量調整弁を設置し、前記室内熱交換器の出口管路近傍、および圧縮機吸込み側に、それぞれ熱交冷媒温度検知センサおよび圧縮機吸込み冷媒温度検知センサを設けたことを特徴とする空気調和機とすることで、除湿弁通過後に、前記除湿弁の冷媒下流側に設置した前記気液分離器で、液冷媒とガス冷媒を分離させ、ガス冷媒をバイパスすることで、蒸発器として熱交換性能にほとんど寄与しないガス成分をバイパスし、蒸発器としての性能を向上させることができ、かつ、気液分離後の液冷媒を分配する場合、従来生じていた気液混合冷媒状態で複数流路に分流させるときの冷媒分配のアンバランスを解消させることができる。   The effect of claim 1 according to the present invention is used at the time of an outdoor unit including a compressor, a four-way valve, an outdoor heat exchanger, an expansion valve, an outdoor fan, and the like, an indoor heat exchanger, an indoor fan, and a dehumidifying operation. An indoor unit including a dehumidification valve, the indoor heat exchanger of the indoor unit, and a connection pipe that circulates a refrigerant to the inside of the outdoor unit leading to the expansion valve, and the indoor heat exchanger; In the air conditioner that connects the outdoor unit and the connection pipe to form a refrigerant pipe path, circulates the refrigerant inside, and can perform a cooling operation or a heating operation, during the cooling operation, the indoor heat exchanger A gas-phase refrigerant separated from the gas-liquid separator by arranging a gas-liquid separator for separating the refrigerant in the middle of the heat exchange path downstream of the dehumidification valve provided in the middle path of the indoor heat exchanger. Bypass piping for allowing the air to flow into the outlet line of the indoor heat exchanger The bypass pipe is provided with a flow control valve, and a heat exchanger temperature detection sensor and a compressor suction refrigerant temperature detection sensor are provided in the vicinity of the outlet pipe of the indoor heat exchanger and on the compressor suction side, respectively. By using the air conditioner characterized in that, after passing through the dehumidifying valve, the gas-liquid separator installed on the downstream side of the refrigerant of the dehumidifying valve separates the liquid refrigerant from the gas refrigerant and bypasses the gas refrigerant. Therefore, the gas component that hardly contributes to the heat exchange performance as an evaporator can be bypassed, the performance as the evaporator can be improved, and the liquid refrigerant after gas-liquid separation is distributed, It is possible to eliminate the imbalance in refrigerant distribution when the liquid is mixed into the plurality of flow paths in the liquid mixed refrigerant state.

また、前記室内熱交換器の出口管路近傍、および圧縮機吸込み側のそれぞれに設けた温度センサにより検出された、熱交冷媒温度と圧縮機吸込み冷媒温度について、通常の冷房運転時は、前記室内熱交換器の出口管路から圧縮機吸込み口に至る経路において、スーパーヒートをする分冷媒温度が上昇するため、「熱交冷媒温度<圧縮機吸込み冷媒温度」の関係が保たれているが、「前記スーパーヒート量が極端に減少する」、あるいは「熱交冷媒温度が圧縮機吸込み冷媒温度よりも高くなる」といった現象が起こった場合は、「熱交冷媒温度≧圧縮機吸込み冷媒温度」の関係となり、「バイパス管に液冷媒が混入し始めた」と判断することができるため、前記流量調整弁を絞ることにより、前記バイパス管への液冷媒混入を防ぐことができる。   In addition, regarding the heat exchange refrigerant temperature and the compressor suction refrigerant temperature detected by the temperature sensors provided in the vicinity of the outlet pipe of the indoor heat exchanger and on the compressor suction side, during normal cooling operation, In the path from the outlet pipe of the indoor heat exchanger to the compressor suction port, the refrigerant temperature rises by the amount of superheating, so the relationship of “heat exchange refrigerant temperature <compressor suction refrigerant temperature” is maintained. , If a phenomenon such as “the amount of super heat is extremely reduced” or “the heat exchange refrigerant temperature becomes higher than the compressor suction refrigerant temperature” occurs, “heat exchange refrigerant temperature ≧ compressor suction refrigerant temperature” Therefore, it can be determined that “the liquid refrigerant has started to be mixed into the bypass pipe”, so that the liquid refrigerant can be prevented from being mixed into the bypass pipe by restricting the flow rate adjusting valve.

本発明に係る請求項2の効果は、請求項1記載の空気調和機において、冷房運転時の冷媒の流れ方向で気液分離を作用させた場合、前記熱交冷媒温度検知センサおよび前記圧縮機吸込み冷媒温度検知センサにより得られる熱交冷媒温度および圧縮機吸込み冷媒温度が、「熱交冷媒温度<圧縮機吸込み冷媒温度」になるように、前記流量調整弁の絞りを調整する制御をもたせたことを特徴としたことで、バイパス配管を通る冷媒量を適宜調整することで、冷房性能を向上させることができる。   According to a second aspect of the present invention, in the air conditioner according to the first aspect, when the gas-liquid separation is applied in the refrigerant flow direction during the cooling operation, the heat exchanger temperature detection sensor and the compressor Control was made to adjust the throttle of the flow rate adjusting valve so that the heat exchange refrigerant temperature and the compressor suction refrigerant temperature obtained by the suction refrigerant temperature detection sensor are “heat exchange refrigerant temperature <compressor suction refrigerant temperature”. With this feature, the cooling performance can be improved by appropriately adjusting the amount of refrigerant passing through the bypass pipe.

本発明に係る請求項3の効果は、請求項1又は2の空気調和機において、冷房運転時の冷媒の流れ方向で気液分離を作用させた場合、前記気液分離器に接続する配管を
(流入配管の断面積)≒(ガス冷媒流出配管の断面積)+(液冷媒流出配管の断面積)
(ガス冷媒流出配管の断面積)<(液冷媒流出配管の断面積)
の条件を満たす気液分離器を有することで、二相流で流入する冷媒がガス冷媒と液冷媒に分離し易くなり、熱交換器としての性能を促進することができる。
The effect of claim 3 according to the present invention is that, in the air conditioner of claim 1 or 2, when gas-liquid separation is applied in the refrigerant flow direction during cooling operation, a pipe connected to the gas-liquid separator is provided. (Cross sectional area of inflow piping) ≒ (Cross sectional area of gas refrigerant outflow piping) + (Cross sectional area of liquid refrigerant outflow piping)
(Cross sectional area of gas refrigerant outflow pipe) <(Cross sectional area of liquid refrigerant outflow pipe)
By having the gas-liquid separator that satisfies the above condition, the refrigerant flowing in the two-phase flow can be easily separated into the gas refrigerant and the liquid refrigerant, and the performance as a heat exchanger can be promoted.

本発明に係る請求項4の効果は、請求項1乃至3記載の何れかに記載の空気調和機において、前記気液分離器の下流側に位置する前記室内熱交換器について、前記室内送風装置からの風速分布に応じて、前記室内熱交換器の各熱交配管Lの長さを「風速が大の位置のL1<風速が小の位置のL2」となるように設定したことを特徴とすることで、風速の遅い、即ち伝熱性能の低い区間の熱交配管の長さを長くとり、また風速の速い、即ち伝熱性能の高い区間の熱交配管の長さを短くとることで、全体の伝熱バランスを良好に確保することができる。   The effect of claim 4 according to the present invention is that, in the air conditioner according to any one of claims 1 to 3, the indoor air blower is provided for the indoor heat exchanger located downstream of the gas-liquid separator. The length of each heat exchange pipe L of the indoor heat exchanger is set such that “L1 at a position where the wind speed is large <L2 where the wind speed is small” according to the wind speed distribution from By increasing the length of the heat exchange pipe in the section where the wind speed is low, that is, the heat transfer performance is low, and shortening the length of the heat exchange pipe in the section where the wind speed is high, that is, the heat transfer performance is high. The overall heat transfer balance can be secured satisfactorily.

本発明に係る請求項5の効果は、請求項1乃至3記載の何れかに記載の空気調和機において、前記気液分離器の下流側に位置する前記室内熱交換器について、前記室内送風装置からの風速分布に応じて、前記室内熱交換器の各冷媒流路配管の太さDを「風速が小の位置のD1<風速が大の位置のD2」となるように設定したことを特徴とすることで、風速の遅い、即ち伝熱性能の低い区間の冷媒流路配管の太さを細くとり、また風速の速い、即ち伝熱性能の高い区間の冷媒流路配管を太くとることで、全体の伝熱バランスを良好に確保することができる。   The effect of claim 5 according to the present invention is the air conditioner according to any one of claims 1 to 3, wherein the indoor air exchanger is located on the downstream side of the gas-liquid separator. The thickness D of each refrigerant flow pipe of the indoor heat exchanger is set so that “D1 at a position where the wind speed is low <D2 where the wind speed is high” according to the wind speed distribution from By reducing the thickness of the refrigerant flow pipe in the section where the wind speed is low, that is, the heat transfer performance is low, and increasing the refrigerant flow pipe in the section where the wind speed is high, that is, the heat transfer performance is high. The overall heat transfer balance can be secured satisfactorily.

本発明に係る請求項6の効果は、請求項1乃至5の何れかに記載の空気調和機において、前記気液分離器は円柱の形状を成し、少なくともその内径を約35mm以上に設定することにより、気液二相流で気液分離器に流入する冷媒をガス冷媒と液冷媒に分離させるときの分離性能を向上させることができ、気液分離器を有する空気調和機の性能を向上させることができる。   According to the sixth aspect of the present invention, in the air conditioner according to any one of the first to fifth aspects, the gas-liquid separator has a cylindrical shape, and at least its inner diameter is set to about 35 mm or more. As a result, the separation performance when the refrigerant flowing into the gas-liquid separator in the gas-liquid two-phase flow is separated into the gas refrigerant and the liquid refrigerant can be improved, and the performance of the air conditioner having the gas-liquid separator is improved. Can be made.

圧縮機,四方弁,室外熱交換器,膨張弁,室外送風装置等を具備する室外機と、室内熱交換器,室内送風装置,除湿運転時に使用する除湿弁等を具備する室内機と、前記室内機の前記室内熱交換器と前記室外機内部に設けた前記膨張弁に至る内部に冷媒を循環させる接続配管により構成され、前記室内熱交換器と前記室外機と前記接続配管を各々接続し冷媒配管経路を構成し、内部で冷媒を循環させ、冷房運転や暖房運転を行うことのできる空気調和機において、冷房運転時、前記室内熱交換器の熱交換路の途中の冷媒を気液分離する気液分離器を前記室内熱交換器の途中経路に設けた除湿弁の下流側に配し、前記気液分離器で分離された気相の冷媒を前記室内熱交換器の出口管路に流入させるバイパス配管を配し、前記バイパス管には流量調整弁を設置し、前記室内熱交換器の出口管路近傍、および圧縮機吸込み側に、それぞれ熱交冷媒温度検知センサおよび圧縮機吸込み冷媒温度検知センサを設けたことを特徴とする空気調和機とすることで、除湿弁通過後に、前記除湿弁の冷媒下流側に設置した前記気液分離器で、液冷媒とガス冷媒を分離させ、ガス冷媒をバイパスすることで、蒸発器として熱交換性能にほとんど寄与しないガス成分をバイパスし、蒸発器としての性能を向上させることができ、かつ、気液分離後の液冷媒を分配する場合、従来生じていた気液混合冷媒状態で複数流路に分流させるときの冷媒分配のアンバランスを解消させることができる。   An outdoor unit comprising a compressor, a four-way valve, an outdoor heat exchanger, an expansion valve, an outdoor air blower, etc., an indoor heat exchanger, an indoor air blower, an indoor unit comprising a dehumidifying valve used during dehumidification operation, and the like, The indoor heat exchanger of the indoor unit and a connection pipe that circulates refrigerant through the interior of the outdoor unit that reaches the expansion valve are connected to the indoor heat exchanger, the outdoor unit, and the connection pipe, respectively. In an air conditioner that configures a refrigerant piping path, circulates the refrigerant inside, and can perform cooling operation or heating operation, during the cooling operation, the refrigerant in the middle of the heat exchange path of the indoor heat exchanger is separated into gas and liquid The gas-liquid separator is disposed downstream of the dehumidifying valve provided in the middle path of the indoor heat exchanger, and the gas-phase refrigerant separated by the gas-liquid separator is supplied to the outlet pipe of the indoor heat exchanger. A bypass pipe to be introduced is arranged, and the bypass pipe has a flow rate. An air conditioner characterized in that a valve is provided and a heat exchanger refrigerant temperature detection sensor and a compressor suction refrigerant temperature detection sensor are provided in the vicinity of the outlet pipe of the indoor heat exchanger and on the compressor suction side, respectively. Thus, after passing through the dehumidifying valve, the gas-liquid separator installed on the downstream side of the refrigerant of the dehumidifying valve separates the liquid refrigerant and the gas refrigerant, and bypasses the gas refrigerant, so that the heat exchange performance as an evaporator When the liquid refrigerant after gas-liquid separation is distributed, the gas component that hardly contributes to the gas can be bypassed and the performance as an evaporator can be improved. It is possible to eliminate the imbalance in refrigerant distribution when the flow is divided.

また、前記室内熱交換器の出口管路近傍、および圧縮機吸込み側のそれぞれに設けた温度センサにより検出された、熱交冷媒温度と圧縮機吸込み冷媒温度について、通常の冷房運転時は、前記室内熱交換器の出口管路から圧縮機吸込み口に至る経路において、スーパーヒートをする分冷媒温度が上昇するため、「熱交冷媒温度<圧縮機吸込み冷媒温度」の関係が保たれているが、「前記スーパーヒート量が極端に減少する」、あるいは「熱交冷媒温度が圧縮機吸込み冷媒温度よりも高くなる」といった現象が起こった場合は、「熱交冷媒温度≧圧縮機吸込み冷媒温度」の関係となり、「バイパス管に液冷媒が混入し始めた」と判断することができるため、前記流量調整弁を絞ることにより、前記バイパス管への液冷媒混入を防ぐことができる。   In addition, regarding the heat exchange refrigerant temperature and the compressor suction refrigerant temperature detected by the temperature sensors provided in the vicinity of the outlet pipe of the indoor heat exchanger and on the compressor suction side, during normal cooling operation, In the path from the outlet pipe of the indoor heat exchanger to the compressor suction port, the refrigerant temperature rises by the amount of superheating, so the relationship of “heat exchange refrigerant temperature <compressor suction refrigerant temperature” is maintained. , If a phenomenon such as “the amount of super heat is extremely reduced” or “the heat exchange refrigerant temperature becomes higher than the compressor suction refrigerant temperature” occurs, “heat exchange refrigerant temperature ≧ compressor suction refrigerant temperature” Therefore, it can be determined that “the liquid refrigerant has started to be mixed into the bypass pipe”, so that the liquid refrigerant can be prevented from being mixed into the bypass pipe by restricting the flow rate adjusting valve.

本発明に係る空調室内に据え付けられる室内機と、屋外に設置される室外機によって構成される空気調和機について、請求項1に記載した気液分離器や流量調整弁を搭載した冷凍サイクルを図1に示す。図1を用いて冷房運転時の冷媒の流れで説明すると、圧縮機1にて圧縮された高温・高圧の気相冷媒は四方弁2により室外熱交換器3に流入する。そして、室外ファン4により室外空気と室外熱交換器3内に流れる冷媒が熱交換することにより冷媒は凝縮され、高温高圧の液相冷媒となって膨張弁5に流入する。   The refrigeration cycle which mounts the gas-liquid separator and flow control valve which were described in Claim 1 about the air conditioner comprised by the indoor unit installed in the air-conditioning room | chamber interior which concerns on this invention, and the outdoor unit installed outdoors is a figure. It is shown in 1. The refrigerant flow during the cooling operation will be described with reference to FIG. 1. The high-temperature and high-pressure gas-phase refrigerant compressed by the compressor 1 flows into the outdoor heat exchanger 3 through the four-way valve 2. Then, the outdoor fan 4 exchanges heat between the outdoor air and the refrigerant flowing in the outdoor heat exchanger 3, whereby the refrigerant is condensed and flows into the expansion valve 5 as a high-temperature and high-pressure liquid-phase refrigerant.

膨張弁5において冷媒は減圧され低温・低圧になり、室内熱交換器6に流入する。図1では冷房運転時において、室内熱交換器6内に設置された気液分離機11に対して、上流側に位置する室内熱交換路を第1室内熱交換器9,下流側に位置する室内熱交換路を第2室内熱交換器10と区別して表記している。まず、第1室内熱交換器9に流入した冷媒は、室内ファン7により室内空気と熱交換し、室内空気は冷やされ、冷媒は蒸発していく。その後、除湿運転時に使用する除湿弁8を通過した気液混合冷媒は、一旦気液分離機11に流入し、ここで分離された気相分の冷媒はバイパス回路14を通って出口配管12へ流れる。この際、バイパス回路上に設置した流量調整弁13の絞りを調整することで、サイクル全体にとっての適切な冷媒バイパス量を調整することができる。一方、気液分離機11により分離された液相分の冷媒は、通常通り第2室内熱交換器10に流入し、ここで再び室内空気と熱交換し、室内空気を冷やし、蒸発していく。バイパス回路14を通過した気相冷媒は出口配管12で合流し、四方弁2を介して圧縮機1に戻され再び高温・高圧の冷媒にされる。このサイクルを繰り返すことにより、空気調和機は冷房運転する。また、暖房運転時は四方弁2により冷媒の流れる方向を切りかえることにより、室内熱交換器6と室外熱交換器3の役割が逆になり、室外熱交換器3が蒸発器になり、室内熱交換器6が凝縮器となるが、その際、バイパス回路14上に設置した流量調整弁13を閉じることで、第2室内熱交換器10に流入する冷媒のバイパス回路14への流入を防ぐことができる。具体的な効果として、冷房運転時は第1室内熱交換器9において熱交換により気液混合状態となった冷媒は、気液分離器により一旦気相分が取り除かれ、液相分が多い状態で下流側の熱交換器において熱交換されるため、全体的に管内冷媒の流速が高速度とならず圧力損失の増加が抑制され、また、液相割合の多い冷媒を用いて熱交換するため、全体の伝熱性能向上にも繋がる。また、この他の効果としては、第2室内熱交換器10にて分流する冷媒のパスバランスの最適化などが挙げられる。これらの効果は冷房能力が大きい条件ほど高い効果が得られる。   In the expansion valve 5, the refrigerant is depressurized to a low temperature / low pressure and flows into the indoor heat exchanger 6. In FIG. 1, during the cooling operation, the indoor heat exchange path located on the upstream side with respect to the gas-liquid separator 11 installed in the indoor heat exchanger 6 is located on the first indoor heat exchanger 9 and on the downstream side. The indoor heat exchange path is distinguished from the second indoor heat exchanger 10. First, the refrigerant flowing into the first indoor heat exchanger 9 exchanges heat with indoor air by the indoor fan 7, the indoor air is cooled, and the refrigerant evaporates. Thereafter, the gas-liquid mixed refrigerant that has passed through the dehumidifying valve 8 used during the dehumidifying operation once flows into the gas-liquid separator 11, and the vapor-phase refrigerant separated here passes through the bypass circuit 14 to the outlet pipe 12. Flowing. At this time, the refrigerant bypass amount appropriate for the entire cycle can be adjusted by adjusting the throttle of the flow rate adjusting valve 13 installed on the bypass circuit. On the other hand, the refrigerant for the liquid phase separated by the gas-liquid separator 11 flows into the second indoor heat exchanger 10 as usual, where it exchanges heat with the room air again, cools the room air, and evaporates. . The gas-phase refrigerant that has passed through the bypass circuit 14 joins at the outlet pipe 12 and is returned to the compressor 1 through the four-way valve 2 to be made high-temperature / high-pressure refrigerant again. By repeating this cycle, the air conditioner is cooled. Also, during the heating operation, the direction of the refrigerant flow is switched by the four-way valve 2 so that the roles of the indoor heat exchanger 6 and the outdoor heat exchanger 3 are reversed, the outdoor heat exchanger 3 becomes an evaporator, and the indoor heat The exchanger 6 serves as a condenser. At that time, the flow rate adjusting valve 13 installed on the bypass circuit 14 is closed to prevent the refrigerant flowing into the second indoor heat exchanger 10 from flowing into the bypass circuit 14. Can do. As a specific effect, during the cooling operation, the refrigerant that has become a gas-liquid mixed state by heat exchange in the first indoor heat exchanger 9 is temporarily removed of the gas phase by the gas-liquid separator, and has a large liquid phase content Since heat is exchanged in the heat exchanger on the downstream side, the flow rate of the refrigerant in the pipe is not increased as a whole, and an increase in pressure loss is suppressed, and heat is exchanged using a refrigerant having a high liquid phase ratio. This also leads to an improvement in overall heat transfer performance. Other effects include optimization of the path balance of the refrigerant that is diverted in the second indoor heat exchanger 10. These effects are higher when the cooling capacity is larger.

図2に、請求項1に記載した気液分離器や流量調整弁を搭載した室内側冷凍サイクルの一例を示す。図2を用いて冷房運転時の冷媒の流れについて説明すると、図上方より流入した冷媒は、第1室内熱交換器9に流入し、熱交換をして通過後、除湿弁8を通って気液分離器11に流入する。気液分離器11により分離された気相分の冷媒は、流量調整弁13により流量調整したバイパス回路14を通過した後、出口配管12へと至る。一方、気液分離器11により分離された液相分の冷媒は、通常通り第2室内熱交換器10に流入し、熱交換して通過した後、出口配管12においてバイパス回路14から流入してきた冷媒と合流し、室外機側へと流出する。   FIG. 2 shows an example of an indoor refrigeration cycle in which the gas-liquid separator and the flow rate adjustment valve according to claim 1 are mounted. The refrigerant flow during the cooling operation will be described with reference to FIG. 2. The refrigerant that has flowed in from the upper part of the figure flows into the first indoor heat exchanger 9, exchanges heat, passes through the dehumidification valve 8, and then passes through the dehumidification valve 8. It flows into the liquid separator 11. The gas phase refrigerant separated by the gas-liquid separator 11 passes through the bypass circuit 14 whose flow rate is adjusted by the flow rate adjusting valve 13 and then reaches the outlet pipe 12. On the other hand, the refrigerant of the liquid phase separated by the gas-liquid separator 11 flows into the second indoor heat exchanger 10 as usual, passes through the heat exchange, and then flows in from the bypass circuit 14 in the outlet pipe 12. It merges with the refrigerant and flows out to the outdoor unit side.

流量調整弁13の絞りを開いていく過程において、室内熱交温度センサ15と圧縮機吸込み温度センサ20の温度差から得られるスーパーヒート量が急激に落ち込んだ場合は、バイパス回路14に液冷媒が流入し始めたものと判断することができるため、サイクル安定時のスーパーヒート量が得られるポイントまで、流量調整弁13の絞りを絞ることで、液冷媒のバイパスを防ぐことができる。   In the process of opening the throttle of the flow rate adjustment valve 13, when the superheat amount obtained from the temperature difference between the indoor heat exchanger temperature sensor 15 and the compressor suction temperature sensor 20 suddenly drops, liquid refrigerant is supplied to the bypass circuit 14. Since it can be determined that the refrigerant has started to flow in, the bypass of the liquid refrigerant can be prevented by narrowing the throttle of the flow rate adjustment valve 13 to the point where the amount of superheat when the cycle is stable can be obtained.

請求項2に記載する制御の具体例について、図1を用いて説明する。まず空気調和機の冷房運転開始後、サイクルが安定し、膨張弁5の開度が一定に落ち着いた後、それまで全閉状態であった流量調整弁13の絞りを徐々に開き、気液分離器11により分離されたガス冷媒を、バイパス回路14を通して出口配管12へとバイパスさせていく。サイクル安定時のスーパーヒート量が維持されていることを、室内熱交温度センサ15と圧縮機吸込み温度センサ20の両センサにより監視しながら、流量調整弁13の絞りを可能な限り開くことにより、最適なガス冷媒のバイパス量に調整することができ、冷房性能を向上させることができる。   A specific example of the control described in claim 2 will be described with reference to FIG. First, after the cooling operation of the air conditioner is started, after the cycle is stabilized and the opening degree of the expansion valve 5 is kept constant, the throttle of the flow rate adjustment valve 13 that has been fully closed until then is gradually opened to separate the gas and liquid. The gas refrigerant separated by the vessel 11 is bypassed to the outlet pipe 12 through the bypass circuit 14. By opening the throttle of the flow rate adjustment valve 13 as much as possible while monitoring the super heat amount at the time of cycle stabilization with both the indoor heat exchanger temperature sensor 15 and the compressor suction temperature sensor 20, It can be adjusted to the optimum bypass amount of the gas refrigerant, and the cooling performance can be improved.

図3は気液分離器11について、気液分離を作用させた時に
(流入配管18の断面積)≒(ガス冷媒流出配管19aの断面積)+(液冷媒流出配 管19の断面積)
(ガス冷媒流出配管19aの断面積)<(液冷媒流出配管19の断面積)
の条件を満たすと共に、流量調整弁13でガス冷媒の流出割合を最適にした場合に、冷媒配管19から流出する冷媒を概ね液冷媒にすることができ、蒸発器としての性能を向上させることができる。例えば、流入配管18の直径をφ9.52にした場合、液冷媒流出配管19をφ7とガス冷媒配管19aをφ6.35にすることで前記の条件を満たすことができる。
FIG. 3 shows the gas-liquid separator 11 when gas-liquid separation is applied (cross-sectional area of the inflow pipe 18) ≈ (cross-sectional area of the gas refrigerant outflow pipe 19a) + (cross-sectional area of the liquid refrigerant outflow pipe 19)
(Cross sectional area of gas refrigerant outflow pipe 19a) <(Cross sectional area of liquid refrigerant outflow pipe 19)
When the flow rate adjustment valve 13 optimizes the outflow rate of the gas refrigerant, the refrigerant flowing out from the refrigerant pipe 19 can be substantially liquid refrigerant, and the performance as an evaporator can be improved. it can. For example, when the diameter of the inflow pipe 18 is φ9.52, the above condition can be satisfied by setting the liquid refrigerant outflow pipe 19 to φ7 and the gas refrigerant pipe 19a to φ6.35.

実施例1で取り挙げた空気調和機において、室内ファン7からの風速分布16に応じて気液分離器11の下流側に位置する第2室内熱交換器10の冷媒流路配管の長さを調整したものを図4に示す。通常ならば気液混相の冷媒が流入するために、熱交換器直前の分流には分流性能の高い、高価な分流器を使用しなければならないが、本発明のように流入前に気液分離器を通過させることで、液単相冷媒が流入する形となり、非常に安定した分流を実現することができるので、熱交換量に合った冷媒流路配列設定ができる。すなわち、図4のように風速が比較的速く、伝熱性能が高い位置に冷媒流路B,冷媒流路Cのような短い冷媒流路を設置し、逆に風速が比較的遅く、伝熱性能が低い位置には冷媒流路A,冷媒流路Dのような長い冷媒流路を設置することで、全体的な熱交換器性能が向上する。   In the air conditioner taken up in the first embodiment, the length of the refrigerant channel pipe of the second indoor heat exchanger 10 located on the downstream side of the gas-liquid separator 11 according to the wind speed distribution 16 from the indoor fan 7 is set. The adjustment is shown in FIG. Normally, since a gas-liquid mixed phase refrigerant flows in, it is necessary to use an expensive flow divider with a high flow-dividing performance for the diversion immediately before the heat exchanger. The liquid single-phase refrigerant flows in by passing through the vessel, and a very stable diversion can be realized. Therefore, it is possible to set the refrigerant flow path arrangement according to the heat exchange amount. That is, as shown in FIG. 4, a short refrigerant flow path such as the refrigerant flow path B and the refrigerant flow path C is installed at a position where the wind speed is relatively fast and the heat transfer performance is high, and conversely the wind speed is relatively slow, By installing long refrigerant flow paths such as the refrigerant flow path A and the refrigerant flow path D at positions where the performance is low, the overall heat exchanger performance is improved.

実施例1で取り挙げた空気調和機において、室内ファン7からの風速分布16に応じて気液分離器11の下流側に位置する第2室内熱交換器10と、第2室内熱交換器10流入前に設けた分岐パイプとを接続する接続管17の太さを調整したものを図5に示す。通常ならば気液混相の冷媒が流入するために、熱交換器直前の分流には分流性能の高い、高価な分流器を使用しなければならないが、本発明のように流入前に気液分離器を通過させることで、液単相冷媒が流入する形となり、非常に安定した分流を実現することができるので、熱交換量に合った冷媒流路配列設定ができる。すなわち、図5のように、風速が比較的速く、伝熱性能が高いところに位置する冷媒流路B,冷媒流路Cへの接続管17には他に比べて太い冷媒配管を採用しており、これにより風速が速く伝熱性能の良い区間により多くの冷媒を流入させることが可能となり、全体的な熱交換器の伝熱性能が向上する。   In the air conditioner taken up in the first embodiment, the second indoor heat exchanger 10 and the second indoor heat exchanger 10 located on the downstream side of the gas-liquid separator 11 according to the wind speed distribution 16 from the indoor fan 7. FIG. 5 shows an adjustment of the thickness of the connecting pipe 17 that connects the branch pipe provided before the inflow. Normally, since a gas-liquid mixed phase refrigerant flows in, it is necessary to use an expensive flow divider with a high flow-dividing performance for the diversion immediately before the heat exchanger. The liquid single-phase refrigerant flows in by passing through the vessel, and a very stable diversion can be realized. Therefore, it is possible to set the refrigerant flow path arrangement according to the heat exchange amount. That is, as shown in FIG. 5, the refrigerant pipe B and the refrigerant pipe C connected to the refrigerant flow path B and the refrigerant flow path C located at a place where the wind speed is relatively high and the heat transfer performance is high employ a thick refrigerant pipe as compared with others. Thus, it becomes possible to allow more refrigerant to flow into the section where the wind speed is fast and the heat transfer performance is good, and the overall heat transfer performance of the heat exchanger is improved.

図6は本発明に係る気液分離器11の内径と性能(COP向上割合)の関係を表した実験結果である。本実験では気液分離器の内径をパラメータにして、性能を測定した結果を表したものであり、本実験結果から気液分離器11の内径を概ねφ35mm以上にすることで性能向上を図ることができる。また、気液分離器11の内径がφ48mm程度で性能が収束しているため、気液分離器11の径Dはφ35mm≦D≦φ48mmにすることで必要以上に内径を大きくすることなく、性能向上を図ることができる。   FIG. 6 shows the experimental results showing the relationship between the inner diameter and the performance (COP improvement ratio) of the gas-liquid separator 11 according to the present invention. In this experiment, the result of measuring the performance with the inner diameter of the gas-liquid separator as a parameter is shown. From the result of this experiment, the inner diameter of the gas-liquid separator 11 is set to approximately 35 mm or more to improve the performance. Can do. Further, since the performance is converged when the gas-liquid separator 11 has an inner diameter of about φ48 mm, the diameter D of the gas-liquid separator 11 is set to φ35 mm ≦ D ≦ φ48 mm without increasing the inner diameter more than necessary. Improvements can be made.

本発明の空気調和機に係る冷凍サイクル全体図である。(実施例1,2)It is a refrigeration cycle whole figure concerning the air harmony machine of the present invention. (Examples 1 and 2) 本発明の空気調和機に係る実施例である。(実施例1)It is an Example which concerns on the air conditioner of this invention. (Example 1) 本発明の空気調和機に係る実施例である。(実施例3)It is an Example which concerns on the air conditioner of this invention. (Example 3) 本発明の空気調和機に係る実施例である。(実施例4)It is an Example which concerns on the air conditioner of this invention. Example 4 本発明の空気調和機に係る実施例である。(実施例5)It is an Example which concerns on the air conditioner of this invention. (Example 5) 本発明の空気調和機に係る実施例である。(実施例6)It is an Example which concerns on the air conditioner of this invention. (Example 6)

符号の説明Explanation of symbols

1 圧縮機
2 四方弁
3 室外熱交換器
4 室外送風ファン
5 膨張弁
6 室内熱交換器
7 室内送風ファン
8 除湿弁
9 第1室内熱交換器
10 第2室内熱交換器
11 気液分離器
12 (室内熱交換器の)出口配管
13 流量調整弁
14 バイパス回路
15 室内熱交温度センサ
16 (室内ファンからの)風速分布
17 (室内熱交換器の)接続管
18 流入配管
19 液冷媒流出配管
19a ガスバイパス流出配管
20 圧縮機吸込み温度センサ
DESCRIPTION OF SYMBOLS 1 Compressor 2 Four-way valve 3 Outdoor heat exchanger 4 Outdoor ventilation fan 5 Expansion valve 6 Indoor heat exchanger 7 Indoor ventilation fan 8 Dehumidification valve 9 1st indoor heat exchanger 10 2nd indoor heat exchanger 11 Gas-liquid separator 12 Outlet pipe 13 (for indoor heat exchanger) Flow rate adjusting valve 14 Bypass circuit 15 Indoor heat exchanger temperature sensor 16 Wind speed distribution 17 (from indoor fan) Connection pipe 18 (for indoor heat exchanger) Inflow pipe 19 Liquid refrigerant outflow pipe 19a Gas bypass outlet pipe 20 Compressor suction temperature sensor

Claims (6)

圧縮機,四方弁,室外熱交換器,膨張弁,室外送風装置を備える室外機と、室内熱交換器,室内送風装置,除湿運転時に使用する除湿弁を備える室内機と、前記室内機の前記室内熱交換器と前記室外機内部に設けた前記膨張弁とに至る内部に冷媒を循環させる接続配管により構成され、前記室内熱交換器と前記室外機と前記接続配管とを各々接続して冷媒配管経路を構成し、前記冷媒配管経路内部で冷媒を循環させて冷房運転や暖房運転を行う空気調和機において、
冷房運転時、前記室内熱交換器の熱交換路の途中に気液分離器を、前記室内熱交換器の途中経路に設けた除湿弁の下流側に配し、
前記気液分離器から出口配管をバイパスするバイパス配管を配し、
前記バイパス配管経路途中に流量調整弁を設置し、
前記室内熱交換器の出口管路の近傍、および圧縮機吸込み側に、それぞれ熱交冷媒温度検知センサおよび圧縮機吸込み冷媒温度検知センサを設けたことを特徴とする空気調和機。
An outdoor unit including a compressor, a four-way valve, an outdoor heat exchanger, an expansion valve, and an outdoor air blowing device, an indoor heat exchanger, an indoor air blowing device, an indoor unit including a dehumidifying valve used during dehumidifying operation, and the indoor unit It is comprised by the connection piping which circulates a refrigerant | coolant inside the indoor heat exchanger and the said expansion valve provided in the said outdoor unit, The refrigerant | coolant is connected by connecting the said indoor heat exchanger, the said outdoor unit, and the said connection piping, respectively. In an air conditioner that configures a piping path and performs cooling operation and heating operation by circulating the refrigerant inside the refrigerant piping path,
During cooling operation, a gas-liquid separator is arranged in the middle of the heat exchange path of the indoor heat exchanger, and is arranged downstream of the dehumidification valve provided in the middle path of the indoor heat exchanger,
Arranging bypass piping to bypass the outlet piping from the gas-liquid separator,
Install a flow control valve in the bypass piping path,
An air conditioner characterized in that a heat exchange refrigerant temperature detection sensor and a compressor suction refrigerant temperature detection sensor are provided in the vicinity of the outlet pipe of the indoor heat exchanger and on the compressor suction side, respectively.
請求項1記載において、冷房運転時の冷媒の流れ方向で気液分離を作用させた場合、前記熱交冷媒温度検知センサおよび前記圧縮機吸込み冷媒温度検知センサにより得られる熱交冷媒温度および圧縮機吸込み冷媒温度が、
熱交冷媒温度<圧縮機吸込み冷媒温度
となるように、前記流量調整弁の絞りを調整することを特徴とする空気調和機。
2. The heat exchange refrigerant temperature and compressor obtained by the heat exchange refrigerant temperature detection sensor and the compressor suction refrigerant temperature detection sensor when gas-liquid separation is applied in the refrigerant flow direction during cooling operation according to claim 1. The suction refrigerant temperature is
An air conditioner characterized by adjusting a throttle of the flow rate adjusting valve so that a heat exchange refrigerant temperature <a compressor suction refrigerant temperature.
請求項1又は2において、冷房運転時の冷媒の流れ方向で気液分離を作用させた場合、前記気液分離器に接続する配管を
(流入配管の断面積)≒(ガス冷媒流出配管の断面積)+(液冷媒流出配管の断面積)
(ガス冷媒流出配管の断面積)<(液冷媒流出配管の断面積)
の条件を満たす気液分離器を有することを特徴とする空気調和機。
In claim 1 or 2, when gas-liquid separation is applied in the refrigerant flow direction during cooling operation, the pipe connected to the gas-liquid separator is (cross-sectional area of the inflow pipe) ≈ (disconnection of the gas refrigerant outflow pipe) (Area) + (Cross sectional area of liquid refrigerant outflow piping)
(Cross sectional area of gas refrigerant outflow pipe) <(Cross sectional area of liquid refrigerant outflow pipe)
An air conditioner comprising a gas-liquid separator that satisfies the following conditions.
請求項1乃至3の何れかにおいて、前記気液分離器の下流側に位置する前記室内熱交換器について、前記室内送風装置からの風速分布に応じて、前記室内熱交換器の各熱交配管Lの長さを、
風速が大の位置のL1<風速が小の位置のL2
と設定したことを特徴とする空気調和機。
4. The heat exchange pipe of the indoor heat exchanger according to claim 1, wherein the indoor heat exchanger located on the downstream side of the gas-liquid separator is in accordance with a wind speed distribution from the indoor blower. The length of L,
L1 where wind speed is large <L2 where wind speed is small
An air conditioner characterized in that
請求項1乃至3の何れかにおいて、前記気液分離器の下流側に位置する前記室内熱交換器について、前記室内送風装置からの風速分布に応じて、前記室内熱交換器の各冷媒流路配管の太さDを、
風速が小の位置のD1<風速が大の位置のD2
と設定したことを特徴とする空気調和機。
4. The refrigerant flow path of the indoor heat exchanger according to claim 1, wherein the indoor heat exchanger located on the downstream side of the gas-liquid separator has each refrigerant flow path of the indoor heat exchanger according to a wind speed distribution from the indoor air blower. The thickness D of the pipe
D1 where the wind speed is small <D2 where the wind speed is large
An air conditioner characterized in that
請求項1乃至5の何れかにおいて、前記気液分離器は円柱の形状を成し、その内径を35mm以上としたことを特徴とする空気調和機。   6. The air conditioner according to claim 1, wherein the gas-liquid separator has a cylindrical shape, and an inner diameter thereof is set to 35 mm or more.
JP2008194269A 2008-07-29 2008-07-29 Air conditioner Pending JP2010032104A (en)

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Publication number Priority date Publication date Assignee Title
CN104634000A (en) * 2013-11-14 2015-05-20 美的集团股份有限公司 Heat exchanger assembly, heat exchange system and air conditioner

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Publication number Priority date Publication date Assignee Title
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