JPH0689949B2 - Air conditioner - Google Patents
Air conditionerInfo
- Publication number
- JPH0689949B2 JPH0689949B2 JP63141730A JP14173088A JPH0689949B2 JP H0689949 B2 JPH0689949 B2 JP H0689949B2 JP 63141730 A JP63141730 A JP 63141730A JP 14173088 A JP14173088 A JP 14173088A JP H0689949 B2 JPH0689949 B2 JP H0689949B2
- Authority
- JP
- Japan
- Prior art keywords
- compressor
- operating frequency
- temperature
- superheat
- 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
Links
Landscapes
- Air Conditioning Control Device (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、空冷ヒートポンプ式空気調和機の膨張弁の制
御に関する。Description: TECHNICAL FIELD The present invention relates to control of an expansion valve of an air-cooled heat pump type air conditioner.
従来の装置は、特開昭62−213655号に記載のように、圧
縮機の吐出ガス温度と高圧側凝縮温度の差が一定になる
ように膨張弁の開閉制御を行い、蒸発器の出口におい
て、常に湿り状態に維持し得るよう上記温度差を設定
し、各凝縮温度に対して過熱度の最適値を決定してい
た。又特開昭62−213655号では別に運転周波数に対して
の過熱度の設定値を決定していたが、両者を同時に考慮
する設定方法については特に配慮されていなかった。In the conventional device, as described in JP-A-62-213655, the expansion valve is controlled to open and close so that the difference between the discharge gas temperature of the compressor and the condensation temperature on the high-pressure side becomes constant, and at the outlet of the evaporator. The above-mentioned temperature difference is set so that the wet state can be always maintained, and the optimum value of the superheat degree is determined for each condensation temperature. Further, in Japanese Patent Laid-Open No. 62-213655, the set value of the superheat degree with respect to the operating frequency was separately determined, but no particular consideration was given to the setting method in which both are considered at the same time.
上記従来技術は、圧縮機周波数が可変であるため、周波
数が変化する速度と、目標とする過熱度に膨張弁を制御
する速度を比較すると、周波数が変化する速度の方が大
きく、周波数に対しての設定値を定めた場合には、冷凍
サイクルの安定化が難しいこと、ならびに高圧側の凝縮
温度に対して設定した場合には、周波数が低い場合に
は、低圧側圧力が高い為に、本来熱交換器出口の冷媒を
湿り状態とする設定値であっても過熱する場合があるこ
と、又周波数が高い場合には、上記熱交換器出口の冷媒
が過度に湿り状態となる場合があることの点について問
題があった。In the above-mentioned conventional technology, since the compressor frequency is variable, when the speed at which the frequency changes and the speed at which the expansion valve is controlled to the target degree of superheat are compared, the speed at which the frequency changes is greater than the frequency. If the set values are set, it is difficult to stabilize the refrigeration cycle, and if set to the high temperature side condensation temperature, the low pressure side is high when the frequency is low, The refrigerant at the outlet of the heat exchanger may overheat even if it is a set value that makes the refrigerant at the outlet wet, and if the frequency is high, the refrigerant at the outlet of the heat exchanger may become excessively wet. There was a problem with that.
本発明の目的は、熱交換器の温度条件、あるいは圧縮機
の回転数が変化した場合にも効率が高く安定した冷凍サ
イクルを形成するように膨張弁を制御しうる制御装置を
提供することにある。An object of the present invention is to provide a control device capable of controlling an expansion valve so as to form a stable refrigeration cycle with high efficiency even when the temperature condition of the heat exchanger or the rotation speed of the compressor changes. is there.
上記目的は、設定過熱度を、冷凍サイクルの安定の良い
吐出側凝縮温度と冷凍サイクル上の効率の高い、圧縮機
運転周波数の両者に関係において設定し、その設定値に
近づけるべく膨張弁の開度を制御することにより達成さ
れる。The purpose is to set the set superheat degree in relation to both the stable discharge side condensation temperature of the refrigeration cycle and the compressor operating frequency with high efficiency on the refrigeration cycle, and to open the expansion valve in order to approach the set value. Achieved by controlling the degree.
まず凝縮温度に対して圧縮機吐出側の過熱度を設定し、
その時の圧縮機運転周波数に応じて上記設定過熱度を補
正することにより目標過熱度を決定し、検知される過熱
度をそれに近づけるよう膨張弁を動作せしめる。それに
より過熱度はあらゆる条件において、熱交換器出口で湿
り状態となるよう制御され、冷凍サイクルを安定的にか
つ効率良く運転することが可能となる。First, set the superheat degree on the compressor discharge side for the condensation temperature,
The target superheat degree is determined by correcting the set superheat degree according to the compressor operating frequency at that time, and the expansion valve is operated so that the detected superheat degree approaches the target superheat degree. As a result, the degree of superheat is controlled to be in a wet state at the outlet of the heat exchanger under all conditions, and the refrigeration cycle can be stably and efficiently operated.
以下、本発明の一実施例を第1図〜第3図により説明す
る。第1図は、本発明を実施する冷凍サイクル系統図で
ある。冷凍サイクルは、圧縮機1、凝縮器2、膨張弁
3、蒸発器4を順次連結し構成されており、冷媒は上記
順路を循環し状態変化をくり返す。膨張弁3の開閉動作
は、圧縮機1の吐出ガス温度Tdをその検知器7及び吐出
ガスの凝縮温度Tcをその検知器8により検知して、その
開度を電気的に制御装置6により制御し、また上記制御
装置6により圧縮機1を駆動する電源を供給制御し、運
転周波数を決定している。第2図及び第3図は冷凍サイ
クルの状態変化を表わすモリエル線図で、この図を参照
して以下説明する。圧縮機1にて加圧圧縮された高温ガ
ス冷媒(B)から、凝縮機2にて冷却され液化して冷媒
(D)は、膨張弁3により減圧され(E)蒸発器4に流
入し、蒸発器4にて外気により吸熱しながら蒸発気化
し、再度圧縮機1に吸入される(A)、ここで膨張弁の
動作について説明する。An embodiment of the present invention will be described below with reference to FIGS. FIG. 1 is a refrigeration cycle system diagram for implementing the present invention. The refrigeration cycle is configured by sequentially connecting the compressor 1, the condenser 2, the expansion valve 3, and the evaporator 4, and the refrigerant circulates through the above-mentioned path to repeat the state change. The expansion valve 3 is opened and closed by detecting the discharge gas temperature Td of the compressor 1 by the detector 7 and the discharge gas condensing temperature Tc by the detector 8, and electrically controlling the opening degree by the controller 6. In addition, the power supply for driving the compressor 1 is controlled by the control device 6 to determine the operating frequency. 2 and 3 are Mollier diagrams showing changes in the state of the refrigeration cycle, which will be described below with reference to these diagrams. The high temperature gas refrigerant (B) compressed and compressed by the compressor 1 is cooled and liquefied by the condenser 2 and the refrigerant (D) is decompressed by the expansion valve 3 and flows into the evaporator 4 (E), The evaporator 4 evaporates and vaporizes while absorbing heat from the outside air, and is again sucked into the compressor 1 (A). Here, the operation of the expansion valve will be described.
圧縮機1の吐出ガス温度Tdと凝縮温度Tcは、それぞれの
温度検知器7,8により検知され制御装置6に入力され
る。制御装置6には、検出される凝縮温度(Tc1,Tc2…T
cn)に対して、過熱度の目標値が(SH1,SH2…SHn)が
設定されている。また圧縮機周波数(Hz1,Hz2,Hzn)に
対しては、上記目標値に対する補正値(△SH1,△SH2…
△SHn)が設定されており、制御装置6は、検知した温
度から導かれる過熱度(Td−Tc)=△Tを上記凝縮温度
に対応する過熱度の目標値(SHn+△SHn)に近づける
べく膨張弁3の開度を制御する。この過熱度の目標値は
熱交換器の温度条件、圧縮機の周波数等の運転条件変化
に対しても、蒸発器出口の冷媒が湿りぎみの状態となる
よう設定されている。すなわち、第3図に示したモリエ
ル線図において、実線で示した定格周波数から圧縮機の
回転数が低下した場合に、凝縮温度のみに基づいて過熱
度SHnを設定すると、圧縮機の吸入圧力が高くなり、ま
た、蒸発器出口の冷媒が過熱され、蒸発器の能力が十分
に利用されない。逆に、圧縮機の回転数が増大すると、
蒸発器出口では冷媒が過度の湿り状態となり、圧縮機の
軸受を損傷する。したがって、圧縮機の回転周波数が定
格周波数より低い場合には過熱度を目標値より低くし、
周波数が高い場合には過熱度を目標値より高くする補正
量△SHnを目標値に付加または減じる。The discharge gas temperature Td and the condensation temperature Tc of the compressor 1 are detected by the respective temperature detectors 7 and 8 and input to the control device 6. The control device 6 includes the detected condensation temperatures (Tc 1 , Tc 2 ... T
against c n), the target value of the degree of superheat is (SH 1, SH 2 ... SH n) are set. For the compressor frequencies (Hz 1 , Hz 2 , Hz n ), correction values (ΔSH 1 , ΔSH 2 ...
ΔSH n ) is set, and the control device 6 sets the superheat degree (Td−Tc) = ΔT derived from the detected temperature to the target value (SH n + ΔSH n ) of the superheat degree corresponding to the condensation temperature. ), The opening of the expansion valve 3 is controlled. The target value of the degree of superheat is set so that the refrigerant at the outlet of the evaporator is in a wet state even when the operating conditions such as the temperature condition of the heat exchanger and the frequency of the compressor are changed. That is, in the Mollier diagram shown in FIG. 3, when the rotation speed of the compressor decreases from the rated frequency shown by the solid line, if the superheat degree SHn is set based only on the condensation temperature, the suction pressure of the compressor will be In addition, the refrigerant at the outlet of the evaporator is overheated, and the capacity of the evaporator is not fully utilized. Conversely, when the rotation speed of the compressor increases,
At the evaporator outlet, the refrigerant becomes excessively wet and damages the compressor bearings. Therefore, if the rotation frequency of the compressor is lower than the rated frequency, lower the degree of superheat below the target value,
When the frequency is high, the correction amount ΔSHn that makes the degree of superheat higher than the target value is added or subtracted from the target value.
定常運転状態において、蒸発器4での吸熱量が少なく冷
凍サイクルが、第2図の実線のように運転されていると
すると、この場合の圧縮機1の吐出側の過熱度△Tは、
凝縮温度Tc2に対する過熱度の設定値SH2よりも小さくな
っている。このときの、吐出ガス温度検知器7、凝縮温
度検知器8にて検出された温度が制御装置6に入力さ
れ、制御装置6では、周波数に対する補正△SH2を加え
て、新しい目標値(SH2+△SH2)まで近づけるよう膨張
弁を絞り方向に動作させる。逆に過熱度が目標値より大
きい場合には膨張弁3を開き、目標値に近づけるよう制
御を行う。In a steady operation state, the heat absorption amount in the evaporator 4 is small, and the refrigeration cycle is operated as shown by the solid line in FIG. 2, the superheat degree ΔT on the discharge side of the compressor 1 in this case is
It is smaller than the set value SH 2 of the degree of superheat for the condensation temperature Tc 2 . At this time, the temperatures detected by the discharge gas temperature detector 7 and the condensation temperature detector 8 are input to the control device 6, and the control device 6 adds a correction ΔSH 2 for the frequency and adds a new target value (SH 2 ) Operate the expansion valve in the throttle direction so that it approaches 2 + △ SH 2 ). On the contrary, when the degree of superheat is larger than the target value, the expansion valve 3 is opened and control is performed so as to approach the target value.
本発明によれば、熱交換器の負荷条件や圧縮機の回転数
の変化に対応して、圧縮機吐出側過熱度のきめ細かな制
御が可能となり、圧縮機、熱交換器の能力を効率高く維
持できるため空気調和機の性能向上が図れる。According to the present invention, it is possible to finely control the superheat degree on the discharge side of the compressor in response to changes in the load condition of the heat exchanger and the rotation speed of the compressor, and to increase the efficiency of the compressor and the heat exchanger efficiently. Since it can be maintained, the performance of the air conditioner can be improved.
又、インバータ駆動の圧縮機は回転数を上昇させた場合
に高負荷となる為の温度上昇を生じ易い。その為、吐出
ガス温度を低くすべく、吸入側湿り度を大として、モー
タコイル温度上昇を低減し、圧縮機の信頼性を向上する
効果がある。In addition, the inverter-driven compressor is liable to have a high load when the number of rotations is increased, and the temperature is likely to increase. Therefore, in order to lower the temperature of the discharged gas, the wetness on the suction side is increased, the temperature rise of the motor coil is reduced, and the reliability of the compressor is improved.
第1図は本発明の一実施例の冷凍サイクル図、第2図は
本発明の一実施例の冷凍モリエル線図、第3図は本発明
の圧縮機の運転周波数に対応するモリエル線図である。 1……圧縮機、2……凝縮器、3……膨張弁、4……蒸
発器、6……制御装置、7……吐出ガス検知器、8……
凝縮温度検知器。FIG. 1 is a refrigeration cycle diagram of one embodiment of the present invention, FIG. 2 is a refrigeration Mollier diagram of one embodiment of the present invention, and FIG. 3 is a Mollier diagram corresponding to the operating frequency of the compressor of the present invention. is there. 1 ... Compressor, 2 ... Condenser, 3 ... Expansion valve, 4 ... Evaporator, 6 ... Control device, 7 ... Discharge gas detector, 8 ...
Condensation temperature detector.
Claims (1)
熱交換器、膨張弁、室内熱交換器、を配管により連結し
冷凍サイクルを形成し、かつ圧縮機の吐出ガス温度およ
び凝縮温度を検知する手段を備えた空気調和機におい
て、前記吐出ガス温度及び凝縮温度により検知される吐
出ガスの過熱度を、あらかじめ設定した複数の吐出ガス
の凝縮温度に対応する各々の過熱度を上記圧縮機の運転
周波数に対し、前記圧縮機の運転周波数が定格運転周波
数より低い場合は小さく、前記圧縮機の運転周波数が定
格運転周波数より高い場合は大きくするよう補正して過
熱度を設定し、この設定過熱度を保持するように膨張弁
の開度を制御することを特徴とする空気調和機。1. A refrigeration cycle is formed by connecting a compressor whose operating frequency is variable, a four-way valve, an outdoor heat exchanger, an expansion valve, and an indoor heat exchanger, and a discharge gas temperature and a condensation temperature of the compressor. In an air conditioner equipped with a means for detecting, the superheat degree of the discharge gas detected by the discharge gas temperature and the condensation temperature, each superheat degree corresponding to the condensation temperature of a plurality of preset discharge gas is compressed. With respect to the operating frequency of the machine, it is small when the operating frequency of the compressor is lower than the rated operating frequency, and is set to be larger when the operating frequency of the compressor is higher than the rated operating frequency, and the superheat is set. An air conditioner characterized by controlling the opening of an expansion valve so as to maintain a set superheat degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63141730A JPH0689949B2 (en) | 1988-06-10 | 1988-06-10 | Air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63141730A JPH0689949B2 (en) | 1988-06-10 | 1988-06-10 | Air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01312358A JPH01312358A (en) | 1989-12-18 |
| JPH0689949B2 true JPH0689949B2 (en) | 1994-11-14 |
Family
ID=15298875
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63141730A Expired - Fee Related JPH0689949B2 (en) | 1988-06-10 | 1988-06-10 | Air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0689949B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003106608A (en) * | 2001-09-26 | 2003-04-09 | Mitsubishi Heavy Ind Ltd | Air conditioner |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03267656A (en) * | 1990-03-19 | 1991-11-28 | Daikin Ind Ltd | Refrigeration equipment |
| JP6594698B2 (en) * | 2015-08-10 | 2019-10-23 | 三菱重工サーマルシステムズ株式会社 | Refrigeration and air conditioning equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0610560B2 (en) * | 1986-10-24 | 1994-02-09 | 株式会社日立製作所 | Control method of expansion valve of air conditioner |
-
1988
- 1988-06-10 JP JP63141730A patent/JPH0689949B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003106608A (en) * | 2001-09-26 | 2003-04-09 | Mitsubishi Heavy Ind Ltd | Air conditioner |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01312358A (en) | 1989-12-18 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |