JPH11108507A - Air conditioner - Google Patents
Air conditionerInfo
- Publication number
- JPH11108507A JPH11108507A JP27084797A JP27084797A JPH11108507A JP H11108507 A JPH11108507 A JP H11108507A JP 27084797 A JP27084797 A JP 27084797A JP 27084797 A JP27084797 A JP 27084797A JP H11108507 A JPH11108507 A JP H11108507A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- receiver
- desiccant
- dryer
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Abstract
(57)【要約】
【課題】レシーバにより余剰冷媒制御を行うマルチ型ヒ
ートポンプ式空気調和機において、暖房運転時液配管内
の冷媒が気液二相流になる影響を受けないで乾燥剤の摩
耗を防止するドライヤの設置法を示す。
【解決手段】アキュムレータ,圧縮機,四方弁,室外熱
交換器,室外膨張装置,レシーバを有する室外機におい
て、冷凍サイクル中の水分量を低減する乾燥剤が内封さ
れたドライヤを、前記室外膨張装置と前記レシーバとの
間に備える。
(57) [Problem] In a multi-type heat pump air conditioner in which surplus refrigerant is controlled by a receiver, abrasion of a desiccant without being affected by a refrigerant in a liquid pipe becoming a gas-liquid two-phase flow during a heating operation. The following describes how to install a dryer to prevent the occurrence. In an outdoor unit having an accumulator, a compressor, a four-way valve, an outdoor heat exchanger, an outdoor expansion device, and a receiver, a dryer in which a desiccant for reducing the amount of water in a refrigeration cycle is enclosed is subjected to the outdoor expansion. A device is provided between the device and the receiver.
Description
【0001】[0001]
【発明の属する技術分野】本発明は蒸気圧縮冷凍サイク
ルを利用して、複数の室内機を同時または個別に運転す
るマルチ型ヒートポンプ式空気調和機に関し、特に冷凍
サイクル中の水分を吸着するドライヤを、液冷媒配管途
中に設置する空気調和機に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multi-type heat pump type air conditioner in which a plurality of indoor units are operated simultaneously or individually using a vapor compression refrigeration cycle, and more particularly, to a dryer for adsorbing moisture in a refrigeration cycle. And an air conditioner installed in the middle of a liquid refrigerant pipe.
【0002】[0002]
【従来の技術】冷凍サイクル内に水分が存在する場合、
冷媒や油の分解劣化の原因となり酸が発生して、摺動部
の摩耗促進,電気絶縁材腐食による絶縁破壊,摺動部の
銅メッキ現象などを生じさせたり、水分自体が氷結した
り冷媒との水化物の生成により膨張装置やストレーナ等
を閉塞させるので、故障の原因となり信頼性を著しく低
下させる。これを回避するため、冷凍サイクル中の水分
を低減するドライヤを設置する方法がとられている。2. Description of the Related Art When moisture is present in a refrigeration cycle,
Acid is generated as a cause of decomposition and deterioration of the refrigerant and oil, causing accelerated wear of sliding parts, dielectric breakdown due to corrosion of electrical insulating material, copper plating phenomenon of sliding parts, freezing of water itself, The formation of hydrates causes clogging of the expansion device, strainer, and the like, which causes a failure and significantly lowers reliability. In order to avoid this, a method of installing a dryer for reducing the moisture in the refrigeration cycle has been adopted.
【0003】ところで、室内機を複数台接続して、同時
運転または個別運転を行うマルチ型ヒートポンプ式空気
調和機では、室内機の運転台数や運転条件の変化に応じ
て必要冷媒量が変化するため、余剰冷媒を貯留するレシ
ーバを室外膨張装置と室内膨張装置の間に設置してい
る。このレシーバの余剰冷媒制御を有効とするために
は、冷房運転時は主に室内膨張装置で膨張し、一方暖房
運転時は主に室外膨張装置で膨張するよう制御すること
が必要であり、この結果液冷媒配管には冷房および暖房
運転いずれでも定常的には常時液冷媒が流れるようにな
る。In a multi-type heat pump type air conditioner that performs simultaneous operation or individual operation by connecting a plurality of indoor units, the required amount of refrigerant changes according to the number of operating indoor units and changes in operating conditions. A receiver for storing the surplus refrigerant is provided between the outdoor expansion device and the indoor expansion device. In order to make the surplus refrigerant control of the receiver effective, it is necessary to perform control so that expansion is mainly performed by the indoor expansion device during the cooling operation, while expansion is mainly performed by the outdoor expansion device during the heating operation. As a result, the liquid refrigerant always flows through the liquid refrigerant pipe constantly in both the cooling operation and the heating operation.
【0004】一方、ドライヤの設置場所としては、ドラ
イヤを通過する冷媒の状態が液冷媒である部分に設置す
るのが好ましい。これは冷媒の密度が高いため水分との
接触確率が高いうえ、流速も低くなるので、水分吸着性
能および乾燥剤の摩耗防止の観点から好適である。冷房
および暖房運転いずれの場合でも液冷媒が流れる部分を
有するマルチ型ヒートポンプ式空気調和機において、液
冷媒配管途中にドライヤを設置する方法が、特開平8−3
27187 号公報,特開平9−21556号公報に開示されてい
る。これら従来の技術では、ドライヤは室外機内の冷房
運転時レシーバの後流となる位置に設置されている。On the other hand, it is preferable to install the dryer at a portion where the state of the refrigerant passing through the dryer is a liquid refrigerant. This is preferable from the viewpoints of moisture adsorption performance and prevention of abrasion of the desiccant since the probability of contact with moisture is high because the density of the refrigerant is high, and the flow velocity is low. In a multi-type heat pump air conditioner having a portion through which a liquid refrigerant flows in both cooling and heating operations, a method of installing a dryer in the middle of a liquid refrigerant pipe is disclosed in
No. 27187, and Japanese Patent Application Laid-Open No. 9-21556. In these conventional techniques, the dryer is installed at a position downstream of the receiver during the cooling operation in the outdoor unit.
【0005】[0005]
【発明が解決しようとする課題】前記従来の技術におい
ては、暖房運転において生ずる液冷媒配管の二相流に対
する乾燥剤摩耗防止への配慮がされていない。すなわ
ち、暖房運転時は厳密には室内膨張装置とレシーバの間
の液冷媒配管は完全な液単相ではなく、二相流になって
いる点に対する配慮がされていない。これを説明するた
め、レシーバの余剰冷媒調節機能について以下に述べ
る。In the above prior art, no consideration is given to the prevention of abrasion of a desiccant against a two-phase flow of a liquid refrigerant pipe generated during a heating operation. That is, during the heating operation, strictly, no consideration is given to the fact that the liquid refrigerant pipe between the indoor expansion device and the receiver is not a complete liquid single phase but a two-phase flow. To explain this, the surplus refrigerant adjustment function of the receiver is described below.
【0006】レシーバの余剰冷媒貯留量は流入冷媒の冷
媒かわき度、およびレシーバの周囲に対する放熱量によ
り、支配される。すなわち流入冷媒のかわき度が0でな
く気泡が入る場合、この気泡はレシーバ容器内上部の気
層に達するので、ここにガス冷媒がたまる。このガス冷
媒はレシーバ容器内側壁面や液層冷媒を介してレシーバ
容器周囲と熱交換するが、通常の運転ではレシーバ容器
内の温度の方が周囲の温度より高いので、ガス冷媒は放
熱して凝縮し、一部は液冷媒となり液層に吸収される。
このガス冷媒の凝縮量と、流入してくるガス冷媒の気泡
量がバランスしていない場合、例えば流入するガス冷媒
の方が、レシーバ容器内のガス冷媒量が増加するので、
これが液面を押し下げ、レシーバ容器内の液層冷媒を放
出することになる。[0006] The amount of surplus refrigerant stored in the receiver is governed by the degree of cleanness of the inflow refrigerant and the amount of heat released to the periphery of the receiver. That is, when the degree of dryness of the inflowing refrigerant is not 0 and air bubbles enter, the air bubbles reach the upper gas layer in the receiver container, and the gas refrigerant accumulates here. This gas refrigerant exchanges heat with the surroundings of the receiver container via the inner wall surface of the receiver container and the liquid layer refrigerant, but in normal operation, the temperature inside the receiver container is higher than the surrounding temperature, so the gas refrigerant releases heat and condenses. Then, a part becomes a liquid refrigerant and is absorbed by the liquid layer.
When the amount of condensed gas refrigerant and the amount of gas bubbles of the inflowing gas refrigerant are not balanced, for example, the inflowing gas refrigerant increases the amount of gas refrigerant in the receiver container.
This pushes down the liquid level and releases the liquid refrigerant in the receiver container.
【0007】これにより冷凍サイクル中を循環する冷媒
量が増えるので、適当な冷媒量になったところでレシー
バに流入する冷媒のかわき度も下がり気泡量が減るの
で、レシーバ液面は安定する。このようにレシーバの放
熱量により、レシーバに流入する冷媒のかわき度が決ま
る。ところで暖房運転時は外気温が低くレシーバ内の冷
媒との温度差が大きく、周囲への放熱量も増加するの
で、レシーバ内ではより多くのガス冷媒が凝縮すること
ができる。この結果として、レシーバに流入する冷媒の
かわき度は大きくなり、気泡がより多い気液二相流とな
る。As a result, the amount of the refrigerant circulating in the refrigeration cycle increases, and when the amount of the refrigerant reaches an appropriate amount, the degree of the refrigerant flowing into the receiver decreases, and the amount of the bubbles decreases, so that the liquid level of the receiver is stabilized. As described above, the degree of heat dissipation of the receiver determines the degree of cuteness of the refrigerant flowing into the receiver. By the way, during the heating operation, the outside air temperature is low, the temperature difference with the refrigerant in the receiver is large, and the amount of heat released to the surroundings increases, so that more gas refrigerant can be condensed in the receiver. As a result, the refrigerant flowing into the receiver has a higher degree of dryness, resulting in a gas-liquid two-phase flow with more bubbles.
【0008】前記従来の技術では、この比較的かわき度
の大きい気液二相流となる暖房運転時レシーバ入口側に
ドライヤを設置しているので、乾燥剤を通過する冷媒の
流速が、密度の低いガス冷媒が混入することでより高速
になるため、乾燥剤に対する流体力が増大し、乾燥剤の
摩耗を促進する原因となる。この結果乾燥剤の摩耗粉が
発生し、冷凍サイクル中を循環して圧縮機に達して摺動
部の摩耗の原因となったり、膨張装置など細部への詰ま
りを起こすので、空気調和機の信頼性を著しく低下させ
る問題がある。In the prior art, a dryer is installed at the receiver inlet side during the heating operation in which the gas-liquid two-phase flow having a relatively large degree of dryness is provided. Therefore, the flow rate of the refrigerant passing through the desiccant is reduced. Since higher speed is achieved by mixing the low gas refrigerant, the fluid force on the desiccant increases, which causes abrasion of the desiccant. As a result, abrasion powder of the desiccant is generated and circulates through the refrigeration cycle to reach the compressor, causing wear of the sliding parts and clogging of details such as the expansion device. There is a problem that the property is significantly reduced.
【0009】さらに前記従来の技術においては、冷房お
よび暖房運転によるドライヤ内の流れ方向の変化に対す
る乾燥剤摩耗防止への配慮がされていない。乾燥剤の摩
耗を防止するためには、冷房および暖房運転のいずれの
場合であっても乾燥剤が流れ方向後流に対し固定され、
擦れない様な構造を有することが必要である。Further, in the above-mentioned prior art, no consideration is given to prevention of abrasion of the desiccant due to a change in the flow direction in the dryer due to cooling and heating operations. In order to prevent the abrasion of the desiccant, the desiccant is fixed with respect to the wake in the flow direction in both the cooling operation and the heating operation,
It is necessary to have a structure that does not rub.
【0010】本発明の第一の目的は、冷房運転あるいは
暖房運転の双方に対し、乾燥剤の摩耗を防止するドライ
ヤを有する空気調和機を提供することにある。A first object of the present invention is to provide an air conditioner having a dryer for preventing abrasion of a desiccant during both a cooling operation and a heating operation.
【0011】一方、オゾン層保護の観点よりR22など
の既存冷媒の代替品であるR407C ,R407E,R41
0AなどのHFC(ハイドロフルオロカーボン)系冷媒
では、平均分子径が比較的小さく水分子に近いHFC3
2(ジフロロメタン)を成分として含む。ところで冷凍
サイクル中の水分を除去する乾燥剤として用いられる、
合成ゼオライトの一種であるモレキュラシーブスは、脱
水結晶格子により形成される細孔を通過する分子のみ吸
着する特徴を持つ。On the other hand, from the viewpoint of protection of the ozone layer, R407C, R407E and R41 which are alternatives to existing refrigerants such as R22.
In HFC (hydrofluorocarbon) -based refrigerants such as 0A, HFC3 whose average molecular diameter is relatively small and is close to water molecules
Contains 2 (difluoromethane) as a component. By the way, used as a desiccant to remove moisture in the refrigeration cycle,
Molecular sieves, which is a kind of synthetic zeolite, has a feature that only molecules passing through pores formed by a dehydrated crystal lattice are adsorbed.
【0012】このふるい効果のため、水分子のような細
孔を通過する比較的小さい分子を選択吸着し、かつ低水
分濃度でも高い水分吸着能力を有するため、冷媒用乾燥
剤としてよく使用されている。平均分子径が水に近いH
FC32は、従来のモレキュラシーブス乾燥剤に吸着さ
れやすく、水分吸着容量を低下させるばかりでなく、H
FC32が分解されて有害な物質が生成され、信頼性を
著しく低下させる問題がある。[0012] Because of this sieving effect, since it selectively adsorbs relatively small molecules passing through pores such as water molecules and has a high water adsorption ability even at a low water concentration, it is often used as a desiccant for refrigerant. I have. H whose average molecular diameter is close to water
FC32 is easily adsorbed by the conventional molecular sieve desiccant, not only reduces the water adsorption capacity, but also
There is a problem that FC32 is decomposed to generate harmful substances, which significantly lowers reliability.
【0013】また、これらHFC系冷媒では、冷媒との
相溶性を確保して油戻りの上で好適な冷凍機油として、
エステル系やエーテル系の冷凍機油が使用される。とこ
ろでエステル系冷凍機油は加水分解反応により有機酸が
発生し、またエーテル系冷媒では酸化劣化反応により過
酸化物が発生して最終的には酸に至るまで酸化され、冷
凍機油の全酸価を上昇させ、摺動部の摩耗促進,電気絶
縁材腐食による絶縁破壊,摺動部の銅メッキ現象などを
生じさせる問題がある。ドライヤに使用される材料とし
ては、以上を踏まえた物を選定する必要があるが、前記
従来の技術では、これらの点に対する配慮がされていな
い。[0013] In addition, these HFC-based refrigerants are suitable as refrigerating machine oils which ensure compatibility with the refrigerant and are suitable for oil return.
Ester or ether refrigeration oils are used. By the way, an ester-based refrigerating machine oil generates an organic acid by a hydrolysis reaction, and an ether-based refrigerant generates a peroxide by an oxidative deterioration reaction and is finally oxidized to an acid, thereby reducing the total acid value of the refrigerating machine oil. This raises the problem of raising the wear of the sliding part, causing dielectric breakdown due to corrosion of the electrical insulating material, and causing copper plating on the sliding part. As the material used for the dryer, it is necessary to select a material based on the above. However, the above-mentioned conventional technology does not consider these points.
【0014】本発明の第二の目的は、冷媒および冷凍機
油の劣化を防止する乾燥剤や、潤滑性を向上する冷凍機
油の成分を示し、信頼性をより一層高めた空気調和機を
提供することにある。A second object of the present invention is to provide a desiccant for preventing deterioration of the refrigerant and the refrigerating machine oil and a component of the refrigerating machine oil for improving lubricating properties, and to provide an air conditioner with further improved reliability. It is in.
【0015】さらに、冷凍サイクルの性能を高めるため
に、室外機に過冷却熱交換器を備える場合や、凝縮液冷
媒と、低圧ガス冷媒の間で熱交換を行う液ガス熱交換器
を備える場合について、前記従来の技術では配慮がされ
ていない。Further, in order to enhance the performance of the refrigeration cycle, a case where the outdoor unit is provided with a supercooling heat exchanger, or a case where a liquid / gas heat exchanger for exchanging heat between the condensed liquid refrigerant and the low-pressure gas refrigerant is provided. No consideration is given to the above-mentioned conventional technology.
【0016】本発明の第三の目的は、過冷却熱交換器や
液ガス熱交換器を備える場合のドライヤの設置箇所を示
し、性能を一層高めた空気調和機を提供することにあ
る。A third object of the present invention is to provide an air conditioner which shows a place where a dryer is installed when a subcooling heat exchanger or a liquid-gas heat exchanger is provided, and further improves performance.
【0017】[0017]
【課題を解決するための手段】本発明の第一の目的を達
成するために、アキュムレータ,圧縮機,四方弁,室外
熱交換器,室外膨張装置,レシーバを有する室外機と、
室内膨張装置,室内熱交換器を有する複数の室内機と
を、液接続配管,ガス接続配管により接続し、冷媒およ
び冷凍機油を封入してなる冷凍サイクルを構成し、前記
四方弁の切り換えにより冷房運転または暖房運転を行
い、冷房運転時は主に前記室内膨張装置で膨張され、一
方暖房運転時は主に前記室外膨張装置で膨張される、ヒ
ートポンプ式空気調和機において、前記冷凍サイクル中
の水分量を低減する乾燥剤が内封されたドライヤを、前
記室外膨張装置と前記レシーバとの間に備える手段を採
用する。In order to achieve the first object of the present invention, an outdoor unit having an accumulator, a compressor, a four-way valve, an outdoor heat exchanger, an outdoor expansion device, and a receiver is provided.
A plurality of indoor units having an indoor expansion device and an indoor heat exchanger are connected by a liquid connection pipe and a gas connection pipe to constitute a refrigeration cycle in which a refrigerant and a refrigerating machine oil are sealed, and cooling is performed by switching the four-way valve. In a heat pump type air conditioner, an operation or a heating operation is performed, and is mainly expanded by the indoor expansion device during a cooling operation, and is mainly expanded by the outdoor expansion device during a heating operation. Means for providing a dryer in which a desiccant for reducing the amount is enclosed between the outdoor expansion device and the receiver is adopted.
【0018】この位置にドライヤを設置することによ
り、暖房運転時はレシーバ底部より導出される液単相冷
媒がドライヤを通過するので、前記課題で示したような
気液二相流となることがない。また、冷房運転時におい
ては、外気温度が暖房運転時より高いので、レシーバ容
器周囲の温度も高く、レシーバ容器内のガス冷媒の凝縮
量も少ない。このため、冷房運転時ドライヤがレシーバ
入口側であっても、ほとんど気泡が入らない液単相に近
い冷媒の状態となる。以上により、冷房および暖房運転
を通じて、乾燥剤の摩耗がほとんど生じないようにする
ことができる。By installing a dryer at this position, during the heating operation, the liquid single-phase refrigerant derived from the bottom of the receiver passes through the dryer, so that a gas-liquid two-phase flow as described in the above problem may occur. Absent. In the cooling operation, the outside air temperature is higher than in the heating operation, so that the temperature around the receiver container is high and the amount of gas refrigerant condensed in the receiver container is small. For this reason, even when the dryer is on the inlet side of the receiver during the cooling operation, the refrigerant is in a state of a liquid single phase with almost no air bubbles. As described above, the wear of the desiccant can be substantially prevented from occurring during the cooling and heating operations.
【0019】さらに、本発明の第一の目的を達成するた
めに、ドライヤは、冷房運転または暖房運転いずれの場
合においても、前記乾燥剤における冷媒の通過方向が一
方向に整流されるよう、弁機構による冷媒回路を備える
手段を採用する。Further, in order to achieve the first object of the present invention, the dryer is provided with a valve so that the passage direction of the refrigerant in the desiccant is rectified in one direction in either the cooling operation or the heating operation. Means including a refrigerant circuit by a mechanism is adopted.
【0020】本手段によれば、乾燥剤における冷媒の通
過方向が常に一方向であるので、乾燥剤の固定方法が容
易となり、また流れ方向の変化による乾燥剤の動きも抑
制されるので、乾燥剤の摩耗防止に対して大きい効果を
得ることが出来る。According to this means, since the passage of the refrigerant through the desiccant is always one direction, the method of fixing the desiccant becomes easy, and the movement of the desiccant due to the change in the flow direction is suppressed. A great effect can be obtained for the prevention of wear of the agent.
【0021】なお、本発明においてドライヤの接続部
が、ドライヤの交換が可能な接続形態とする手段を採用
することは、圧縮機やサイクル部品の交換時において、
ドライヤも新品に交換して水分除去能力を復活させて、
交換作業時に混入する水分を除去できるので、誠に好ま
しい形態である。交換可能な接続形態とは、例えばユニ
オンとフレアナットによる接続方法が挙げられる。In the present invention, the means for setting the connection portion of the dryer so that the dryer can be replaced is adopted when replacing the compressor or cycle parts.
Replace the dryer with a new one and restore the water removal ability.
This is indeed the preferred form, since it is possible to remove water mixed during the replacement operation. The exchangeable connection form includes, for example, a connection method using a union and a flare nut.
【0022】次に、本発明の第二の目的を達成するため
に、冷媒にHFC系冷媒を使用したとき、特にHFC3
2が含まれるHFC系混合冷媒を使用したときに、乾燥
剤にKカチオン交換率を0.25 以上としたNaA型モ
レキュラシーブスを使用する手段を採用する。さらに
は、乾燥剤はモレキュラシーブス結晶50%以上を有
し、結晶を繋ぐバインダにアルミナ,リン酸系物質を使
用しない手段を採用する。Next, in order to achieve the second object of the present invention, when an HFC-based refrigerant is used
When an HFC-based mixed refrigerant containing No. 2 is used, a means using NaA-type molecular sieves having a K cation exchange rate of 0.25 or more as a desiccant is employed. Further, the desiccant has a molecular sieve crystal of 50% or more, and a means that does not use an alumina or phosphoric acid-based substance as a binder connecting the crystals is employed.
【0023】NaA型モレキュラシーブスは、結晶格子
中のNa(ナトリウム)カチオンにより、その細孔径が
約4Åとなっている。このため平均分子径が3.3ÅのH
FC32が容易に通過してしまう。ところがNaカチオンを
K(カリウム)カチオンに置換することで、細孔径をよ
り狭めることができ、細孔径を3Åとできる。細孔径に
影響する殆どのNaカチオンがKカチオンに置換するた
めにはその交換率が0.25 であることが必要なので、
HFC32の吸着量低減のために、それ以上のKカチオ
ン置換率とした。The NaA-type molecular sieve has a pore diameter of about 4 ° due to Na (sodium) cation in the crystal lattice. Therefore, the average molecular diameter of H
FC32 passes easily. However, by replacing the Na cation with the K (potassium) cation, the pore diameter can be further narrowed, and the pore diameter can be reduced to 3 mm. In order for most Na cations affecting the pore diameter to be replaced by K cations, the exchange rate must be 0.25,
In order to reduce the amount of HFC32 adsorbed, the K cation substitution rate was set to a higher value.
【0024】また、乾燥剤のバインダにアルミナやリン
酸系物質を使用すると、エステル系やエーテル系の冷凍
機油の劣化を促進するばかりか、酸捕捉剤や極圧添加剤
などを吸着消費してしまうので、これらを含まない上
に、モレキュラシーブス結晶も50%以上多量に含まれ
ることとすることが、冷凍機油の劣化防止に効果的であ
る。When alumina or phosphoric acid is used as a desiccant binder, it not only promotes deterioration of ester or ether refrigerating machine oils, but also adsorbs and consumes acid scavengers and extreme pressure additives. Therefore, it is effective to prevent the deterioration of the refrigerating machine oil by including not only these but also a large amount of molecular sieve crystals of 50% or more.
【0025】さらに、本発明の第二の目的を達成するた
めに、冷凍機油にエステル系冷凍機油を使用する手段を
採用する。Further, in order to achieve the second object of the present invention, means for using an ester-based refrigerating machine oil as the refrigerating machine oil is employed.
【0026】エステル系冷凍機油とは、例えばペンタエ
リスリトールやトリメチロールプロパンのような多価ア
ルコールと、炭素数5から9の直鎖または分岐脂肪酸を
エステル化反応させて得られるエステルを主成分とする
冷凍機油であり、分子構造中のカルボニル基の分極作用
により、分子分極の大きいHFC系冷媒と相溶性が高
く、耐荷重性にも優れるものである。本発明のドライヤ
と併用することで、加水分解の原因である水分が低減さ
れているので、エステルの加水分解を抑制し、有機酸の
発生を防止することができる。The ester refrigerating machine oil is mainly composed of an ester obtained by subjecting a polyhydric alcohol such as pentaerythritol or trimethylolpropane to an esterification reaction of a linear or branched fatty acid having 5 to 9 carbon atoms. It is a refrigerating machine oil that has high compatibility with HFC-based refrigerants having large molecular polarization due to the polarization action of carbonyl groups in the molecular structure, and has excellent load resistance. When used in combination with the dryer of the present invention, the water that causes the hydrolysis is reduced, so that the hydrolysis of the ester can be suppressed and the generation of organic acids can be prevented.
【0027】さらに、本発明の第二の目的を達成するた
めに、冷凍機油にエーテル系冷凍機油を使用する手段を
採用し、さらにはこのエーテル系冷凍機油にリン酸エス
テル系極圧添加剤0.1% 以上を添加する手段を採用す
る。Further, in order to achieve the second object of the present invention, means for using an ether-based refrigerating machine oil as the refrigerating machine oil is employed. Use a means of adding 1% or more.
【0028】エーテル系冷凍機油とは、分子結合中にエ
ーテル結合を含む直鎖または環状炭化水素を主成分とす
る冷凍機油のことで、この分極作用により、分子分極の
大きいHFC系冷媒と相溶性が高い。本発明のドライヤ
と併用することで、酸化劣化加速の要因である水分が低
減されているので、酸化劣化を抑制し、有機酸の発生を
防止することができる。さらに耐荷重性を改善するリン
酸エステル系極圧添加剤、例えばTCP(トリクレジル
ホスフェイト)を添加しても、水分と反応して加水分解
してしまうことを防止できるので、添加剤も有効に作用
することができる。リン酸エステル系極圧添加剤による
潤滑性改善の効果が得られる、0.1%以上の添加が有
効である。The ether-based refrigerating machine oil is a refrigerating machine oil containing a linear or cyclic hydrocarbon containing an ether bond in a molecular bond as a main component, and is compatible with an HFC-based refrigerant having a large molecular polarization by its polarization action. Is high. When used in combination with the dryer of the present invention, moisture, which is a factor of acceleration of oxidative deterioration, is reduced, so that oxidative deterioration can be suppressed and generation of organic acids can be prevented. Furthermore, even if a phosphate ester-based extreme pressure additive for improving load resistance, for example, TCP (tricresyl phosphate) is added, it is possible to prevent hydrolysis by reaction with moisture. It can work effectively. The addition of 0.1% or more, which is effective in improving the lubricity by the phosphate extreme pressure additive, is effective.
【0029】次に、本発明の第三の目的を達成するため
に、室外膨張装置とドライヤの間に、過冷却熱交換機を
備える手段を採用する。Next, in order to achieve the third object of the present invention, means for providing a supercooling heat exchanger between the outdoor expansion device and the dryer is employed.
【0030】さらに本発明の第三の目的を達成するため
に、アキュムレータ前流または後流の低圧ガス冷媒と、
冷房運転時前記レシーバ後流の高圧液冷媒との間で熱交
換を行う液ガス熱交換器を備える手段を採用する。In order to further achieve the third object of the present invention, a low-pressure gas refrigerant upstream or downstream of an accumulator is provided.
In the cooling operation, a means including a liquid-gas heat exchanger for performing heat exchange with the high-pressure liquid refrigerant downstream of the receiver is employed.
【0031】過冷却熱交換器およびガス液熱交換器を使
用することで、より一層高い熱交換効率を得ることがで
き、空気調和機の性能を向上するのに極めて有効な手段
である。By using a supercooling heat exchanger and a gas-liquid heat exchanger, a higher heat exchange efficiency can be obtained, which is a very effective means for improving the performance of an air conditioner.
【0032】[0032]
【発明の実施の形態】以下、図面を参照して実施の形態
を説明する。図1は、本発明の第1の実施の形態を示す
冷凍サイクルの構成図である。1はインバータ可変容量
圧縮機、2は一定速圧縮機、3はアキュムレータ、4は
オイルタンク、5は四方弁、6は室外熱交換器、7は室
外送風機、8は室外膨張装置、9は過冷却熱交換器、1
0はドライヤ、11はモイスチャーインジケータ、12
はレシーバ、13はガス液熱交換器、14は液阻止弁、
20はガス阻止弁であり、室外機21を構成する。ま
た、16a,16bは室内膨張装置、17a,17bは
室内熱交換器、18a,18bは室内送風機であり、室
内機22a,22bを構成する。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram of a refrigeration cycle showing a first embodiment of the present invention. 1 is an inverter variable displacement compressor, 2 is a constant speed compressor, 3 is an accumulator, 4 is an oil tank, 5 is a four-way valve, 6 is an outdoor heat exchanger, 7 is an outdoor blower, 8 is an outdoor expansion device, and 9 is excess. Cooling heat exchanger, 1
0 is dryer, 11 is moisture indicator, 12
Is a receiver, 13 is a gas-liquid heat exchanger, 14 is a liquid check valve,
Reference numeral 20 denotes a gas check valve, which constitutes an outdoor unit 21. Further, 16a and 16b are indoor expansion devices, 17a and 17b are indoor heat exchangers, and 18a and 18b are indoor blowers, which constitute indoor units 22a and 22b.
【0033】さらに、室内機22a,22bは、液接続
配管15,ガス接続配管19で室外機21に連結され、
インバータ可変容量圧縮機1または一定速圧縮機2のい
ずれかまたは同時の運転、および室外送風機15,室内
送風機16の運転により、空気調和が行われる。Further, the indoor units 22a and 22b are connected to the outdoor unit 21 by a liquid connection pipe 15 and a gas connection pipe 19,
Air conditioning is performed by operating either the inverter variable displacement compressor 1 or the constant speed compressor 2 or simultaneously and operating the outdoor blower 15 and the indoor blower 16.
【0034】作動流体として用いられる冷媒にはオゾン
層を破壊しないハイドロフルオロカーボン(HFC)か
ら構成される冷媒を使用するのがよく、例えばR407
C,R407E,R410A,R404A,R507A
が挙げられるが、本実施例ではジフルオロメタン(HF
C32),ペンタフルオロエタン(HFC125)、
1,1,1,2−テトラフルオロエタン(HFC134
a)の三種類が各々23:25:52重量%で構成され
ているR407Cを使用する。As the refrigerant used as the working fluid, it is preferable to use a refrigerant composed of hydrofluorocarbon (HFC) which does not destroy the ozone layer.
C, R407E, R410A, R404A, R507A
In this embodiment, difluoromethane (HF) is used.
C32), pentafluoroethane (HFC125),
1,1,1,2-tetrafluoroethane (HFC134
R407C is used in which each of the three types a) is composed of 23: 25: 52% by weight.
【0035】また、冷媒と組み合わせる冷凍機油とし
て、冷凍サイクル内の油戻り性の観点から相溶性のある
エステル系,エーテル系、またはカーボネート系冷凍機
油を使用するのが有効である。これらの冷凍機油はHF
C冷媒と溶解性を持たせるために、カルボニル基やエー
テル結合など酸素原子導入による極性分子を基材に使用
している。本実施例ではエーテル系冷凍機油を使用する
こととする。さらにこの冷凍機油にリン酸エステル系極
圧添加剤TCP(トリクレジルホスフェイト)を0.3
% 添加した物を使用する。As a refrigerating machine oil to be combined with a refrigerant, it is effective to use a compatible ester, ether or carbonate refrigerating machine oil from the viewpoint of oil return in the refrigerating cycle. These refrigerating machine oils are HF
In order to have solubility with the C refrigerant, a polar molecule such as a carbonyl group or an ether bond by introducing an oxygen atom is used for the base material. In this embodiment, an ether-based refrigerator oil is used. Furthermore, a phosphate ester-based extreme pressure additive TCP (tricresyl phosphate) was added to this refrigerator oil at 0.3.
Use the added product.
【0036】また、ドライヤ10の乾燥剤にはKカチオ
ン交換率を0.25以上としたNaA型モレキュラシーブ
スを使用する。さらに、乾燥剤はモレキュラシーブス結
晶50%以上を有し、かつ結晶を繋ぐバインダにアルミ
ナ,リン酸系物質を使用していないものを適用する。As the desiccant of the dryer 10, NaA type molecular sieves having a K cation exchange rate of 0.25 or more is used. Further, a desiccant having a molecular sieve crystal of 50% or more and using no alumina or phosphoric acid-based substance as a binder connecting the crystals is used.
【0037】次に本発明の動作を説明する。まず冷房運
転の場合、インバータ可変容量圧縮機1または一定速圧
縮機2から吐出されたガス冷媒は、室外熱交換器6で凝
縮する。凝縮液冷媒は室外膨張装置8で絞られることな
く過冷却熱交換器9で殆どかわき度0の液冷媒となって
ドライヤ10を通過し脱水される。冷房運転時において
は、外気温度が暖房運転時より高いので、レシーバ12
容器周囲の温度も高く、レシーバ容器内のガス冷媒の凝
縮量も少ない。Next, the operation of the present invention will be described. First, in the case of the cooling operation, the gas refrigerant discharged from the inverter variable displacement compressor 1 or the constant speed compressor 2 is condensed in the outdoor heat exchanger 6. The condensed liquid refrigerant is not throttled by the outdoor expansion device 8, becomes a liquid refrigerant of almost zero cuteness in the supercooling heat exchanger 9, passes through the dryer 10, and is dehydrated. During the cooling operation, the outside air temperature is higher than during the heating operation.
The temperature around the container is high, and the amount of gas refrigerant condensed in the receiver container is small.
【0038】このため、冷房運転時ドライヤ10がレシ
ーバ入口側であっても、ほとんど気泡が入らない液単相
に近い冷媒が通過するので、乾燥剤が摩耗することがな
い。レシーバ12を出た液冷媒はさらにガス液熱交換器
13において放熱して過冷却されるので、室内膨張装置
16a,16bにて膨張された冷媒の室内熱交換器17
a,17b入口での比エンタルピが小さくなるので、冷
媒の潜熱が有効に利用され、性能を向上させる効果があ
る。For this reason, even when the dryer 10 is on the receiver inlet side during the cooling operation, the refrigerant near the liquid single phase containing almost no air bubbles passes therethrough, so that the desiccant does not wear. The liquid refrigerant that has exited the receiver 12 is further radiated and supercooled in the gas-liquid heat exchanger 13, so that the refrigerant expanded in the indoor expansion devices 16a and 16b is used in the indoor heat exchanger 17 of the refrigerant.
Since the specific enthalpy at the inlets a and 17b is reduced, the latent heat of the refrigerant is effectively used, and the performance is improved.
【0039】室内熱交換器17a,17bで蒸発気化し
たガス冷媒は、室外機21に戻り、ガス液熱交換器13
で液冷媒から受熱して加熱されるので、圧縮機吸入部で
の過熱度が適度に付き、湿り圧縮しないので圧縮機の効
率が高い条件で運転でき、性能が向上する。さらに液冷
媒がアキュムレータ3に貯留されにくくなるので、非共
沸冷媒特有の組成変動を防止することができる。The gas refrigerant evaporated and vaporized in the indoor heat exchangers 17a and 17b returns to the outdoor unit 21 and is returned to the gas liquid heat exchanger 13
Since the heat is received from the liquid refrigerant and heated, the degree of superheat at the compressor suction section is moderate, and the compressor is not wet-compressed, so that the compressor can be operated under high efficiency conditions and the performance is improved. Further, since the liquid refrigerant is less likely to be stored in the accumulator 3, the composition fluctuation peculiar to the non-azeotropic refrigerant can be prevented.
【0040】次に暖房運転の場合を説明する。インバー
タ可変容量圧縮機1または一定速圧縮機2から吐出され
たガス冷媒は、室内熱交換器17a,17bで凝縮す
る。暖房運転では外気温度が低いので、レシーバ12の
放熱量も大きくなり、レシーバ12容器内でのガス冷媒
凝縮量は増加して、液接続管15等を通過する冷媒は、
気液二相となっている。しかしレシーバ12導出管は下
部の液冷媒を導出してドライヤ10に至るので、ドライ
ヤ10を通過する冷媒は殆どかわき度0の液冷媒とな
り、乾燥剤が摩耗することがない。さらに過冷却熱交換
器9で過冷却するので液冷媒の比エンタルピは小さくな
り、冷媒の潜熱が有効に利用され、性能を向上させる効
果がある。Next, the case of the heating operation will be described. The gas refrigerant discharged from the inverter variable displacement compressor 1 or the constant speed compressor 2 is condensed in the indoor heat exchangers 17a and 17b. In the heating operation, since the outside air temperature is low, the heat radiation amount of the receiver 12 also increases, the amount of gas refrigerant condensed in the receiver 12 container increases, and the refrigerant passing through the liquid connection pipe 15 and the like,
It is a gas-liquid two-phase. However, the outlet pipe of the receiver 12 draws out the lower liquid refrigerant and reaches the dryer 10, so that the refrigerant passing through the dryer 10 becomes almost zero in the liquid refrigerant, and the desiccant does not wear. Further, since the liquid refrigerant is supercooled by the supercooling heat exchanger 9, the specific enthalpy of the liquid refrigerant is reduced, and the latent heat of the refrigerant is effectively used, thereby improving the performance.
【0041】本実施例では、ドライヤ10により酸化劣
化加速の要因である水分が低減されているので、酸化劣
化を抑制し、有機酸の発生を防止することができる。さ
らにリン酸エステル系極圧添加剤が水分と反応して加水
分解してしまうことを防止できるので、添加剤も有効に
作用することができる。In this embodiment, since the moisture which is a factor of acceleration of the oxidative deterioration is reduced by the dryer 10, the oxidative deterioration can be suppressed and the generation of the organic acid can be prevented. Further, since the phosphate extreme pressure additive can be prevented from reacting with water and being hydrolyzed, the additive can also act effectively.
【0042】また、乾燥剤NaA型モレキュラシーブス
のK(カリウム)カチオン置換率を0.25 以上とした
ので、モレキュラシーブスの細孔径を約3Åとすること
ができ、平均分子径が3.3Å のHFC32の吸着量が
低減されたので、水分吸着容量を低下させることや、H
FC32が分解されて有害な物質が生成されることをほ
とんどなくすことができる。Further, since the K (potassium) cation substitution rate of the desiccant NaA type molecular sieve is 0.25 or more, the pore diameter of the molecular sieve can be about 3 mm, and the average molecular diameter is 3.3 mm. Since the adsorption amount of HFC32 has been reduced, it is possible to reduce the water adsorption capacity,
FC32 can be almost completely decomposed to generate harmful substances.
【0043】また、乾燥剤のバインダにアルミナやリン
酸系物質を使用していないうえ、モレキュラシーブスの
結晶を50%以上含んだ乾燥剤を使用するので、冷凍機
油の劣化を促進することがなく、酸捕捉剤や極圧添加剤
などが著しく減少したり冷凍機油が劣化されることがな
い。Further, since the binder of the desiccant does not use alumina or a phosphoric acid-based substance and uses a desiccant containing at least 50% of molecular sieve crystals, deterioration of the refrigerating machine oil is not promoted. In addition, the acid scavenger, extreme pressure additive and the like are not significantly reduced, and the refrigerating machine oil is not deteriorated.
【0044】図2は、本発明の第1の実施の形態に使用
されるドライヤの第一例を示す構成図である。30は容
器、31は乾燥剤、32はフィルタ、33,34,3
5,36は整流弁、37はユニオンを示す。FIG. 2 is a configuration diagram showing a first example of a dryer used in the first embodiment of the present invention. 30 is a container, 31 is a desiccant, 32 is a filter, 33, 34, 3
Reference numerals 5 and 36 denote rectifying valves, and 37 denotes a union.
【0045】図3は、本発明の第1の実施の形態に使用
されるドライヤの第二例を示す構成図である。40は容
器、41は乾燥剤、42はフィルタ、43はバネ、44
はフレア継手、45は逆止弁を示す。FIG. 3 is a configuration diagram showing a second example of a dryer used in the first embodiment of the present invention. 40 is a container, 41 is a desiccant, 42 is a filter, 43 is a spring, 44
Denotes a flare joint, and 45 denotes a check valve.
【0046】いずれのドライヤの構造とも整流弁33,
34,35,36,逆止弁45の整流効果により、冷房
時は実線矢印、暖房時は点線矢印の方向へ冷媒が流れ
る。本実施例によれば、乾燥剤31,41における冷媒
の通過方向が常に一方向であるので、乾燥剤31,41
の固定方法が容易となり、また流れ方向の変化による乾
燥剤の動きも抑制されるので、乾燥剤の摩耗防止に対し
て大きい効果を得ることが出来る。The rectifying valve 33,
Due to the rectifying effects of the valves 34, 35, 36 and the check valve 45, the refrigerant flows in the direction of the solid arrow during cooling and in the direction of the dotted arrow during heating. According to the present embodiment, the passage direction of the refrigerant in the desiccants 31 and 41 is always one direction.
Since the method of fixing the desiccant becomes easy and the movement of the desiccant due to the change in the flow direction is suppressed, a great effect can be obtained in preventing the desiccant from being worn.
【0047】なお、本実施例においてドライヤの容器3
0,40の接続部が、ドライヤの交換が可能なフレアナ
ットによる接続方法となっているので、圧縮機やサイク
ル部品の交換時において、ドライヤも新品に交換して水
分除去能力を復活させて、交換作業時に混入する水分を
除去できるので、信頼性を向上させることができる。In this embodiment, the dryer container 3
Since the connection portion of 0, 40 is a connection method using a flare nut that can replace the dryer, when replacing the compressor or cycle parts, the dryer is also replaced with a new one to restore the moisture removal ability, Since moisture mixed during the replacement operation can be removed, reliability can be improved.
【0048】[0048]
【発明の効果】本発明によれば、乾燥剤の摩耗を防止で
きるので、摺動部摩耗増大や細部詰まりを生じることが
なく、さらに冷媒および冷凍機油の分解劣化を防止し、
添加剤の効果を最大限引き出すことができるので、信頼
性の高い空気調和機を得ることができる。According to the present invention, since the abrasion of the desiccant can be prevented, the abrasion of the sliding portion does not increase and clogging of the details does not occur, and the degradation of the refrigerant and the refrigerating machine oil is prevented.
Since the effect of the additive can be maximized, a highly reliable air conditioner can be obtained.
【0049】さらに、本発明によれば、熱交換性能を有
効に引き出せるので、性能が一層向上された空気調和機
を得ることができる。Further, according to the present invention, since the heat exchange performance can be effectively brought out, an air conditioner with further improved performance can be obtained.
【図1】本発明の第1の実施の形態を示す冷凍サイクル
の構成図。FIG. 1 is a configuration diagram of a refrigeration cycle showing a first embodiment of the present invention.
【図2】本発明の第1の実施の形態に使用されるドライ
ヤの第一例を示す構成図。FIG. 2 is a configuration diagram showing a first example of a dryer used in the first embodiment of the present invention.
【図3】本発明の第1の実施の形態に使用されるドライ
ヤの第二例を示す構成図。FIG. 3 is a configuration diagram showing a second example of a dryer used in the first embodiment of the present invention.
1…インバータ可変容量圧縮機、2…一定速圧縮機、3
…アキュムレータ、4…オイルタンク、5…四方弁、6
…室外熱交換器、7…室外送風機、8…室外膨張装置、
9…過冷却熱交換器、10…ドライヤ、11…モイスチ
ャーインジケータ、12…レシーバ、13…ガス液熱交
換器、14…液阻止弁、15…液接続配管、16a,1
6b…室内膨張装置、17a,17b…室内熱交換器、
18a,18b…室内送風機、19…ガス接続配管、2
0…ガス阻止弁、21…室外機、22a,22b…室内
機、30,40…容器、31,41…乾燥剤、32,4
2…フィルタ、33,34,35,36…整流弁、37
…ユニオン、43…バネ、44…フレア継手、45…逆
止弁。1 ... Inverter variable displacement compressor, 2 ... Constant speed compressor, 3
... accumulator, 4 ... oil tank, 5 ... four-way valve, 6
... outdoor heat exchanger, 7 ... outdoor blower, 8 ... outdoor expansion device,
9 ... Supercooling heat exchanger, 10 ... Dryer, 11 ... Moisture indicator, 12 ... Receiver, 13 ... Gas liquid heat exchanger, 14 ... Liquid check valve, 15 ... Liquid connection piping, 16a, 1
6b indoor expansion device, 17a, 17b indoor heat exchanger,
18a, 18b: indoor blower, 19: gas connection pipe, 2
0: gas check valve, 21: outdoor unit, 22a, 22b: indoor unit, 30, 40: container, 31, 41: desiccant, 32, 4
2. Filter, 33, 34, 35, 36 ... Rectifying valve, 37
... union, 43 ... spring, 44 ... flare joint, 45 ... check valve.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 中山 進 静岡県清水市村松390番地 株式会社日立 製作所空調システム事業部内 (72)発明者 坪江 宏明 静岡県清水市村松390番地 株式会社日立 製作所空調システム事業部内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Susumu Nakayama 390 Muramatsu, Shimizu-shi, Shizuoka Prefecture Inside Air Conditioning Systems Division, Hitachi, Ltd. (72) Inventor Hiroaki Tsuboe 390 Muramatsu, Shimizu-shi, Shizuoka Air Conditioning System, Hitachi, Ltd. Within the business division
Claims (1)
交換器,室外膨張装置,レシーバを有する室外機と、室
内膨張装置,室内熱交換器を有する複数の室内機とを、
液接続配管,ガス接続配管により接続し、冷媒および冷
凍機油を封入してなる冷凍サイクルを構成し、前記四方
弁の切り換えにより冷房運転または暖房運転を行い、冷
房運転時は主に前記室内膨張装置で膨張され、一方暖房
運転時は主に前記室外膨張装置で膨張される、ヒートポ
ンプ式空気調和機において、前記冷凍サイクル中の水分
量を低減する乾燥剤が内封されたドライヤを、前記室外
膨張装置と前記レシーバとの間に備えたことを特徴とす
る空気調和機。An outdoor unit having an accumulator, a compressor, a four-way valve, an outdoor heat exchanger, an outdoor expansion device, and a receiver, and a plurality of indoor units having an indoor expansion device, an indoor heat exchanger,
A refrigeration cycle in which a refrigerant and a refrigerating machine oil are sealed is connected by a liquid connection pipe and a gas connection pipe, and a cooling operation or a heating operation is performed by switching the four-way valve. During the cooling operation, the indoor expansion device is mainly used. In the heat pump type air conditioner, which is expanded mainly by the outdoor expansion device during the heating operation, the dryer in which the desiccant for reducing the amount of water in the refrigeration cycle is enclosed is subjected to the outdoor expansion. An air conditioner provided between a device and the receiver.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27084797A JPH11108507A (en) | 1997-10-03 | 1997-10-03 | Air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27084797A JPH11108507A (en) | 1997-10-03 | 1997-10-03 | Air conditioner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11108507A true JPH11108507A (en) | 1999-04-23 |
Family
ID=17491828
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27084797A Pending JPH11108507A (en) | 1997-10-03 | 1997-10-03 | Air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11108507A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1473526A3 (en) * | 2003-05-01 | 2005-09-07 | LG Electronics Inc. | Air conditioner and outdoor unit therefor |
| EP1475585A3 (en) * | 2003-05-01 | 2005-09-07 | Lg Electronics Inc. | Air conditioner and outdoor unit therefor |
| JP2006162081A (en) * | 2004-12-02 | 2006-06-22 | Hitachi Ltd | Refrigeration cycle equipment |
| JP2009139037A (en) * | 2007-12-07 | 2009-06-25 | Mitsubishi Heavy Ind Ltd | Refrigerant circuit |
| JP2013113470A (en) * | 2011-11-28 | 2013-06-10 | Fuji Koki Corp | Refrigerant drier |
| JP2013117345A (en) * | 2011-12-02 | 2013-06-13 | Fuji Koki Corp | Refrigerant dryer |
| JP2021162213A (en) * | 2020-03-31 | 2021-10-11 | ダイキン工業株式会社 | Refrigeration cycle equipment |
| US11519642B2 (en) | 2017-06-22 | 2022-12-06 | Lg Electronics Inc. | Air conditioner |
-
1997
- 1997-10-03 JP JP27084797A patent/JPH11108507A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1473526A3 (en) * | 2003-05-01 | 2005-09-07 | LG Electronics Inc. | Air conditioner and outdoor unit therefor |
| EP1475585A3 (en) * | 2003-05-01 | 2005-09-07 | Lg Electronics Inc. | Air conditioner and outdoor unit therefor |
| US7407002B2 (en) | 2003-05-01 | 2008-08-05 | Lg Electronics Inc. | Air conditioner and outdoor unit therefor |
| JP2006162081A (en) * | 2004-12-02 | 2006-06-22 | Hitachi Ltd | Refrigeration cycle equipment |
| JP2009139037A (en) * | 2007-12-07 | 2009-06-25 | Mitsubishi Heavy Ind Ltd | Refrigerant circuit |
| JP2013113470A (en) * | 2011-11-28 | 2013-06-10 | Fuji Koki Corp | Refrigerant drier |
| JP2013117345A (en) * | 2011-12-02 | 2013-06-13 | Fuji Koki Corp | Refrigerant dryer |
| US11519642B2 (en) | 2017-06-22 | 2022-12-06 | Lg Electronics Inc. | Air conditioner |
| JP2021162213A (en) * | 2020-03-31 | 2021-10-11 | ダイキン工業株式会社 | Refrigeration cycle equipment |
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