JPH01312358A - Air conditioner - Google Patents

Air conditioner

Info

Publication number
JPH01312358A
JPH01312358A JP14173088A JP14173088A JPH01312358A JP H01312358 A JPH01312358 A JP H01312358A JP 14173088 A JP14173088 A JP 14173088A JP 14173088 A JP14173088 A JP 14173088A JP H01312358 A JPH01312358 A JP H01312358A
Authority
JP
Japan
Prior art keywords
degree
compressor
frequency
temperature
superheat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP14173088A
Other languages
Japanese (ja)
Other versions
JPH0689949B2 (en
Inventor
Takashi Sano
孝 佐野
Masamichi Hanada
花田 正道
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP63141730A priority Critical patent/JPH0689949B2/en
Publication of JPH01312358A publication Critical patent/JPH01312358A/en
Publication of JPH0689949B2 publication Critical patent/JPH0689949B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

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

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to control of an expansion valve of an air-cooled heat pump type air conditioner.

〔従来の技術〕[Conventional technology]

−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62−218655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ri特に配慮され
ていなかった。
- The conventional device is disclosed in Japanese Patent Application Laid-Open No. 62-213655. As described in the above issue, the expansion valve is controlled to open and close so that the difference between the discharge gas temperature of the compressor and the high-pressure side condensation temperature is constant, and the above temperature is maintained at the outlet of the evaporator so that a moist state can be maintained at all times. The difference was set, and the optimal value of the degree of superheating was determined for each condensation temperature. Further, in Japanese Patent Application Laid-Open No. 62-218655, the setting value of the degree of superheating is determined separately for the operating frequency, but no special consideration is given to a setting method that takes both factors into consideration at the same time.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

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ほおが
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ることの点について
問題があった。
In the above conventional technology, since the compressor frequency is variable, when comparing the speed at which the frequency changes and the speed at which the expansion valve is controlled to the target degree of superheating, the speed at which the frequency changes is large. It is difficult to stabilize the refrigeration cycle if the setting value is set for the high pressure side, and if the setting value is set for the condensing temperature on the high pressure side, the pressure on the low pressure side is high when the frequency is low. Even if the setting value is such that the refrigerant at the heat exchanger outlet is originally wet, it may overheat, and if the frequency is high, the refrigerant at the heat exchanger outlet 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 that can control an expansion valve so as to form a highly efficient and stable refrigeration cycle even when the temperature condition of a heat exchanger or the rotation speed of a compressor changes. be.

〔課題を解決するための手段〕[Means to solve the problem]

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##湿温度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利μsすることにより達成
される。
The above purpose is to set the set superheat degree in relation to both the stable discharge side of the refrigeration cycle, the humidity temperature, the high efficiency compressor operating frequency on the refrigeration cycle, and to adjust the expansion valve to approach the set value. This is achieved by controlling the opening degree μs.

〔作用〕[Effect]

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
度をこ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cU能となる。
First, set the degree of superheat on the compressor discharge side relative to the condensing temperature,
A target degree of superheat is determined by correcting the set degree of superheat according to the compressor operating frequency at that time, and the expansion valve is operated so as to bring the detected degree of superheat closer to this. As a result, the degree of superheating is controlled under all conditions so that the heat exchanger exit is in a wet state, and the refrigeration cycle can be operated stably and efficiently.

〔実施例〕〔Example〕

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62、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
路を循壊し状態変化をくり返す。膨張弁8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T cをその検知68により検知して、
その開度な電気的に制御@l裟置装により行い、また上
記制御装置6より圧縮機lを駆動する電源を供給制御卸
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41にて加圧圧縮され
た高温ガス冷媒0から、凝、縮機2にて冷却され液化し
た冷媒0は、膨張弁3により減圧さ7′1.(ト)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に吸入される囚、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. 1 to 3. FIG. 1 is a refrigeration cycle system diagram in which the present invention is implemented. The refrigeration cycle consists of compressor 1, condensation 62, and expansion valve 3.
, evaporators 4 are successively connected, and the refrigerant circulates through the above-mentioned route and undergoes repeated state changes. The opening/closing operation of the expansion valve 8 is performed by detecting the discharge gas temperature Td of the compressor 1 by the detector 7 and the condensation temperature Tc of the discharge gas by the detector 68.
The degree of opening is electrically controlled by a device, and the control device 6 controls the supply of power to drive the compressor 1 to determine the operating frequency. FIGS. 2, 3, and 3 are Mollier diagrams showing changes in the state of the refrigeration cycle, and the following description will be made with reference to these diagrams. The high-temperature gas refrigerant 0 compressed in the compression 41 is cooled and liquefied in the condenser 2, and then the pressure is reduced by the expansion valve 3 7'1. (g) The air flows into the evaporator 4, where it is evaporated while absorbing heat from the outside air, and then sucked into the compressor 1 again.Here, the operation of the expansion valve will be explained.

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、検出される凝縮部(Tc1.
 Tc2・・・Tcn)に対して、過熱度の目標値が(
SHl、 SH2・・・5Hn)が設定されている。ま
た圧縮機周波数(Hx1+ Hzz・・・Hzn)に対
しても、 上記目標値に対する補正値(Δ8H1゜ΔS
H2・・・Δ5Hn)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)=
ΔTが上記凝縮温度に対応する過熱度の目標値(SH1
十Δ5Hn)に近づけるべく膨張弁3の開度を1tjl
J呻する。この過熱度の目標値Vi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図においいては、定格周波数でのモリエ
ル線図を実線にて示すが、ここで凝縮温度により設定し
たSHnにおいて、蒸発器出口での過熱度は少ないが、
周波数が低くなった場合は、SHnのままの設定値では
吸入圧力が高く蒸発器出口での冷媒が過熱されており、
蒸発器の能力を充分に利用していないこととなる。一方
周波数が高い場合には逆に蒸発器出口では冷媒が過度の
湿り状態となるために圧縮機1の軸受を損傷する結果と
なる。従りて周波数に対して、周波数の低い場合には過
熱度の目標値を低くシ、周波数の高い場合には過熱度の
目標値を大とする補正値ΔSHnを設けたものである。
The discharge gas temperature Td and condensation temperature Tc of the compressor 1 are detected by respective temperature detectors 7.8 and input to the control device 6. The control device 6 includes a condensing section (Tc1.
Tc2...Tcn), the target value of superheat degree is (
SHl, SH2...5Hn) are set. Also, for the compressor frequency (Hx1+Hz...Hzn), the correction value (Δ8H1゜ΔS
H2...Δ5Hn) is set, and the control device 6 calculates the degree of superheat (Td - Tc) derived from the detected temperature.
ΔT is the target value of superheat degree (SH1) corresponding to the above condensation temperature.
The opening degree of the expansion valve 3 is increased by 1tjl to bring it closer to 1Δ5Hn).
J groan. The target value Vi of the degree of superheating is set so that the refrigerant at the outlet of the evaporator remains slightly wet even when operating conditions such as the temperature condition of the heat exchanger and the frequency of the compressor change. In other words, in Fig. 3, the Mollier diagram at the rated frequency is shown as a solid line, but here, at SHn set by the condensing temperature, the degree of superheating at the evaporator outlet is small, but
If the frequency becomes low, if the setting value is SHn, the suction pressure is high and the refrigerant at the evaporator outlet is overheated.
This means that the capacity of the evaporator is not fully utilized. On the other hand, if the frequency is high, the refrigerant becomes excessively wet at the evaporator outlet, resulting in damage to the bearings of the compressor 1. Therefore, a correction value ΔSHn is provided for the frequency, which lowers the target value of the degree of superheat when the frequency is low, and increases the target value of the degree of superheat when the frequency is high.

定状運転状態において、蒸発器4での 熱量舎が少なく
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ΔTは
、凝縮温度T C2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ΔSH2を
加えて、目標値に相当する(SH2+Δ8H2)まで近
づけるよう膨張弁を絞り方向に動作をせる。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 state of operation, if the evaporator 4 has a small amount of heat and the refrigeration cycle is operated as shown by the solid line in Figure 2, the degree of superheat ΔT on the discharge side of the compressor 1 in this case is It is smaller than the set value SH2 of the degree of superheating with respect to the temperature TC2. At this time, the temperature detected by the discharge gas temperature detector 7 and the condensing temperature 8 is input to the control device 6, and the control device 6 adds a correction ΔSH2 to the frequency until it reaches the target value (SH2+Δ8H2). Move the expansion valve in the throttle direction to bring it closer. Conversely, if the degree of superheat is greater than the target value, the expansion valve 3 is opened and control is performed to bring it closer to the target value.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、熱交換器3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 degree of superheating on the discharge side of the compressor in response to changes in the load condition of the heat exchanger 3 and the rotational speed of the compressor, thereby efficiently increasing the capacity of the compressor and heat exchanger. Since it can be maintained at a high level, 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
ガス温度を怠くすべく、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。
Furthermore, when the rotational speed of an inverter-driven compressor is increased, the temperature is likely to rise due to the high load. Therefore, in order to reduce the discharge gas temperature, the humidity on the suction side is increased, which has the effect of reducing the rise in motor coil temperature and improving the reliability of the compressor.

【図面の簡単な説明】[Brief explanation of the drawing]

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ニル綴図、第8図は不発明
の圧縮機の2!!!転周波数に対応するモリエル線図で
ある。 1・・・圧縮機  2・・・凝縮機  3・・・膨張弁
瘍・・・蒸発器  5・・・制御盤  7・・・吐出ガ
ス検知器  8・・・凝縮温度倹矧器。 エンタルピー                  1
シタtと−3柳朕ff6    生制御方≠し
Fig. 1 is a refrigeration cycle diagram of an embodiment of the present invention, Fig. 2 is a refrigeration cycle diagram of an embodiment of the invention, and Fig. 8 is a refrigeration cycle diagram of an embodiment of the invention. ! ! FIG. 4 is a Mollier diagram corresponding to the rotation frequency. 1... Compressor 2... Condenser 3... Expansion valve... Evaporator 5... Control panel 7... Discharged gas detector 8... Condensing temperature regulator. enthalpy 1
Sita t and -3 Yanagi ff6 raw control method≠shi

Claims (1)

【特許請求の範囲】[Claims]  運転周波数の可変な圧縮機、四方弁、室外熱交換器、
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
、周波数が低い場合は小さく、周波数が高い場合は大き
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。
Compressor with variable operating frequency, four-way valve, outdoor heat exchanger,
In an air conditioner that connects an expansion valve and an indoor heat exchanger via piping to form a refrigeration cycle, and is equipped with means for detecting the discharge gas temperature and condensation temperature of a compressor, the detection is performed based on the discharge gas temperature and condensation temperature. The degree of superheating of the discharged gas that corresponds to the condensation temperature of a plurality of discharged gases set in advance is set to be small when the frequency is low, and to be large when the frequency is high, with respect to the operating frequency of the compressor. An air conditioner characterized in that the degree of superheat is set by correcting the degree of superheat, and the opening degree of an expansion valve is controlled so as to maintain the set degree of superheat.
JP63141730A 1988-06-10 1988-06-10 Air conditioner Expired - Fee Related JPH0689949B2 (en)

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 true JPH01312358A (en) 1989-12-18
JPH0689949B2 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 (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03267656A (en) * 1990-03-19 1991-11-28 Daikin Ind Ltd Refrigeration equipment
JP2017036881A (en) * 2015-08-10 2017-02-16 三菱重工業株式会社 Refrigeration and air conditioning equipment

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003106608A (en) * 2001-09-26 2003-04-09 Mitsubishi Heavy Ind Ltd Air conditioner

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63108162A (en) * 1986-10-24 1988-05-13 株式会社日立製作所 Method of controlling expansion valve for air conditioner

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63108162A (en) * 1986-10-24 1988-05-13 株式会社日立製作所 Method of controlling expansion valve for air conditioner

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03267656A (en) * 1990-03-19 1991-11-28 Daikin Ind Ltd Refrigeration equipment
JP2017036881A (en) * 2015-08-10 2017-02-16 三菱重工業株式会社 Refrigeration and air conditioning equipment

Also Published As

Publication number Publication date
JPH0689949B2 (en) 1994-11-14

Similar Documents

Publication Publication Date Title
US10837685B2 (en) HVAC refrigerant charging and relieving systems and methods
JP3823444B2 (en) Air conditioner
JP4779791B2 (en) Air conditioner
JP2001272149A (en) Show case cooling device
JPH01312358A (en) Air conditioner
JP3021987B2 (en) Refrigeration equipment
JP3225738B2 (en) Air conditioner
JPH0534578B2 (en)
JPH06137691A (en) Refrigerant circuit controller
JPS63297784A (en) Protecting device for refrigeration device
JP3306455B2 (en) Air conditioner
JP3434094B2 (en) High pressure protection device and condensing pressure control device in refrigeration system
JPS63108162A (en) Method of controlling expansion valve for air conditioner
JP4176677B2 (en) Air conditioner
JP2904354B2 (en) Air conditioner
JP3353367B2 (en) Air conditioner
JPH03213957A (en) Air conditioner
KR100339543B1 (en) The operation method for improving starting property of a inverter air conditioner
JP7680212B2 (en) Dehumidifier and method for controlling dehumidifier
JPH06272971A (en) Air conditioner
JPH0351667A (en) Separate type air conditioner
JPS63290352A (en) Heat pump type air conditioner
JP2703070B2 (en) Multi refrigeration cycle
JPS63290353A (en) Heat pump type air conditioner
JPS62116861A (en) Air conditioner

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees