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JP3495486B2 - Air conditioner - Google Patents
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JP3495486B2 - Air conditioner - Google Patents

Air conditioner

Info

Publication number
JP3495486B2
JP3495486B2 JP33522095A JP33522095A JP3495486B2 JP 3495486 B2 JP3495486 B2 JP 3495486B2 JP 33522095 A JP33522095 A JP 33522095A JP 33522095 A JP33522095 A JP 33522095A JP 3495486 B2 JP3495486 B2 JP 3495486B2
Authority
JP
Japan
Prior art keywords
temperature
compressor
air conditioner
opening
expansion valve
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.)
Expired - Fee Related
Application number
JP33522095A
Other languages
Japanese (ja)
Other versions
JPH09178273A (en
Inventor
泰史 佐野
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.)
Carrier Japan Corp
Original Assignee
Toshiba Carrier 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 Toshiba Carrier Corp filed Critical Toshiba Carrier Corp
Priority to JP33522095A priority Critical patent/JP3495486B2/en
Publication of JPH09178273A publication Critical patent/JPH09178273A/en
Application granted granted Critical
Publication of JP3495486B2 publication Critical patent/JP3495486B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/21Refrigerant outlet evaporator temperature

Landscapes

  • Air Conditioning Control Device (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、スーパヒート量
の一定値制御を行なう空気調和機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner for controlling a constant value of superheat amount.

【0002】[0002]

【従来の技術】空気調和機では、冷房負荷あるいは暖房
負荷に応じて圧縮機の能力(運転周波数)を制御する。
同時に、冷媒のスーパヒート量SHを検出し、そのスーパ
ヒート量SHが予め定められている一定値となるよう、冷
凍サイクル中の電動膨張弁の開度を制御している。
2. Description of the Related Art In an air conditioner, the capacity (operating frequency) of a compressor is controlled according to a cooling load or a heating load.
At the same time, the superheat amount SH of the refrigerant is detected, and the opening degree of the electric expansion valve during the refrigeration cycle is controlled so that the superheat amount SH becomes a predetermined constant value.

【0003】また、空気調和機では、過負荷運転時に圧
縮機の内部温度が過度に上昇することがある。いわゆる
過熱である。この過熱が生じると、冷媒の分解、圧縮機
内の潤滑油の劣化、圧縮機モータの絶縁性能の劣化な
ど、種々の不具合を生じる。
In an air conditioner, the internal temperature of the compressor may rise excessively during overload operation. So-called overheating. When this overheating occurs, various problems such as the decomposition of the refrigerant, the deterioration of the lubricating oil in the compressor, the deterioration of the insulation performance of the compressor motor, and the like occur.

【0004】そこで、従来、圧縮機の吐出冷媒温度を検
知し、その吐出冷媒温度が所定値以上になると圧縮機の
運転周波数を低減し、吐出冷媒温度の上昇を抑えて上記
の不具合を解消するものがある。いわゆる吐出温度制御
である。
Therefore, conventionally, the discharge refrigerant temperature of the compressor is detected, and when the discharge refrigerant temperature exceeds a predetermined value, the operating frequency of the compressor is reduced to suppress the rise of the discharge refrigerant temperature and solve the above-mentioned problems. There is something. This is so-called discharge temperature control.

【0005】[0005]

【発明が解決しようとする課題】圧縮機の運転周波数を
低減する吐出温度制御では、空調能力が低下し、快適性
を損なうという問題がある。この発明は上記の事情を考
慮したもので、第1ないし第4の発明の空気調和機は、
快適性を損なうことなく、圧縮機の過熱を防止して圧縮
機の寿命向上が図れることを目的とする。
In the discharge temperature control for reducing the operating frequency of the compressor, there is a problem that the air conditioning capacity decreases and the comfort is impaired. The present invention takes the above circumstances into consideration, and the air conditioners of the first to fourth inventions include:
An object of the present invention is to prevent overheating of the compressor and improve the life of the compressor without impairing comfort.

【0006】第5ないし第7の発明の空気調和機は、快
適性を損なうことなく、圧縮機の過熱を防止して圧縮機
の寿命向上が図れるとともに、冷房と暖房の別にかかわ
らずスーパヒート量SHを適確に検出してスーパヒート量
制御の信頼性向上が図れることを目的とする。
In the air conditioner of the fifth to seventh inventions, overheating of the compressor can be prevented and life of the compressor can be improved without impairing comfort, and the superheat amount SH regardless of cooling or heating. Is accurately detected to improve the reliability of superheat amount control.

【0007】第8ないし第16の発明の空気調和機は、
圧縮機の起動時の過熱や液バックを防ぎつつスーパヒー
ト量制御への安定かつスムーズな移行が可能なことを目
的とする。
The air conditioner of the eighth to sixteenth inventions comprises:
The object is to enable stable and smooth transition to superheat amount control while preventing overheating and liquid back at the time of starting the compressor.

【0008】[0008]

【課題を解決するための手段】第1の発明の空気調和機
は、圧縮機、凝縮器、電動膨張弁、蒸発器を順次接続し
た冷凍サイクルを備え、冷媒のスーパヒート量SHが目標
値SHO一定となるよう電動膨張弁の開度を制御するもの
であって、圧縮機の吐出冷媒温度Tdを検知する検知手
段と、この検知手段の検知温度Tdが高くなるほど検知
温度Tdに応じて目標値 SHO を低下方向に段階的に補正
する補正手段と、を備える。
The air conditioner of the first invention comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the refrigerant superheat amount SH is constant at a target value SHO. For controlling the opening degree of the electric expansion valve so that the discharge refrigerant temperature Td of the compressor is detected, and detection is performed as the detection temperature Td of the detecting means increases.
And a correction unit that gradually corrects the target value SHO in the decreasing direction according to the temperature Td .

【0009】第2の発明の空気調和機は、能力可変の圧
縮機、凝縮器、電動膨張弁、蒸発器を順次接続した冷凍
サイクルを備え、冷媒のスーパヒート量SHが目標値SHO
一定となるよう電動膨張弁の開度を制御するものにおい
て、圧縮機の吐出冷媒温度Tdを検知する検知手段と、
この検知手段の検知温度Tdおよび圧縮機の運転周波数
Fに応じて目標値SHO を補正する補正手段と、を備え
る。
The air conditioner of the second invention comprises a refrigeration cycle in which a compressor having variable capacity, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the superheat amount SH of the refrigerant is a target value SHO.
In the one that controls the opening degree of the electric expansion valve so as to be constant, a detection unit that detects the discharge refrigerant temperature Td of the compressor,
And a correction unit that corrects the target value SHO according to the detection temperature Td of the detection unit and the operating frequency F of the compressor.

【0010】第3の発明の空気調和機は、圧縮機、凝縮
器、電動膨張弁、蒸発器を順次接続した冷凍サイクルを
備え、冷媒のスーパヒート量SHが目標値SHO 一定となる
よう電動膨張弁の開度を制御するものにおいて、圧縮機
のケース温度Tcaを検知する検知手段と、この検知手段
の検知温度Tcaに応じて目標値SHO を補正する補正手段
と、を備える。
The air conditioner of the third invention comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve and an evaporator are sequentially connected, and an electric expansion valve so that the superheat amount SH of the refrigerant becomes a target value SHO constant. In order to control the opening of the compressor, a detecting means for detecting the case temperature Tca of the compressor and a correcting means for correcting the target value SHO according to the detected temperature Tca of the detecting means are provided.

【0011】第4の発明の空気調和機は、圧縮機、凝縮
器、電動膨張弁、蒸発器を順次接続した冷凍サイクルを
備え、冷媒のスーパヒート量SHが目標値SHO 一定となる
よう電動膨張弁の開度を制御するものにおいて、圧縮機
の吐出冷媒温度Tdを検知する検知手段と、圧縮機のケ
ース温度Tcaを検知する検知手段と、これら検知手段の
検知温度Td,Tcaに応じて目標値SHO を補正する補正
手段と、を備える。
An air conditioner of a fourth invention comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and an electric expansion valve so that the superheat amount SH of the refrigerant becomes a target value SHO constant. For controlling the opening of the compressor, a detecting means for detecting the discharge refrigerant temperature Td of the compressor, a detecting means for detecting the case temperature Tca of the compressor, and a target value according to the detected temperatures Td, Tca of these detecting means. And a correction means for correcting the SHO.

【0012】第5の発明の空気調和機は、圧縮機、四方
弁、室外熱交換器、電動膨張弁、室内熱交換器を順次接
続したヒートポンプ式冷凍サイクルを備え、冷媒のスー
パヒート量SHが目標値SHO 一定となるよう電動膨張弁の
開度を制御するものにおいて、冷凍サイクルの液側配管
と圧縮機の吸込側配管との間に絞り装置を介して設けた
バイパスと、このバイパスの低圧側の冷媒温度Tuを検
知する第1検知手段と、暖房時に室外熱交換器に流入す
る冷媒の温度Teを検知する第2検知手段と、圧縮機の
吸込冷媒温度Tsを検知する第3検知手段と、第1検知
手段の検知温度Tuおよび第2検知手段の検知温度Te
のいずれか一方を冷媒の疑似飽和温度として選択する選
択手段と、この選択手段で選択される疑似飽和温度と第
3検知手段の検知温度Tsとから上記スーパヒート量SH
を検出する検出手段と、圧縮機の吐出冷媒温度Tdまた
はケース温度Tcaを検知する検知手段と、この検知手段
の検知温度に応じて目標値SHO を補正する補正手段と、
を備える。
The air conditioner of the fifth invention is equipped with a heat pump type refrigeration cycle in which a compressor, a four-way valve, an outdoor heat exchanger, an electric expansion valve, and an indoor heat exchanger are sequentially connected, and the superheat amount SH of the refrigerant is a target. In the one that controls the opening of the electric expansion valve to keep the value SHO constant, a bypass provided via a throttle device between the liquid side pipe of the refrigeration cycle and the suction side pipe of the compressor, and the low pressure side of this bypass Detecting means for detecting the refrigerant temperature Tu of the refrigerant, second detecting means for detecting the temperature Te of the refrigerant flowing into the outdoor heat exchanger during heating, and third detecting means for detecting the suction refrigerant temperature Ts of the compressor. , The detection temperature Tu of the first detection means and the detection temperature Te of the second detection means
The superheat amount SH based on the selection means for selecting one of the above as the pseudo saturation temperature of the refrigerant, and the pseudo saturation temperature selected by this selection means and the detection temperature Ts of the third detection means.
Detecting means for detecting the discharge refrigerant temperature Td or the case temperature Tca of the compressor, and a correcting means for correcting the target value SHO according to the detected temperature of the detecting means.
Equipped with.

【0013】第6の発明の空気調和機は、第5の発明の
選択手段が、[(Te−Tu)≧所定値K]の条件が成
立するとき検知温度Tuを疑似飽和温度として選択する
手段と、上記条件が成立しないとき検知温度Teを疑似
飽和温度として選択する手段と、を備える。
In the air conditioner of the sixth invention, the selecting means of the fifth invention selects the detected temperature Tu as the pseudo saturation temperature when the condition of [(Te-Tu) ≧ predetermined value K] is satisfied. And means for selecting the detected temperature Te as the pseudo saturation temperature when the above conditions are not satisfied.

【0014】第7の発明の空気調和機は、第5の発明の
選択手段が、[(Te−Tu)≧所定値K]の条件が成
立するとき検知温度Tuを疑似飽和温度として選択する
手段と、上記条件が成立せず[Te<Tu]の条件が成
立するとき検知温度Teを疑似飽和温度として選択する
手段と、上記両条件が共に成立しないとき[Te−(T
e−Tu)2 /K]の演算値を疑似飽和温度として選択
する手段と、を備えている。
In the air conditioner of the seventh invention, the selecting means of the fifth invention selects the detection temperature Tu as the pseudo saturation temperature when the condition of [(Te-Tu) ≧ predetermined value K] is satisfied. And means for selecting the detected temperature Te as the pseudo saturation temperature when the above condition is not satisfied and the condition [Te <Tu] is satisfied, and [Te- (T
e-Tu) 2 / K] is selected as the pseudo saturation temperature.

【0015】第8の発明の空気調和機は、圧縮機、凝縮
器、電動膨張弁、蒸発器を順次接続した冷凍サイクルを
備え、圧縮機の起動に伴い電動膨張弁の開度を所定の初
期開度へと移行制御し、その後、冷媒のスーパヒート量
SHが目標値SHO 一定となるよう電動膨張弁の開度を制御
するものであって、起動からスーパヒート量SHが設定値
SH1 に至るまでの経過時間に応じて上記初期開度を補正
する制御手段を備えている。
The air conditioner of the eighth invention comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve and an evaporator are sequentially connected, and the opening degree of the electric expansion valve is set to a predetermined initial value when the compressor is started. Transition control to the opening degree, then the superheat amount of the refrigerant
It controls the opening of the electric expansion valve so that SH is constant at the target value SHO.
Control means is provided to correct the initial opening according to the time elapsed until reaching SH 1 .

【0016】第9の発明の空気調和機は、第8の発明の
制御手段が、上記経過時間に応じた量だけ初期開度を開
方向に補正する。第10の発明の空気調和機は、圧縮
機、凝縮器、電動膨張弁、蒸発器を順次接続した冷凍サ
イクルを備え、圧縮機の起動に伴い電動膨張弁の開度を
所定の初期開度へと移行制御し、その後、冷媒のスーパ
ヒート量SHが目標値SHO 一定となるよう電動膨張弁の開
度を制御するものであって、起動に伴う上記初期開度へ
の移行に際し、電動膨張弁の開度を、先ずはスーパヒー
ト量SHが設定値SH1 を超えて設定値SH2 (>SH1 )に至
るまで圧縮機の運転周波数に対応する基本開度に設定
し、スーパヒート量SHが設定値SH2 を超えたら基本開度
より大きい起動開度αまで増大してその状態を保持し、
スーパヒート量SHが設定値SH1 まで低下したところで起
動開度αから上記初期開度へと絞る第1制御手段と、起
動からスーパヒート量SHが設定値SH1 に至るまでの経過
時間に応じて上記初期開度を補正する第2制御手段と、
を備える。
In the air conditioner of the ninth invention, the control means of the eighth invention corrects the initial opening degree in the opening direction by an amount according to the elapsed time. An air conditioner of a tenth invention comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the opening of the electric expansion valve is set to a predetermined initial opening when the compressor is started. It controls the opening of the electric expansion valve so that the superheat amount SH of the refrigerant becomes constant at the target value SHO, and the transition of the electric expansion valve to the initial opening accompanying startup is performed. the opening, first sets the basic opening corresponding to the operating frequency of the compressor until the superheat amount SH set value SH 1 beyond setpoint SH 2 (> SH 1), superheat amount SH set value When SH 2 is exceeded, the starting opening α that is larger than the basic opening is increased and the state is maintained,
When the superheat amount SH drops to the set value SH 1, the first control means for narrowing the starting opening α to the above initial opening, and the above according to the elapsed time from the start until the superheat amount SH reaches the set value SH 1 Second control means for correcting the initial opening,
Equipped with.

【0017】第11の発明の空気調和機は、第10の発
明の第1制御手段が、電動膨張弁の開度を起動開度αか
ら初期開度へ絞る過程で、絞りを所定値ずつ徐々に進め
る制御を行なう第12の発明の空気調和機は、第11の
発明の第1制御手段が、電動膨張弁の開度を起動開度α
から初期開度へ徐々に絞る過程で、スーパヒート量SHが
設定値SH3 (>SH2 )まで下降したとき、その時点で開
度の絞りを終了し、目標値SHO一定のための開度制御へ
移る制御を行なう。
In the air conditioner of the eleventh invention, the first control means of the tenth invention gradually narrows the opening of the electric expansion valve from the starting opening α to the initial opening by a predetermined value. In the air conditioner of the twelfth aspect of the invention that performs control to proceed to, the first control means of the eleventh aspect of the invention sets the opening degree of the electric expansion valve to the starting opening degree α.
When the superheat amount SH falls to the set value SH 3 (> SH 2 ) in the process of gradually reducing from the initial opening to the initial opening, the opening is stopped at that point and the opening is controlled to keep the target value SHO constant. Control to move to.

【0018】第13の発明の空気調和機は、第8ないし
第12の発明のいずれかにおいて、圧縮機の吐出冷媒温
度Tdを検知する検知手段と、この検知手段の検知温度
Tdが所定値以上に上昇したとき、起動に伴う上記初期
開度への移行制御を終了し、検知温度Tdの上昇を抑え
るための吐出温度制御に移る制御手段と、を備えてい
る。
An air conditioner according to a thirteenth aspect of the present invention is the air conditioner according to any one of the eighth to twelfth aspects of the present invention, wherein a detecting means for detecting the refrigerant discharge temperature Td of the compressor and a temperature Td detected by the detecting means are equal to or more than a predetermined value. Control means for terminating the shift control to the initial opening degree upon startup and shifting to the discharge temperature control for suppressing the rise in the detected temperature Td.

【0019】第14の発明の空気調和機は、圧縮機、凝
縮器、電動膨張弁、蒸発器を順次接続した冷凍サイクル
を備え、圧縮機の起動に伴い電動膨張弁の開度を所定の
初期開度へと移行制御し、その後、冷媒のスーパヒート
量SHが目標値SHO 一定となるよう電動膨張弁の開度を制
御するものであって、起動に伴う上記初期開度への移行
に際し、電動膨張弁の開度を、所定の起動開度αまで増
大して保持し、スーパヒート量SHが設定値SH1 まで低下
したところで起動開度αから上記初期開度へと絞る制御
手段と、電動膨張弁の開度を起動開度αまで増大して保
持した後、スーパヒート量SHが設定値SH1 まで低下しな
いまま所定時間が経過したとき、起動開度αの保持を解
除して目標値SHO 一定のための開度制御へ移る制御手段
と、を備える。
The air conditioner of the fourteenth invention comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the opening degree of the electric expansion valve is set to a predetermined initial value when the compressor is started. It controls the opening degree of the electric expansion valve so that the superheat amount SH of the refrigerant becomes the target value SHO at a constant value. The opening of the expansion valve is increased to a predetermined starting opening α and is maintained, and when the superheat amount SH drops to a set value SH 1, control means for reducing the starting opening α to the above-mentioned initial opening, and electric expansion After the valve opening is increased to the starting opening α and maintained, if the predetermined amount of time elapses without the superheat amount SH decreasing to the set value SH 1 , the starting opening α is released and the target value SHO becomes constant. Control means for shifting to the opening degree control for.

【0020】第15の発明の空気調和機は、第10、第
11、第12および第14の発明のいずれかにおいて、
起動に伴う初期開度への移行制御中に圧縮機が運転中断
したとき、その圧縮機の運転再開に伴い上記移行制御を
再開する制御手段と、この移行制御の再開時、起動開度
αを前回の移行制御時よりも小さい値に補正する制御手
段と、を備える。
An air conditioner of a fifteenth invention is the air conditioner of any one of the tenth, eleventh, twelfth and fourteenth inventions,
When the operation of the compressor is interrupted during the transition control to the initial opening degree upon start-up, the control means for restarting the transition control along with the restart of the operation of the compressor, and the restarting degree α of the startup opening α when the transition control is restarted And a control unit that corrects the value to a value smaller than that in the previous transition control.

【0021】第16の発明の空気調和機は、第10、第
11および第12の発明のいずれかにおいて、起動に伴
う初期開度への移行制御中に圧縮機が運転中断したと
き、その圧縮機の運転再開に伴い上記移行制御を再開す
る制御手段と、この移行制御の再開時、設定値SH2 を前
回の移行制御時よりも大きな値に補正する制御手段と、
を備える。
The air conditioner of the sixteenth invention is the air conditioner of any one of the tenth, eleventh and twelfth inventions, wherein when the operation of the compressor is interrupted during the control of shifting to the initial opening degree upon start-up, the compression thereof is performed. Control means for restarting the above-mentioned transfer control with restarting of the machine, and control means for correcting the set value SH 2 to a value larger than that at the previous transfer control when restarting this transfer control,
Equipped with.

【0022】[0022]

【発明の実施の形態】以下、この発明の一実施例につい
て図面を参照して説明する。図1に示すように、能力可
変圧縮機1の吐出口に四方弁2を介して室外熱交換器3
を配管接続し、その室外熱交換器3に電動膨張弁(パル
スモータバルブ;PMV)4を介して室内熱交換器5を
配管接続する。さらに、室内熱交換器5に、上記四方弁
2を介して圧縮機1の吸込口を配管接続する。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. As shown in FIG. 1, an outdoor heat exchanger 3 is connected to a discharge port of a variable capacity compressor 1 via a four-way valve 2.
Is connected to a pipe, and the indoor heat exchanger 5 is connected to the outdoor heat exchanger 3 via an electric expansion valve (pulse motor valve; PMV) 4. Further, the suction port of the compressor 1 is connected to the indoor heat exchanger 5 via the four-way valve 2 by piping.

【0023】つまり、冷房時は四方弁2の流路を冷房モ
ードに設定することにより、実線矢印の方向に冷媒を流
して冷房サイクルを形成し、室外熱交換器3を凝縮器、
室内熱交換器5を蒸発器として機能させる。
That is, during cooling, the flow path of the four-way valve 2 is set to the cooling mode so that the refrigerant flows in the direction of the solid line arrow to form the cooling cycle, and the outdoor heat exchanger 3 is connected to the condenser,
The indoor heat exchanger 5 functions as an evaporator.

【0024】暖房時は、四方弁2の流路を暖房モードに
切換えることにより、破線矢印の方向に冷媒を流して暖
房サイクルを形成し、室内熱交換器5を凝縮器、室外熱
交換器3を蒸発器として機能させる。
During heating, the flow path of the four-way valve 2 is switched to the heating mode to flow the refrigerant in the direction of the dashed arrow to form a heating cycle, and the indoor heat exchanger 5 is changed to the condenser and the outdoor heat exchanger 3 Function as an evaporator.

【0025】室外熱交換器3と電動膨張弁4との間の液
側配管から、圧縮機1の吸込側配管にかけて、バイパス
6を配管接続する。このバイパス6に、絞り装置として
キャピラリチューブ7を設ける。
The bypass 6 is pipe-connected from the liquid side pipe between the outdoor heat exchanger 3 and the electric expansion valve 4 to the suction side pipe of the compressor 1. A capillary tube 7 is provided in the bypass 6 as a diaphragm device.

【0026】圧縮機1の吐出側配管に、吐出冷媒温度T
dを検知するための温度センサ11を取付ける。室外熱
交換器3の近傍の液側配管に、温度センサ12を取付け
る。温度センサ12は、暖房時、室外熱交換器3に流入
する冷媒の温度Teを検知するもので、室外熱交換器3
の着霜検知用として利用される。室内熱交換器5の近傍
に、吸込空気温度(以下、室内温度と称す)Taを検知
するための室内温度センサ13を設ける。圧縮機1の吸
込側配管に、吸込冷媒温度Tsを検知するための温度セ
ンサ14を取付ける。バイパス6において、キャピラリ
チューブ7より下流側の低圧側配管に温度センサ15を
取付ける。温度センサ15は、バイパス6の低圧側の冷
媒温度Tuを検知する。圧縮機1のケースに温度センサ
16を取付ける。温度センサ16は、圧縮機1のケース
温度Tcaを検知する。
In the discharge side pipe of the compressor 1, the discharge refrigerant temperature T
A temperature sensor 11 for detecting d is attached. The temperature sensor 12 is attached to the liquid side pipe near the outdoor heat exchanger 3. The temperature sensor 12 detects the temperature Te of the refrigerant flowing into the outdoor heat exchanger 3 during heating, and the outdoor heat exchanger 3
It is used for frost detection. An indoor temperature sensor 13 for detecting the intake air temperature (hereinafter, referred to as indoor temperature) Ta is provided near the indoor heat exchanger 5. A temperature sensor 14 for detecting the suction refrigerant temperature Ts is attached to the suction side pipe of the compressor 1. In the bypass 6, a temperature sensor 15 is attached to the low pressure side pipe downstream of the capillary tube 7. The temperature sensor 15 detects the refrigerant temperature Tu on the low pressure side of the bypass 6. The temperature sensor 16 is attached to the case of the compressor 1. The temperature sensor 16 detects the case temperature Tca of the compressor 1.

【0027】商用交流電源20に、インバータ回路21
を接続するとともに、降圧トランス22を介して制御部
30を接続する。インバータ回路21は、電源電圧を整
流し、それをスイッチングにより、制御部30からの指
令に応じた周波数(および電圧)の交流に変換し、出力
する。この出力を駆動電力として圧縮機1に供給してい
る。インバータ回路21の出力周波数のことを、以下、
圧縮機1の運転周波数Fと称する。
The commercial AC power source 20 is provided with an inverter circuit 21.
And the control unit 30 via the step-down transformer 22. The inverter circuit 21 rectifies the power supply voltage, converts the power supply voltage into alternating current having a frequency (and voltage) according to a command from the control unit 30, and outputs the alternating current. This output is supplied to the compressor 1 as drive power. The output frequency of the inverter circuit 21 is
It is referred to as the operating frequency F of the compressor 1.

【0028】制御部30に、四方弁2、電動膨張弁4、
温度センサ11,12,13,14,15、インバータ
回路21、および受光部31を接続する。受光部31
は、リモートコントロール式の操作器32から発せられ
る赤外線光を受光する。操作器32は、使用者のキー操
作により入力される運転条件を赤外線光にて空気調和機
本体に送信する。操作器32のことを、以下、リモコン
と略称する。
The control unit 30 includes a four-way valve 2, an electric expansion valve 4,
The temperature sensors 11, 12, 13, 14, 15, the inverter circuit 21, and the light receiving section 31 are connected. Light receiving part 31
Receives infrared light emitted from the remote control type operation device 32. The operation device 32 transmits operating conditions input by a user's key operation to the air conditioner body by infrared light. The operation device 32 will be abbreviated as a remote controller hereinafter.

【0029】 そして、制御部30は、主要な機能手段
として次の(1)ないし(4)を有する。 (1)温度センサ15の検知温度Tuを冷媒の擬似飽和
温度として選択し、その擬似飽和温度と温度センサ14
の検知温度Tsとから蒸発器における冷媒のスーパヒー
ト量SHを検出する検出手段。
The control unit 30 has the following (1) to (4) as main functional means. (1) The detection temperature Tu of the temperature sensor 15 is selected as the pseudo saturation temperature of the refrigerant, and the pseudo saturation temperature and the temperature sensor 14 are selected.
A detection means for detecting the superheat amount SH of the refrigerant in the evaporator from the detected temperature Ts.

【0030】(2)検出したスーパヒート量SHが目標値
SHO 一定となるよう電動膨張弁4の開度を所定値ずつ制
御するスーパヒート量制御手段。 (3)温度センサ11の検知温度(吐出冷媒温度)Td
が所定値d3 未満のとき、その検知温度Tdに応じてス
ーパヒート量制御の目標値SHO を補正する補正手段。具
体的には、検知温度Tdが高くなるほど目標値SHO を低
下方向に補正していく。この補正にスーパヒート量制御
が追従することで電動膨張弁4の開度増大を図り、圧縮
機1に液バック気味に冷媒が戻して冷凍サイクルの過熱
状態を抑制させる。
(2) The detected superheat amount SH is the target value
SHO Superheat amount control means for controlling the opening degree of the electric expansion valve 4 by a predetermined value so as to be constant. (3) Temperature detected by the temperature sensor 11 (discharged refrigerant temperature) Td
Is less than the predetermined value d 3, a correction means for correcting the target value SHO of the superheat amount control according to the detected temperature Td. Specifically, the target value SHO is corrected downward as the detected temperature Td increases. When the superheat amount control follows this correction, the opening degree of the electric expansion valve 4 is increased, and the refrigerant is returned to the compressor 1 in a liquid-backed manner to suppress the overheated state of the refrigeration cycle.

【0031】(4)目標値SHO の補正にもかかわらず、
温度センサ11の検知温度Tdが所定値d3 以上に上昇
すると、スーパヒート量制御に優先する形で、電動膨張
弁4の開度を所定制御量ずつさらに増大する吐出温度制
御手段。この制御は、過熱を確実に抑えるためのもので
ある。
(4) Despite the correction of the target value SHO,
When the detection temperature Td of the temperature sensor 11 rises above a predetermined value d 3, with priority type to superheat amount control, discharge temperature control means to further increase the degree of opening of the electric expansion valve 4 by a predetermined control amount. This control is for surely suppressing overheating.

【0032】つぎに、作用を説明する。冷房運転時は、
図1の実線矢印の方向に冷媒を流し、室外熱交換器3を
凝縮器、室内熱交換器5を蒸発器として機能させる。こ
れにより、室内を冷房する。
Next, the operation will be described. During cooling operation,
Refrigerant is caused to flow in the direction of the solid line arrow in FIG. 1 so that the outdoor heat exchanger 3 functions as a condenser and the indoor heat exchanger 5 functions as an evaporator. This cools the room.

【0033】暖房運転時は、四方弁2の流路を切換えて
図1の破線矢印の方向に冷媒を流し、室内熱交換器7を
凝縮器、室外熱交換器5を蒸発器として機能させる。こ
れにより、室内を暖房する。
During the heating operation, the flow path of the four-way valve 2 is switched to allow the refrigerant to flow in the direction of the broken arrow in FIG. 1 so that the indoor heat exchanger 7 functions as a condenser and the outdoor heat exchanger 5 functions as an evaporator. This heats the room.

【0034】この冷房および暖房運転時、リモコン32
による設定室内温度と室内温度センサ13の検知温度T
aとの差を空調負荷として求め、その空調負荷に応じて
圧縮機1の運転周波数Fを制御する。この制御により、
室内温度を設定室内温度へと収束させる。
During the cooling and heating operation, the remote controller 32
The set indoor temperature by T and the detected temperature T of the indoor temperature sensor 13
The difference from a is obtained as an air conditioning load, and the operating frequency F of the compressor 1 is controlled according to the air conditioning load. By this control,
Allow the room temperature to converge to the set room temperature.

【0035】また、冷房および暖房運転時、冷凍サイク
ルの液側配管を通る冷媒の一部がバイパス6に流入す
る。流入した冷媒はキャピラリチューブ7を通り、圧縮
機1に吸込口に導かれる。このとき、バイパス6の低圧
側(下流側)を流れる冷媒の温度Tuが温度センサ15
で検知され、圧縮機1に吸込まれる冷媒の温度Tsが温
度センサ14で検知される。温度センサ15の検知温度
Tuは疑似飽和温度に相当する。
During the cooling and heating operations, part of the refrigerant passing through the liquid side pipe of the refrigeration cycle flows into the bypass 6. The inflowing refrigerant passes through the capillary tube 7 and is guided to the compressor 1 through the suction port. At this time, the temperature Tu of the refrigerant flowing on the low pressure side (downstream side) of the bypass 6 is determined by the temperature sensor 15.
The temperature Ts of the refrigerant sucked into the compressor 1 is detected by the temperature sensor 14. The detection temperature Tu of the temperature sensor 15 corresponds to the pseudo saturation temperature.

【0036】制御部30は、所定の制御インターバル
(たとえば1分)で次の制御を実行する。温度センサ1
4の検知温度Tsと温度センサ15の検知温度Tuとの
差(=Ts−Tu)を冷媒のスーパヒート量SHとして求
める。このスーパヒート量SHと目標値SHO との差(=SH
−SHO )に基づき、電動膨張弁4の現時点の開度に対す
る開度操作量(駆動パルス数)を求める。そして、求め
た開度操作量だけ実際に電動膨張弁4の開度を操作す
る。
The control unit 30 executes the following control at a predetermined control interval (for example, 1 minute). Temperature sensor 1
The difference (= Ts-Tu) between the detected temperature Ts of No. 4 and the detected temperature Tu of the temperature sensor 15 is obtained as the superheat amount SH of the refrigerant. Difference between this superheat amount SH and target value SHO (= SH
-SHO), the opening degree operation amount (driving pulse number) with respect to the current opening degree of the electric expansion valve 4 is obtained. Then, the opening degree of the electric expansion valve 4 is actually operated by the calculated opening operation amount.

【0037】この開度操作により、圧縮機1の能力変化
にかかわらずスーパヒート量SHが目標値SHO 一定に維持
され、冷凍サイクルが安定する。目標値SHO について
は、通常値“5deg”を予め定めており、その通常値を温
度センサ11の検知温度Tdに応じて適宜に補正する。
たとえば、図2に示すように、設定値d1 ,d2 ,d3
(d1 <d2 <d3 )を用意し、Td<d1 では通常目
標値SHO (=“5deg ”)、d1 <Td≦d2 の領域で
は通常目標値SHO より“2deg”低い値、d2 <Td≦d
3 の領域では通常目標値SHO より“4deg”低い値をそれ
ぞれ使用する。
By this opening operation, the superheat amount SH is kept constant at the target value SHO regardless of the change in the capacity of the compressor 1, and the refrigeration cycle is stabilized. As for the target value SHO, a normal value "5deg" is set in advance, and the normal value is appropriately corrected according to the detected temperature Td of the temperature sensor 11.
For example, as shown in FIG. 2, set values d 1 , d 2 , d 3
(D 1 <d 2 <d 3 ) is prepared, and when Td <d 1 , the normal target value SHO (= “5deg”), and in the region of d 1 <Td ≦ d 2 , the value is “2deg” lower than the normal target value SHO. , D 2 <Td ≦ d
In the area of 3 , usually use a value that is “4deg” lower than the target value SHO.

【0038】冷凍サイクルが過熱状態となって圧縮機1
の吐出冷媒温度Tdが上昇した場合には、目標値SHO を
先ずは通常より“2deg”低い“3deg”に下げることにな
る。目標値SHO が下がると、それにスーパヒート量制御
が追従して電動膨張弁4の開度が増大方向に変化する。
この開度増により、圧縮機1に液バック気味に冷媒を戻
し、冷凍サイクルの過熱を抑制する。
The refrigeration cycle becomes overheated and the compressor 1
When the discharge refrigerant temperature Td of No. 1 increases, the target value SHO is first lowered to "3deg" which is "2deg" lower than usual. When the target value SHO decreases, the superheat amount control follows it and the opening degree of the electric expansion valve 4 changes in the increasing direction.
With this increase in the opening degree, the refrigerant is returned to the compressor 1 in a liquid backed manner, and overheating of the refrigeration cycle is suppressed.

【0039】これでも吐出冷媒温度Tdの上昇が続く場
合には、目標値SHO をさらに“2deg”低い“1deg”に下
げる。これにより、電動膨張弁4の開度がさらに増大方
向に変化し、過熱に対する抑制効果がさらに高まる。
If the discharge refrigerant temperature Td continues to rise, the target value SHO is further lowered by "2deg" to "1deg". As a result, the opening degree of the electric expansion valve 4 further changes in the increasing direction, and the effect of suppressing overheating is further enhanced.

【0040】このように、吐出冷媒温度Tdが高くなる
ほど目標値SHO を低下方向に補正していくことにより、
冷凍サイクルの過熱状態を十分に抑制することができ、
圧縮機1の寿命向上が図れる。圧縮機1の運転周波数F
については空調負荷に応じた制御を継続しており、よっ
て本来の冷房または暖房が続いて快適性が損なわれな
い。
As described above, the target value SHO is corrected toward the lower side as the discharge refrigerant temperature Td becomes higher,
Can sufficiently suppress the overheated state of the refrigeration cycle,
The life of the compressor 1 can be improved. Operating frequency F of compressor 1
With respect to the above, the control according to the air conditioning load is continued, so that the original cooling or heating does not continue and the comfort is not impaired.

【0041】ところで、目標値SHO を補正したにもかか
わらず、過熱を抑制できずに吐出冷媒温度Tdの上昇が
続くことがある。吐出冷媒温度Tdが設定値d3 を超え
た場合、スーパヒート量制御に優先する形で吐出温度制
御を実行する。すなわち、吐出温度制御では、電動膨張
弁4の開度をさらに増して圧縮機1に液バック気味に冷
媒を戻し、検知温度Tdのそれ以上の上昇を確実に抑え
て過熱を解消する。
By the way, although the target value SHO is corrected, overheating may not be suppressed and the discharge refrigerant temperature Td may continue to rise. When the discharge refrigerant temperature Td exceeds the set value d 3 , the discharge temperature control is executed in the form of giving priority to the superheat amount control. That is, in the discharge temperature control, the opening degree of the electric expansion valve 4 is further increased to return the refrigerant to the compressor 1 in a liquid backed manner, and further increase in the detected temperature Td is reliably suppressed to eliminate overheating.

【0042】この吐出温度制御への移行に当たっては、
前段としてスーパヒート量制御による段階的な開度増が
継続する状態となるので、ムーズな移行が可能であり、
移行時に吐出冷媒温度Tdが大きくオーバーシュートす
るなどの不具合が未然に防止される。これは、冷凍サイ
クルの安定に大きく貢献する。
In shifting to the discharge temperature control,
As a former stage, the gradual opening increase by superheat amount control will continue, so a smooth transition is possible,
Problems such as a large overshoot of the discharged refrigerant temperature Td during the transition can be prevented. This greatly contributes to the stability of the refrigeration cycle.

【0043】[第1変形例]上記実施例では、スーパヒ
ート量制御の目標値SHO を吐出冷媒温度Tdに応じて補
正したが、吐出冷媒温度Tdおよび圧縮機1の運転周波
数Fに応じて補正してもよい。
[First Modification] In the above embodiment, the target value SHO for superheat amount control is corrected according to the discharge refrigerant temperature Td, but it is corrected according to the discharge refrigerant temperature Td and the operating frequency F of the compressor 1. May be.

【0044】この場合、運転周波数Fを設定するための
周波数指令値に対応して通常目標値SHO を図3に示すよ
うに割り当てている。たとえば、許容最低運転周波数F
minの周波数指令値“S3”に対し、通常目標値SHO =10d
eg 。中程度の周波数指令値“S8”に対し、通常目標値S
HO =5deg 。許容最高運転周波数Fmax の周波数指令
値“SF”に対し、通常目標値SHO =3deg を割り当てて
いる。
In this case, the normal target value SHO is assigned as shown in FIG. 3 corresponding to the frequency command value for setting the operating frequency F. For example, the minimum allowable operating frequency F
Normal target value SHO = 10d for the frequency command value "S3" of min
eg. Normal target value S for medium frequency command value "S8"
HO = 5deg. The normal target value SHO = 3deg is assigned to the frequency command value "SF" of the maximum allowable operating frequency Fmax.

【0045】運転周波数Fが高いところでは冷凍サイク
ルが過熱し易い状況にあることを考慮し、運転周波数F
が高いところで通常目標値SHO を下げておく補正を加
え、予め過熱し難い状況を作るようにしている。これに
より、検知温度Tdの上昇が少なくなって検知温度Td
に応じた目標値補正(つまり電動膨張弁4の開度増)の
機会が減り、制御のふらつきが解消されて冷凍サイクル
が安定する。
Considering that the refrigeration cycle is likely to overheat at a high operating frequency F, the operating frequency F
When the temperature is high, the target value SHO is usually lowered so that it is difficult to overheat in advance. As a result, the rise in the detected temperature Td is reduced and the detected temperature Td
The chance of target value correction (that is, increase in the opening degree of the electric expansion valve 4) according to is reduced, the control fluctuation is eliminated, and the refrigeration cycle is stabilized.

【0046】なお、冷房運転で冷媒の循環量が少ない場
合、外気温度の影響で圧縮機1の吸込冷媒温度Tsが大
きく上昇すると、検出スーパヒート量SHが実際よりも大
きい方に変化して電動膨張弁4の開度が不要にも増大方
向に制御されることがある。この状態が継続すると、冷
凍サイクルが液バック気味のまま安定してしまう心配が
ある。ただし、低循環量時、つまり運転周波数Fが低い
場合は、上記のように通常目標値SHO が高く設定される
ことで電動膨張弁4の開度が予め縮小された状態にある
ので、たとえ検出スーパヒート量SHが実際よりも大きい
方に変化して電動膨張弁4の開度が増大方向に制御され
ても、電動膨張弁4の開度はそれほど大きくならず、よ
って液バック気味の安定を回避できる。
When the refrigerant circulation amount is small in the cooling operation and the suction refrigerant temperature Ts of the compressor 1 is greatly increased due to the influence of the outside air temperature, the detected superheat amount SH changes to a larger value than the actual value and the electric expansion is performed. The opening of the valve 4 may be unnecessarily controlled in the increasing direction. If this state continues, there is a concern that the refrigeration cycle will be stable with a liquid back. However, when the circulation amount is low, that is, when the operating frequency F is low, the opening degree of the electric expansion valve 4 is reduced in advance by setting the normal target value SHO high as described above. Even if the superheat amount SH changes to a value larger than the actual value and the opening degree of the electric expansion valve 4 is controlled in the increasing direction, the opening degree of the electric expansion valve 4 does not increase so much, and thus the stability of the liquid back tendency is avoided. it can.

【0047】[第2変形例]スーパヒート量制御の目標
値SHO を、吐出冷媒温度Tdでなく、温度センサ16で
検知される圧縮機1のケース温度Tcaに応じて補正して
もよい。
[Second Modification] The target value SHO for superheat amount control may be corrected according to the case temperature Tca of the compressor 1 detected by the temperature sensor 16 instead of the discharge refrigerant temperature Td.

【0048】この場合、図4に示すように、ケース温度
Tcaに対して設定値40℃,50℃,60℃を用意し、Tca<
40℃では通常目標値SHO =5deg 、40℃<Tca≦50℃の
領域では通常目標値SHO より“2deg”低い値、50℃<T
ca≦60℃の領域では通常目標値SHO より“4deg”低い値
をそれぞれ使用する。
In this case, as shown in FIG. 4, set values of 40 ° C., 50 ° C. and 60 ° C. are prepared for the case temperature Tca, and Tca <
At 40 ℃, the normal target value SHO = 5deg, and in the range of 40 ℃ <Tca ≤ 50 ℃, "2deg" lower than the normal target value SHO, 50 ℃ <T
In the region of ca ≤ 60 ° C, use a value that is "4deg" lower than the target value SHO.

【0049】このように、吐出冷媒温度Tdに代えてケ
ース温度Tcaを用いることにより、圧縮機1の過熱を直
接的に捕らえた圧縮機保護優先の制御となる。 [第3変形例]スーパヒート量制御の目標値SHO を、吐
出冷媒温度Tdおよびケース温度Tcaの両方に応じて補
正してもよい。
As described above, by using the case temperature Tca instead of the discharge refrigerant temperature Td, the compressor protection priority control by directly catching the overheat of the compressor 1 is performed. [Third Modification] The target value SHO for superheat amount control may be corrected according to both the discharge refrigerant temperature Td and the case temperature Tca.

【0050】この場合、吐出冷媒温度Tdが上昇すれば
その吐出冷媒温度Tdに応じた制御に入り、圧縮機1が
過熱してケース温度Tcaが上昇すればそのケース温度T
caに応じた制御に入る。
In this case, if the discharge refrigerant temperature Td rises, control is started according to the discharge refrigerant temperature Td. If the compressor 1 overheats and the case temperature Tca rises, the case temperature Td increases.
Enter control according to ca.

【0051】[第4変形例]上記実施例では、バイパス
6の出口側冷媒温度(温度センサ15の検知温度)Tu
を冷媒の疑似飽和温度として選択し、それと吸込冷媒温
度(温度センサ14の検知温度)Tsとからスーパヒー
ト量SHを検出したが、室外熱交換器3の近傍の着霜検知
用の温度センサ12の検知温度Teおよび出口側冷媒温
度Tuのいずれか一方を冷媒の疑似飽和温度として選択
し、それと吸込冷媒温度Tsとを用いてスーパヒート量
SHを検出するようにしてもよい。
[Fourth Modification] In the above embodiment, the refrigerant temperature on the outlet side of the bypass 6 (the temperature detected by the temperature sensor 15) Tu.
Was selected as the pseudo saturation temperature of the refrigerant, and the superheat amount SH was detected from it and the suction refrigerant temperature (detection temperature of the temperature sensor 14) Ts, but the temperature sensor 12 for detecting frost near the outdoor heat exchanger 3 was detected. Either one of the detected temperature Te and the outlet side refrigerant temperature Tu is selected as the pseudo saturation temperature of the refrigerant, and by using it and the suction refrigerant temperature Ts, the superheat amount
SH may be detected.

【0052】冷房時は、バイパス6におけるキャピラリ
チューブ7の両端で圧力損失が大きくなり、バイパス6
に冷媒が流れる。その結果、出口側冷媒温度Tuを疑似
飽和温度として有効に利用することができる。
During cooling, the pressure loss becomes large at both ends of the capillary tube 7 in the bypass 6 and the bypass 6
Refrigerant flows into. As a result, the outlet side refrigerant temperature Tu can be effectively used as the pseudo saturation temperature.

【0053】ただし、暖房時は、バイパス6におけるキ
ャピラリチューブ7の両端で圧力差が小さく、このため
バイパス6を冷媒が流れにくくなり、出口側冷媒温度T
uを疑似飽和温度として利用することには無理がある。
適切なスーパヒート量SHを検出できない。
However, at the time of heating, the pressure difference between both ends of the capillary tube 7 in the bypass 6 is small, so that it becomes difficult for the refrigerant to flow through the bypass 6 and the outlet side refrigerant temperature T
It is unreasonable to use u as the pseudo saturation temperature.
The appropriate superheat amount SH cannot be detected.

【0054】そこで、冷房時は検知温度Tuを疑似飽和
温度として用い、暖房時は温度センサ12の検知温度
(室外熱交換器3に流入する冷媒の温度)Teを疑似飽
和温度として用いることが考えられる。
Therefore, it is considered that the detected temperature Tu is used as the pseudo saturation temperature during cooling, and the temperature detected by the temperature sensor 12 (the temperature of the refrigerant flowing into the outdoor heat exchanger 3) Te is used as the pseudo saturation temperature during heating. To be

【0055】しかしながら、暖房時の検知温度Teは実
際の飽和温度より高い値を示すため、その検知温度Te
を疑似飽和温度として用いたのでは、スーパヒート量SH
の検出に誤差が生じ、電動膨張弁4の開度が絞られ過ぎ
て過熱気味のサイクルとなる心配がある。
However, since the detected temperature Te during heating shows a value higher than the actual saturation temperature, the detected temperature Te
Is used as the pseudo saturation temperature, the superheat amount SH
There is a concern that an error may occur in the detection of the above condition, and the opening degree of the electric expansion valve 4 may be excessively narrowed, resulting in a cycle of overheating.

【0056】対策として、図5に示すように、圧縮機1
の運転周波数Fが50Hz未満の低いところでは検知温度T
eを疑似飽和温度として選択する。圧縮機1の運転周波
数Fが50Hz以上の高いところでは検知温度Tuを疑似飽
和温度として選択するのである。
As a countermeasure, as shown in FIG. 5, the compressor 1
Temperature T is lower than 50Hz, detection temperature T
Select e as the pseudo saturation temperature. When the operating frequency F of the compressor 1 is 50 Hz or higher, the detected temperature Tu is selected as the pseudo saturation temperature.

【0057】暖房時の室外熱交換器3における圧力損失
特性を図6に示している。Tjは室外熱交換器3の蒸発
温度であって実際の飽和温度に相当し、温度差“Te−
Tj”が室外熱交換器3における圧力損失に対応する。
運転周波数Fの上昇、つまり冷媒循環流量の増大に伴
い、温度差“Te−Tj”が大きくなっている。
FIG. 6 shows the pressure loss characteristics of the outdoor heat exchanger 3 during heating. Tj is the evaporation temperature of the outdoor heat exchanger 3 and corresponds to the actual saturation temperature, and the temperature difference "Te-
Tj ″ corresponds to the pressure loss in the outdoor heat exchanger 3.
The temperature difference "Te-Tj" increases as the operating frequency F increases, that is, the refrigerant circulation flow rate increases.

【0058】図6の特性から明らかなように、暖房時で
も、運転周波数Fが低い場合は検知温度Teと実際の飽
和温度(=蒸発温度Tj)との差が小さく、よって検知
温度Teを疑似飽和温度として用いてもスーパヒート量
SHを適切に検出することが可能である。つまり、過熱気
味のサイクルになる心配がない。
As is clear from the characteristics of FIG. 6, even during heating, when the operating frequency F is low, the difference between the detected temperature Te and the actual saturation temperature (= evaporation temperature Tj) is small, so the detected temperature Te is simulated. Superheat amount even when used as saturation temperature
It is possible to detect SH appropriately. In other words, there is no risk of overheating.

【0059】さらに、図6の特性から判るのは、運転周
波数Fが高いところでは圧力損失が十分に大きくなり、
よって暖房時でもバイパス6に十分に冷媒が流れること
である。つまり、暖房時でも、運転周波数Fが高い側に
あれば、検知温度Tuを疑似飽和温度として用いること
により、スーパヒート量SHを適切に検出することができ
る。
Further, it can be seen from the characteristics of FIG. 6 that the pressure loss becomes sufficiently large at a high operating frequency F,
Therefore, the refrigerant sufficiently flows into the bypass 6 even during heating. That is, even during heating, if the operating frequency F is on the high side, the superheat amount SH can be appropriately detected by using the detected temperature Tu as the pseudo saturation temperature.

【0060】このように、暖房時でも、検知温度Tu,
Teのいずれか一方を選択し、それを疑似飽和温度とし
て用いてスーパヒート量SHを検出することにより、常に
適切なスーパヒート量SHを捕らえることができ、信頼性
の高いスーパヒート量制御が可能となる。
Thus, the detected temperature Tu,
By selecting one of Te and using it as the pseudo saturation temperature to detect the superheat amount SH, an appropriate superheat amount SH can always be captured, and reliable superheat amount control becomes possible.

【0061】[第5変形例]第4変形例では、検知温度
Te,Tuのいずれか一方を運転周波数Fに応じて選択
したが、図6の特性の温度差“Te−Tj”が温度差
(=Te−Tu)と相似の関係にあることに着目し、そ
の温度差(=Te−Tu)の大小に応じて検知温度T
e,Tuのいずれか一方を選択してもよい。
[Fifth Modification] In the fourth modification, one of the detected temperatures Te and Tu is selected according to the operating frequency F. However, the temperature difference "Te-Tj" of the characteristic shown in FIG. 6 is the temperature difference. Paying attention to the similar relationship with (= Te-Tu), the detected temperature T depends on the magnitude of the temperature difference (= Te-Tu).
Either e or Tu may be selected.

【0062】すなわち、[(Te−Tu)≧所定値K]
の条件が成立する場合(運転周波数Fが高めで冷媒循環
量が多い場合)、検知温度Teが実際の飽和温度より高
過ぎる状態にあって検知温度Teの使用は好ましくない
との判断の下に、一方の検知温度Tuを疑似飽和温度と
して選択し、スーパヒート量SHを検出する。もちろん、
暖房時でもバイパス6に十分に冷媒が流れる状況にあ
り、疑似飽和温度としての検知温度Tuの使用は十分に
可能である。
That is, [(Te-Tu) ≧ predetermined value K]
When the condition of is satisfied (when the operating frequency F is high and the refrigerant circulation amount is large), the detected temperature Te is too high than the actual saturation temperature, and it is judged that the use of the detected temperature Te is not preferable. One of the detected temperatures Tu is selected as the pseudo saturation temperature, and the superheat amount SH is detected. of course,
Even during heating, the refrigerant is sufficiently flowing into the bypass 6, and the detected temperature Tu as the pseudo saturation temperature can be used sufficiently.

【0063】所定値Kは、たとえば“1deg”である。上
記の条件が成立しないとき、つまり[(Te−Tu)<
所定値K]のとき、検知温度Teが実際の飽和温度に近
い状態にあって検知温度Teの使用が可能であるとの判
断の下に、検知温度Teを疑似飽和温度として選択して
スーパヒート量SHを検出する。
The predetermined value K is, for example, "1 deg". When the above conditions are not satisfied, that is, [(Te-Tu) <
When the detected temperature Te is close to the actual saturation temperature and the detected temperature Te can be used when the predetermined value K], the detected temperature Te is selected as the pseudo saturation temperature and the superheat amount is selected. Detect SH.

【0064】[第6変形例]第5変形例では、条件不成
立時つまり[(Te−Tu)<所定値K]のとき、検知
温度Teを疑似飽和温度として選択したが、実際の飽和
温度に近いのが検知温度Tuの方であるとすれば、温度
差(=Te−Tu)分だけスーパヒート量SHの検出に誤
差が生じることになる。この誤差はスーパヒート量制御
の段差となって現われる。
[Sixth Modification] In the fifth modification, the detected temperature Te is selected as the pseudo saturation temperature when the condition is not satisfied, that is, [(Te-Tu) <predetermined value K]. If the detected temperature Tu is closer, an error will occur in the detection of the superheat amount SH by the temperature difference (= Te-Tu). This error appears as a step in superheat amount control.

【0065】対策として、条件不成立時は、[Te−
(Te−Tu)2 /K]の演算を行ない、演算値を疑似
飽和温度としてスーパヒート量SHを検出する。これによ
り、条件成立時の検知温度Tuの選択に基づくスーパヒ
ート量制御と、条件不成立時の検知温度Teの選択に基
づくスーパヒート量制御との間に段差がなくなり、滑ら
かなスーパヒート量制御が可能となって冷凍サイクルの
安定性が向上する。
As a countermeasure, when the condition is not satisfied, [Te-
(Te−Tu) 2 / K] is calculated, and the calculated value is used as the pseudo saturation temperature to detect the superheat amount SH. Thereby, there is no step between the superheat amount control based on the selection of the detected temperature Tu when the condition is satisfied and the superheat amount control based on the selection of the detected temperature Te when the condition is not satisfied, and smooth superheat amount control is possible. The stability of the refrigeration cycle is improved.

【0066】なお、条件不成立時であっても、[Te<
Tu]の場合には、検知温度Teが実際の飽和温度に十
分に近い状態にあって、検出誤差の心配がないとの判断
の下に、上記演算値でなく、検知温度Teをそのまま疑
似飽和温度として選択する。演算がない分だけ処理時間
が早くなる。
Even when the condition is not satisfied, [Te <
In the case of [Tu], the detected temperature Te is sufficiently close to the actual saturation temperature, and if it is determined that there is no concern about detection error, the detected temperature Te is pseudo saturated as it is instead of the calculated value. Select as temperature. The processing time becomes faster because there is no calculation.

【0067】[一実施例における起動制御] (1)ところで、上記実施例では、圧縮機1の起動に際
し、スーパヒート量SHと目標値SHO に応じたスーパヒー
ト量制御に入る前に、電動膨張弁4の開度を所定の初期
開度PLS へと移行する起動制御を行なう。この起動制御
は、圧縮機1の起動時にスーパヒート量SHが一時的に大
きく増大する現象に対処したもので、スーパヒート量制
御へのスムーズな移行を目的としている。
[Startup Control in One Embodiment] (1) By the way, in the above embodiment, when the compressor 1 is started, the electric expansion valve 4 is operated before the superheat amount control corresponding to the superheat amount SH and the target value SHO. The startup control is performed to shift the opening of to a predetermined initial opening PLS. This start-up control deals with the phenomenon that the superheat amount SH temporarily increases greatly when the compressor 1 is started, and is aimed at a smooth transition to the superheat amount control.

【0068】すなわち、スーパヒート量SHの変化をSH曲
線として図7に示しており、その変化に対処するべく、
電動膨張弁4の開度を、先ず起動開度αに設定してその
状態を保持し(少なくともm分間たとえば 2分間)、ス
ーパヒート量SHが設定値SH1まで低下したところで起動
開度αから初期開度PLS へと絞っていく。電動膨張弁4
の開度が初期開度PLS に達したら、スーパヒート量制御
に移行する。
That is, the change in the superheat amount SH is shown in FIG. 7 as an SH curve, and in order to cope with the change,
First, the opening degree of the electric expansion valve 4 is set to the starting opening α, and the state is maintained (at least m minutes, for example, 2 minutes). When the superheat amount SH drops to the set value SH 1 , the starting opening α is initially set. Open to PLS. Electric expansion valve 4
When the opening of reaches the initial opening PLS, it shifts to superheat amount control.

【0069】起動開度αは、圧縮機1の運転周波数Fに
対応する基本開度より大きく、たとえば駆動パルス数 3
80発に相当する開度である。初期開度PLS は、とりあえ
ず定める値であり、たとえば駆動パルス数 180発に相当
する。基本開度は、たとえば駆動パルス数 150発に相当
する。設定値SH1 は“3deg”である。
The starting opening α is larger than the basic opening corresponding to the operating frequency F of the compressor 1, and for example, the driving pulse number 3
The opening is equivalent to 80 shots. The initial opening PLS is a value determined for the time being and corresponds to, for example, 180 drive pulses. The basic opening corresponds to, for example, 150 driving pulses. The setting value SH 1 is “3deg”.

【0070】起動後、スーパヒート量SHが設定値SH1
至るまでの経過時間nをカウントしており、その経過時
間nに応じた量だけ初期開度PLS を開方向に補正する。
SH曲線Aの場合、起動からスーパヒート量SHが設定値SH
1 に至るまでの経過時間nが 2分であり、初期開度PLS
の補正値 PLSn としてそのまま初期開度PLS を設定す
る。SH曲線Bの場合、起動からスーパヒート量SHが設定
値SH1 に至るまでの経過時間nが約 4分半であり、初期
開度PLS の補正値 PLSn として PLSb を設定している。
After the start-up, the elapsed time n until the superheat amount SH reaches the set value SH 1 is counted, and the initial opening PLS is corrected in the opening direction by an amount corresponding to the elapsed time n.
In the case of SH curve A, the superheat amount SH from the start is the set value SH
The elapsed time n to reach 1 is 2 minutes, and the initial opening PLS
Set the initial opening PLS as is as the correction value PLS n . In the case of the SH curve B, the elapsed time n from the start-up until the superheat amount SH reaches the set value SH 1 is about 4 minutes and a half, and PLS b is set as the correction value PLS n for the initial opening PLS.

【0071】SH曲線Cの場合、起動からスーパヒート量
SHが設定値SH1 に至るまでの経過時間nが約 7分半であ
り、初期開度PLS の補正値 PLSn として PLSb より大き
いPLSc を設定する。SH曲線Dの場合は、起動からスー
パヒート量SHが設定値SH1に至るまでの経過時間nが約1
0分であり、初期開度PLS の補正値 PLSn としてPLSc
り大きい PLSd を設定する。SH曲線Eの例では、スーパ
ヒート量SHが設定値SH1 に至ることなく起動から上限値
の12分が経過しており、初期開度PLS の補正値 PLSn
して起動開度αを設定する。
In the case of SH curve C, the amount of superheat from the start
SH is the elapsed time n is about 7 minutes and a half up to the set value SH 1, sets the PLS b greater PLS c as the correction value PLS n of initial opening PLS. In the case of SH curve D, the elapsed time n from startup to when the superheat amount SH reaches the set value SH 1 is about 1
0 minutes, it sets the PLS c greater PLS d as a correction value PLS n of initial opening PLS. In the example of the SH curve E, the superheat amount SH does not reach the set value SH 1 and the upper limit value of 12 minutes has elapsed from the startup, and the startup opening α is set as the correction value PLS n of the initial opening PLS.

【0072】補正後の初期開度 PLSn は、下式の演算に
より求める。 PLSn =PLS +(α−PLS )/(12分−m)・(n−
m) スーパヒート量SHが増大してから下がり切るまでの経過
時間が長いということは、冷凍サイクルが過熱気味の状
態にあるということで、スーパヒート量制御に入ってす
ぐに過熱気味が解消されるよう、初期開度PLS を予め大
きく設定するのである。実際にスーパヒート量制御に入
ったとき、電動膨張弁4に対する開度の操作量は少なく
てすみ、冷凍サイクルを早期に安定させることができ
る。
The corrected initial opening PLS n is calculated by the following equation. PLS n = PLS + (α-PLS) / (12 min-m) ・ (n-
m) The long elapsed time from when the superheat amount SH increases to when it completely falls means that the refrigeration cycle is in a state of overheating, so it seems that overheating will be eliminated immediately after entering the superheat amount control. , The initial opening PLS is set large in advance. When actually entering the superheat amount control, the operation amount of the opening degree to the electric expansion valve 4 can be small and the refrigeration cycle can be stabilized early.

【0073】スーパヒート量SHが増大してから下がり切
るまでの経過時間を決定する要因として、電動膨張弁4
の開度だけでなく、配管長、冷媒封入量、運転停止時間
(冷媒寝込み量に対応)などがあり、これら要因を吸収
しつつ常に安定した運転状態を確保することができる。
The electric expansion valve 4 is a factor that determines the elapsed time from when the superheat amount SH increases to when it completely falls.
In addition to the opening degree, there are a pipe length, a refrigerant filling amount, an operation stop time (corresponding to the refrigerant stagnation amount), and the like, and it is possible to always maintain a stable operating state while absorbing these factors.

【0074】スーパヒート量SHが設定値SH1 まで低下し
ないまま上限値の12分が経過するSH曲線Eの例では、起
動開度αの保持を解除して直ちにスーパヒート量制御へ
移行する。
In the example of the SH curve E in which the upper limit value of 12 minutes elapses without the superheat amount SH decreasing to the set value SH 1 , the holding of the starting opening α is released and the control immediately shifts to the superheat amount control.

【0075】(2)電動膨張弁4の開度を起動開度αか
ら初期開度補正値 PLSn へ絞る過程では、絞りを所定値
(たとえば15パルス/毎秒)ずつ徐々に進める。これに
より、スーパヒート量SHをオーバーシュートなく初期開
度補正値 PLSn へ到達させることができ、スーパヒート
量制御へのスムーズな移行が可能である。
(2) In the process of narrowing the opening of the electric expansion valve 4 from the starting opening α to the initial opening correction value PLS n , the opening is gradually advanced by a predetermined value (for example, 15 pulses / second). As a result, the superheat amount SH can reach the initial opening correction value PLS n without overshooting, and a smooth transition to the superheat amount control is possible.

【0076】[起動制御の変形例] (1)圧縮機1の起動時、図8に示すように、電動膨張
弁4の開度を、先ずはスーパヒート量SHが設定値SH1
超えて設定値SH2 (>SH1 )に至るまで圧縮機1の運転
周波数に対応する基本開度に設定し、スーパヒート量SH
が設定値SH2 を超えたら基本開度より大きい起動開度α
まで増大してその状態を保持し、スーパヒート量SHが設
定値SH1 まで低下したところで起動開度αから初期開度
PLS へと絞っていく。設定値SH2 は“4deg”である。
[Modification of Startup Control] (1) When the compressor 1 is started, as shown in FIG. 8, the opening degree of the electric expansion valve 4 is first set so that the superheat amount SH exceeds the set value SH 1. Set the basic opening corresponding to the operating frequency of the compressor 1 up to the value SH 2 (> SH 1 ) and set the superheat amount SH
Is greater than the set value SH 2 , the starting opening α that is larger than the basic opening α
To the initial value when the superheat amount SH drops to the set value SH 1
Focus on PLS. The setting value SH 2 is “4deg”.

【0077】そして、起動後、スーパヒート量SHが設定
値SH1 に至るまでの経過時間をカウントし、経過時間に
応じた量だけ初期開度PLS を開方向に補正する。スーパ
ヒート量SHが設定値SH2 を超えるかどうかは、その後の
スーパヒート量SHが上昇を続けるかどうかの判断基準と
なる。すなわち、スーパヒート量SHが設定値SH2 を超え
た場合には、スーパヒート量SHがさらに上昇を続けると
の予測の下に、そこで初めて、開度を起動開度αまで増
大するのである。
After the start, the elapsed time until the superheat amount SH reaches the set value SH 1 is counted, and the initial opening PLS is corrected in the opening direction by an amount according to the elapsed time. Whether or not the superheat amount SH exceeds the set value SH 2 is a criterion for determining whether or not the subsequent superheat amount SH continues to rise. That is, when the superheat amount SH exceeds the set value SH 2 , the opening degree is increased to the starting opening α for the first time under the prediction that the superheat amount SH continues to further increase.

【0078】図7に示した制御では、起動と同時に電動
膨張弁4の開度を起動開度αに設定するが、状況によっ
ては液バック気味のサイクルとなってそれが継続してし
まう心配がある。
In the control shown in FIG. 7, the opening degree of the electric expansion valve 4 is set to the starting opening degree α at the same time as the start-up. However, depending on the situation, there is a concern that the cycle becomes liquid back-like and that it continues. is there.

【0079】そこで、スーパヒート量SHの上昇が続くと
予測される場合のみ、電動膨張弁4の開度を起動開度α
まで増大するようにしている。これにより、液バックを
回避することができ、圧縮機1の寿命向上が図れる。
Therefore, only when it is predicted that the superheat amount SH continues to increase, the opening degree of the electric expansion valve 4 is set to the starting opening degree α.
I am trying to increase. Thereby, liquid back can be avoided and the life of the compressor 1 can be improved.

【0080】なお、電動膨張弁4の開度を起動開度αか
ら初期開度補正値 PLSn へと徐々に絞る過程を図9に示
している。 (2)電動膨張弁4の開度を起動開度αから初期開度補
正値 PLSn へ徐々に絞る過程で、図9に示すように、ス
ーパヒート量SHが設定値SH3 (>SH2 )まで下降した場
合には、その時点で開度の絞りを終了し、スーパヒート
量制御へ移る。設定値SH2 は“5deg”である。
FIG. 9 shows a process in which the opening degree of the electric expansion valve 4 is gradually reduced from the starting opening degree α to the initial opening degree correction value PLS n . (2) In the process of gradually narrowing the opening of the electric expansion valve 4 from the starting opening α to the initial opening correction value PLS n , as shown in FIG. 9, the superheat amount SH is set to a set value SH 3 (> SH 2 ). When the temperature is lowered to, the throttle of the opening is finished at that point, and the superheat amount control is started. The set value SH 2 is “5deg”.

【0081】スーパヒート量SHが設定値SH3 (>SH2
まで下降したかどうかは、スーパヒート量制御に移行し
たときの開度が絞り過ぎの状態となるかどうかの判断基
準となる。すなわち、スーパヒート量SHが設定値SH3
(>SH2 )まで下降した場合には、スーパヒート量制御
に移行したときの開度が絞り過ぎの状態となって冷媒流
量不足を生じるとの予測の下に、そこで絞りを終了して
スーパヒート量へ移るのである。
The superheat amount SH is the set value SH 3 (> SH 2 )
Whether or not it has fallen to is a criterion for determining whether or not the degree of opening at the time of shifting to the superheat amount control becomes too narrow. That is, the superheat amount SH is the set value SH 3
If it is lowered to (> SH 2 ), the throttle will be stopped and the superheat amount will be terminated with the prediction that the opening will be too narrow when the control shifts to superheat amount control, resulting in insufficient refrigerant flow. To move to.

【0082】(3)起動制御に際し、温度センサ11の
検知温度(圧縮機1の吐出冷媒温度)Tdが所定値以上
に上昇したとき、起動に伴う初期開度補正値 PLSn への
移行制御を終了し、検知温度Tdの上昇を抑えるための
吐出温度制御に移る。
(3) When the temperature detected by the temperature sensor 11 (the temperature of the refrigerant discharged from the compressor 1) Td rises above a predetermined value during the startup control, the transition control to the initial opening correction value PLS n associated with the startup is performed. After that, the discharge temperature control for suppressing the increase of the detection temperature Td is started.

【0083】すなわち、冷媒吐出温度Tdの異常上昇を
優先的に抑えて過熱を防ぐようにしている。 (4)スーパヒート量SHが設定値SH1 まで低下しないま
ま上限値の12分が経過した場合には、起動開度αの保持
を解除して直ちにスーパヒート量制御へ移行する。この
例を図10に示している。
That is, the abnormal rise in the refrigerant discharge temperature Td is preferentially suppressed to prevent overheating. (4) When the upper limit value of 12 minutes elapses without the superheat amount SH decreasing to the set value SH 1 , the holding of the starting opening α is released and the process immediately shifts to the superheat amount control. This example is shown in FIG.

【0084】(5)起動制御中(つまり12分内)に圧縮
機1が室内温度制御に基づいて運転中断いわゆるサーモ
オフすると、その圧縮機1の運転再開いわゆるサーモオ
ンに伴い当該起動制御(初期開度補正値 PLSn への移行
制御)を再開する。この再開時、起動開度αを前回の起
動制御時よりも小さい値に補正する。
(5) When the operation of the compressor 1 is interrupted during the start control (that is, within 12 minutes) based on the indoor temperature control, that is, when the thermostat is turned off, the start control (initial opening degree) is performed when the operation of the compressor 1 is restarted, that is, the thermostat is turned on. Restart control of shift to correction value PLS n ). At the time of this restart, the starting opening α is corrected to a value smaller than that at the previous starting control.

【0085】起動開度αの補正は、短時間のうちに運転
が断続されることに起因する液バック量の低減を図り、
圧縮機1を保護するためのものである。 (6)起動制御中(つまり12分内)に圧縮機1が室内温
度制御に基づいて運転中断いわゆるサーモオフすると、
その圧縮機1の運転再開いわゆるサーモオンに伴い当該
起動制御(初期開度補正値 PLSn への移行制御)を再開
する。この再開時、設定値SH2 を前回の起動制御時より
も大きな値に補正する。
The correction of the starting opening α aims to reduce the liquid back amount due to the intermittent operation in a short time,
It is for protecting the compressor 1. (6) During start-up control (that is, within 12 minutes), when the compressor 1 stops operation based on indoor temperature control, so-called thermo-off,
The operation control of the compressor 1 is restarted, so that the start-up control (control to shift to the initial opening correction value PLS n ) is restarted with the so-called thermo-on. At this restart, the set value SH 2 is corrected to a value larger than that at the previous startup control.

【0086】設定値SH2 の補正は、再起動時の開度が起
動開度αよりも小さい開度に保持される時間を長くする
ためのものであり、(4)と同じく、液バック量の低減
を図って圧縮機1を保護する効果がある。なお、この発
明は上記実施例に限定されるものではなく、要旨を変え
ない範囲で種々変形実施可能である。
The correction of the set value SH 2 is for prolonging the time during which the opening degree at the time of restart is kept smaller than the starting opening degree α. Has the effect of protecting the compressor 1 by reducing The present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the scope of the invention.

【0087】[0087]

【発明の効果】以上述べたようにこの発明によれば、第
1ないし第4の発明の空気調和機は、圧縮機の吐出冷媒
温度に応じてスーパヒート量制御の目標値SHO を補正す
るようにしたので、快適性を損なうことなく、圧縮機の
過熱を防止して圧縮機の寿命向上が図れる。
As described above, according to the present invention, the air conditioner of the first to fourth inventions corrects the target value SHO of the superheat amount control according to the refrigerant temperature discharged from the compressor. Therefore, overheating of the compressor can be prevented and the life of the compressor can be improved without impairing comfort.

【0088】第5ないし第7の発明の空気調和機は、疑
似飽和温度を適切に捕らえるようにしたので、快適性を
損なうことなく、圧縮機の過熱を防止して圧縮機の寿命
向上が図れるとともに、冷房と暖房の別にかかわらずス
ーパヒート量SHを適確に検出してスーパヒート量制御の
信頼性向上が図れる。
In the air conditioner of the fifth to seventh inventions, since the pseudo saturation temperature is properly captured, overheating of the compressor can be prevented and the life of the compressor can be improved without impairing comfort. At the same time, the superheat amount SH can be accurately detected regardless of whether it is cooling or heating, and the reliability of the superheat amount control can be improved.

【0089】第8ないし第16の発明の空気調和機は、
電動膨張弁の初期開度を冷凍サイクルの状態に応じて補
正するようにしたので、圧縮機の起動時の過熱や液バッ
クを防ぎつつスーパヒート量制御への安定かつスムーズ
な移行が可能である。
The air conditioners of the eighth to sixteenth inventions are:
Since the initial opening of the electric expansion valve is corrected according to the state of the refrigeration cycle, stable and smooth transition to superheat amount control is possible while preventing overheating and liquid back at the time of starting the compressor.

【図面の簡単な説明】[Brief description of drawings]

【図1】この発明の一実施例の全体的な構成を示す図。FIG. 1 is a diagram showing the overall configuration of an embodiment of the present invention.

【図2】同実施例の吐出冷媒温度Tdに応じた目標値SH
O の補正条件を示す図。
FIG. 2 is a target value SH according to a discharge refrigerant temperature Td of the embodiment.
The figure which shows the correction conditions of O.

【図3】同実施例の第1変形例における周波数指令値と
通常目標値SHO との対応を示す図。
FIG. 3 is a diagram showing a correspondence between a frequency command value and a normal target value SHO in a first modified example of the same embodiment.

【図4】同実施例の第2変形例におけるケース温度Tca
に応じた目標値SHO の補正条件を示す図。
FIG. 4 is a case temperature Tca in a second modification of the embodiment.
The figure which shows the correction conditions of the target value SHO according to.

【図5】同実施例の第4変形例における運転周波数Fに
応じたスーパヒート量検出を説明するための図。
FIG. 5 is a diagram for explaining superheat amount detection according to an operating frequency F in a fourth modified example of the same embodiment.

【図6】同実施例の第4変形例における暖房時の室外熱
交換器における圧力損失特性を示す図。
FIG. 6 is a diagram showing a pressure loss characteristic of the outdoor heat exchanger during heating in the fourth modification of the embodiment.

【図7】同実施例におけるの起動制御時のスーパヒート
量変化を示す図。
FIG. 7 is a diagram showing a change in superheat amount during start-up control in the same embodiment.

【図8】同実施例の起動制御の変形例におけるスーパヒ
ート量SHの変化を示す図。
FIG. 8 is a diagram showing changes in the superheat amount SH in a modification of the startup control of the same embodiment.

【図9】同実施例の起動制御の変形例におけるスーパヒ
ート量SHの変化の別の例を示す図。
FIG. 9 is a diagram showing another example of changes in the superheat amount SH in a modification of the startup control of the same embodiment.

【図10】同実施例の起動制御の変形例におけるスーパ
ヒート量SHの変化のさらに別の例を示す図。
FIG. 10 is a diagram showing yet another example of changes in the superheat amount SH in a modification of the startup control of the same embodiment.

【符号の説明】[Explanation of symbols]

1…圧縮機、2…四方弁、3…室外熱交換器、4…電動
膨張弁、5…室内熱交換器、6…バイパス、7…キャピ
ラリチューブ(絞り装置)、11,12,14,15…
温度センサ、13…室内温度センサ、21…インバータ
回路、30…制御部。
DESCRIPTION OF SYMBOLS 1 ... Compressor, 2 ... Four-way valve, 3 ... Outdoor heat exchanger, 4 ... Electric expansion valve, 5 ... Indoor heat exchanger, 6 ... Bypass, 7 ... Capillary tube (throttle device), 11, 12, 14, 15 …
Temperature sensor, 13 ... Indoor temperature sensor, 21 ... Inverter circuit, 30 ... Control section.

Claims (16)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 圧縮機、凝縮器、電動膨張弁、蒸発器を
順次接続した冷凍サイクルを備え、冷媒のスーパヒート
量SHが目標値SHO一定となるよう電動膨張弁の開度を制
御する空気調和機において、 前記圧縮機の吐出冷媒温度Tdを検知する検知手段と、
この検知手段の検知温度Tdが高くなるほど検知温度T
dに応じて前記目標値 SHO を低下方向に段階的に補正す
る補正手段と、を備えたことを特徴とする空気調和機。
1. An air conditioner that comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and controls the opening of the electric expansion valve so that the superheat amount SH of the refrigerant becomes a target value SHO constant. A detector for detecting a refrigerant discharge temperature Td of the compressor,
The higher the detection temperature Td of the detection means, the higher the detection temperature T
An air conditioner comprising: a correction unit that gradually corrects the target value SHO in a decreasing direction according to d .
【請求項2】 能力可変の圧縮機、凝縮器、電動膨張
弁、蒸発器を順次接続した冷凍サイクルを備え、冷媒の
スーパヒート量SHが目標値SHO 一定となるよう電動膨張
弁の開度を制御する空気調和機において、 前記圧縮機の吐出冷媒温度Tdを検知する検知手段と、
この検知手段の検知温度Tdおよび前記圧縮機の運転周
波数Fに応じて前記目標値SHO を補正する補正手段と、
を備えたことを特徴とする空気調和機。
2. A refrigeration cycle in which a variable capacity compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the opening of the electric expansion valve is controlled so that the superheat amount SH of the refrigerant becomes a target value SHO. In the air conditioner, detecting means for detecting the refrigerant discharge temperature Td of the compressor,
Correction means for correcting the target value SHO according to the detected temperature Td of the detection means and the operating frequency F of the compressor;
An air conditioner characterized by having.
【請求項3】 圧縮機、凝縮器、電動膨張弁、蒸発器を
順次接続した冷凍サイクルを備え、冷媒のスーパヒート
量SHが目標値SHO 一定となるよう電動膨張弁の開度を制
御する空気調和機において、 前記圧縮機のケース温度Tcaを検知する検知手段と、こ
の検知手段の検知温度Tcaに応じて前記目標値SHO を補
正する補正手段と、を備えたことを特徴とする空気調和
機。
3. An air conditioner that comprises a refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and controls the opening of the electric expansion valve so that the superheat amount SH of the refrigerant becomes a target value SHO. An air conditioner, comprising: a detector that detects a case temperature Tca of the compressor; and a corrector that corrects the target value SHO according to the detected temperature Tca of the detector.
【請求項4】 圧縮機、凝縮器、電動膨張弁、蒸発器を
順次接続した冷凍サイクルを備え、冷媒のスーパヒート
量SHが目標値SHO 一定となるよう電動膨張弁の開度を制
御する空気調和機において、 前記圧縮機の吐出冷媒温度Tdを検知する検知手段と、
前記圧縮機のケース温度Tcaを検知する検知手段と、こ
れら検知手段の検知温度Td,Tcaに応じて前記目標値
SHO を補正する補正手段と、を備えたことを特徴とする
空気調和機。
4. An air conditioner comprising a refrigeration cycle in which a compressor, a condenser, an electric expansion valve and an evaporator are sequentially connected, and which controls the opening of the electric expansion valve so that the superheat amount SH of the refrigerant becomes a target value SHO. A detector for detecting a refrigerant discharge temperature Td of the compressor,
Detecting means for detecting the case temperature Tca of the compressor, and the target value according to the detected temperatures Td, Tca of these detecting means.
An air conditioner characterized by comprising a correction means for correcting SHO.
【請求項5】 圧縮機、四方弁、室外熱交換器、電動膨
張弁、室内熱交換器を順次接続したヒートポンプ式冷凍
サイクルを備え、冷媒のスーパヒート量SHが目標値SHO
一定となるよう電動膨張弁の開度を制御する空気調和機
において、 前記冷凍サイクルの液側配管と圧縮機の吸込側配管との
間に絞り装置を介して設けたバイパスと、このバイパス
の低圧側の冷媒温度Tuを検知する第1検知手段と、暖
房時に前記室外熱交換器に流入する冷媒の温度Teを検
知する第2検知手段と、前記圧縮機の吸込冷媒温度Ts
を検知する第3検知手段と、前記第1検知手段の検知温
度Tuおよび第2検知手段の検知温度Teのいずれか一
方を冷媒の疑似飽和温度として選択する選択手段と、こ
の選択手段で選択される疑似飽和温度と前記第3検知手
段の検知温度Tsとから前記スーパヒート量SHを検出す
る検出手段と、前記圧縮機の吐出冷媒温度Tdまたはケ
ース温度Tcaを検知する検知手段と、この検知手段の検
知温度に応じて前記目標値SHO を補正する補正手段と、
を備えたことを特徴とする空気調和機。
5. A heat pump type refrigeration cycle in which a compressor, a four-way valve, an outdoor heat exchanger, an electric expansion valve, and an indoor heat exchanger are sequentially connected, and the superheat amount SH of the refrigerant is a target value SHO.
In an air conditioner that controls the opening of an electric expansion valve so as to be constant, a bypass provided via a throttle device between the liquid side pipe of the refrigeration cycle and the suction side pipe of the compressor, and a low pressure of this bypass. Side detecting means for detecting the side refrigerant temperature Tu, second detecting means for detecting the temperature Te of the refrigerant flowing into the outdoor heat exchanger during heating, and the suction refrigerant temperature Ts of the compressor.
And a selection means for selecting one of the detection temperature Tu of the first detection means and the detection temperature Te of the second detection means as the pseudo saturation temperature of the refrigerant, and the selection means. Detecting means for detecting the superheat amount SH from the pseudo saturation temperature and the detected temperature Ts of the third detecting means, detecting means for detecting the discharge refrigerant temperature Td of the compressor or the case temperature Tca, and the detecting means of this detecting means. Correction means for correcting the target value SHO according to the detected temperature,
An air conditioner characterized by having.
【請求項6】 請求項5に記載の空気調和機において、 選択手段は、[(Te−Tu)≧所定値K]の条件が成
立するとき検知温度Tuを疑似飽和温度として選択する
手段と、前記条件が成立しないとき検知温度Teを疑似
飽和温度として選択する手段と、を備えたことを特徴と
する空気調和機。
6. The air conditioner according to claim 5, wherein the selecting means selects the detected temperature Tu as a pseudo saturation temperature when the condition of [(Te−Tu) ≧ predetermined value K] is satisfied, Means for selecting the detected temperature Te as the pseudo saturation temperature when the above conditions are not satisfied, the air conditioner.
【請求項7】 請求項5に記載の空気調和機において、 選択手段は、[(Te−Tu)≧所定値K]の条件が成
立するとき検知温度Tuを疑似飽和温度として選択する
手段と、前記条件が成立せず[Te<Tu]の条件が成
立するとき検知温度Teを疑似飽和温度として選択する
手段と、前記両条件が共に成立しないとき[Te−(T
e−Tu)2 /K]の演算値を疑似飽和温度として選択
する手段と、を備えたことを特徴とする空気調和機。
7. The air conditioner according to claim 5, wherein the selecting means selects the detected temperature Tu as the pseudo saturation temperature when the condition of [(Te-Tu) ≧ predetermined value K] is satisfied, Means for selecting the detected temperature Te as the pseudo saturation temperature when the above condition is not satisfied and the condition [Te <Tu] is satisfied, and [Te- (T
e-Tu) 2 / K] is selected as a pseudo saturation temperature, and an air conditioner.
【請求項8】 圧縮機、凝縮器、電動膨張弁、蒸発器を
順次接続した冷凍サイクルを備え、圧縮機の起動に伴い
電動膨張弁の開度を所定の初期開度へと移行制御し、そ
の後、冷媒のスーパヒート量SHが目標値SHO 一定となる
よう電動膨張弁の開度を制御する空気調和機において、 起動から前記スーパヒート量SHが設定値SH1 に至るまで
の経過時間に応じて前記初期開度を補正する制御手段、
を備えたことを特徴とする空気調和機。
8. A refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the opening of the electric expansion valve is controlled to shift to a predetermined initial opening when the compressor is started, After that, in the air conditioner that controls the opening of the electric expansion valve so that the refrigerant superheat amount SH becomes the target value SHO, in the air conditioner, depending on the elapsed time from startup until the superheat amount SH reaches the set value SH 1. Control means for correcting the initial opening,
An air conditioner characterized by having.
【請求項9】 請求項8に記載の空気調和機において、 制御手段は、前記経過時間に応じた量だけ初期開度を開
方向に補正する手段を備えたことを特徴とする空気調和
機。
9. The air conditioner according to claim 8, wherein the control means includes means for correcting the initial opening degree in the opening direction by an amount according to the elapsed time.
【請求項10】 圧縮機、凝縮器、電動膨張弁、蒸発器
を順次接続した冷凍サイクルを備え、圧縮機の起動に伴
い電動膨張弁の開度を所定の初期開度へと移行制御し、
その後、冷媒のスーパヒート量SHが目標値SHO 一定とな
るよう電動膨張弁の開度を制御する空気調和機におい
て、 起動に伴う前記初期開度への移行に際し、前記電動膨張
弁の開度を、先ずは前記スーパヒート量SHが設定値SH1
を超えて設定値SH2 (>SH1 )に至るまで前記圧縮機の
運転周波数に対応する基本開度に設定し、スーパヒート
量SHが設定値SH2 を超えたら前記基本開度より大きい起
動開度αまで増大してその状態を保持し、スーパヒート
量SHが前記設定値SH1 まで低下したところで前記起動開
度αから前記初期開度へと絞る第1制御手段と、起動か
らスーパヒート量SHが前記設定値SH1 に至るまでの経過
時間に応じて前記初期開度を補正する第2制御手段と、
を備えたことを特徴とする空気調和機。
10. A refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the opening of the electric expansion valve is controlled to shift to a predetermined initial opening when the compressor is started,
After that, in the air conditioner that controls the opening degree of the electric expansion valve so that the superheat amount SH of the refrigerant becomes the target value SHO, in the transition to the initial opening degree due to start-up, the opening degree of the electric expansion valve is changed to First, the superheat amount SH is the set value SH 1
The basic opening corresponding to the operating frequency of the compressor is set until the set value SH 2 (> SH 1 ) is exceeded, and when the superheat amount SH exceeds the set value SH 2 , the start opening larger than the basic opening is set. The first control means for reducing the starting opening α to the initial opening when the superheat amount SH decreases to the set value SH 1 and the superheat amount SH from the start are increased. Second control means for correcting the initial opening according to the elapsed time until reaching the set value SH 1 .
An air conditioner characterized by having.
【請求項11】 請求項10に記載の空気調和機におい
て、 第1制御手段は、電動膨張弁の開度を起動開度αから初
期開度へ絞る過程で、絞りを所定値ずつ徐々に進めるこ
とを特徴とする空気調和機。
11. The air conditioner according to claim 10, wherein the first control means gradually advances the throttle by a predetermined value in the process of reducing the opening of the electric expansion valve from the starting opening α to the initial opening. An air conditioner characterized by that.
【請求項12】 請求項11に記載の空気調和機におい
て、 第1制御手段は、電動膨張弁の開度を起動開度αから初
期開度へ徐々に絞る過程で、スーパヒート量SHが設定値
SH3 (>SH2 )まで下降したとき、その時点で開度の絞
りを終了し、前記目標値SHO 一定のための開度制御へ移
ることを特徴とすることを特徴とする空気調和機。
12. The air conditioner according to claim 11, wherein the first control means gradually reduces the opening degree of the electric expansion valve from the starting opening degree α to the initial opening degree, and the superheat amount SH is set to a set value.
An air conditioner characterized in that when it has descended to SH 3 (> SH 2 ), the throttle of the opening is terminated at that point, and the operation proceeds to opening control for maintaining the target value SHO constant.
【請求項13】 請求項8ないし請求項12のいずれか
に記載の空気調和機において、 前記圧縮機の吐出冷媒温度Tdを検知する検知手段と、
この検知手段の検知温度Tdが所定値以上に上昇したと
き、起動に伴う前記初期開度への移行制御を終了し、検
知温度Tdの上昇を抑えるための吐出温度制御に移る制
御手段と、を備えたことを特徴とする空気調和機。
13. The air conditioner according to claim 8, further comprising a detection unit that detects a discharge refrigerant temperature Td of the compressor.
When the detection temperature Td of the detection means rises to a predetermined value or more, the control means for ending the transition control to the initial opening degree upon start-up and shifting to the discharge temperature control for suppressing the rise of the detection temperature Td. An air conditioner characterized by being equipped.
【請求項14】 圧縮機、凝縮器、電動膨張弁、蒸発器
を順次接続した冷凍サイクルを備え、圧縮機の起動に伴
い電動膨張弁の開度を所定の初期開度へと移行制御し、
その後、冷媒のスーパヒート量SHが目標値SHO 一定とな
るよう電動膨張弁の開度を制御する空気調和機におい
て、 起動に伴う前記初期開度への移行に際し、前記電動膨張
弁の開度を、所定の起動開度αまで増大して保持し、前
記スーパヒート量SHが設定値SH1 まで低下したところで
前記起動開度αから前記初期開度へと絞る制御手段と、
前記電動膨張弁の開度を前記起動開度αまで増大して保
持した後、前記スーパヒート量SHが設定値SH1 まで低下
しないまま所定時間が経過したとき、起動開度αの保持
を解除して前記目標値SHO 一定のための開度制御へ移る
制御手段と、を備えたことを特徴とすることを特徴とす
る空気調和機。
14. A refrigeration cycle in which a compressor, a condenser, an electric expansion valve, and an evaporator are sequentially connected, and the opening of the electric expansion valve is controlled to shift to a predetermined initial opening when the compressor is started,
After that, in the air conditioner that controls the opening degree of the electric expansion valve so that the superheat amount SH of the refrigerant becomes the target value SHO, in the transition to the initial opening degree due to start-up, the opening degree of the electric expansion valve is changed to A control means for increasing and maintaining a predetermined starting opening α, and narrowing down from the starting opening α to the initial opening when the superheat amount SH decreases to a set value SH 1 .
After increasing the opening degree of the electric expansion valve to the starting opening degree α and holding it, when the predetermined time elapses without decreasing the superheat amount SH to the set value SH 1 , the holding of the starting opening degree α is released. And a control unit that shifts to an opening degree control for maintaining the target value SHO constant, the air conditioner.
【請求項15】 請求項10、請求項11、請求項12
および請求項14のいずれかに記載の空気調和機におい
て、 起動に伴う前記初期開度への移行制御中に前記圧縮機が
運転中断したとき、その圧縮機の運転再開に伴い前記移
行制御を再開する制御手段と、この移行制御の再開時、
前記起動開度αを前回の移行制御時よりも小さい値に補
正する制御手段と、を備えたことを特徴とすることを特
徴とする空気調和機。
15. The method according to claim 10, claim 11, and claim 12.
15. The air conditioner according to claim 14, wherein when the operation of the compressor is interrupted during the transition control to the initial opening degree upon start-up, the transition control is restarted with the restart of the operation of the compressor. Control means to perform and when restarting this transition control,
An air conditioner comprising: a control unit that corrects the starting opening α to a value smaller than that at the time of the previous transition control.
【請求項16】 請求項10、請求項11および請求項
12のいずれかに記載の空気調和機において、 起動に伴う前記初期開度への移行制御中に前記圧縮機が
運転中断したとき、その圧縮機の運転再開に伴い前記移
行制御を再開する制御手段と、この移行制御の再開時、
前記設定値SH2 を前回の移行制御時よりも大きな値に補
正する制御手段と、を備えたことを特徴とすることを特
徴とする空気調和機。
16. The air conditioner according to any one of claims 10, 11, and 12, when the operation of the compressor is interrupted during transition control to the initial opening upon start-up, Control means for restarting the transfer control with restart of the compressor, and when restarting the transfer control,
An air conditioner comprising: a control unit that corrects the set value SH 2 to a value larger than that at the time of the previous transition control.
JP33522095A 1995-12-22 1995-12-22 Air conditioner Expired - Fee Related JP3495486B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33522095A JP3495486B2 (en) 1995-12-22 1995-12-22 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33522095A JP3495486B2 (en) 1995-12-22 1995-12-22 Air conditioner

Publications (2)

Publication Number Publication Date
JPH09178273A JPH09178273A (en) 1997-07-11
JP3495486B2 true JP3495486B2 (en) 2004-02-09

Family

ID=18286111

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33522095A Expired - Fee Related JP3495486B2 (en) 1995-12-22 1995-12-22 Air conditioner

Country Status (1)

Country Link
JP (1) JP3495486B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2532992A1 (en) 2011-06-09 2012-12-12 Mitsubishi Heavy Industries Multi-type air conditioner and control method therefor

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1149366C (en) 1999-10-18 2004-05-12 大金工业株式会社 Refrigeration equipment
JP3853550B2 (en) * 1999-11-12 2006-12-06 三菱電機株式会社 Air conditioner
JP2003106608A (en) * 2001-09-26 2003-04-09 Mitsubishi Heavy Ind Ltd Air conditioner
JP4836573B2 (en) * 2005-12-27 2011-12-14 東芝キヤリア株式会社 Air conditioner and control method of air conditioner
JP4951383B2 (en) * 2007-03-29 2012-06-13 三洋電機株式会社 Refrigeration cycle equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2532992A1 (en) 2011-06-09 2012-12-12 Mitsubishi Heavy Industries Multi-type air conditioner and control method therefor

Also Published As

Publication number Publication date
JPH09178273A (en) 1997-07-11

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