JPH0618100A - Control method and control device for air conditioner - Google Patents

Control method and control device for air conditioner

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Publication number
JPH0618100A
JPH0618100A JP4178388A JP17838892A JPH0618100A JP H0618100 A JPH0618100 A JP H0618100A JP 4178388 A JP4178388 A JP 4178388A JP 17838892 A JP17838892 A JP 17838892A JP H0618100 A JPH0618100 A JP H0618100A
Authority
JP
Japan
Prior art keywords
control
amount
target value
control target
operation amount
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.)
Pending
Application number
JP4178388A
Other languages
Japanese (ja)
Inventor
Masataka Ozeki
正高 尾関
Minoru Tagashira
實 田頭
Shozo Funakura
正三 船倉
Kazuo Nakatani
和生 中谷
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP4178388A priority Critical patent/JPH0618100A/en
Publication of JPH0618100A publication Critical patent/JPH0618100A/en
Pending legal-status Critical Current

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  • Air Conditioning Control Device (AREA)

Abstract

PURPOSE:To provide a control method and a control device, which are capable of controlling a controlled object excellently when a controlled variable has a saturation area, and an air conditioner. CONSTITUTION:At air conditioner is provided with a first fuzzy operating means 1, operating a controlled target value (rf) based on a controlled variable (y) outputted from a controlled object 9 having a saturating area, a comparing means 2, comparing the controlled target value (rf) with the controlled variable (y), two sets of fundamental control means 3A, 3B, operating two different manipulated variables UA, UB based on the result of the comparison, and a second fuzzy operating means 8, operating the manipulated variable Uf of the controlled object 9 based on the operated two manipulated variables UA, UB while considering the controlled variable (y).

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、上限値または下限値も
しくはその両方が存在する制御量を持つ制御対象に対す
る制御方法、制御装置、その制御方法を利用した空気調
和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 control method for a controlled object having a controlled variable having an upper limit value, a lower limit value, or both, and an air conditioner using the control method.

【0002】[0002]

【従来の技術】従来、非線形な量を制御するためには、
非線形制御が用いられている。非線形制御は、非線形な
制御量の動特性を詳しく解析してその特性にあった制御
系を構成するものである。
2. Description of the Related Art Conventionally, in order to control a nonlinear quantity,
Non-linear control is used. The non-linear control is to analyze a dynamic characteristic of a non-linear control amount in detail and construct a control system suitable for the characteristic.

【0003】また、簡易で実用的な方法として制御量の
非線形性を微小区間において線形近似する方法がある。
制御量の非線形な動特性を線形近似して、その動特性が
近似した線形性と多少異なってもうまく制御を実行でき
るような制御系を構成する。このような制御方式として
は、制御量と制御目標値の差である制御偏差に対して、
比例演算、積分演算かつ比例演算、微分演算かつ比例演
算を行い、その演算結果の和により操作量を決定する、
いわゆるPID制御方式が広く採用されている。図4に
その構成を示す。図において、制御目標値rと制御対象
9からの出力である制御量yとを用いて、比較手段2で
制御偏差eを検出する。検出した制御偏差eは、PID
コントローラ3に入力される。PIDコントローラ3は
内部で制御偏差eを比例演算手段4、積分演算かつ比例
演算手段5、微分演算かつ比例演算手段6に入力し、各
々の演算結果を加算手段7により加算することにより操
作量uを出力する。その操作量uを用いて制御対象9を
操作するものである。ここで、Kp、Ki、Kdは各演
算手段4,5,6における比例演算の係数である。
As a simple and practical method, there is a method of linearly approximating the nonlinearity of the control amount in a minute section.
A control system is constructed that linearly approximates the nonlinear dynamic characteristics of the control amount and that can control well even if the dynamic characteristics are slightly different from the approximate linearity. As such a control method, with respect to the control deviation which is the difference between the control amount and the control target value,
Proportional operation, integral operation and proportional operation, differential operation and proportional operation are performed, and the operation amount is determined by the sum of the operation results.
The so-called PID control method is widely adopted. The structure is shown in FIG. In the figure, the comparison means 2 detects the control deviation e using the control target value r and the control amount y which is the output from the controlled object 9. The detected control deviation e is the PID
It is input to the controller 3. The PID controller 3 internally inputs the control deviation e to the proportional calculation means 4, the integral calculation / proportional calculation means 5, and the differential calculation / proportional calculation means 6, and the respective calculation results are added by the addition means 7 to thereby manipulate the operation amount u. Is output. The control target 9 is operated using the operation amount u. Here, Kp, Ki, and Kd are the coefficients of the proportional calculation in each calculation means 4, 5, and 6.

【0004】[0004]

【発明が解決しようとする課題】非線形制御の場合、各
操作量に対する制御量の非線形な挙動を十分解析するこ
とによって、良い制御性能を得ることが可能となる。し
かしながら、例えば冷凍サイクルの過熱度や過冷却度な
どのように上限値あるいは下限値がある(飽和領域を有
する)非線形な量を制御量とする場合は、図3に示す操
作量と制御量の関係を示す特性曲線の点aと点bのよう
に、制御量が上限値および下限値の時の操作量を一意的
に決定することができない。そのため、制御量の非線形
な挙動を十分解析する事ができず、性能の良い非線形制
御系を構成するのは困難であるという課題がある。
In the case of non-linear control, good control performance can be obtained by sufficiently analyzing the non-linear behavior of the control amount for each manipulated variable. However, when the control amount is a non-linear amount having an upper limit value or a lower limit value (having a saturation region) such as the degree of superheat or the degree of subcooling of the refrigeration cycle, the operation amount and the control amount shown in FIG. It is not possible to uniquely determine the manipulated variable when the controlled variable is the upper limit value and the lower limit value, unlike the points a and b of the characteristic curve indicating the relationship. Therefore, there is a problem that it is difficult to sufficiently analyze the nonlinear behavior of the controlled variable, and it is difficult to construct a nonlinear control system with good performance.

【0005】一方、PID制御方式を代表とする線形制
御では、冷凍サイクルの過熱度や過冷却度などのように
上限値あるいは下限値がある非線形な量を制御量とする
場合は、制御量が上限値および下限値になっている時と
なっていない時とでは、動特性の違いが大きすぎて良い
制御性能を得る事ができない。図3に示す操作量と制御
量の関係図から分かるように、制御量が上限値および下
限値になっているときは操作量を変更しても、制御量は
ほとんど変化しない。そのため、上限値および下限値に
なっていない時の制御量に対して、制御量が素早く目標
値に一致するようなコントローラを構成すると、制御量
が上限値および下限値になっているときには、操作量を
多少変更しても制御量には影響が現れないため、制御量
が上限値および下限値以外の目標値に一致するのにはか
なりの時間が必要になる。逆に、上限値および下限値に
なっているときの制御量に対して、制御量が素早く目標
値に一致するようなコントローラを構成すると、制御量
が少し変化しても操作量が大きく変更されるので、制御
量が上限値および下限値になっていない時には、操作量
や制御量がハンチングしてしまうなどの課題がある。
On the other hand, in the linear control typified by the PID control method, when the control amount is a non-linear amount having an upper limit value or a lower limit value such as the degree of superheat or supercooling of the refrigeration cycle, the control amount is When the upper limit value and the lower limit value are not reached, the difference in dynamic characteristics is too large to obtain good control performance. As can be seen from the relationship diagram between the manipulated variable and the controlled variable shown in FIG. 3, when the controlled variable is at the upper limit value and the lower limit value, the controlled variable hardly changes even if the manipulated variable is changed. Therefore, if you configure the controller so that the control amount quickly matches the target value for the control amount when the upper limit value and the lower limit value are not reached, the Even if the amount is changed to some extent, the controlled amount is not affected, so that it takes a considerable time for the controlled amount to match the target value other than the upper limit value and the lower limit value. Conversely, if the controller is configured so that the control amount quickly matches the target value for the control amount when the upper limit value and the lower limit value are reached, the manipulated variable will change significantly even if the control amount changes slightly. Therefore, when the control amount does not reach the upper limit value and the lower limit value, there is a problem that the operation amount and the control amount hunt.

【0006】本発明は、従来のこのような課題を考慮
し、制御量が飽和領域を有する場合でも制御対象を良好
に制御できる制御方法、制御装置、空気調和装置を提供
することを目的とするものである。
The present invention has been made in view of the above problems of the prior art, and an object of the present invention is to provide a control method, a control device, and an air conditioner capable of controlling a controlled object well even when the controlled variable has a saturated region. It is a thing.

【0007】[0007]

【課題を解決するための手段】請求項1の本発明は、制
御量が飽和領域を有する制御対象から出力される制御量
に基づいて、制御目標値を選択し、その選択された制御
目標値と制御量とを比較し、その比較結果に基づき、制
御対象の操作量を演算し、その演算された操作量によっ
て制御対象を制御する制御方法である。
According to the present invention of claim 1, a control target value is selected on the basis of a control amount output from a control object having a control amount having a saturation region, and the selected control target value is selected. And the control amount are compared, the operation amount of the control target is calculated based on the comparison result, and the control target is controlled by the calculated operation amount.

【0008】請求項4の本発明は、制御量が飽和領域を
有する制御対象から出力される制御量と所定の制御目標
値とを比較し、その比較結果に基づき、制御対象の操作
量を複数種類の演算方法により演算し、制御量を考慮し
ながら、演算された複数個の操作量に基づいて、一つの
操作量を演算し、その一つの操作量によって制御対象を
制御する制御方法である。
According to a fourth aspect of the present invention, a controlled variable output from a controlled object having a saturated control area is compared with a predetermined control target value, and a plurality of manipulated variables of the controlled object are compared based on the comparison result. This is a control method in which one operation amount is calculated based on a plurality of calculated operation amounts while performing the calculation by various kinds of operation methods and considering the control amount, and the control target is controlled by the one operation amount. .

【0009】請求項6の本発明は、制御量が飽和領域を
有する制御対象から出力される制御量に基づいて、制御
目標値を選択する目標値選択手段と、その選択された制
御目標値と制御量とを比較する比較手段と、その比較結
果に基づき、制御対象の操作量を演算する制御演算手段
とを備えた制御装置である。
According to a sixth aspect of the present invention, a target value selecting means for selecting a control target value based on a control amount output from a controlled object having a saturated control region, and the selected control target value. The control device includes a comparison unit that compares the control amount and a control calculation unit that calculates the operation amount of the control target based on the comparison result.

【0010】請求項8の本発明は、制御量が飽和領域を
有する制御対象から出力される制御量と所定の制御目標
値とを比較する比較手段と、その比較結果に基づき、制
御対象の操作量を複数種類の演算方法により演算する複
数制御演算手段と、制御量を考慮しながら、演算された
複数個の操作量に基づいて、一つの操作量を演算する操
作量演算手段とを備えた制御装置である。
According to the present invention of claim 8, a comparison means for comparing a control amount output from a control target having a saturation region of the control amount with a predetermined control target value, and an operation of the control target based on the comparison result. A plurality of control calculation means for calculating the quantity by a plurality of kinds of calculation methods and a manipulated variable calculation means for calculating one manipulated quantity based on the plurality of calculated manipulated quantities while considering the control quantity are provided. It is a control device.

【0011】請求項9の本発明は、制御量は圧縮機の吸
入過熱度であり、制御目標値は過熱度であり、操作量は
冷媒の膨張機能の膨張能力である請求項1又は2記載の
制御方法を利用した空気調和装置である。
According to the present invention of claim 9, the control amount is the suction superheat degree of the compressor, the control target value is the superheat degree, and the operation amount is the expansion capacity of the expansion function of the refrigerant. It is an air conditioner using the control method of.

【0012】[0012]

【作用】本発明は、制御量と比較する制御目標値を制御
量に基づいて選択するので、制御対象の制御量が飽和領
域又はその付近にある場合に、制御量を速やかに制御目
標値に一致させ得る操作量を演算する。
According to the present invention, the control target value to be compared with the control amount is selected based on the control amount. Therefore, when the control amount of the controlled object is in the saturation region or in the vicinity thereof, the control amount is quickly set to the control target value. The amount of operation that can be matched is calculated.

【0013】また、制御対象の操作量を複数種類の演算
方法により演算し、制御量を考慮しながら、それら操作
量に基づいて、一つの操作量を演算するので、制御対象
の制御量が飽和領域又はその付近にある場合に、制御量
を速やかに制御目標値に一致させ得る操作量を演算す
る。
Further, since the manipulated variable of the controlled object is computed by a plurality of types of computing methods and one manipulated variable is computed based on the manipulated variables while considering the controlled variables, the controlled variable of the controlled subject is saturated. When it is in the region or in the vicinity thereof, an operation amount that allows the control amount to quickly coincide with the control target value is calculated.

【0014】[0014]

【実施例】以下に、本発明をその実施例を示す図面に基
づいて説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the drawings showing its embodiments.

【0015】図1は、本発明にかかる一実施例の制御装
置(又は制御方法)の基本構成を示すブロック図、図2
は、同制御装置(又は制御方法)を用いた空気調和装置
の構成図である。すなわち、図1の制御装置は、制御量
yに基づき制御目標値を演算する第1ファジィ演算手段
1と、その演算された制御目標値rfと制御量yとを比
較する比較手段2と、その比較結果eを異なる方法で2
つの操作量UA,UBを演算する基本制御手段3A,3B
と、制御量yを考慮してそれら操作量UA,UBから一つ
の操作量Ufを演算する第2ファジィ演算手段8から構
成されている。又、操作量Ufは制御対象9に入力さ
れ、制御対象9を制御して、制御対象9から制御量yが
出力される。
FIG. 1 is a block diagram showing the basic configuration of a control device (or control method) according to an embodiment of the present invention, FIG.
FIG. 3 is a configuration diagram of an air conditioner using the same control device (or control method). That is, the control device of FIG. 1 includes first fuzzy calculation means 1 for calculating a control target value based on the control amount y, comparison means 2 for comparing the calculated control target value rf with the control amount y, and The comparison result e can be changed by 2
Basic control means 3A, 3B for calculating one manipulated variable UA, UB
And a second fuzzy computing means 8 for computing one manipulated variable Uf from these manipulated variables UA and UB in consideration of the controlled variable y. Further, the manipulated variable Uf is input to the controlled object 9, the controlled object 9 is controlled, and the controlled variable y is output from the controlled object 9.

【0016】また、図2の空気調和装置は、冷媒を圧縮
する圧縮機10と、圧縮機10の冷媒出口側に接続され
た四方弁13と、その四方弁13に接続された熱源側熱
交換器11及び利用側熱交換器12と、熱源側熱交換器
11及び利用側熱交換器12の間に接続された電子式膨
張弁14等から構成されている。又、圧縮機10の冷媒
入口部には過熱度検出手段15が設けられている。以上
の構成において、圧縮機10から吐出された高温高圧の
ガス冷媒は四方弁13(ここでは暖房時であるとし、実
線で示す接続とする)を通って、利用側熱交換器12に
入る。ここで、ガス冷媒は外気(例えば室内空気)に熱
を放出して凝縮し液冷媒になる。その後、電子式膨張弁
14で減圧されることにより気液2相になり、熱源側熱
交換器11で外気から熱を吸収して再びガス冷媒とな
り、四方弁13を通過して圧縮機10に吸入される。こ
のとき、利用側熱交換器12より熱が放出されるので、
空気調和装置は暖房運転となる。一方、四方弁13を破
線側に切り換えた場合は、冷媒の流路は逆になり、熱源
側熱交換器11で熱を外気に放出し、利用側熱交換器1
2では熱を吸収するようになるので、空気調和装置は冷
房運転となる。
The air conditioner shown in FIG. 2 has a compressor 10 for compressing a refrigerant, a four-way valve 13 connected to the refrigerant outlet side of the compressor 10, and a heat source side heat exchange connected to the four-way valve 13. It is composed of a vessel 11 and a use side heat exchanger 12, and an electronic expansion valve 14 connected between the heat source side heat exchanger 11 and the use side heat exchanger 12. Further, a superheat detection means 15 is provided at the refrigerant inlet portion of the compressor 10. In the above-described configuration, the high-temperature and high-pressure gas refrigerant discharged from the compressor 10 passes through the four-way valve 13 (here, heating is performed, and the connection is shown by a solid line), and then enters the use-side heat exchanger 12. Here, the gas refrigerant releases heat to the outside air (for example, indoor air) and condenses into a liquid refrigerant. After that, the pressure is reduced by the electronic expansion valve 14 to become a gas-liquid two phase, the heat source side heat exchanger 11 absorbs heat from the outside air and becomes a gas refrigerant again, and passes through the four-way valve 13 to the compressor 10. Inhaled. At this time, since heat is released from the use side heat exchanger 12,
The air conditioner operates in heating mode. On the other hand, when the four-way valve 13 is switched to the broken line side, the flow path of the refrigerant is reversed, and the heat source side heat exchanger 11 releases heat to the outside air, and the use side heat exchanger 1
In 2 the heat is absorbed, so the air conditioner is in cooling operation.

【0017】次に、上記実施例の動作を、図2の空気調
和装置に用いた場合について説明する。
Next, the operation of the above embodiment will be described when it is used in the air conditioner of FIG.

【0018】まず、圧縮機10の吸入口付近にある過熱
度検出手段15により圧縮機10の吸入過熱度(制御
量)を検出する(制御量の特性は図3の点線で示す曲線
を参照)。検出した過熱度(制御量)の値に応じて、第
1ファジィ演算手段1で各制御目標値riに対するメン
バーシップ値μiを演算し、どの目標値をどの程度の割
合で採用するかを(数1)に基づいて決定する。ここ
で、制御目標値r1は、通常の制御目標値よりも大きい
値に設定されており、過熱度が0deg付近(下限値で
ある飽和領域を示す)になった場合に、対応するメンバ
ーシップ値μ1が大きくなる。制御目標値r2は、通常の
制御目標値であり、過熱度が0degよりはるかに大き
い場合(本来制御すべき制御目標値)に、対応するメン
バーシップ値μ2が大きくなる。
First, the superheat detection means 15 located near the suction port of the compressor 10 detects the intake superheat (control amount) of the compressor 10 (see the curve shown by the dotted line in FIG. 3 for the characteristic of the control amount). . According to the value of the detected degree of superheat (control amount), the first fuzzy calculation means 1 calculates the membership value μ i for each control target value r i , and which target value is adopted at what ratio. It is determined based on (Equation 1). Here, the control target value r 1 is set to a value larger than the normal control target value, and when the degree of superheat becomes near 0 deg (indicating the saturation region which is the lower limit value), the corresponding membership The value μ 1 increases. The control target value r 2 is a normal control target value, and when the degree of superheat is much larger than 0 deg (the control target value to be controlled originally), the corresponding membership value μ 2 becomes large.

【0019】[0019]

【数1】rf = Σμi*ri [ 0 ≦ μi
1、i=1,2 ] rfは実際の制御に用いる目標値 μiは制御目標値riに対するメンバーシップ値 第1ファジィ演算手段1の演算結果より求められた目標
値rfと過熱度検出手段15により検出した過熱度(制
御量)とを比較手段2で比較して、制御偏差eを得る。
制御偏差eを用いて、基本制御手段3A、3Bでそれぞ
れの制御方法を用いて各操作量uA、uBを演算する。基
本制御手段3A、3Bは共にPIDコントローラを用い
ており、内部で制御偏差eを各比例演算手段4A、4
B、各積分演算かつ比例演算手段5A、5B、各微分演
算かつ比例演算手段6A、6Bに入力し、各々の演算結
果を各加算手段7A、7Bで加算して、各操作量uA
Bを決定する。そして、過熱度検出手段15で検出し
た過熱度(制御量)の値に応じて、第2ファジィ演算手
段8で各操作量に対するメンバーシップ値を演算し、ど
の操作量をどの割合で採用するかを(数2)に基づいて
決定する。ここで、基本制御手段3Aは制御量が制御目
標値に急速に一致するように構成されており、過熱度が
0deg付近になった場合に、対応するメンバーシップ
値μAが大きくなる。基本制御手段3Bは制御量が制御
目標値に緩やかに一致するように構成されており、過熱
度が0degよりはるかに大きい場合に、対応するメン
バーシップ値μBが大きくなる。
## EQU1 ## r f = Σμ i * r i [0 ≤ μ i
1, i = 1, 2] r f is a target value used in actual control μ i is a membership value with respect to the control target value r i The target value r f and the degree of superheat obtained from the calculation result of the first fuzzy calculation means 1 The comparison means 2 compares the degree of superheat (control amount) detected by the detection means 15 to obtain the control deviation e.
Using the control deviation e, the basic control means 3A, 3B calculate respective manipulated variables u A , u B by using respective control methods. Both the basic control means 3A and 3B use PID controllers, and the control deviation e is internally calculated by the proportional calculation means 4A and 4A.
B, each integral calculation and proportional calculation means 5A, 5B, each differential calculation and proportional calculation means 6A, 6B, each calculation result is added by each addition means 7A, 7B, each manipulated variable u A ,
Determine u B. Then, in accordance with the value of the degree of superheat (control amount) detected by the degree of superheat detection means 15, the second fuzzy operation means 8 calculates the membership value for each operation amount, and which operation amount is to be adopted at what ratio. Is determined based on (Equation 2). Here, the basic control means 3A is configured so that the control amount rapidly coincides with the control target value, and when the degree of superheat approaches 0 deg, the corresponding membership value μ A becomes large. The basic control means 3B is configured so that the control amount gently matches the control target value, and when the degree of superheat is much larger than 0 deg, the corresponding membership value μ B becomes large.

【0020】[0020]

【数2】uf = Σμi*ui [ 0 ≦ μi
1、i=A,B ] ufは実際の制御に用いる操作量(膨張弁開度) μiは制御目標値riに対するメンバーシップ値 第2ファジィ演算手段8の演算結果ufを電子式膨張弁
14の開度(操作量)として制御対象(空気調和装置)
9を運転する。
## EQU00002 ## u f = Σμ i * u i [0 ≤ μ i
1, i = A, B] u f is an operation amount (expansion valve opening) μ i used for actual control is a membership value with respect to a control target value r i . The calculation result u f of the second fuzzy calculation means 8 is expressed by an electronic formula. Control target (air conditioner) as the opening degree (operation amount) of the expansion valve 14
Drive 9

【0021】このような制御構成にすると、過熱度が0
deg付近になった時には制御目標値が大きくなり、ま
た、基本制御手段は制御量が制御目標値に急速に一致す
るものが選択されるため、過熱度の変化に対する電子式
膨張弁14の開度の変更量は大きくなり、過熱度は素早
く目標値に近づく。さらに、過熱度が0degより大き
くなると、制御目標値は通常の制御目標値となり、ま
た、基本制御手段は制御量が制御目標値に緩やかに一致
するものが選択されるため、過熱度の変化に対する電子
式膨張弁14の開度の変更量は小さくなり、ハンチング
することなくなめらかに過熱度を制御目標値に一致させ
ることができる。
With such a control structure, the degree of superheat is 0.
When it becomes close to deg, the control target value becomes large, and since the basic control means selects the one in which the control amount rapidly matches the control target value, the opening degree of the electronic expansion valve 14 with respect to the change in the superheat degree is selected. The change amount of becomes large, and the degree of superheat approaches the target value quickly. Further, when the degree of superheat becomes larger than 0 deg, the control target value becomes a normal control target value, and the basic control means selects the one whose control amount gently matches the control target value. The amount of change in the opening degree of the electronic expansion valve 14 is small, and the degree of superheat can be smoothly matched with the control target value without hunting.

【0022】以上のように、冷凍サイクルにおける圧縮
機10の吸入過熱度が0deg付近の場合には、コント
ローラのゲインを大きくするか、または目標値を大きく
して、制御量の変化が小さくても膨張機構の膨張能力が
大きく変更されるようにし、逆に、吸入過熱度が0de
gよりはるかに大きい場合には、コントローラのゲイン
を小さくし、通常の目標値を用いて、制御量の変化が大
きくても膨張機構の膨張能力がそれほど大きく変更され
ないようにし、その切換をファジィ論理を用いて行うこ
とにより、制御量(吸入過熱度)が上限値や下限値(0
deg)になったときでも制御量(吸入過熱度)を制御
目標値に素早くなめらかに一致させることができる。
As described above, when the intake superheat of the compressor 10 in the refrigeration cycle is near 0 deg, the controller gain may be increased or the target value may be increased to reduce the change in the control amount. The expansion capacity of the expansion mechanism is changed significantly, and conversely, the intake superheat is 0 de
When it is much larger than g, the gain of the controller is made small, and the normal target value is used so that the expansion capacity of the expansion mechanism is not changed so much even if the change of the control amount is large, and the switching is performed by the fuzzy logic. When the control amount (intake superheat degree) is set to the upper limit value or the lower limit value (0
Even when it becomes deg), the control amount (suction superheat degree) can be quickly and smoothly matched with the control target value.

【0023】さらに、外乱や運転状態に変更があった場
合でも圧縮機10の吸入過熱度が目標値に速く到達し、
長い間0degになることがなくなるので、液圧縮の可
能性も低くなり、機器の信頼性や効率を向上させること
ができる。
Further, even when there is a disturbance or a change in the operating state, the intake superheat of the compressor 10 quickly reaches the target value,
Since it does not become 0 deg for a long time, the possibility of liquid compression is reduced, and the reliability and efficiency of the device can be improved.

【0024】なお、上記実施例では、制御方法あるいは
制御装置を空気調和装置に利用する例を説明したが、こ
れに限らず、生産設備における温度や圧力などのプロセ
ス量の制御や自動車など乗り物の速度制御などに適用し
ても勿論よい。
In the above embodiment, an example in which the control method or the control device is used for the air conditioner has been described, but the present invention is not limited to this, and control of process amounts such as temperature and pressure in production equipment and vehicles such as automobiles. Of course, it may be applied to speed control or the like.

【0025】また、上記実施例では、制御目標値の変更
及び制御対象の操作量の演算にファジィ論理を用いた
が、これに限らず、例えば重みづけ演算などにより求め
るようにしてもよい。
Further, in the above embodiment, the fuzzy logic is used for changing the control target value and calculating the manipulated variable of the controlled object, but the present invention is not limited to this, and may be calculated by weighting calculation, for example.

【0026】また、上記実施例では、PID制御を用い
た2つの基本制御手段をファジィ論理で切り換え、基本
制御手段に入力される2つの制御目標値をファジィ論理
で変更する方法を用いた場合で説明したが、基本制御手
段の制御方式や数、制御目標値の数はこれに限定される
ものではない。又、基本制御手段の切り換えと制御目標
値の変更とはどちらか一方のみを用いて構成してもよ
い。
Further, in the above embodiment, the method of switching the two basic control means using the PID control by the fuzzy logic and changing the two control target values input to the basic control means by the fuzzy logic is used. Although explained, the control method and number of basic control means and the number of control target values are not limited to this. Further, only one of the switching of the basic control means and the change of the control target value may be used.

【0027】また、上記実施例では、制御量として圧縮
機の吸入過熱度を例に説明したが、これに限らず、蒸発
器出口の過熱度や凝縮器出口の過冷却度を用いても同様
な効果が得られる。
In the above embodiment, the suction superheat degree of the compressor has been described as an example of the control amount. However, the control quantity is not limited to this, and the superheat degree at the outlet of the evaporator or the supercooling degree at the outlet of the condenser is also used. Can be obtained.

【0028】また、上記実施例では、空気調和装置は1
台の熱源側熱交換器11と1台の利用側熱交換器12を
備えた1対1の空気調和装置で説明したが、これに限ら
ず、利用側熱交換器が複数台接続されたマルチエアコン
や、ダクトシステムでも同様な効果が得られることは明
かである。特に、制御方式そのものは、空気調和装置に
とどまらず生産設備における温度や圧力などのプロセス
量の制御や自動車など乗り物の速度制御などでも適用す
ることができる。
In the above embodiment, the air conditioner has one
The one-to-one air conditioner including the heat source side heat exchanger 11 and the one use side heat exchanger 12 has been described, but the present invention is not limited to this, and a plurality of use side heat exchangers are connected. It is clear that the same effect can be obtained with an air conditioner or duct system. In particular, the control method itself can be applied not only to the air conditioner, but also to control of process amounts such as temperature and pressure in production equipment and speed control of vehicles such as automobiles.

【0029】また、上記実施例では、制御装置を専用の
ハードウェアにより構成したが、同様の機能をコンピュ
ータを用いてソフトウェア的に構成してもよい。
Further, in the above embodiment, the control device is constituted by dedicated hardware, but the same function may be constituted by software using a computer.

【0030】[0030]

【発明の効果】以上述べたところから明らかなように本
発明は、制御量と比較する制御目標値を制御量に基づい
て選択し、あるいは制御対象の操作量を複数種類の演算
方法により演算し、制御量を考慮しながら、それら操作
量に基づいて、一つの操作量を演算するので、制御量が
飽和領域を有する場合でも制御対象を良好に制御できる
という長所を有する。
As is apparent from the above description, according to the present invention, the control target value to be compared with the control amount is selected based on the control amount, or the operation amount of the controlled object is calculated by a plurality of kinds of calculation methods. Since one manipulated variable is calculated based on the manipulated variables while considering the controlled variables, there is an advantage that the controlled object can be well controlled even when the controlled variable has a saturation region.

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

【図1】本発明にかかる一実施例の制御装置(又は制御
方法)の基本構成を示すブロック図である。
FIG. 1 is a block diagram showing a basic configuration of a control device (or control method) according to an embodiment of the present invention.

【図2】同実施例の制御方法を用いた空気調和装置の構
成図である。
FIG. 2 is a configuration diagram of an air conditioner using the control method of the embodiment.

【図3】制御量に上限値や下限値がある場合の操作量と
制御量の関係を示す図である。
FIG. 3 is a diagram showing a relationship between an operation amount and a control amount when the control amount has an upper limit value and a lower limit value.

【図4】従来の制御装置の構成を示すブロック図であ
る。
FIG. 4 is a block diagram showing a configuration of a conventional control device.

【符号の説明】[Explanation of symbols]

1 第1ファジィ演算手段 2 比較手段 3A、3B 基本制御手段 4A、4B 比例演算手段 5A、5B 積分演算かつ比例演算手段 6A、6B 微分演算かつ比例演算手段 7A、7B 加算手段 8 第2ファジィ演算手段 9 制御対象(空気調和装置) 10 圧縮機 11 熱源側熱交換器 12 利用側熱交換器 13 四方弁 14 電子式膨張弁 15 過熱度検出手段 DESCRIPTION OF SYMBOLS 1 1st fuzzy operation means 2 Comparing means 3A, 3B Basic control means 4A, 4B Proportional operation means 5A, 5B Integral operation and proportional operation means 6A, 6B Differential operation and proportional operation means 7A, 7B Addition means 8 2nd fuzzy operation means 9 Control target (air conditioner) 10 Compressor 11 Heat source side heat exchanger 12 Utilization side heat exchanger 13 Four-way valve 14 Electronic expansion valve 15 Superheat detection means

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中谷 和生 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazuo Nakatani 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 制御量が飽和領域を有する制御対象から
出力される制御量に基づいて、制御目標値を選択し、そ
の選択された前記制御目標値と前記制御量とを比較し、
その比較結果に基づき、前記制御対象の操作量を演算
し、その演算された操作量によって前記制御対象を制御
することを特徴とする制御方法。
1. A control target value is selected based on a control amount output from a control target whose control amount has a saturation region, and the selected control target value and the control amount are compared,
A control method comprising calculating an operation amount of the controlled object based on the comparison result, and controlling the controlled object according to the calculated operation amount.
【請求項2】 制御目標値の選択は、ファジィ論理を用
いて行うことを特徴とする請求項1記載の制御方法。
2. The control method according to claim 1, wherein the control target value is selected by using fuzzy logic.
【請求項3】 制御量が飽和領域を有する制御対象から
出力される制御量に基づいて、前記制御量が前記飽和領
域又はその付近のときに、制御目標値を所定の制御目標
値から変更し、その変更された前記制御目標値と前記制
御量とを比較し、その比較結果に基づき、前記制御対象
の操作量を演算し、その演算された操作量によって前記
制御対象を制御することを特徴とする制御方法。
3. The control target value is changed from a predetermined control target value when the control amount is at or near the saturation region, based on the control amount output from a controlled object having a saturation region. Comparing the changed control target value and the control amount, calculating an operation amount of the control target based on the comparison result, and controlling the control target by the calculated operation amount. And control method.
【請求項4】 制御量が飽和領域を有する制御対象から
出力される制御量と所定の制御目標値とを比較し、その
比較結果に基づき、前記制御対象の操作量を複数種類の
演算方法により演算し、前記制御量を考慮しながら、前
記演算された複数個の操作量に基づいて、一つの操作量
を演算し、その一つの操作量によって前記制御対象を制
御することを特徴とする制御方法。
4. A control amount output from a control target having a saturation region of control amount is compared with a predetermined control target value, and the operation amount of the control target is calculated by a plurality of types of calculation methods based on the comparison result. A control characterized by calculating one operation amount based on the calculated plurality of operation amounts while considering the control amount, and controlling the control target by the one operation amount. Method.
【請求項5】 一つの操作量の演算は、ファジィ論理を
用いて行うことを特徴とする請求項4記載の制御方法。
5. The control method according to claim 4, wherein the calculation of one operation amount is performed by using fuzzy logic.
【請求項6】 制御量が飽和領域を有する制御対象から
出力される制御量に基づいて、制御目標値を選択する目
標値選択手段と、その選択された前記制御目標値と前記
制御量とを比較する比較手段と、その比較結果に基づ
き、前記制御対象の操作量を演算する制御演算手段とを
備えたことを特徴とする制御装置。
6. A target value selecting means for selecting a control target value based on a control amount output from a control target having a control area having a saturation region, and the selected control target value and control amount. A control device comprising: comparing means for comparing; and control calculating means for calculating an operation amount of the controlled object based on the comparison result.
【請求項7】 制御量が飽和領域を有する制御対象から
出力される制御量に基づいて、前記制御量が前記飽和領
域又はその付近のときに、制御目標値を所定の制御目標
値から変更する目標値変更手段と、その変更された前記
制御目標値と前記制御量とを比較する比較手段と、その
比較結果に基づき、前記制御対象の操作量を演算する制
御演算手段とを備えたことを特徴とする制御装置。
7. The control target value is changed from a predetermined control target value when the control amount is at or near the saturation region, based on the control amount output from a controlled object having a saturation region. A target value changing means, a comparing means for comparing the changed control target value with the control amount, and a control calculating means for calculating an operation amount of the controlled object based on the comparison result. Characteristic control device.
【請求項8】 制御量が飽和領域を有する制御対象から
出力される制御量と所定の制御目標値とを比較する比較
手段と、その比較結果に基づき、前記制御対象の操作量
を複数種類の演算方法により演算する複数制御演算手段
と、前記制御量を考慮しながら、前記演算された複数個
の操作量に基づいて、一つの操作量を演算する操作量演
算手段とを備えたことを特徴とする制御装置。
8. A comparison means for comparing a control amount output from a control target having a control amount with a saturation region with a predetermined control target value, and a plurality of operation amounts of the control target based on the comparison result. A plurality of control calculation means for calculating by a calculation method, and an operation amount calculation means for calculating one operation amount based on the plurality of calculated operation amounts while considering the control amount. Control device.
【請求項9】 制御量は圧縮機の吸入過熱度であり、前
記制御目標値は過熱度であり、前記操作量は冷媒の膨張
機能の膨張能力である請求項1又は4記載の制御方法を
利用したことを特徴とする空気調和装置。
9. The control method according to claim 1, wherein the control amount is a suction superheat degree of the compressor, the control target value is a superheat degree, and the operation amount is an expansion capacity of the expansion function of the refrigerant. An air conditioner characterized by being used.
JP4178388A 1992-07-06 1992-07-06 Control method and control device for air conditioner Pending JPH0618100A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4178388A JPH0618100A (en) 1992-07-06 1992-07-06 Control method and control device for air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4178388A JPH0618100A (en) 1992-07-06 1992-07-06 Control method and control device for air conditioner

Publications (1)

Publication Number Publication Date
JPH0618100A true JPH0618100A (en) 1994-01-25

Family

ID=16047625

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4178388A Pending JPH0618100A (en) 1992-07-06 1992-07-06 Control method and control device for air conditioner

Country Status (1)

Country Link
JP (1) JPH0618100A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990007250A1 (en) * 1988-12-13 1990-06-28 Science & Tec Microphone with interferometric detection of acoustic pressure
WO2009004780A1 (en) * 2007-06-29 2009-01-08 Daikin Industries, Ltd. Freezing apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990007250A1 (en) * 1988-12-13 1990-06-28 Science & Tec Microphone with interferometric detection of acoustic pressure
WO2009004780A1 (en) * 2007-06-29 2009-01-08 Daikin Industries, Ltd. Freezing apparatus
JP2009014212A (en) * 2007-06-29 2009-01-22 Daikin Ind Ltd Refrigerating device
AU2008272384B2 (en) * 2007-06-29 2011-01-27 Daikin Industries, Ltd. Refrigeration system

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