JP2013210124A - Air conditioner - Google Patents

Air conditioner Download PDF

Info

Publication number
JP2013210124A
JP2013210124A JP2012079878A JP2012079878A JP2013210124A JP 2013210124 A JP2013210124 A JP 2013210124A JP 2012079878 A JP2012079878 A JP 2012079878A JP 2012079878 A JP2012079878 A JP 2012079878A JP 2013210124 A JP2013210124 A JP 2013210124A
Authority
JP
Japan
Prior art keywords
temperature
compressor
frequency
target
indoor
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.)
Granted
Application number
JP2012079878A
Other languages
Japanese (ja)
Other versions
JP5818734B2 (en
Inventor
Naomichi Tamura
直道 田村
Yohei Baba
要平 馬場
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP2012079878A priority Critical patent/JP5818734B2/en
Publication of JP2013210124A publication Critical patent/JP2013210124A/en
Application granted granted Critical
Publication of JP5818734B2 publication Critical patent/JP5818734B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Air Conditioning Control Device (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an air conditioner which can perform energy saving operation after the operation condition which can perform effective energy saving operation is discerned.SOLUTION: A capacity ratio α of which a sum capacity of an indoor device in which the temperature difference in the room temperature for a preset temperature exceeds a predetermined temperature is divided by the sum capacity of the total indoor devices under operation is calculated, and when the capacity ratio α is less than a predetermined ratio and the frequency of a compressor 1 is less than the lower limit of the frequency range where a high compressor efficiency can obtain more than a predetermined level, if it is during the air conditioning period, while lowering target evaporation temperature instead of the target maintenance control, the control is performed which raises an upper limit of the frequency of the compressor 1, whereas if it is during the heating period, while raising target condensation temperature instead of target maintenance control, the control is performed which raises an upper limit of the frequency of the compressor 1.

Description

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

従来より、1台の室外機に複数の室内機を接続して冷凍サイクルを構成するマルチタイプの空気調和機がある。この種の空気調和機では、各室内機が設置される各部屋の設定温度と運転中の各室内機が検出する室内温度との差温に基づいて、室外機に設置された圧縮機の周波数や各室内機にそれぞれ設置された各電子膨張弁の開度を制御し、各部屋の室内温度を設定温度に近づける制御を行っている(例えば、特許文献1参照)。   Conventionally, there is a multi-type air conditioner in which a plurality of indoor units are connected to one outdoor unit to constitute a refrigeration cycle. In this type of air conditioner, the frequency of the compressor installed in the outdoor unit is based on the difference between the set temperature of each room in which each indoor unit is installed and the indoor temperature detected by each operating indoor unit. In addition, the opening degree of each electronic expansion valve installed in each indoor unit is controlled to control the room temperature in each room close to the set temperature (see, for example, Patent Document 1).

圧縮機の周波数制御や各室内機の電子膨張弁の開度制御の具体的な手法については各種提案されている。例えば、設定温度と室内温度との差温の大きい部屋の室内機が十分な空調能力(冷房能力又は暖房能力)を発揮できるように、冷房時は目標蒸発温度、暖房時は目標凝縮温度を決定している。そして、その目標蒸発温度又は目標凝縮温度となるように圧縮機の周波数を制御し、また、過熱度(冷房時)又は過冷却度(暖房時)が目標値となるように各電子膨張弁の開度を個別に制御することが一般的に行われている。   Various specific methods for frequency control of the compressor and opening control of the electronic expansion valve of each indoor unit have been proposed. For example, determine the target evaporating temperature during cooling and the target condensing temperature during heating so that indoor units in a room with a large difference between the set temperature and room temperature can exhibit sufficient air conditioning capacity (cooling capacity or heating capacity). doing. Then, the frequency of the compressor is controlled so as to be the target evaporation temperature or the target condensation temperature, and each electronic expansion valve is controlled so that the degree of superheat (at the time of cooling) or the degree of supercooling (at the time of heating) becomes a target value. In general, the opening degree is individually controlled.

特開2005−24153号公報(第4頁)JP 2005-24153 A (page 4)

ところで、近年では空気調和機に対して省エネ制御が求められている。しかしながら、差温が大きい室内機に合わせて目標蒸発温度、目標凝縮温度を決定する従来制御では、各室内機の差温にバラツキがある場合、例えば仮に1台でも差温が大きい室内機があると、その室内機に合わせて空調能力を高めるべく、目標蒸発温度を下げる又は目標凝縮温度を上げる制御を行うことになる。冷凍サイクルでは、目標蒸発温度を低くするほど、また目標凝縮温度を高くするほど運転効率が低下するため、1台の差温の大きい室内機に合わせて目標蒸発温度、目標凝縮温度を決定することは省エネの観点から好ましくない。   By the way, in recent years, energy-saving control is required for air conditioners. However, in the conventional control in which the target evaporating temperature and the target condensing temperature are determined according to the indoor unit having a large temperature difference, if there is a variation in the temperature difference between the indoor units, for example, even one unit has a large temperature difference. In order to increase the air conditioning capacity in accordance with the indoor unit, control for lowering the target evaporation temperature or raising the target condensation temperature is performed. In the refrigeration cycle, the lower the target evaporation temperature and the higher the target condensing temperature, the lower the operating efficiency. Therefore, determine the target evaporating temperature and the target condensing temperature according to one indoor unit with a large temperature difference. Is not preferable from the viewpoint of energy saving.

一方、差温の大きい室内機が複数台あるにも関わらず、高い省エネ効果を得ようとして、空調能力を高める制御を行わないようにした場合、室内の快適性が損なわれてしまう。このように、複数台の室内機を有する空気調和機では、省エネ運転を効果的に行える運転状況の見極めが難しいという問題があった。   On the other hand, when there is a plurality of indoor units having a large temperature difference and the control for increasing the air conditioning capability is not performed in order to obtain a high energy saving effect, the indoor comfort is impaired. As described above, in an air conditioner having a plurality of indoor units, there is a problem that it is difficult to determine an operation state in which energy-saving operation can be effectively performed.

本発明はこのような点に鑑みなされたもので、省エネ運転を効果的に行える運転状況を見極めた上で省エネ運転を行うことが可能な空気調和機を提供することを目的とする。   The present invention has been made in view of these points, and an object of the present invention is to provide an air conditioner capable of performing an energy-saving operation after determining an operation state in which the energy-saving operation can be effectively performed.

本発明に係る空気調和機は、圧縮機及び室外熱交換器を有する室外機と、絞り装置及び室内熱交換器を有し、冷房及び暖房の少なくとも一方の運転が可能な複数の室内機と、冷房時は、室内機が設置される各部屋の設定温度と、室内機で検出した室内温度との差温に基づいて目標蒸発温度を決定し、暖房時は、差温に基づいて目標凝縮温度を決定し、決定した目標蒸発温度又は目標凝縮温度を維持するように圧縮機の周波数を制御する目標維持制御を行う制御装置とを備え、制御装置は、差温が予め設定した所定温度以上となる室内機の合計容量を、運転中の全室内機の合計容量で除算した容積比率を計算し、容積比率が所定比率未満で且つ圧縮機の周波数が、所定レベル以上の高圧縮機効率を得ることができる周波数範囲の下限値未満の場合には、冷房時であれば目標維持制御に代えて、目標蒸発温度を下げると共に圧縮機の周波数の上限値を上げる制御を行い、暖房時であれば目標維持制御に代えて、目標凝縮温度を上げると共に圧縮機の周波数の上限値を上げる制御を行うものである。   An air conditioner according to the present invention includes an outdoor unit having a compressor and an outdoor heat exchanger, a plurality of indoor units having a throttle device and an indoor heat exchanger, and capable of operating at least one of cooling and heating, During cooling, the target evaporation temperature is determined based on the temperature difference between the set temperature of each room where the indoor unit is installed and the room temperature detected by the indoor unit. During heating, the target condensation temperature is determined based on the temperature difference. And a control device that performs target maintenance control for controlling the frequency of the compressor so as to maintain the determined target evaporation temperature or target condensation temperature, and the control device has a differential temperature that is equal to or higher than a preset predetermined temperature. The volume ratio obtained by dividing the total capacity of the indoor units by the total capacity of all the indoor units in operation is calculated, and high compressor efficiency is obtained in which the volume ratio is less than the predetermined ratio and the frequency of the compressor is equal to or higher than the predetermined level. If the frequency range is less than the lower limit In the case of cooling, instead of the target maintenance control, control is performed to lower the target evaporation temperature and increase the upper limit value of the compressor frequency, and in the case of heating, the target condensation temperature is set instead of the target maintenance control. The control is performed to raise the upper limit value of the compressor frequency as well as raising the compressor frequency.

本発明によれば、容量比率と圧縮機周波数とに基づいて省エネ運転を効果的に行える運転状況を見極めた上で、省エネ運転を行うことができる。   According to the present invention, an energy-saving operation can be performed after ascertaining an operation situation in which an energy-saving operation can be effectively performed based on the capacity ratio and the compressor frequency.

本発明の一実施の形態に係る空気調和機の構成図である。It is a block diagram of the air conditioner which concerns on one embodiment of this invention. 温度差ΔTに応じた目標蒸発温度の決定方法の説明図である。It is explanatory drawing of the determination method of target evaporation temperature according to temperature difference (DELTA) T. 圧縮機の周波数を制御したときの部屋の温度変化を示す図である。It is a figure which shows the temperature change of the room when controlling the frequency of a compressor. 蒸発温度毎の圧縮機効率特性を示した図である。It is the figure which showed the compressor efficiency characteristic for every evaporation temperature. 温度差ΔTに応じた目標凝縮温度の決定方法の説明図である。It is explanatory drawing of the determination method of the target condensation temperature according to temperature difference (DELTA) T. 凝縮温度毎の圧縮機効率特性を示した図である。It is the figure which showed the compressor efficiency characteristic for every condensation temperature. 本発明の一実施の形態に係る空気調和機の構成を示すブロック図である。It is a block diagram which shows the structure of the air conditioner which concerns on one embodiment of this invention. 本発明の一実施の形態に係る空気調和機の制御動作を示すフローチャートである。It is a flowchart which shows the control action of the air conditioner which concerns on one embodiment of this invention. 容積比率αと圧縮機周波数上限との関係を示す図である。It is a figure which shows the relationship between volume ratio (alpha) and a compressor frequency upper limit.

(空気調和機の構成)
図1は、本発明の一実施の形態に係る空気調和機の構成図である。
空気調和機は、室外機Aと、複数の室内機B1、B2、B3(各室内機を区別しない場合は総称してBと符号を付す)とを備えている。各室内機Bは室外機Aに対して並列に接続されており、それぞれ別々の部屋に設置されて各部屋の空調を行う。なお、室内機がここでは3台設置された例を示しているが、室内機の設置台数は3台に限られない。室外機Aと複数の室内機Bは、後述の冷凍サイクルを構成しており、冷凍サイクル内を冷媒が循環することで室内空調を行う。
(Configuration of air conditioner)
FIG. 1 is a configuration diagram of an air conditioner according to an embodiment of the present invention.
The air conditioner includes an outdoor unit A and a plurality of indoor units B1, B2, and B3 (when each indoor unit is not distinguished, they are collectively referred to as B). Each indoor unit B is connected in parallel to the outdoor unit A, and is installed in a separate room to perform air conditioning of each room. Although an example in which three indoor units are installed is shown here, the number of indoor units installed is not limited to three. The outdoor unit A and the plurality of indoor units B constitute a refrigeration cycle, which will be described later, and perform indoor air conditioning by circulating refrigerant in the refrigeration cycle.

まず、室外機Aの構成について説明する。室外機Aは、圧縮機1と、油分離器2と、四方弁3と、室外熱交換器4と、アキュムレータ7とを備えている。また、室外機Aには、油分離器2で分離した油を開閉弁8a及びキャピラリーチューブ8bを介して圧縮機1の吸入側に戻す返油回路8を備えている。室外機Aは更に、室外熱交換器4に空気を送風する室外送風機9を備えている。   First, the configuration of the outdoor unit A will be described. The outdoor unit A includes a compressor 1, an oil separator 2, a four-way valve 3, an outdoor heat exchanger 4, and an accumulator 7. The outdoor unit A also includes an oil return circuit 8 that returns the oil separated by the oil separator 2 to the suction side of the compressor 1 through the on-off valve 8a and the capillary tube 8b. The outdoor unit A further includes an outdoor fan 9 that blows air to the outdoor heat exchanger 4.

圧縮機1は、周波数を可変することが可能な圧縮機であり、吸入したガス冷媒を圧縮して高温高圧のガス冷媒として吐出し、冷凍サイクルに冷媒を循環させるものである。   The compressor 1 is a compressor capable of changing the frequency, compresses the sucked gas refrigerant, discharges it as a high-temperature and high-pressure gas refrigerant, and circulates the refrigerant in the refrigeration cycle.

油分離器2は、圧縮機1から吐出された冷媒から油を分離するものである。   The oil separator 2 is for separating oil from the refrigerant discharged from the compressor 1.

四方弁3は、冷凍サイクルにおける冷媒の流路を切り換えるものである。四方弁3の流路の切り換えは、後述の室外制御装置100から出力される駆動信号に基づいて実施され、圧縮機1から吐出された冷媒を室外熱交換器4に送る流路、又は室内熱交換器6に送る流路に切り換える。四方弁3の切り換えにより冷房運転又は暖房運転の切り換えが可能となっている。なお、空気調和機は冷房及び暖房の少なくともどちらか一方が可能であればよく、よって、四方弁3は必ずしも必須の構成ではなく、省略可能である。   The four-way valve 3 switches the refrigerant flow path in the refrigeration cycle. Switching of the flow path of the four-way valve 3 is performed based on a drive signal output from an outdoor control device 100 described later, and a flow path for sending refrigerant discharged from the compressor 1 to the outdoor heat exchanger 4 or indoor heat. It switches to the flow path sent to the exchanger 6. Switching between the cooling operation and the heating operation is possible by switching the four-way valve 3. The air conditioner only needs to be capable of at least one of cooling and heating. Therefore, the four-way valve 3 is not necessarily an essential configuration and can be omitted.

室外熱交換器4は、流入する冷媒と室外送風機9からの外気との間で熱交換を実施するものである。なお、図1では室外送風機9によって外気と熱交換される場合を記載したが、水配管と熱交換されるプレート式や二重管式のようなものとしてもよい。   The outdoor heat exchanger 4 performs heat exchange between the inflowing refrigerant and the outside air from the outdoor blower 9. In FIG. 1, the case where heat is exchanged with the outside air by the outdoor fan 9 is described. However, a plate type or a double pipe type that exchanges heat with the water pipe may be used.

アキュムレータ7は、圧縮機1の吸入側に設置されており、アキュムレータ7内に流入した冷媒をガス冷媒と液冷媒とに分離して、余剰な液冷媒を貯留すると共に、ガス冷媒を圧縮機1に送る機能を有する。   The accumulator 7 is installed on the suction side of the compressor 1, separates the refrigerant flowing into the accumulator 7 into gas refrigerant and liquid refrigerant, stores excess liquid refrigerant, and stores the gas refrigerant in the compressor 1. The function to send to.

次に、室内機Bの構成について説明する。なお、各室内機B1、B2、B3は同様の構成となっている。
室内機Bは、絞り装置5と室内熱交換器6とを有し、これらが直列に冷媒配管で接続されている。室内機B1には更に、室内熱交換器6に室内空気を送る室内送風機11を備えている。
Next, the configuration of the indoor unit B will be described. Each indoor unit B1, B2, B3 has the same configuration.
The indoor unit B has the expansion device 5 and the indoor heat exchanger 6, and these are connected in series by refrigerant piping. The indoor unit B1 further includes an indoor blower 11 that sends room air to the indoor heat exchanger 6.

絞り装置5は、流入する冷媒を膨張及び減圧させるものであり、開度を調整可能な電動膨張弁で構成されている。   The expansion device 5 expands and depressurizes the inflowing refrigerant, and is composed of an electric expansion valve whose opening degree can be adjusted.

室内熱交換器6は、流入する冷媒と室内送風機11からの室内空気との間で熱交換を実施するものである。   The indoor heat exchanger 6 performs heat exchange between the refrigerant flowing in and the indoor air from the indoor blower 11.

室外機Aと各室内機Bとは延長配管により接続され、圧縮機1、油分離器2、四方弁3、室外熱交換器4、絞り装置5、室内熱交換器6及びアキュムレータ7が順次接続されて冷凍サイクルが構成されている。なお、冷凍サイクルの構成は図示のものに限定されず、少なくとも圧縮機1、室外熱交換器4、絞り装置5及び室内熱交換器6を備えた構成とすればよい。   The outdoor unit A and each indoor unit B are connected by an extension pipe, and a compressor 1, an oil separator 2, a four-way valve 3, an outdoor heat exchanger 4, an expansion device 5, an indoor heat exchanger 6 and an accumulator 7 are sequentially connected. Thus, a refrigeration cycle is configured. Note that the configuration of the refrigeration cycle is not limited to that shown in the drawing, and may be a configuration including at least the compressor 1, the outdoor heat exchanger 4, the expansion device 5, and the indoor heat exchanger 6.

(センサ類及び制御装置)
次に、空気調和機に備えられたセンサ類及び制御装置について説明する。
室外機Aは、圧縮機1の吸入圧力を検出する吸入圧力センサ21と、圧縮機1の吐出圧力を検出する吐出圧力センサ22とを備えている。
(Sensors and control device)
Next, sensors and control devices provided in the air conditioner will be described.
The outdoor unit A includes a suction pressure sensor 21 that detects the suction pressure of the compressor 1 and a discharge pressure sensor 22 that detects the discharge pressure of the compressor 1.

室外機Aは、室外機Aを構成する各部の動作を制御する室外制御装置100を備えており、各室内機Bそれぞれに設けられた後述の室内制御装置110との間で、通信手段としての通信線120によりセンサ情報や制御情報等を送受信可能に接続されている。室外制御装置100は、マイクロコンピュータで構成され、CPU、RAM及びROM等を備えており、ROMには制御プログラムが記憶されている。   The outdoor unit A includes an outdoor control device 100 that controls the operation of each unit constituting the outdoor unit A, and communicates with an indoor control device 110 (described later) provided in each indoor unit B as a communication means. The communication line 120 is connected so that sensor information and control information can be transmitted and received. The outdoor control device 100 is composed of a microcomputer and includes a CPU, a RAM, a ROM, and the like, and a control program is stored in the ROM.

室外制御装置100は、吸入圧力センサ21及び吐出圧力センサ22で検出された検出圧力を取得でき、また、室内熱交換器6の容量と、後述の室内温度検出センサ33で検出された室内温度と、設定温度とを含む各種情報を通信線120を介して各室内機Bの室内制御装置110から取得できるようになっている。室外制御装置100は、これらの各種情報と予め搭載されている制御プログラムに基づいて、圧縮機1の周波数制御、四方弁3の切り換え、室外送風機9の回転数制御、開閉弁8aの開閉制御等の室外機A全体の制御を行う。   The outdoor control device 100 can acquire the detected pressure detected by the suction pressure sensor 21 and the discharge pressure sensor 22, and the capacity of the indoor heat exchanger 6 and the indoor temperature detected by the indoor temperature detection sensor 33 described later can be obtained. Various information including the set temperature can be acquired from the indoor control device 110 of each indoor unit B via the communication line 120. The outdoor control device 100 controls the frequency of the compressor 1, the switching of the four-way valve 3, the rotational speed control of the outdoor blower 9, the open / close control of the on-off valve 8 a, etc. based on these various information and a preinstalled control program. The whole outdoor unit A is controlled.

室内機Bは、室内熱交換器6の液側に設けられて冷媒の温度を検出する液側温度センサ31と、室内熱交換器6のガス側に設けられて冷媒の温度を検出するガス側温度センサ32と、を備えている。また、室内機Bに流入する室内空気の温度(室内温度)を検出する室内温度検出センサ33を備えている。   The indoor unit B is provided on the liquid side of the indoor heat exchanger 6 to detect the temperature of the refrigerant, and the liquid side temperature sensor 31 is provided on the gas side of the indoor heat exchanger 6 to detect the temperature of the refrigerant. And a temperature sensor 32. Moreover, the indoor temperature detection sensor 33 which detects the temperature (room temperature) of the indoor air which flows into the indoor unit B is provided.

また、室内機Bは、室内機Bを構成する各部の動作を制御する室内制御装置110を備えている。室内制御装置110は、マイクロコンピュータで構成され、CPU、RAM及びROM等を備えている。また、室内機Bには、室内機Bを個別に操作するためのリモコン12が接続されており、使用者が設定温度などを入力できるようになっている。   In addition, the indoor unit B includes an indoor control device 110 that controls the operation of each part constituting the indoor unit B. The indoor control device 110 is composed of a microcomputer and includes a CPU, a RAM, a ROM, and the like. Further, the indoor unit B is connected to a remote controller 12 for individually operating the indoor unit B so that a user can input a set temperature or the like.

また、室内機Bには、制御基板(図示せず)に設けたスイッチにより、自己が発揮できる冷暖房能力(室内熱交換器6の容量に相当)に応じた機種設定がなされている。室内機Bの室内制御装置110は、その制御基板(図示せず)上のスイッチの設定によって自己の室内熱交換器6の容量(以下、室内機の容量という)を把握できるようになっている。   In the indoor unit B, a model is set according to the cooling / heating capacity (corresponding to the capacity of the indoor heat exchanger 6) that can be exhibited by a switch provided on a control board (not shown). The indoor control device 110 of the indoor unit B can grasp the capacity of its own indoor heat exchanger 6 (hereinafter referred to as the capacity of the indoor unit) by setting a switch on its control board (not shown). .

室内制御装置110は、運転状態(冷房運転しているか、暖房運転しているか)と、各種センサ31〜33により検出された温度と、リモコン12から設定された設定温度とを取り込めるようになっており、これらの情報に基づいて絞り装置5の開度制御や、室内送風機11の回転数制御を行う。また、室内制御装置110は、室外機Aの室外制御装置100との間でセンサ情報や制御情報等を送受信可能となっている。すなわち、室内制御装置110と室外制御装置100により空気調和機全体を制御する制御装置が構成されている。   The indoor control device 110 can capture the operating state (whether it is in cooling operation or heating operation), the temperature detected by the various sensors 31 to 33, and the set temperature set from the remote controller 12. Therefore, the opening degree control of the expansion device 5 and the rotational speed control of the indoor blower 11 are performed based on these pieces of information. The indoor control device 110 can transmit and receive sensor information and control information to and from the outdoor control device 100 of the outdoor unit A. That is, the indoor control device 110 and the outdoor control device 100 constitute a control device that controls the entire air conditioner.

なお、上記の構成例では室外制御装置100と室内制御装置110との間でデータ通信を行うことにより連携処理を行う構成を示したが、室内制御装置110の全ての機能を室外制御装置100に持たせた構成としてもよい。   In the above configuration example, the configuration in which the cooperation processing is performed by performing data communication between the outdoor control device 100 and the indoor control device 110 is shown, but all the functions of the indoor control device 110 are provided to the outdoor control device 100. It is good also as the structure given.

(冷房運転動作)
次に、図1に基づいて空気調和機の冷房運転について説明する。冷房運転を実施する場合、制御装置は予め、圧縮機1から吐出された冷媒が室外熱交換器4へ流れるように四方弁3の流路を切り換える(図1の実線側)。圧縮機1によって圧縮された高温高圧の冷媒は、圧縮機1から吐出された後、四方弁3を介して室外熱交換器4に流入する。この室外熱交換器4に流入した冷媒は、室外送風機9によって送られてくる外気と熱交換して凝縮し、高圧の液冷媒となって室外熱交換器4を流出する。室外熱交換器4を流出した液冷媒は、分岐して、それぞれ各室内機Bの絞り装置5に流入する。絞り装置5に流入した液冷媒は、膨張・減圧されて低圧の冷媒となり、それぞれ室内熱交換器6に流入する。室内熱交換器6に流入した冷媒は、室内送風機11によって送られてくる室内空気と熱交換して蒸発し、室内熱交換器6から流出する。各室内熱交換器6から流出した冷媒は合流した後、四方弁3、アキュムレータ7を経由して圧縮機1に戻される。以上の動作を繰り返すことにより室内を冷房する。
(Cooling operation)
Next, the cooling operation of the air conditioner will be described based on FIG. When carrying out the cooling operation, the control device switches the flow path of the four-way valve 3 in advance so that the refrigerant discharged from the compressor 1 flows to the outdoor heat exchanger 4 (solid line side in FIG. 1). The high-temperature and high-pressure refrigerant compressed by the compressor 1 is discharged from the compressor 1 and then flows into the outdoor heat exchanger 4 through the four-way valve 3. The refrigerant that has flowed into the outdoor heat exchanger 4 is condensed by exchanging heat with the outside air sent by the outdoor blower 9 and becomes high-pressure liquid refrigerant and flows out of the outdoor heat exchanger 4. The liquid refrigerant that has flowed out of the outdoor heat exchanger 4 branches and flows into the expansion device 5 of each indoor unit B. The liquid refrigerant flowing into the expansion device 5 is expanded and depressurized to become a low-pressure refrigerant, and flows into the indoor heat exchanger 6 respectively. The refrigerant that has flowed into the indoor heat exchanger 6 evaporates by exchanging heat with the indoor air sent by the indoor blower 11 and flows out of the indoor heat exchanger 6. The refrigerant flowing out from each indoor heat exchanger 6 joins and then returns to the compressor 1 via the four-way valve 3 and the accumulator 7. The room is cooled by repeating the above operation.

(暖房運転動作)
図1に基づいて、空気調和機の暖房運転について説明する。暖房運転を実施する場合、制御装置は予め、圧縮機1から吐出された冷媒が室内熱交換器6へ流れるように四方弁3の流路を切り換える(図1の点線側)。圧縮機1によって圧縮された高温高圧の冷媒は、圧縮機1から吐出された後、四方弁3を経由し、その後、分岐して各室内熱交換器6に流入する。室内熱交換器6に流入した冷媒は、室内送風機11によって送られてくる室内空気と熱交換して凝縮し、高圧の液冷媒となって室内熱交換器6を流出する。室内熱交換器6を流出した冷媒は、それぞれ絞り装置5に流入し、絞り装置5によって膨張・減圧され、低圧の冷媒となる。各絞り装置5から流出した低圧の冷媒は合流して室外熱交換器4に流入する。室外熱交換器4に流入した冷媒は、室外送風機9によって送られる室外空気と熱交換して蒸発し、室外熱交換器4から流出する。室外熱交換器4から流出した冷媒は四方弁3、アキュムレータ7を経由して圧縮機1に戻る。以上の動作を繰り返すことにより室内を暖房する。
(Heating operation)
The heating operation of the air conditioner will be described based on FIG. When the heating operation is performed, the control device switches the flow path of the four-way valve 3 in advance so that the refrigerant discharged from the compressor 1 flows to the indoor heat exchanger 6 (dotted line side in FIG. 1). The high-temperature and high-pressure refrigerant compressed by the compressor 1 is discharged from the compressor 1, then passes through the four-way valve 3, and then branches and flows into each indoor heat exchanger 6. The refrigerant that has flowed into the indoor heat exchanger 6 is condensed by exchanging heat with the indoor air sent by the indoor blower 11 and becomes high-pressure liquid refrigerant and flows out of the indoor heat exchanger 6. The refrigerant that has flowed out of the indoor heat exchanger 6 flows into the expansion device 5 and is expanded and depressurized by the expansion device 5 to become a low-pressure refrigerant. The low-pressure refrigerant that has flowed out of each expansion device 5 joins and flows into the outdoor heat exchanger 4. The refrigerant flowing into the outdoor heat exchanger 4 evaporates by exchanging heat with the outdoor air sent by the outdoor blower 9 and flows out of the outdoor heat exchanger 4. The refrigerant that has flowed out of the outdoor heat exchanger 4 returns to the compressor 1 via the four-way valve 3 and the accumulator 7. The room is heated by repeating the above operation.

(冷房時の能力制御)
次に、冷房時の能力制御について説明する。
冷房時は、蒸発温度が目標蒸発温度となるように圧縮機1の周波数を制御する。具体的には、蒸発温度が目標蒸発温度よりも低ければ、圧縮機1の周波数を減少させて冷房能力を下げ、蒸発温度が目標蒸発温度よりも高ければ、圧縮機1の周波数を増加させて冷房能力を上げる。目標蒸発温度は、例えば次の図2に示すように差温ΔT(設定温度と室内温度との差温)に応じて変化させる。
(Capacity control during cooling)
Next, capacity control during cooling will be described.
During cooling, the frequency of the compressor 1 is controlled so that the evaporation temperature becomes the target evaporation temperature. Specifically, if the evaporation temperature is lower than the target evaporation temperature, the frequency of the compressor 1 is decreased to lower the cooling capacity. If the evaporation temperature is higher than the target evaporation temperature, the frequency of the compressor 1 is increased. Increase cooling capacity. For example, as shown in FIG. 2 below, the target evaporation temperature is changed according to a temperature difference ΔT (a temperature difference between the set temperature and the room temperature).

図2は、温度差ΔTに応じた目標蒸発温度の決定方法の説明図である。図2において横軸は差温ΔT、縦軸は目標蒸発温度である。図2に示すグラフは、差温ΔTのときに十分な冷却能力を発揮できる目標蒸発温度を示している。
図2に示すように、差温ΔTが大きくなるに連れ、目標蒸発温度を下げるようにしている。また、差温ΔTが所定の温度T0以上のときには、最低目標蒸発温度に設定する。なお、目標蒸発温度を決定するための差温ΔTには、各室内機Bの差温ΔTのうち最も大きいものを代表として使用する。
FIG. 2 is an explanatory diagram of a method for determining the target evaporation temperature according to the temperature difference ΔT. In FIG. 2, the horizontal axis represents the temperature difference ΔT, and the vertical axis represents the target evaporation temperature. The graph shown in FIG. 2 shows the target evaporation temperature at which sufficient cooling capacity can be exhibited when the temperature difference ΔT.
As shown in FIG. 2, the target evaporation temperature is lowered as the temperature difference ΔT increases. When the temperature difference ΔT is equal to or higher than the predetermined temperature T0, the minimum target evaporation temperature is set. As the temperature difference ΔT for determining the target evaporation temperature, the largest temperature difference ΔT of each indoor unit B is used as a representative.

すなわち、冷房中の各部屋それぞれの差温ΔTを検出し、各差温ΔTのうち最も大きい差温ΔTに基づいて図2に基づき目標蒸発温度を決定する。よって、その差温ΔTを検出した室内機Bで十分な冷却能力が発揮される蒸発温度が目標蒸発温度として決定されることになる。そして、室外機Aは、吸入圧力センサ21により検出された吸入圧力を換算して得られる蒸発温度が、上記のようにして決定した目標蒸発温度となるように圧縮機1の周波数を制御すると共に、室外送風機9の回転数を制御する。   That is, the temperature difference ΔT of each room during cooling is detected, and the target evaporation temperature is determined based on FIG. 2 based on the largest temperature difference ΔT among the temperature differences ΔT. Therefore, the evaporation temperature at which sufficient cooling capacity is exhibited in the indoor unit B that has detected the temperature difference ΔT is determined as the target evaporation temperature. The outdoor unit A controls the frequency of the compressor 1 so that the evaporation temperature obtained by converting the suction pressure detected by the suction pressure sensor 21 becomes the target evaporation temperature determined as described above. The rotational speed of the outdoor blower 9 is controlled.

図3は、圧縮機の周波数を制御したときの部屋の温度変化を示す図である。
図3に示したように、圧縮機1の周波数が低いときは部屋の温度が上昇し、周波数が高いときは部屋の温度が低下する。
FIG. 3 is a diagram illustrating a temperature change in the room when the frequency of the compressor is controlled.
As shown in FIG. 3, when the frequency of the compressor 1 is low, the room temperature increases, and when the frequency is high, the room temperature decreases.

また、各室内機Bのそれぞれは、自己の室内熱交換器6の出口冷媒の過熱度が目標過熱度に一定になるように自己の絞り装置5を調整する制御を行う。   Further, each indoor unit B performs control to adjust its expansion device 5 so that the degree of superheat of the outlet refrigerant of its own indoor heat exchanger 6 becomes constant at the target degree of superheat.

(冷房時の圧縮機効率)
図4は、蒸発温度毎の圧縮機効率特性を示した図で、横軸に圧縮機周波数、縦軸に圧縮機効率を取っている。圧縮機効率特性は、圧縮機1内部の構造やモーターの巻き数等の構造的要素によって決まるものである。図4において(1)は蒸発温度Taのときの圧縮機効率特性、(2)は蒸発温度To(>Ta)のときの圧縮機効率特性、(3)は蒸発温度Tb(>To)のときの圧縮機効率特性を示している。
(Compressor efficiency during cooling)
FIG. 4 is a graph showing compressor efficiency characteristics for each evaporation temperature, with the horizontal axis representing the compressor frequency and the vertical axis representing the compressor efficiency. The compressor efficiency characteristics are determined by structural elements such as the internal structure of the compressor 1 and the number of windings of the motor. In FIG. 4, (1) is the compressor efficiency characteristic at the evaporation temperature Ta, (2) is the compressor efficiency characteristic at the evaporation temperature To (> Ta), and (3) is at the evaporation temperature Tb (> To). Shows the compressor efficiency characteristics.

まず、図4に基づいて、圧縮機周波数の増減に伴う圧縮機効率の変化について説明する。図4上の点O(圧縮機周波数fo、蒸発温度To)で運転しているときに、圧縮機周波数を増加させた場合、蒸発温度が低下する。すなわち、点Oから右下へ遷移して点Aとなる。また逆に圧縮機周波数を減少させたときは蒸発温度が上昇する。すなわち点Oから左上へ遷移して点Bとなる。   First, based on FIG. 4, the change of the compressor efficiency accompanying the increase / decrease in a compressor frequency is demonstrated. When operating at the point O (compressor frequency fo, evaporation temperature To) in FIG. 4, if the compressor frequency is increased, the evaporation temperature decreases. That is, the point A changes to the lower right to become a point A. Conversely, when the compressor frequency is decreased, the evaporation temperature rises. That is, a transition is made from the point O to the upper left to become a point B.

次に、図4に基づいて、高圧縮機効率が得られる周波数範囲について説明する。図4に示すように、蒸発温度を下げると、一般には圧縮機効率が低下するが、蒸発温度を下げても、所定レベルε1以上の高圧縮機効率を得ることができる周波数範囲が存在する。図4において最も蒸発温度の低い圧縮機効率特性(1)の例で説明すると、圧縮機効率特性(1)は他の(2)、(3)よりも全体的に圧縮機効率が低いものの、圧縮機周波数がf1〜f2の範囲では、所定レベルε1以上の高圧縮機効率とすることができる。   Next, the frequency range in which high compressor efficiency can be obtained will be described with reference to FIG. As shown in FIG. 4, when the evaporation temperature is lowered, the compressor efficiency is generally lowered. However, there is a frequency range in which a high compressor efficiency of a predetermined level ε1 or more can be obtained even when the evaporation temperature is lowered. In the example of the compressor efficiency characteristic (1) having the lowest evaporation temperature in FIG. 4, the compressor efficiency characteristic (1) is generally lower in compressor efficiency than the other (2) and (3). When the compressor frequency is in the range of f1 to f2, high compressor efficiency of a predetermined level ε1 or higher can be achieved.

よって、冷房時の圧縮機1の現在の周波数が例えばf1よりも低いfoであれば、蒸発温度をToからTaに下げても、周波数はfaであり高圧縮機効率が得られる周波数範囲内であるため、高圧縮機効率が見込める。したがって、目標蒸発温度を下げることにより運転効率は悪くなるが、その中でも、高圧縮機効率が得られる周波数範囲f1〜f2内で圧縮機周波数を上げるようにすることによって、運転効率低下の下げ幅を小さくできる。なお、この周波数範囲f1〜f2は予め空気調和機の制御装置に記憶されている。   Therefore, if the current frequency of the compressor 1 at the time of cooling is fo lower than f1, for example, even if the evaporation temperature is lowered from To to Ta, the frequency is fa and within a frequency range where high compressor efficiency can be obtained. Therefore, high compressor efficiency can be expected. Therefore, although the operation efficiency is deteriorated by lowering the target evaporation temperature, among them, the reduction in the operation efficiency is reduced by increasing the compressor frequency within the frequency range f1 to f2 in which high compressor efficiency is obtained. Can be reduced. The frequency ranges f1 to f2 are stored in advance in the control device of the air conditioner.

(冷房時の容積比率αに応じた切り換え制御)
次に、本実施の形態の特徴的な制御である、容積比率αに応じた切り換え制御について説明する。容積比率αは次式で算出する。
容積比率α=差温ΔTが予め設定した所定温度(例えば1℃)以上の各室内機の室内熱交換器6の合計容量/運転中の全ての室内機の室内熱交換器6の合計容量
ここでは容積比率による関係を記載したが、室内機運転容量でも構わない。
(Switching control according to volume ratio α during cooling)
Next, switching control according to the volume ratio α, which is characteristic control of the present embodiment, will be described. The volume ratio α is calculated by the following formula.
Volume ratio α = total capacity of indoor heat exchanger 6 of each indoor unit in which differential temperature ΔT is equal to or higher than a predetermined temperature (for example, 1 ° C.) / Total capacity of indoor heat exchanger 6 of all indoor units in operation Then, although the relationship by volume ratio was described, indoor unit operation capacity may be sufficient.

容積比率αが所定比率(例えば、30%)以上のとき、言い換えれば、能力が足りない室内機が多い場合は、省エネ運転よりも室内温度を設定温度にすることを優先して目標蒸発温度を維持する制御、つまり差温ΔTが最も大きい室内機で能力が出る目標蒸発温度で運転する。一方、容積比率αが所定比率未満のとき、言い換えれば、能力が足りない室内機が少ない場合は、圧縮機周波数を上げることによって圧縮機効率を上げることができるかどうかをチェック(具体的には現在の圧縮機周波数が周波数下限値f1未満かどうかをチェック)し、圧縮機効率を上げることができる場合は、目標蒸発温度を所定温度(例えば1℃)下げて、圧縮機周波数の上限を所定周波数(例えば10Hz)、増加させる。この制御とすると、上述したように目標蒸発温度を下げることにより、運転効率が悪くなるが、その中でも、高圧縮機効率が得られる周波数範囲f1〜f2内で圧縮機周波数を上げるようにすることによって、効率低下の下げ幅を小さくできる。   When the volume ratio α is equal to or higher than a predetermined ratio (for example, 30%), in other words, when there are many indoor units with insufficient capacity, the target evaporation temperature is set with priority given to setting the room temperature to the set temperature rather than the energy-saving operation. The control is maintained, that is, the operation is performed at the target evaporation temperature at which the capacity is obtained in the indoor unit having the largest temperature difference ΔT. On the other hand, when the volume ratio α is less than the predetermined ratio, in other words, when there are few indoor units with insufficient capacity, it is checked whether the compressor efficiency can be increased by increasing the compressor frequency (specifically, If the current compressor frequency is less than the lower frequency limit f1) and the compressor efficiency can be increased, the target evaporation temperature is lowered by a predetermined temperature (for example, 1 ° C.), and the upper limit of the compressor frequency is predetermined. Increase the frequency (for example, 10 Hz). With this control, as described above, the operation efficiency is deteriorated by lowering the target evaporation temperature, but among them, the compressor frequency is increased within the frequency range f1 to f2 in which high compressor efficiency is obtained. Thus, the reduction in efficiency can be reduced.

(暖房時の能力制御)
次に、暖房時の能力制御について説明する。
暖房時は、凝縮温度が目標凝縮温度となるように圧縮機1の周波数を制御する。具体的には、凝縮温度が目標凝縮温度よりも低ければ圧縮機1の周波数を増加させて暖房能力を上げ、凝縮温度が目標凝縮温度よりも高ければ、圧縮機1の周波数を減少させて冷房能力を下げる。目標凝縮温度は、例えば次の図5に示すように差温ΔT(設定温度と室内温度との差温)に応じて変化させる。
(Capacity control during heating)
Next, capacity control during heating will be described.
During heating, the frequency of the compressor 1 is controlled so that the condensation temperature becomes the target condensation temperature. Specifically, if the condensation temperature is lower than the target condensation temperature, the frequency of the compressor 1 is increased to increase the heating capacity. If the condensation temperature is higher than the target condensation temperature, the frequency of the compressor 1 is decreased to perform cooling. Decrease ability. The target condensing temperature is changed according to, for example, a temperature difference ΔT (a temperature difference between the set temperature and the room temperature) as shown in FIG.

図5は、温度差ΔTに応じた目標凝縮温度の決定方法の説明図である。図5において横軸は差温ΔT、縦軸は目標凝縮温度である。図5に示すグラフは、差温ΔTのときに十分な暖房能力を発揮できる目標凝縮温度を示している。
図5に示すように、差温ΔTが大きくなるに連れ、目標凝縮温度を上げるようにしている。また、差温ΔTが所定の温度T0以上のときには、最高目標凝縮温度に設定する。なお、目標凝縮温度を決定するための差温ΔTには、各室内機Bの差温ΔTのうち最も大きいものを代表として使用する。
FIG. 5 is an explanatory diagram of a method for determining the target condensing temperature according to the temperature difference ΔT. In FIG. 5, the horizontal axis represents the temperature difference ΔT, and the vertical axis represents the target condensation temperature. The graph shown in FIG. 5 shows the target condensation temperature at which sufficient heating capacity can be exhibited when the temperature difference ΔT.
As shown in FIG. 5, the target condensation temperature is raised as the temperature difference ΔT increases. When the temperature difference ΔT is equal to or higher than the predetermined temperature T0, the maximum target condensing temperature is set. As the temperature difference ΔT for determining the target condensing temperature, the largest temperature difference ΔT of each indoor unit B is used as a representative.

すなわち、暖房中の各部屋それぞれの差温ΔTを検出し、各差温ΔTのうち最も大きいものに基づいて目標凝縮温度を決定する。そして、室外機Aは、吐出圧力センサ22により検出された吐出圧力を換算して得られる凝縮温度が、上記のようにして決定した目標凝縮温度となるように圧縮機1の周波数を制御すると共に、室外送風機9の回転数を制御する。   That is, the temperature difference ΔT of each room being heated is detected, and the target condensing temperature is determined based on the largest temperature difference among the temperature differences ΔT. The outdoor unit A controls the frequency of the compressor 1 so that the condensation temperature obtained by converting the discharge pressure detected by the discharge pressure sensor 22 becomes the target condensation temperature determined as described above. The rotational speed of the outdoor blower 9 is controlled.

また、各室内機Bのそれぞれは、自己の室内熱交換器6の出口冷媒の過冷却度が目標過冷却度に一定になるように自己の絞り装置5を調整する制御を行う。   Each indoor unit B performs control to adjust its expansion device 5 so that the degree of subcooling of the outlet refrigerant of its own indoor heat exchanger 6 becomes constant to the target degree of subcooling.

(暖房時の圧縮機効率)
図6は、凝縮温度毎の圧縮機効率特性を示した図で、横軸に圧縮機周波数、縦軸に圧縮機効率を取っている。圧縮機効率特性は、圧縮機1内部の構造やモーターの巻き数等の構造的要素によって決まるものである。図6において(1)は凝縮温度Taのときの圧縮機効率特性、(2)は凝縮温度To(<Ta)のときの圧縮機効率特性、(3)は凝縮温度Tb(<To)のときの圧縮機効率特性を示している。
(Compressor efficiency during heating)
FIG. 6 is a diagram showing compressor efficiency characteristics for each condensation temperature, with the horizontal axis representing the compressor frequency and the vertical axis representing the compressor efficiency. The compressor efficiency characteristics are determined by structural elements such as the internal structure of the compressor 1 and the number of windings of the motor. In FIG. 6, (1) is the compressor efficiency characteristic at the condensation temperature Ta, (2) is the compressor efficiency characteristic at the condensation temperature To (<Ta), and (3) is at the condensation temperature Tb (<To). Shows the compressor efficiency characteristics.

まず、図6に基づいて、圧縮機周波数の増減に伴う圧縮機効率の変化について説明する。図6上の点O(圧縮機周波数fo、凝縮温度To)で運転しているときに、圧縮機周波数を増加させた場合、凝縮温度が上昇する。すなわち、点Oから右下へ遷移して点Aとなる。また逆に圧縮機周波数を減少させた場合、凝縮温度が低下する。すなわち点Oから左上へ遷移して点Bとなる。   First, based on FIG. 6, the change of the compressor efficiency accompanying the increase / decrease in a compressor frequency is demonstrated. When operating at the point O (compressor frequency fo, condensing temperature To) in FIG. 6, if the compressor frequency is increased, the condensing temperature rises. That is, the point A changes to the lower right to become a point A. Conversely, when the compressor frequency is decreased, the condensation temperature decreases. That is, a transition is made from the point O to the upper left to become a point B.

次に、図6に基づいて、高圧縮機効率が得られる周波数範囲について説明する。図6に示すように、凝縮温度を上げると、一般には圧縮機効率が低下するが、凝縮温度を上げても、所定レベルε1以上の高圧縮機効率を得ることができる圧縮機周波数範囲が存在する。図6において最も凝縮温度の高い圧縮機効率特性(1)の例で説明すると、圧縮機効率特性(1)は他の(2)、(3)よりも全体的に圧縮機効率が低いものの、圧縮機周波数がf1〜f2の範囲では、所定レベルε1以上の高圧縮機効率とすることができる。   Next, the frequency range in which high compressor efficiency can be obtained will be described with reference to FIG. As shown in FIG. 6, when the condensation temperature is raised, the compressor efficiency generally decreases. However, even if the condensation temperature is raised, there is a compressor frequency range in which a high compressor efficiency higher than a predetermined level ε1 can be obtained. To do. In the example of the compressor efficiency characteristic (1) having the highest condensation temperature in FIG. 6, although the compressor efficiency characteristic (1) is generally lower in the compressor efficiency than the other (2) and (3), When the compressor frequency is in the range of f1 to f2, high compressor efficiency of a predetermined level ε1 or higher can be achieved.

よって、暖房時の圧縮機1の現在の周波数が例えばf1よりも低いfoであれば、凝縮温度をToからTaに上げても、周波数はfaであり高圧縮機効率が得られる周波数範囲内であるため、高圧縮機効率が見込める。したがって、目標凝縮温度を下げることにより、運転効率は悪くなるが、その中でも、高圧縮機効率が得られる周波数範囲f1〜f2内で圧縮機周波数を上げるようにすることによって、運転効率低下の下げ幅を小さくできる。   Therefore, if the current frequency of the compressor 1 at the time of heating is fo lower than f1, for example, even if the condensation temperature is increased from To to Ta, the frequency is fa and within a frequency range where high compressor efficiency can be obtained. Therefore, high compressor efficiency can be expected. Therefore, although the operation efficiency is deteriorated by lowering the target condensation temperature, among them, the reduction of the operation efficiency is lowered by increasing the compressor frequency within the frequency range f1 to f2 in which high compressor efficiency is obtained. The width can be reduced.

(暖房時の容積比率αに応じた切り換え制御)
次に、本実施の形態の特徴的な制御である、容積比率αに応じた切り換え制御について説明する。容積比率αは次式で算出する。
容積比率α=差温ΔTが予め設定した所定温度(例えば1℃)以上の各室内機の室内熱交換器6の合計容量/運転中の全ての室内機の室内熱交換器6の合計容量
ここでは、暖房時において例えば容積比率αが40%のときに圧縮機効率が最大となる圧縮機周波数(ここでは50Hz)となるようなシステムを選択している。ここでは容積比率による関係を記載したが、室内機運転容量でも構わない。
(Switching control according to volume ratio α during heating)
Next, switching control according to the volume ratio α, which is characteristic control of the present embodiment, will be described. The volume ratio α is calculated by the following formula.
Volume ratio α = total capacity of indoor heat exchanger 6 of each indoor unit in which differential temperature ΔT is equal to or higher than a predetermined temperature (for example, 1 ° C.) / Total capacity of indoor heat exchanger 6 of all indoor units in operation In the heating, for example, a system is selected such that the compressor frequency (here, 50 Hz) is maximized when the volume ratio α is 40%. Here, the relationship by the volume ratio is described, but the indoor unit operation capacity may be used.

容積比率αが所定比率(例えば30%)以上のとき、言い換えれば、能力が足りない室内機が多い場合は、省エネ制御よりも室内温度を設定温度にすることを優先して目標凝縮温度を維持、つまり差温ΔTが最も大きい室内機で能力が出る目標凝縮温度で運転する。一方、容積比率αが所定比率未満のとき、言い換えれば、能力が足りない室内機が少ない場合は、圧縮機周波数を上げることによって圧縮機効率を上げることができるかどうかをチェック(具体的には現在の圧縮機周波数が周波数下限値f1未満かどうかをチェック)し、圧縮機効率を上げることができる場合は、目標凝縮温度を所定温度(例えば1℃)上げて、圧縮機周波数の上限を所定周波数(例えば10Hz)、増加させる。この制御とすると、上述したように目標凝縮温度を上げることにより、運転効率が悪くなるが、その中でも高圧縮機効率が得られる周波数範囲f1〜f2内で圧縮機周波数を上げるようにすることによって、効率低下の下げ幅を小さくできる。   When the volume ratio α is greater than or equal to a predetermined ratio (for example, 30%), in other words, when there are many indoor units with insufficient capacity, the target condensing temperature is maintained with priority given to setting the room temperature to a set temperature rather than energy-saving control. In other words, the indoor unit with the largest temperature difference ΔT is operated at the target condensation temperature at which the capacity is obtained. On the other hand, when the volume ratio α is less than the predetermined ratio, in other words, when there are few indoor units with insufficient capacity, it is checked whether the compressor efficiency can be increased by increasing the compressor frequency (specifically, If the current compressor frequency is less than the lower frequency limit f1) and the compressor efficiency can be increased, the target condensation temperature is increased by a predetermined temperature (for example, 1 ° C.), and the upper limit of the compressor frequency is predetermined. Increase the frequency (for example, 10 Hz). With this control, as described above, raising the target condensation temperature degrades the operating efficiency, but among them, by raising the compressor frequency within the frequency range f1 to f2 where high compressor efficiency is obtained. Thus, the reduction in efficiency can be reduced.

(制御ブロック図)
図7は、本発明の一実施の形態に係る空気調和機の構成を示すブロック図である。以下、図7及び前述の図1を参照して空気調和機に備えられた制御装置及び計測データの流れについて説明する。
(Control block diagram)
FIG. 7 is a block diagram showing a configuration of an air conditioner according to an embodiment of the present invention. Hereinafter, the flow of the control device and measurement data provided in the air conditioner will be described with reference to FIG. 7 and FIG. 1 described above.

室外制御装置100は、CPUと制御プログラムにより、蒸発温度・凝縮温度換算部101と、差温・容積比率計算部102と、目標蒸発温度・目標凝縮温度計算部103と、圧縮機周波数決定部104とが機能的に構成されている。本実施の形態は、上述したように、各部屋それぞれの差温ΔTと各室内機Bの容量とを考慮して目標蒸発温度を変更すると共に、圧縮機周波数を決定する点に特徴を有しており、この特徴的な制御が、各処理部によって実現される。   The outdoor control device 100 includes an evaporation temperature / condensation temperature conversion unit 101, a differential temperature / volume ratio calculation unit 102, a target evaporation temperature / target condensation temperature calculation unit 103, and a compressor frequency determination unit 104 by a CPU and a control program. Are functionally configured. As described above, the present embodiment is characterized in that the target evaporation temperature is changed in consideration of the temperature difference ΔT of each room and the capacity of each indoor unit B, and the compressor frequency is determined. This characteristic control is realized by each processing unit.

蒸発温度・凝縮温度換算部101は吸入圧力センサ21で検出された吸入圧力を蒸発温度に換算すると共に、吐出圧力センサ22で検出された吐出圧力を凝縮温度に換算し、蒸発温度及び凝縮温度を目標蒸発温度・目標凝縮温度計算部103及び圧縮機周波数決定部104に渡す。   The evaporation temperature / condensation temperature conversion unit 101 converts the suction pressure detected by the suction pressure sensor 21 into an evaporation temperature, converts the discharge pressure detected by the discharge pressure sensor 22 into a condensation temperature, and sets the evaporation temperature and the condensation temperature. It passes to the target evaporation temperature / target condensation temperature calculation unit 103 and the compressor frequency determination unit 104.

差温・容積比率計算部102は、各室内制御装置110からの室内温度と設定温度とに基づいて差温ΔTを計算すると共に、各室内制御装置110からの各室内機の容量に基づいて容積比率αを計算し、計算した差温ΔTと容積比率αとを目標蒸発温度・目標凝縮温度計算部103に渡す。なお、ここでは各室内制御装置110のそれぞれが室内温度及び設定温度を室外機Aに通信する例を説明したが、各室内制御装置110のそれぞれで差温ΔTを計算して室外機Aの室外制御装置100に送信してもよい。   The differential temperature / volume ratio calculation unit 102 calculates the differential temperature ΔT based on the indoor temperature and the set temperature from each indoor control device 110, and the volume based on the capacity of each indoor unit from each indoor control device 110. The ratio α is calculated, and the calculated differential temperature ΔT and the volume ratio α are passed to the target evaporation temperature / target condensation temperature calculation unit 103. Here, the example in which each of the indoor control devices 110 communicates the indoor temperature and the set temperature to the outdoor unit A has been described. However, each of the indoor control devices 110 calculates the differential temperature ΔT to calculate the outdoor temperature of the outdoor unit A. You may transmit to the control apparatus 100.

目標蒸発温度・目標凝縮温度計算部103は、冷房時は、蒸発温度・凝縮温度換算部101からの蒸発温度、差温ΔT及び容積比率αに基づいて目標蒸発温度を計算して圧縮機周波数決定部104に渡す。目標蒸発温度・目標凝縮温度計算部103は、暖房時は、蒸発温度・凝縮温度換算部101からの凝縮温度、差温ΔT及び容積比率αに基づいて目標凝縮温度を計算して圧縮機周波数決定部104に渡す処理を行う。   The target evaporation temperature / target condensation temperature calculation unit 103 determines the compressor frequency by calculating the target evaporation temperature based on the evaporation temperature, the differential temperature ΔT and the volume ratio α from the evaporation temperature / condensation temperature conversion unit 101 during cooling. To the unit 104. The target evaporation temperature / target condensation temperature calculation unit 103 calculates the compressor frequency by calculating the target condensation temperature based on the condensation temperature, the differential temperature ΔT and the volume ratio α from the evaporation temperature / condensation temperature conversion unit 101 during heating. Processing to be passed to the unit 104 is performed.

圧縮機周波数決定部104は、冷房時は、目標蒸発温度・目標凝縮温度計算部103からの目標蒸発温度と、蒸発温度・凝縮温度換算部101からの蒸発温度とに基づいて圧縮機1の周波数を決定する。暖房時は、目標蒸発温度・目標凝縮温度計算部103からの目標凝縮温度と、蒸発温度・凝縮温度換算部101からの凝縮温度とに基づいて圧縮機1の周波数を決定する。   During cooling, the compressor frequency determining unit 104 determines the frequency of the compressor 1 based on the target evaporation temperature from the target evaporation temperature / target condensation temperature calculation unit 103 and the evaporation temperature from the evaporation temperature / condensation temperature conversion unit 101. To decide. At the time of heating, the frequency of the compressor 1 is determined based on the target condensation temperature from the target evaporation temperature / target condensation temperature calculation unit 103 and the condensation temperature from the evaporation temperature / condensation temperature conversion unit 101.

(制御フロー)
図8は、本発明の一実施の形態に係る空気調和機の制御動作を示すフローチャートである。次に、空気調和機の制御動作について図8を参照して説明する。ここでは、全ての室内機Bが冷房運転しており、全ての室内機Bにおいて差温ΔTが1℃以下で、安定した運転状況から、例えば窓が開けられるなどして室内機B1で差温ΔTが大きくなり、室内機B1での差温ΔTが2℃に変化した状況にあるものとする。また、室内機B2、B3での各差温ΔTは0.5℃で、容積比率αは20%であるものとする。そして、運転状況が変化する前の安定した運転状況(圧縮機周波数、蒸発温度)が、図4の点Oで示される状況にあるものとする。なお、図8のフローチャートでは、差温ΔTや所定比率等について具体的な数値を用いているが、これは一例を示したに過ぎず、それらは実使用条件等に応じて適宜設定すれば良い。
(Control flow)
FIG. 8 is a flowchart showing the control operation of the air conditioner according to the embodiment of the present invention. Next, the control operation of the air conditioner will be described with reference to FIG. Here, all the indoor units B are in cooling operation, and in all the indoor units B, the temperature difference ΔT is 1 ° C. or less. It is assumed that ΔT increases and the temperature difference ΔT in the indoor unit B1 changes to 2 ° C. In addition, each temperature difference ΔT in the indoor units B2 and B3 is 0.5 ° C., and the volume ratio α is 20%. Then, it is assumed that the stable operation state (compressor frequency, evaporation temperature) before the operation state changes is in a state indicated by a point O in FIG. In the flowchart of FIG. 8, specific numerical values are used for the temperature difference ΔT, the predetermined ratio, and the like. However, this is merely an example, and these may be set as appropriate according to actual use conditions. .

空気調和機は冷房運転を開始しており(S1)、運転開始時の過渡的な温度変化中であるか否かを判断する(S2)。具体的には各室内機Bのそれぞれにおける差温ΔTの時間変化をチェックし、差温ΔTの時間変化が0.5℃以上の室内機Bがあれば、運転開始時の過渡的な温度変化中にある、と判断する。一方、差温ΔTの時間変化が何れの室内機Bでも0.5℃未満の場合は、運転開始時の過渡的な温度変化中ではないと判断する。なお、ステップS2では、運転開始時の過渡的な温度変化ではなく、室内負荷による温度変化が生じているのかどうかを確認できればよく、ここでは差温ΔTの時間変化を監視したが、冷房運転開始からの運転時間が所定時間経過したかを監視するようにしてもよい。   The air conditioner has started a cooling operation (S1), and determines whether a transient temperature change at the start of the operation is in progress (S2). Specifically, the time change of the differential temperature ΔT in each indoor unit B is checked, and if there is an indoor unit B whose time difference of the differential temperature ΔT is 0.5 ° C. or more, a transient temperature change at the start of operation. Judge that it is inside. On the other hand, when the time change of the temperature difference ΔT is less than 0.5 ° C. in any indoor unit B, it is determined that the temperature is not changing transiently at the start of operation. In step S2, it is only necessary to check whether the temperature change due to the indoor load is occurring instead of the transient temperature change at the start of operation. Here, the time change of the differential temperature ΔT is monitored. It may be configured to monitor whether a predetermined time has elapsed since the start of the operation.

そして、ここでは過渡的な温度変化中ではないため、ステップS2で「いいえ」に進み、続いて、各室内機Bのうち、差温ΔTが1℃(所定温度)よりも大きい室内機があるかどうかをチェックする(S3)。この温度は、部屋の負荷と空調能力で決めればよく、上述したように1℃以外でも構わない。ここでは、室内機B1の差温ΔTが1℃以下であった状態から2℃に変化した状態であるため、ステップS3で「はい」に進み、続いて容積比率αが30%(所定比率)未満か否かを判断する(S4)。   In this case, since there is no transitional temperature change, the process proceeds to “No” in step S2. Subsequently, among the indoor units B, there is an indoor unit having a differential temperature ΔT larger than 1 ° C. (predetermined temperature). Is checked (S3). This temperature may be determined by the load on the room and the air conditioning capacity, and may be other than 1 ° C. as described above. Here, since the temperature difference ΔT of the indoor unit B1 is changed from 2 ° C. to 2 ° C., the process proceeds to “Yes” in step S3, and then the volume ratio α is 30% (predetermined ratio). It is judged whether it is less than (S4).

ここで、ステップS4で用いる容積比率αの所定比率の決定方法について説明する。
図9は、容積比率αと圧縮機周波数上限との関係を示す図で、横軸に容積比率α、縦軸に圧縮機周波数上限を取っている。図9には、冷房時と暖房時のそれぞれについて示している。
圧縮機効率と圧縮機周波数との関係は、上述したように圧縮機1内部の構造やモーターの巻き数等の構造的要素によって決まっている(図4参照)。圧縮機効率が最も良くなるときの圧縮機周波数は、図4では50Hzであり、図9の冷房側の特性において、圧縮機周波数が50Hzとなるときの容積比率αである30%を、所定比率に決定する。なお、所定比率は50%未満の値となる。
Here, a method for determining the predetermined ratio of the volume ratio α used in step S4 will be described.
FIG. 9 is a diagram showing the relationship between the volume ratio α and the compressor frequency upper limit, in which the horizontal axis represents the volume ratio α and the vertical axis represents the compressor frequency upper limit. FIG. 9 shows each of cooling and heating.
As described above, the relationship between the compressor efficiency and the compressor frequency is determined by structural elements such as the internal structure of the compressor 1 and the number of turns of the motor (see FIG. 4). The compressor frequency when the compressor efficiency is the best is 50 Hz in FIG. 4, and in the cooling side characteristics of FIG. 9, 30%, which is the volume ratio α when the compressor frequency is 50 Hz, is a predetermined ratio. To decide. The predetermined ratio is less than 50%.

図8のフローの説明に戻る。
ステップS4で容積比率αが30%未満か否かを判断する。容積比率αが30%以上の場合、換言すれば差温ΔTの大きい室内機が多い場合は、目標蒸発温度を維持する(S10)。つまり、上記図2で説明したように、差温ΔTの最も大きい室内機B1において十分な冷却能力が発揮できる蒸発温度を目標蒸発温度として決定し、その決定した目標蒸発温度に維持する制御(目標維持制御)を行う。よって、差温ΔTの大きい室内機が多く、ステップS4で「いいえ」となる場合には、省エネ運転は行わず、室内温度を設定温度にすることを優先した制御となる。
Returning to the description of the flow of FIG.
In step S4, it is determined whether the volume ratio α is less than 30%. When the volume ratio α is 30% or more, in other words, when there are many indoor units having a large temperature difference ΔT, the target evaporation temperature is maintained (S10). That is, as described with reference to FIG. 2 above, the control is performed such that the evaporation temperature at which sufficient cooling capacity can be exhibited in the indoor unit B1 having the largest temperature difference ΔT is determined as the target evaporation temperature and maintained at the determined target evaporation temperature (target Maintenance control). Therefore, when there are many indoor units having a large temperature difference ΔT and “NO” is determined in step S4, the energy-saving operation is not performed, and the control is given priority to setting the room temperature to the set temperature.

ここでは、容積比率αが20%であるため、ステップS4で「はい」に進み、続いて現在の圧縮機周波数が、高圧縮機効率となる周波数範囲f1〜f2(図2参照)の下限値f1未満か否かを判断する(S5)。   Here, since the volume ratio α is 20%, the process proceeds to “Yes” in step S4, and then the lower limit value of the frequency range f1 to f2 (see FIG. 2) in which the current compressor frequency becomes high compressor efficiency. It is determined whether it is less than f1 (S5).

ここでは、運転状況が図4の点Oで示す状況であり、圧縮機周波数がfoで高圧縮機効率となる周波数範囲の下限値f1よりも小さいため、ステップS5で「はい」となり、目標蒸発温度を1℃下げると共に、周波数上限を10Hz上げる(S6)。   Here, the operating state is a state indicated by a point O in FIG. 4, and the compressor frequency is smaller than the lower limit value f1 of the frequency range in which high compressor efficiency is achieved at fo. The temperature is lowered by 1 ° C. and the upper frequency limit is raised by 10 Hz (S6).

なお、このステップS6において、周波数上限を10Hz上げた後の周波数上限が50Hz未満とする。そして、ステップS6で決定した目標蒸発温度となるように、周波数上限の範囲内で圧縮機周波数を上げる制御を行う(S7)。このように、ステップS4、5の両方の判断で「はい」の場合には、S10の制御に代えて、ステップS6、7の制御を行う。   In this step S6, the frequency upper limit after raising the frequency upper limit by 10 Hz is assumed to be less than 50 Hz. And control which raises a compressor frequency within the range of a frequency upper limit is performed so that it may become the target evaporation temperature determined by step S6 (S7). As described above, when “Yes” is determined in both the steps S4 and S5, the control in steps S6 and S7 is performed instead of the control in S10.

そして、圧縮機周波数を上げる制御を行うことで、室内機B1(差温ΔTが最も大きい室内機)の差温ΔTが0.5℃以下に下がり(S8)、室内温度が設定温度に近づいてくると、目標蒸発温度を1℃上げると共に、圧縮機周波数上限を元に戻す(S9)。そして、目標蒸発温度を維持してステップS1に戻り、同様の処理を繰り返す。   Then, by performing control to increase the compressor frequency, the differential temperature ΔT of the indoor unit B1 (the indoor unit having the largest differential temperature ΔT) is lowered to 0.5 ° C. or less (S8), and the indoor temperature approaches the set temperature. Then, the target evaporation temperature is raised by 1 ° C., and the upper limit of the compressor frequency is restored (S9). Then, the target evaporation temperature is maintained, the process returns to step S1, and the same process is repeated.

ここで、本制御による省エネ効果について説明する。図8に示したフローにより、容積比率αが30%未満で、圧縮機周波数がf1未満場合、S6、S7の制御を行うことになる。この場合、S10の制御を行う場合に比べて、蒸発温度を高くした運転ができるため、省エネ効果を得ることができる。   Here, the energy-saving effect by this control is demonstrated. According to the flow shown in FIG. 8, when the volume ratio α is less than 30% and the compressor frequency is less than f1, the control of S6 and S7 is performed. In this case, since the operation at a higher evaporation temperature can be performed as compared with the case of performing the control of S10, an energy saving effect can be obtained.

以上説明したように、本実施の形態によれば、容量比率αが所定比率未満で且つ圧縮機周波数が高圧縮機効率を得られる周波数範囲の下限値未満のとき、省エネ運転を効果的に行える運転状況であると判断し、目標蒸発温度を下げると共に圧縮機周波数を上げるようにしたので、効率の良い運転が可能となり、省エネ運転が実現できる。   As described above, according to this embodiment, when the capacity ratio α is less than the predetermined ratio and the compressor frequency is less than the lower limit value of the frequency range where high compressor efficiency can be obtained, energy-saving operation can be effectively performed. Since it is determined that the operation is in progress and the target evaporation temperature is lowered and the compressor frequency is raised, efficient operation is possible and energy-saving operation can be realized.

そして、目標蒸発温度を上昇・下降させてトータルとして省エネ運転が実現できる。   Further, energy saving operation can be realized as a total by raising and lowering the target evaporation temperature.

なお、図8では冷房運転の場合を記載しているが、暖房運転の場合は、ステップS6で目標凝縮温度を例えば+1℃とし、ステップS9では目標蒸発温度を例えば−1℃とし、ステップS10では目標凝縮温度を維持するようにすればよい。その他のステップは冷房運転のときと同じである。   Although FIG. 8 shows the case of the cooling operation, in the case of the heating operation, the target condensation temperature is set to, for example, + 1 ° C. in step S6, the target evaporation temperature is set to, for example, −1 ° C. in step S9, and in step S10 The target condensing temperature may be maintained. Other steps are the same as in the cooling operation.

また、図8のフローの説明では、差温ΔTが大きい室内機Bが1台の場合を例に説明したが、差温ΔTが大きい室内機Bが複数台の場合でも同様である。   In the description of the flow of FIG. 8, the case where there is one indoor unit B having a large temperature difference ΔT is described as an example, but the same applies to the case where there are a plurality of indoor units B having a large temperature difference ΔT.

また、図8のフローでは、ステップS6、ステップS9で目標蒸発温度と圧縮機周波数の上限値とを変更する制御としたが、圧縮機周波数を変更する制御でも構わない。   Further, in the flow of FIG. 8, the control is performed to change the target evaporation temperature and the upper limit value of the compressor frequency in step S6 and step S9, but the control may be performed to change the compressor frequency.

また、図8のフローでは、ステップS8で室内機Bの差温ΔTを判定したが、差温ΔTが小さくなることと、容積比率が小さくなることとの間には相関関係があるため、差温ΔTの判定に代えて、容量比率で判定してもよい。   Further, in the flow of FIG. 8, the temperature difference ΔT of the indoor unit B is determined in step S8. However, since there is a correlation between the difference temperature ΔT becoming smaller and the volume ratio becoming smaller, there is a difference. Instead of determining the temperature ΔT, it may be determined by a capacity ratio.

1 圧縮機、2 油分離器、3 四方弁、4 室外熱交換器、5 絞り装置、6 室内熱交換器、7 アキュムレータ、8 返油回路、8a 開閉弁、8b キャピラリーチューブ、9 室外送風機、11 室内送風機、12 リモコン、21 吸入圧力センサ、22 吐出圧力センサ、31 液側温度センサ、32 ガス側温度センサ、33 室内温度検出センサ、100 室外制御装置、101 蒸発温度・凝縮温度換算部、102 差温・容積比率計算部、103 目標蒸発温度・目標凝縮温度計算部、104 圧縮機周波数決定部、110 室内制御装置、120 通信線、A 室外機、B(B1、B2、B3) 室内機。   DESCRIPTION OF SYMBOLS 1 Compressor, 2 Oil separator, 3 Four way valve, 4 Outdoor heat exchanger, 5 Throttling device, 6 Indoor heat exchanger, 7 Accumulator, 8 Oil return circuit, 8a On-off valve, 8b Capillary tube, 9 Outdoor blower, 11 Indoor fan, 12 Remote control, 21 Suction pressure sensor, 22 Discharge pressure sensor, 31 Liquid side temperature sensor, 32 Gas side temperature sensor, 33 Indoor temperature detection sensor, 100 Outdoor control device, 101 Evaporation temperature / condensation temperature conversion unit, 102 Difference Temperature / volume ratio calculation unit, 103 target evaporation temperature / target condensation temperature calculation unit, 104 compressor frequency determination unit, 110 indoor control device, 120 communication line, A outdoor unit, B (B1, B2, B3) indoor unit.

Claims (1)

圧縮機及び室外熱交換器を有する室外機と、
絞り装置及び室内熱交換器を有し、冷房及び暖房の少なくとも一方の運転が可能な複数の室内機と、
冷房時は、前記室内機が設置される各部屋の設定温度と、前記室内機で検出した室内温度との差温に基づいて目標蒸発温度を決定し、暖房時は、前記差温に基づいて目標凝縮温度を決定し、決定した前記目標蒸発温度又は前記目標凝縮温度を維持するように前記圧縮機の周波数を制御する目標維持制御を行う制御装置とを備え、
前記制御装置は、
前記差温が予め設定した所定温度以上となる室内機の合計容量を、運転中の全室内機の合計容量で除算した容積比率を計算し、前記容積比率が所定比率未満で且つ前記圧縮機の周波数が、所定レベル以上の高圧縮機効率を得ることができる周波数範囲の下限値未満の場合には、
前記冷房時であれば前記目標維持制御に代えて、前記目標蒸発温度を下げると共に前記圧縮機の周波数の上限値を上げる制御を行い、
前記暖房時であれば前記目標維持制御に代えて、前記目標凝縮温度を上げると共に前記圧縮機の周波数の上限値を上げる制御を行う
ことを特徴とする空気調和機。
An outdoor unit having a compressor and an outdoor heat exchanger;
A plurality of indoor units having an expansion device and an indoor heat exchanger and capable of operating at least one of cooling and heating;
During cooling, the target evaporation temperature is determined based on the temperature difference between the set temperature of each room where the indoor unit is installed and the room temperature detected by the indoor unit, and during heating, based on the temperature difference. A controller for determining a target condensation temperature and performing a target maintenance control for controlling a frequency of the compressor so as to maintain the determined target evaporation temperature or the target condensation temperature;
The controller is
A volume ratio obtained by dividing the total capacity of the indoor units in which the differential temperature is equal to or higher than a preset predetermined temperature by the total capacity of all the indoor units in operation is calculated, and the volume ratio is less than the predetermined ratio and the compressor If the frequency is less than the lower limit of the frequency range where high compressor efficiency above a predetermined level can be obtained,
Instead of the target maintenance control during cooling, the target evaporation temperature is lowered and the upper limit value of the compressor frequency is increased.
An air conditioner that performs control to raise the target condensation temperature and raise the upper limit of the frequency of the compressor instead of the target maintenance control during the heating.
JP2012079878A 2012-03-30 2012-03-30 Air conditioner Active JP5818734B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012079878A JP5818734B2 (en) 2012-03-30 2012-03-30 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012079878A JP5818734B2 (en) 2012-03-30 2012-03-30 Air conditioner

Publications (2)

Publication Number Publication Date
JP2013210124A true JP2013210124A (en) 2013-10-10
JP5818734B2 JP5818734B2 (en) 2015-11-18

Family

ID=49528110

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012079878A Active JP5818734B2 (en) 2012-03-30 2012-03-30 Air conditioner

Country Status (1)

Country Link
JP (1) JP5818734B2 (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104633840A (en) * 2013-11-15 2015-05-20 珠海格力电器股份有限公司 Control method of air conditioning system and air conditioning system
JP2015163277A (en) * 2015-06-15 2015-09-10 株式会社ユニバーサルエンターテインメント Game information display device
CN105180349A (en) * 2015-08-05 2015-12-23 广东美的制冷设备有限公司 Air conditioner and control method and device of air conditioner
CN106123218A (en) * 2016-06-24 2016-11-16 珠海格力电器股份有限公司 A kind of method for determining operation parameters for air-conditioning, device and air-conditioning
CN106196517A (en) * 2016-09-30 2016-12-07 广东美的制冷设备有限公司 Multi-split air conditioner control method, device and multi-split air conditioner
WO2018185911A1 (en) * 2017-04-06 2018-10-11 三菱電機株式会社 Air conditioning system
CN108758976A (en) * 2018-06-19 2018-11-06 广东美的制冷设备有限公司 Control method, device and the air-conditioning with it of air-conditioning
CN109916090A (en) * 2018-11-29 2019-06-21 青岛经济技术开发区海尔热水器有限公司 Heat-pump water heater control method and Teat pump boiler
US10466673B2 (en) 2016-03-04 2019-11-05 Samsung Electronics Co., Ltd. Control device for air conditioning and control method thereof
CN110657554A (en) * 2019-10-21 2020-01-07 宁波奥克斯电气股份有限公司 Air conditioner condensation prevention control method and device and air conditioner
JP2020046124A (en) * 2018-09-20 2020-03-26 株式会社富士通ゼネラル Air conditioning device
JP2020046123A (en) * 2018-09-20 2020-03-26 株式会社富士通ゼネラル Air conditioning device
CN110929408A (en) * 2019-12-02 2020-03-27 芜湖倡蓝新能源科技有限责任公司 Compressor frequency calculation of variable frequency air conditioner
CN112066525A (en) * 2020-08-13 2020-12-11 珠海格力电器股份有限公司 Multi-split air conditioner control method and device, multi-split air conditioner, storage medium and processor
CN112556227A (en) * 2020-12-22 2021-03-26 珠海格力电器股份有限公司 Air conditioning unit, frequency converter cooling system and control method thereof
CN115751619A (en) * 2022-11-29 2023-03-07 青岛海尔空调器有限总公司 Air conditioner compressor control method, device, equipment and storage medium

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0261466A (en) * 1988-08-25 1990-03-01 Daikin Ind Ltd Operation control device of air conditioning apparatus
JP2003247742A (en) * 2002-02-26 2003-09-05 Matsushita Electric Ind Co Ltd Multi-chamber type air conditioner and control method thereof
JP2008175409A (en) * 2007-01-16 2008-07-31 Mitsubishi Electric Corp Operation control method of air conditioning system, and air conditioning system
JP2010151421A (en) * 2008-12-26 2010-07-08 Daikin Ind Ltd Air conditioning system
JP2011202913A (en) * 2010-03-26 2011-10-13 Mitsubishi Heavy Ind Ltd Multi air conditioning device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0261466A (en) * 1988-08-25 1990-03-01 Daikin Ind Ltd Operation control device of air conditioning apparatus
JP2003247742A (en) * 2002-02-26 2003-09-05 Matsushita Electric Ind Co Ltd Multi-chamber type air conditioner and control method thereof
JP2008175409A (en) * 2007-01-16 2008-07-31 Mitsubishi Electric Corp Operation control method of air conditioning system, and air conditioning system
JP2010151421A (en) * 2008-12-26 2010-07-08 Daikin Ind Ltd Air conditioning system
JP2011202913A (en) * 2010-03-26 2011-10-13 Mitsubishi Heavy Ind Ltd Multi air conditioning device

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104633840B (en) * 2013-11-15 2017-05-10 珠海格力电器股份有限公司 Control method of air conditioning system and air conditioning system
CN104633840A (en) * 2013-11-15 2015-05-20 珠海格力电器股份有限公司 Control method of air conditioning system and air conditioning system
JP2015163277A (en) * 2015-06-15 2015-09-10 株式会社ユニバーサルエンターテインメント Game information display device
CN105180349A (en) * 2015-08-05 2015-12-23 广东美的制冷设备有限公司 Air conditioner and control method and device of air conditioner
CN105180349B (en) * 2015-08-05 2017-11-10 广东美的制冷设备有限公司 Air conditioner and its control method and control device
US10466673B2 (en) 2016-03-04 2019-11-05 Samsung Electronics Co., Ltd. Control device for air conditioning and control method thereof
CN106123218B (en) * 2016-06-24 2020-01-24 珠海格力电器股份有限公司 Operation parameter determination method and device for air conditioner and air conditioner
CN106123218A (en) * 2016-06-24 2016-11-16 珠海格力电器股份有限公司 A kind of method for determining operation parameters for air-conditioning, device and air-conditioning
CN106196517A (en) * 2016-09-30 2016-12-07 广东美的制冷设备有限公司 Multi-split air conditioner control method, device and multi-split air conditioner
CN106196517B (en) * 2016-09-30 2019-09-17 广东美的制冷设备有限公司 Multi-split air conditioner control method, device and multi-split air conditioner
JPWO2018185911A1 (en) * 2017-04-06 2019-07-25 三菱電機株式会社 Air conditioning system
WO2018185911A1 (en) * 2017-04-06 2018-10-11 三菱電機株式会社 Air conditioning system
CN108758976A (en) * 2018-06-19 2018-11-06 广东美的制冷设备有限公司 Control method, device and the air-conditioning with it of air-conditioning
JP7159736B2 (en) 2018-09-20 2022-10-25 株式会社富士通ゼネラル air conditioner
JP2020046124A (en) * 2018-09-20 2020-03-26 株式会社富士通ゼネラル Air conditioning device
JP2020046123A (en) * 2018-09-20 2020-03-26 株式会社富士通ゼネラル Air conditioning device
JP7193775B2 (en) 2018-09-20 2022-12-21 株式会社富士通ゼネラル air conditioner
CN109916090A (en) * 2018-11-29 2019-06-21 青岛经济技术开发区海尔热水器有限公司 Heat-pump water heater control method and Teat pump boiler
CN110657554A (en) * 2019-10-21 2020-01-07 宁波奥克斯电气股份有限公司 Air conditioner condensation prevention control method and device and air conditioner
CN110929408A (en) * 2019-12-02 2020-03-27 芜湖倡蓝新能源科技有限责任公司 Compressor frequency calculation of variable frequency air conditioner
CN110929408B (en) * 2019-12-02 2023-02-17 芜湖倡蓝新能源科技有限责任公司 Compressor frequency calculation of variable frequency air conditioner
CN112066525A (en) * 2020-08-13 2020-12-11 珠海格力电器股份有限公司 Multi-split air conditioner control method and device, multi-split air conditioner, storage medium and processor
CN112556227A (en) * 2020-12-22 2021-03-26 珠海格力电器股份有限公司 Air conditioning unit, frequency converter cooling system and control method thereof
CN115751619A (en) * 2022-11-29 2023-03-07 青岛海尔空调器有限总公司 Air conditioner compressor control method, device, equipment and storage medium

Also Published As

Publication number Publication date
JP5818734B2 (en) 2015-11-18

Similar Documents

Publication Publication Date Title
JP5818734B2 (en) Air conditioner
JP5125124B2 (en) Refrigeration equipment
JP7190682B2 (en) refrigeration cycle system
JP6584497B2 (en) Refrigeration cycle apparatus and refrigeration cycle apparatus abnormality detection system
JP6109205B2 (en) Refrigeration cycle apparatus and control method of refrigeration cycle apparatus
JPWO2016071947A1 (en) Refrigeration cycle apparatus and refrigeration cycle apparatus abnormality detection system
JP5418622B2 (en) Refrigeration equipment
JP5598353B2 (en) Air conditioner
JPWO2014102940A1 (en) Refrigeration cycle apparatus and control method of refrigeration cycle apparatus
WO2008015930A1 (en) Air conditioner
EP3260792B1 (en) Air conditioning system control device, air conditioning system, air conditioning control program, and air conditioning system control method
JP5034066B2 (en) Air conditioner
JP6628911B1 (en) Refrigeration cycle device
WO2014192052A1 (en) Air-conditioning device
JP6172702B2 (en) Multi-type air conditioning system
JP2008241065A (en) Refrigerating device and oil returning method of refrigerating device
JP5506433B2 (en) Multi-type air conditioner
JP5582838B2 (en) Multi-type air conditioner
JP6020162B2 (en) Air conditioner
KR20110105230A (en) Air conditioner and control method of the same
JP2011242097A (en) Refrigerating apparatus
KR20070077639A (en) Multi air-conditioner and its control method
JP2012207866A (en) Air conditioner
JPWO2017094172A1 (en) Air conditioner
KR101075299B1 (en) Air conditioner and method of controlling the same

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20140707

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20150323

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150331

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150525

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20150901

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20150929

R150 Certificate of patent or registration of utility model

Ref document number: 5818734

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250