JPH0745976B2 - Refrigeration cycle controller - Google Patents
Refrigeration cycle controllerInfo
- Publication number
- JPH0745976B2 JPH0745976B2 JP26129886A JP26129886A JPH0745976B2 JP H0745976 B2 JPH0745976 B2 JP H0745976B2 JP 26129886 A JP26129886 A JP 26129886A JP 26129886 A JP26129886 A JP 26129886A JP H0745976 B2 JPH0745976 B2 JP H0745976B2
- Authority
- JP
- Japan
- Prior art keywords
- valve opening
- temperature
- opening
- valve
- refrigeration cycle
- 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
- 238000005057 refrigeration Methods 0.000 title claims description 24
- 238000001514 detection method Methods 0.000 claims description 3
- 238000010586 diagram Methods 0.000 description 7
- 238000013459 approach Methods 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Air Conditioning Control Device (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、電動式膨張弁を用いた冷凍サイクルの制御装
置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigeration cycle control device using an electric expansion valve.
従来の技術 近年、冷凍サイクルの冷媒流量を制御する装置として、
マイクロコンピュータにより多様な制御が可能な、電動
式膨張弁の開発が進んでいる。BACKGROUND ART In recent years, as a device for controlling the refrigerant flow rate of a refrigeration cycle,
Development of an electrically driven expansion valve that can be controlled in various ways by a microcomputer is in progress.
以下図面を参照しながら、上述した従来の電動式膨張弁
による冷凍サイクルの制御装置の一例について説明す
る。An example of the conventional refrigeration cycle control device using the above-described electric expansion valve will be described below with reference to the drawings.
第4図は冷凍サイクルの構成を示すものである。第4図
において1は圧縮機、2は熱交換器、3は電動式膨張
弁、4は熱交換器、5は吹出温度を検出する吹出温度セ
ンサー、6bは吐出温度センサー5の信号により電動式膨
張弁3を制御する制御装置である。FIG. 4 shows the structure of the refrigeration cycle. In FIG. 4, 1 is a compressor, 2 is a heat exchanger, 3 is an electric expansion valve, 4 is a heat exchanger, 5 is a blow-out temperature sensor for detecting the blow-out temperature, and 6b is an electric type by the signal of the discharge temperature sensor 5. It is a control device that controls the expansion valve 3.
第5図は制御装置のブロック図である。制御装置6bは吐
出温度センサー5等からなる温度検出手段7、冷凍サイ
クルの運転状況に応じて吐出温度の目標値を設定する目
標温度設定手段8、吐出温度検出手段7の出力と目標温
度設定手段8の出力を比較する温度比較手段9、温度比
較手段の出力によって弁開度を算出する弁開度演算手段
10、弁開度演算手段の出力に応じた弁開度を出力する弁
開度出力手段15で構成されている。FIG. 5 is a block diagram of the control device. The control device 6b includes a temperature detecting means 7 including a discharge temperature sensor 5 and the like, a target temperature setting means 8 for setting a target value of the discharge temperature according to the operating condition of the refrigeration cycle, an output of the discharge temperature detecting means 7 and a target temperature setting means Temperature comparison means 9 for comparing the outputs of 8 and valve opening calculation means for calculating the valve opening by the output of the temperature comparison means
10. The valve opening output means 15 outputs the valve opening according to the output of the valve opening calculation means.
以上のように構成された冷凍サイクルおよび制御回路の
動作について第7図,第8図を参照しながら説明する。The operation of the refrigeration cycle and the control circuit configured as described above will be described with reference to FIGS. 7 and 8.
第7図は電動式膨張弁5の動作を表わすフローチャート
であり、第8図は代表的な吐出温度、電動式膨張弁5の
弁開度、および冷凍サイクルのEERの変化を示したもの
である。FIG. 7 is a flowchart showing the operation of the electric expansion valve 5, and FIG. 8 shows changes in typical discharge temperature, valve opening of the electric expansion valve 5, and EER of the refrigeration cycle. .
動作としては、まず、吐出温センサー5からなる吐出温
度検出手段7で検出した吐出温度Tdと、目標温度設定手
段8で設定した温度Tsとの温度差ΔTdを温度比較手段9
で求める。そしてこの温度差ΔTdに応じた弁開度を弁開
度演算手段10により決定し、弁開度出力手段15により電
動式膨張弁5の開度を変更する。弁開度演算手段10での
演算内容は、吐出温度Tdが目標値Tsと大きく異なる場合
は、電動式膨張弁5の弁開度を大きく変更し、吐出温度
Tdが目標値Tsに近づくにつれ弁開度の変更度合いを小さ
くして、吐出温度Tdが目標値Ts±ΔThの温度域に入れば
弁開度の変更を行なわず、吐出温度Tdを目標値Tsの近づ
けようとするものである。なお、一度設定された弁開度
は最低ある時間保持されている。As the operation, first, the temperature difference ΔTd between the discharge temperature Td detected by the discharge temperature detection means 7 including the discharge temperature sensor 5 and the temperature Ts set by the target temperature setting means 8 is calculated by the temperature comparison means 9
Ask in. Then, the valve opening degree according to the temperature difference ΔTd is determined by the valve opening degree calculation means 10, and the valve opening degree output means 15 changes the opening degree of the electric expansion valve 5. If the discharge temperature Td is significantly different from the target value Ts, the valve opening degree calculation means 10 changes the valve opening degree of the electrically driven expansion valve 5 to a large value.
As Td approaches the target value Ts, the degree of change in the valve opening is reduced, and if the discharge temperature Td falls within the temperature range of the target value Ts ± ΔTh, the valve opening is not changed and the discharge temperature Td is changed to the target value Ts. It is something that tries to get closer to. In addition, the valve opening degree set once is held for a certain period of time.
発明が解決しようとする問題点 しかしながら上記のような構成では、吐出温度Tdの目標
値はTs±ΔThという温度幅をもった領域となり、冷凍サ
イクルのEERが最高になる最も望ましい吐出温度Tsへ正
確に近づけることが困難であり、さらに吐出温度Tdは温
度幅±ΔThの両端へかたよる可能性がある。これらはわ
ずかな外乱に対しても、再び弁開度変更動作を行ない吐
出温度がTdが安定するまで時間がかかるという問題点が
あった。Problems to be Solved by the Invention However, in the above-described configuration, the target value of the discharge temperature Td is a region having a temperature width of Ts ± ΔTh, and the EER of the refrigeration cycle is the highest, and the target discharge temperature Ts is accurate. Is difficult to approach, and there is a possibility that the discharge temperature Td will bend toward both ends of the temperature range ± ΔTh. These have a problem that it takes time until the discharge temperature Td is stabilized by performing the valve opening changing operation again even with a slight disturbance.
本発明は上記問題点に鑑み、吐出温度Tdをより正確に目
標値に近づけ、かつ外乱に対しても不要な弁開度の変更
をなくし、高効率で安定性の高い冷凍サイクルを提供す
ることを目的としている。In view of the above problems, the present invention provides a highly efficient and highly stable refrigeration cycle that more accurately brings the discharge temperature Td closer to a target value and eliminates unnecessary changes in valve opening even with respect to disturbance. It is an object.
問題点を解決するための手段 上記問題点を解決するために本発明の冷凍サイクルの制
御装置は、従来例の制御装置と同様の温度検出手段、目
標温度設定手段、温度比較手段、弁開度演算手段、弁開
度出力手段と新たに弁開度比較手段、最大弁開度記憶手
段、最小弁開度記憶手段、平均弁開度演算手段、を弁開
度出力手段の前段に設け、さらに温度不感帯発生手段を
設けたものである。Means for Solving the Problems In order to solve the above problems, the control device of the refrigeration cycle of the present invention has the same temperature detecting means, target temperature setting means, temperature comparing means, and valve opening degree as those of the conventional control device. A calculation means, a valve opening output means, and a new valve opening comparison means, a maximum valve opening storage means, a minimum valve opening storage means, and an average valve opening calculation means are provided in the preceding stage of the valve opening output means. A temperature dead zone generating means is provided.
作用 本発明は上記した構成によって、弁開度演算手段の出力
が、現時点までの最大弁開度であるか、最小弁開度であ
るかを弁開度比較手段で検出し、最大弁開度であると検
出されたときは、そのときの弁開度を最大弁開度記憶手
段へ記憶し、最小弁開度であると検出されたときは、そ
のときの弁開度を最小弁開度記憶手段へ記憶する。そし
て弁開度の最大値,最小値は、吐出温度が目標値を中心
にハンチングするために生じるものであるので、最小弁
開度と最大弁開度の平均値を平均弁開度演算手段で求め
ると、その弁開度は、吐出温度を目標値にするのに最も
適切な弁開度となっているので、吐出温度を精度良く制
御することができる。The present invention has the above-described configuration, and the valve opening degree comparing means detects whether the output of the valve opening degree calculating means is the maximum valve opening degree or the minimum valve opening degree up to the present time. When it is detected that the valve opening at that time is stored in the maximum valve opening storage means, and when it is detected as the minimum valve opening, the valve opening at that time is set to the minimum valve opening. Store in the storage means. Since the maximum value and the minimum value of the valve opening degree occur because the discharge temperature hunts around the target value, the average value of the minimum valve opening degree and the maximum valve opening degree is calculated by the average valve opening degree calculation means. When found, the valve opening degree is the most appropriate valve opening degree for making the discharge temperature the target value, so the discharge temperature can be controlled with high accuracy.
さらに、平均弁開度演算手段の出力が発生した場合目標
値の温度のプラス側とマイナス側に、弁開度変更を停止
する温度不感帯を設定し、温度不感帯発生手段を平均弁
開度演算手段の出口に接続することで、目標値に正確に
近づいた吐出温度が、外乱によって多少変動しても、吐
出温度は温度不感帯から出ず安定した制御が可能とな
る。Further, when the output of the average valve opening calculating means is generated, a temperature dead zone for stopping the change of the valve opening is set on the plus side and the minus side of the temperature of the target value, and the temperature dead zone generating means is set to the average valve opening calculating means. By connecting to the outlet of, the discharge temperature does not come out of the temperature dead zone and stable control is possible even if the discharge temperature accurately approaching the target value fluctuates to some extent due to disturbance.
実施例 以下、本発明の一実施例の冷凍サイクルの制御装置につ
いて説明する。Embodiment Hereinafter, a refrigeration cycle control device according to an embodiment of the present invention will be described.
第1図は一実施例の冷凍サイクル図であり、圧縮機1、
熱交換器2、電動式膨張弁3、熱交換器4が環状に連結
されている。電動式膨張弁3の弁開度は、吐出温センサ
ー5の検出温度を入力信号とする制御装置6aによって制
御される。図中実線矢印は冷媒の流通方向を示す。FIG. 1 is a refrigeration cycle diagram of one embodiment, in which the compressor 1,
The heat exchanger 2, the electric expansion valve 3, and the heat exchanger 4 are connected in an annular shape. The valve opening degree of the electrically driven expansion valve 3 is controlled by the control device 6a which uses the temperature detected by the discharge temperature sensor 5 as an input signal. In the figure, the solid line arrow indicates the flow direction of the refrigerant.
第2図は上記制御装置6aのブロック図である。温度検出
手段7の出力と目標温度設定手段8の出力を温度比較手
段9で比較し、その出力に応じて、弁開度演算手段10で
弁開度を求める。FIG. 2 is a block diagram of the control device 6a. The output of the temperature detecting means 7 and the output of the target temperature setting means 8 are compared by the temperature comparing means 9, and the valve opening degree calculating means 10 determines the valve opening degree according to the output.
求めた弁開度が現在までの最大弁開度であるか、最小弁
開度であるかを弁開度比較手段11で検出し、最大弁開度
であると検出されたときは、そのときの弁開度を最大弁
開度記憶手段12へ記憶し、最小弁開度であると検出され
たときは、そのときの弁開度を最小弁開度記憶手段13へ
記憶する。この最大直,最小値を平均弁開度演算手段14
へ入力し、平均弁開度((最大弁開度+最小弁開度)/
2)を弁開度出力手段15より出力し、このとき、温度不
感帯発生手段16により、目標温度のプラス側とマイナス
側に弁開度の変更を停止する温度不感帯を発生する。The valve opening comparison means 11 detects whether the obtained valve opening is the maximum valve opening up to the present or the minimum valve opening, and when it is detected as the maximum valve opening, then, The valve opening degree is stored in the maximum valve opening storage means 12, and when it is detected as the minimum valve opening degree, the valve opening degree at that time is stored in the minimum valve opening storage means 13. This maximum straightness and minimum value are average valve opening calculating means 14
To the average valve opening ((maximum valve opening + minimum valve opening) /
2) is output from the valve opening output means 15, and at this time, the temperature dead zone generating means 16 generates a temperature dead zone for stopping the change of the valve opening on the plus side and the minus side of the target temperature.
第3図は本実施例の制御のフローチャートである。第4
図は、目標温度Tsに対する吐出温度の変化、弁開度の変
化、冷凍サイクルのEERの変化を示したものである。FIG. 3 is a flowchart of the control of this embodiment. Fourth
The figure shows changes in the discharge temperature, changes in the valve opening, and changes in the EER of the refrigeration cycle with respect to the target temperature Ts.
以下、第3図,第4図について説明する。Hereinafter, FIGS. 3 and 4 will be described.
吐出温度Tdを検出して、目標温度Tsと比較する。その結
果、吐出温度が低い場合には弁開度をΔP減少する。そ
のままの弁開度でΔt時間維持し、再度吐出温度Tdと目
標温度Tsを比較する。このとき吐出温度Tdが目標温度Ts
より高ければ、弁開度をΔp増加させ、増加させる前の
弁開度を最小弁開度(PMIN)として記憶しておく。同様
にΔt時間ごとに吐出温度Tdが目標温度Tsの比較をくり
返し、吐出温度Tdが目標温度Tsより高い状態から低い状
態に変わったとき、つまり弁開度の変化がΔP増加から
ΔP減少へ変化したとき、ΔP減少する前の弁開度を最
大弁開度(PMAX)とする。The discharge temperature Td is detected and compared with the target temperature Ts. As a result, when the discharge temperature is low, the valve opening is reduced by ΔP. The valve opening is maintained as it is for Δt time, and the discharge temperature Td and the target temperature Ts are compared again. At this time, the discharge temperature Td is the target temperature Ts
If it is higher, the valve opening is increased by Δp, and the valve opening before the increase is stored as the minimum valve opening (P MIN ). Similarly, the discharge temperature Td is repeatedly compared with the target temperature Ts every Δt time, and when the discharge temperature Td changes from a state higher than the target temperature Ts to a state lower, that is, the change in the valve opening degree changes from ΔP increase to ΔP decrease. At this time, the valve opening before decreasing by ΔP is set to the maximum valve opening (P MAX ).
最大弁開度(PMAX)、最小弁開度(PMIN)が確定する
と、その平均値((PMAX+PMIN)/2)へ弁開度を変更す
る。When the maximum valve opening (P MAX ) and minimum valve opening (P MIN ) are confirmed, the valve opening is changed to the average value ((P MAX + P MIN ) / 2).
さらに、平均弁開度演算手段14の出力が発生した場合、
目標温度Tsのプラス側とマイナス側にそれぞれTs+ΔT
h,Ts−ΔThの温度ラインを設け、検出した吐出温度Tdが
Ts+ΔTh以下でかつTs−ΔTh以上であるときは、電動式
膨張弁の開度の変更は行なわない。Furthermore, when the output of the average valve opening calculation means 14 occurs,
Ts + ΔT on the plus and minus sides of the target temperature Ts
A temperature line of h, Ts-ΔTh is provided, and the detected discharge temperature Td
When Ts + ΔTh or less and Ts−ΔTh or more, the opening degree of the electric expansion valve is not changed.
その結果、吐出温度Tdを目標温度Tsへより早く、より正
確に近づけることができ、高効率で、外乱に強い安定性
の高い冷凍サイクルが実現できる。As a result, the discharge temperature Td can be brought closer to the target temperature Ts faster and more accurately, and a refrigeration cycle with high efficiency and high stability against external disturbance can be realized.
発明の効果 以上のように本発明は、冷凍サイクルの所定箇所の温度
を温度検出手段で検出し、目標温度設定手段の出力と温
度比較手段で比較し、温度比較手段の出力に応じて弁開
度演算手段により弁開度を決定し、弁開度出力手段より
出力し電動膨張弁の弁開度を変更する制御装置におい
て、最大弁開度,最小弁開度を求める弁開度比較手段,
最大弁開度,最小弁開度を記憶する最大弁開度記憶手段
最小弁開度記憶手段,最大弁開度と最小弁開度の平均弁
開度を求める平均弁開度演算手段を設け、さらに平均弁
開度演算手段の出力が発生した場合、目標温度設定手段
の出力のプラス側とマイナス側に弁開度の変更を停止す
る不感帯を設けることで吐出温度を目標温度にするため
の弁開度を、最大弁開度と最小弁開度の平均弁開度とし
て求めることができ、吐出温度をより早く、より正確に
目標温度に近づけることができ、高効率の冷凍サイクル
が実現できると同時に、外乱に対して安定度の高い冷凍
サイクルが実現できる。As described above, according to the present invention, the temperature of the predetermined portion of the refrigeration cycle is detected by the temperature detecting means, the output of the target temperature setting means is compared with the temperature comparing means, and the valve is opened according to the output of the temperature comparing means. In the control device that determines the valve opening by the degree calculation means and changes the valve opening of the electric expansion valve by outputting from the valve opening output means, the valve opening comparison means for determining the maximum valve opening and the minimum valve opening,
A maximum valve opening storage means for storing the maximum valve opening and the minimum valve opening, a minimum valve opening storage means, and an average valve opening calculation means for obtaining an average valve opening of the maximum valve opening and the minimum valve opening are provided. Further, when the output of the average valve opening calculation means is generated, a dead zone for stopping the change of the valve opening is provided on the plus side and the minus side of the output of the target temperature setting means, so that the valve for adjusting the discharge temperature to the target temperature is provided. The opening can be calculated as the average valve opening of the maximum valve opening and the minimum valve opening, and the discharge temperature can be brought closer to the target temperature faster and more accurately, and a highly efficient refrigeration cycle can be realized. At the same time, a refrigeration cycle with high stability against disturbance can be realized.
第1図は本発明の一実施例を示す冷凍サイクル図、第2
図は本発明の制御装置のブロック図、第3図は同制御装
置の制御内容を示すフローチャート、第4図は同冷凍サ
イクルにおける代表的な吐出温度、弁開度、EER特性を
示すタイムチャート、第5図,第6図は従来例の冷凍サ
イクル図および、制御装置のブロック図、第7図,第8
図は従来例の制御内容を示すフローチャートおよび代表
的な吐出温度、弁開度、EER特性の変化を示すタイムチ
ャートである。 1……圧縮機、2,4……熱交換器、3……電動式膨張
弁、11……弁開度比較手段、12……最大弁開度記憶手
段、13……最小弁開度記憶手段、14……平均弁開度演算
手段、7……温度検出手段、8……目標温度設定手段、
9……温度比較手段、10……弁開度演算手段、15……弁
開度出力手段、16……温度不感帯発生手段。FIG. 1 is a refrigeration cycle diagram showing an embodiment of the present invention, and FIG.
FIG. 3 is a block diagram of the control device of the present invention, FIG. 3 is a flow chart showing the control contents of the control device, and FIG. 4 is a time chart showing typical discharge temperature, valve opening degree and EER characteristic in the refrigeration cycle, 5 and 6 are a refrigeration cycle diagram of a conventional example and a block diagram of a control device, FIG. 7 and FIG.
The figure is a flow chart showing the control contents of a conventional example and a time chart showing changes in typical discharge temperature, valve opening, and EER characteristics. 1 ... compressor, 2,4 ... heat exchanger, 3 ... motorized expansion valve, 11 ... valve opening comparison means, 12 ... maximum valve opening storage means, 13 ... minimum valve opening memory Means, 14 ... Average valve opening calculation means, 7 ... Temperature detection means, 8 ... Target temperature setting means,
9: temperature comparison means, 10: valve opening calculation means, 15: valve opening output means, 16: temperature dead zone generation means.
Claims (1)
サイクルを構成し、前記冷凍サイクルの所定箇所の温度
を温度検出手段で比較し、その検出温度と目標温度設定
手段の目標温度を温度比較手段で比較し、前記検出温度
が目標温度以上の場合は前記電動膨張弁を一定量開き、
前記検出温度が目標温度未満の場合は前記電動式膨張弁
を一定量閉じる動作を行なう弁開度出力手段を具備した
制御装置において、前記電動式膨張弁の動作が開動作か
ら閉動作に変化した場合、閉動作に変化する直前の弁開
度を最大弁開度とする最大弁開度演算手段と、閉動作か
ら開動作へ変化した場合、開動作に変化する直前の弁開
度を最小弁開度とする最小弁開度演算手段と、前記最大
弁開度と前記最小弁開度が決定した時点で前記最大弁開
度と前記最小弁開度から平均弁開度を求める平均弁開度
演算手段とを設け、さらに前記平均弁開度演算手段の出
力を弁開度演算手段に出力して、前記電動膨張弁の弁開
度を前記平均弁開度に維持するとともに、前記平均弁開
度演算手段の出力が発生した場合、前記目標温度と前記
温度検出手段での検出温度の比較を行なわない温度不感
帯を前記目標温度を中心にプラス側とマイナス側にまた
がるように設けた冷凍サイクルの制御装置。1. A refrigeration cycle is constituted by a compressor, a heat exchanger, an electric expansion valve, etc., temperature of a predetermined portion of the refrigeration cycle is compared by a temperature detecting means, and the detected temperature and a target of a target temperature setting means. The temperatures are compared by the temperature comparison means, and when the detected temperature is equal to or higher than the target temperature, the electric expansion valve is opened by a certain amount
When the detected temperature is lower than the target temperature, in the control device including the valve opening output means for closing the electric expansion valve by a certain amount, the operation of the electric expansion valve is changed from the opening operation to the closing operation. In this case, the maximum valve opening calculation means that sets the valve opening immediately before the closing operation to the maximum opening, and when the closing operation changes to the opening operation, the valve opening immediately before the opening operation changes to the minimum valve opening. A minimum valve opening calculation means that is an opening, and an average valve opening that determines an average valve opening from the maximum valve opening and the minimum valve opening when the maximum valve opening and the minimum valve opening are determined. And an output of the average valve opening calculation means is output to the valve opening calculation means to maintain the valve opening of the electric expansion valve at the average valve opening and to open the average valve opening. When the output of the temperature calculation means is generated, the target temperature and the temperature detection means Controller outgoing refrigeration cycle temperature dead zone is not carried out a comparison of the temperature is provided to span the positive and negative sides around the target temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26129886A JPH0745976B2 (en) | 1986-10-31 | 1986-10-31 | Refrigeration cycle controller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26129886A JPH0745976B2 (en) | 1986-10-31 | 1986-10-31 | Refrigeration cycle controller |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63116058A JPS63116058A (en) | 1988-05-20 |
| JPH0745976B2 true JPH0745976B2 (en) | 1995-05-17 |
Family
ID=17359853
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26129886A Expired - Fee Related JPH0745976B2 (en) | 1986-10-31 | 1986-10-31 | Refrigeration cycle controller |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0745976B2 (en) |
-
1986
- 1986-10-31 JP JP26129886A patent/JPH0745976B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63116058A (en) | 1988-05-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |