JP3039941B2 - Refrigeration equipment - Google Patents
Refrigeration equipmentInfo
- Publication number
- JP3039941B2 JP3039941B2 JP1321434A JP32143489A JP3039941B2 JP 3039941 B2 JP3039941 B2 JP 3039941B2 JP 1321434 A JP1321434 A JP 1321434A JP 32143489 A JP32143489 A JP 32143489A JP 3039941 B2 JP3039941 B2 JP 3039941B2
- Authority
- JP
- Japan
- Prior art keywords
- expansion valve
- control
- refrigerant
- degree
- electric expansion
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2600/00—Control issues
- F25B2600/21—Refrigerant outlet evaporator temperature
Landscapes
- Air Conditioning Control Device (AREA)
- Feedback Control In General (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、冷凍装置に係り、特に幅広い運転範囲にわ
たつて安定した冷媒流量制御を行うために好適な冷凍装
置に関する。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigeration system, and more particularly to a refrigeration system suitable for performing stable refrigerant flow control over a wide operating range.
従来の装置は、特開昭56−44569号公報に記載のよう
に、冷凍サイクルの蒸発器の冷媒過熱度を、電動膨張弁
の弁開度をPI制御(比例+積分動作)によつて制御する
構成となつていた。As described in JP-A-56-44569, a conventional apparatus controls the degree of superheat of refrigerant in an evaporator of a refrigeration cycle by PI control (proportional + integral operation) of a valve opening of an electric expansion valve. Configuration.
近年、冷凍装置における電子化技術の導入スピードは
目ざましいものがあり、インバータ制御圧縮機,電動膨
張弁等の採用により、冷凍装置の運転範囲は大きく広が
りつつある。特に、電動膨張弁による冷媒制御は、液戻
り防止,過度な冷媒の過熱防止、および性能向上を図る
うえで、重要である。In recent years, the introduction speed of the computerization technology in the refrigerating apparatus has been remarkable, and the operation range of the refrigerating apparatus has been greatly expanded by adopting an inverter control compressor, an electric expansion valve and the like. In particular, refrigerant control by an electric expansion valve is important for preventing liquid return, preventing excessive refrigerant overheating, and improving performance.
しかしながら、従来における膨張弁の制御方式として
は、温度膨張弁に代表されるように、現状の蒸発器の過
熱度の信号のみに基づく比例制御や、前記従来技術のよ
うに、蒸発器の過熱度と、過熱度の時間変化に基づいた
PI制御,PID制御(比例+積分+微分動作に基づく制御)
が用いられていた。これらの制御方式では、数式を用い
て制御を行うため、対象とする冷媒過熱度の動的な特性
の正確な情報を必要とし、この情報の正確度によつて制
御が良好に行えるか、どうかが決まつてくる。冷凍装置
の運転が広い範囲で行われると、冷媒過熱度の動的な特
性も大きく変化するため、従来技術で良好な制御を行う
ためには、PI制御の制御定数を、種々の運転状況に応じ
て切り換えることが必要となる。実際には、制御が非常
に複雑となるため、前記従来技術は実用的ではなく、実
際には制御性の不十分さを認めているのが現状である。However, as a conventional expansion valve control method, as represented by a temperature expansion valve, a proportional control based only on a current evaporator superheat degree signal or a superheat degree of an evaporator And the degree of superheat over time
PI control, PID control (control based on proportional + integral + differential operation)
Was used. In these control methods, since control is performed using mathematical formulas, accurate information on the dynamic characteristics of the target superheat degree of the refrigerant is required, and whether the control can be properly performed based on the accuracy of this information is required. Will be decided. When the operation of the refrigeration system is performed over a wide range, the dynamic characteristics of the refrigerant superheat greatly change.Therefore, in order to perform good control with the conventional technology, the control constant of PI control must be adjusted to various operating conditions. It is necessary to switch accordingly. Actually, since the control becomes very complicated, the above-mentioned conventional technology is not practical, and in reality, the present situation recognizes that controllability is insufficient.
本発明の目的は、電動膨張弁の制御を冷媒過熱度の状
態を表す情報と、この情報に関する経験則から求めた制
御ルールに基づいて行い、幅広い運転範囲にわたつて、
安定した冷媒流量制御を行い得る冷凍装置を提供するこ
とにある。An object of the present invention is to control an electric expansion valve based on information indicating a state of a refrigerant superheat degree and a control rule obtained from an empirical rule regarding this information, and over a wide operating range,
An object of the present invention is to provide a refrigeration apparatus capable of performing stable refrigerant flow control.
前記目的を達成するため、本発明は冷凍サイクル中の
冷媒温度差を検知する検知手段と、冷媒温度差の情報に
対応させて、経験則に基づき電動膨張弁の開度操作量に
関する制御ルールを記憶したメモリ装置と、前記検知手
段から冷媒温度差に関する情報を取り込み、前記メモリ
装置から前記情報に対応する制御ルールを取り込み、電
動膨張弁の開度操作量を演算して出力するフアジー推論
プロセツサとを有する制御装置を配備したものである。In order to achieve the above object, the present invention provides a detecting means for detecting a refrigerant temperature difference during a refrigeration cycle, and a control rule relating to the opening degree operation amount of the electric expansion valve based on an empirical rule corresponding to the information of the refrigerant temperature difference. A memory device, and a fuzzy inference processor that fetches information about a refrigerant temperature difference from the detection unit, fetches a control rule corresponding to the information from the memory device, calculates and outputs an operation amount of opening of an electric expansion valve. A control device having the following is provided.
本発明では、冷媒温度差の検知手段により、冷凍サイ
クル中の冷媒温度差を検知する。In the present invention, the refrigerant temperature difference detecting means detects the refrigerant temperature difference in the refrigeration cycle.
一方、制御装置のメモリ装置には、冷媒温度差の情報
に対応させて、経験則に基づき電動膨張弁の開度操作量
に関する制御ルールを予め記憶させておく。On the other hand, in the memory device of the control device, a control rule relating to the opening degree operation amount of the electric expansion valve is stored in advance based on an empirical rule in association with the information of the refrigerant temperature difference.
そこで、制御装置のフアジー推論プロセツサでは、前
記検知手段から冷媒温度差に関する情報を取り込み、前
記メモリ装置から前記情報に対応する制御ルールを取り
込むみ、この二つから電動膨張弁に与える開度操作量を
演算し、出力する。Therefore, the fuzzy inference processor of the control device fetches information on the refrigerant temperature difference from the detection means and fetches a control rule corresponding to the information from the memory device. Is calculated and output.
したがつて、本発明によれば、冷媒過熱度の変化状況
に応じて、経験則から求めた制御ルールに基づいて、電
動膨張弁の開度操作量を算出できるので、幅広い運転範
囲にわたつて安定した冷媒流量制御が可能となる。Therefore, according to the present invention, it is possible to calculate the opening operation amount of the electric expansion valve based on the control rule obtained from the empirical rule according to the change state of the refrigerant superheat degree, and therefore, over a wide operating range. Stable refrigerant flow control is possible.
以下、本発明の実施例を図面により説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.
第1図は本発明の第1の実施例を時す系統図、第2図
および第3図はフアジー推論における制御ルールおよび
制御状況想定図、第4図(a)〜(c)はフアジー推論
におけるメンバシツプ関数を示す図である。1 is a system diagram showing a first embodiment of the present invention, FIGS. 2 and 3 are control rule and control situation assumption diagrams in fuzzy inference, and FIGS. 4 (a) to 4 (c) are fuzzy inferences. FIG. 6 is a diagram showing a membership function in FIG.
その第1図に示す第1の実施例の冷凍装置は、圧縮機
1と、凝縮器2と、凝縮器用送風機2′と、電動膨張弁
3と、蒸発器4と、蒸発器用送風機4′と、制御装置5
と、蒸発器出口冷媒温度を検知するセンサ6と、蒸発器
入口冷媒温度を検知するセンサ7とを備えて構成されて
いる。The refrigerating apparatus of the first embodiment shown in FIG. 1 comprises a compressor 1, a condenser 2, a condenser blower 2 ', an electric expansion valve 3, an evaporator 4, and an evaporator blower 4'. , Control device 5
And a sensor 6 for detecting the evaporator outlet refrigerant temperature, and a sensor 7 for detecting the evaporator inlet refrigerant temperature.
この実施例では、冷凍サイクル中の温度差のうち、セ
ンサ6および7によつて検知される蒸発器出入口温度
差、すなわち蒸発器冷媒過熱度が適正となるように、制
御装置5によつて、電動膨張弁3の開度を制御するよう
にしている。蒸発器4の過熱度を検知する手段として
は、蒸発器入口冷媒温度のセンサ7の代わりに、圧力セ
ンサを用いて冷媒の飽和温度を検知して、過熱度を求め
る手段もある。In this embodiment, among the temperature differences during the refrigeration cycle, the controller 5 controls the evaporator inlet / outlet temperature difference detected by the sensors 6 and 7, that is, the evaporator refrigerant superheat degree to be appropriate. The opening of the electric expansion valve 3 is controlled. As means for detecting the degree of superheat of the evaporator 4, there is also means for detecting the saturation temperature of the refrigerant by using a pressure sensor instead of the sensor 7 for the refrigerant temperature at the evaporator inlet to obtain the degree of superheat.
前記制御装置5は、冷媒温度差設定器8と、温度差演
算器9と、フアジー推論プロセツサ10と、制御ルールの
メモリ装置11と、膨張弁制御器12とを有して構成されて
いる。The controller 5 includes a refrigerant temperature difference setting device 8, a temperature difference calculator 9, a fuzzy inference processor 10, a control rule memory device 11, and an expansion valve controller 12.
このような構成において、冷凍装置の運転中は一定時
間毎に、センサ6および7からの検知信号は、冷媒温度
差演算器9に取り込まれ、蒸発器冷媒過熱度が算出され
るとともに、冷媒温度差設定器8から入力される過熱度
設定値との偏差、および偏差の時刻変化が演算される。
これらの情報を基に電動膨張弁3の開度操作量を求める
フアジー推論は、メモリ装置11に記憶された次のような
制御ルールを基にして実行される。すなわち、 R1:もし冷媒過熱度の偏差eが負で大きく、偏差の時間
変化Δeがゼロであれば、電動膨張弁の開度を大きく閉
める。In such a configuration, the detection signals from the sensors 6 and 7 are taken into the refrigerant temperature difference calculator 9 at regular intervals during the operation of the refrigeration system, and the evaporator refrigerant superheat degree is calculated and the refrigerant temperature is calculated. The deviation from the superheat degree set value input from the difference setting unit 8 and the time change of the deviation are calculated.
The fuzzy inference for obtaining the opening operation amount of the electric expansion valve 3 based on these pieces of information is executed based on the following control rules stored in the memory device 11. That is, R1: If the deviation e of the refrigerant superheat degree is negative and large and the time change Δe of the deviation is zero, the opening of the electric expansion valve is largely closed.
R2:もし冷媒過熱度の偏差eがゼロで、偏差の時間変化
Δeが正で大きければ、電動膨張弁の開度を大きく開け
る。R2: If the deviation e of the refrigerant superheat degree is zero and the time change Δe of the deviation is positive and large, the opening of the electric expansion valve is greatly opened.
R3:もし冷媒過熱度の偏差eが正で大きく、偏差の時間
変化Δeがゼロであれば、電動膨張弁の開度を大きく開
ける。R3: If the deviation e of the refrigerant superheat degree is positive and large and the time change Δe of the deviation is zero, the opening of the electric expansion valve is greatly opened.
R4:……等である。R4: ... and so on.
前記制御ルールは、経験則から求めた電動膨張弁の開
度を変化させて、冷媒過熱度を設定値に制御するための
ルールであり、表の形でまとめて示すと第2図のように
なる。The control rule is a rule for controlling the degree of superheat of the refrigerant to a set value by changing the opening degree of the electric expansion valve obtained from an empirical rule, and is shown in a table as shown in FIG. Become.
第2図中で、記号はPB:正で大きい,PM:正で中程度,P
S:正で小さい,ZO:ゼロ,NS:負で小さい,NM:負の中程度,N
B:負で大きい、を示している。また、eは冷媒過熱度の
偏差,Δeは冷媒過熱度の偏差の時間変化を示してお
り、たとえば前記ルール1(R1:)では、e=NBで、Δ
e=ZOならば、電動膨張弁の開度変化ΔU=NBとするこ
とを表している。In FIG. 2, the symbols are PB: positive and large, PM: positive and medium, P
S: Positive and small, ZO: Zero, NS: Negative and small, NM: Negative medium, N
B: Negative and large. Further, e indicates a deviation of the refrigerant superheat degree, and Δe indicates a time change of the deviation of the refrigerant superheat degree. For example, in the rule 1 (R1 :), e = NB and Δe
If e = ZO, it indicates that the change in the opening degree of the electric expansion valve is ΔU = NB.
第3図は冷媒過熱度の偏差eを0に制御する状態を表
しており、図中に示した1〜13までの番号はこの状態の
時に適用する制御ルールの番号を示しており、第2図中
の番号に対応している。FIG. 3 shows a state in which the deviation e of the refrigerant superheat degree is controlled to 0, and the numbers 1 to 13 shown in the figure show the numbers of the control rules applied in this state. It corresponds to the numbers in the figure.
前記制御ルールは、冷媒過熱度の偏差e,冷媒過熱度の
偏差の時間変化Δe,電動膨張弁の開度変化ΔUの関係を
第2図のように段階的に定めてあるので、きめ細かい制
御を行う場合には、前記冷媒過熱度の偏差eおよび偏差
の時間変化Δeの中間値では、前記制御ルールの前件部
(IF部)をどの程度満たしているかの度合を算出して、
その度合に応じた電動膨張弁の開度を推定する必要があ
る。そのため、フアジー推論プロセツサ10においては、
前記度合を、冷媒過熱度の偏差eおよび偏差の時間変化
Δe,電動膨張弁の開度変化ΔUに対するフアジー変数の
メンバシツプ関数を利用して算出する。Since the control rule defines the relationship between the refrigerant superheat degree deviation e, the time change Δe of the refrigerant superheat degree deviation and the opening degree change ΔU of the electric expansion valve stepwise as shown in FIG. 2, fine control is performed. When performing, the degree of the degree of satisfaction of the antecedent part (IF part) of the control rule is calculated by the intermediate value of the deviation e of the refrigerant superheat degree and the time change Δe of the deviation,
It is necessary to estimate the opening degree of the electric expansion valve according to the degree. Therefore, in the fuzzy inference processor 10,
The degree is calculated using a membership function of a fuzzy variable with respect to the deviation e of the refrigerant superheat degree, the time change Δe of the deviation, and the opening change ΔU of the electric expansion valve.
第4図(a)は冷媒過熱度の偏差eに対するフアジー
変数EPB,EPM,EPS,EZO,ENS,ENM,ENBのメンバシツプ関数
μEPB(e),μEPM(e),μEPS(e),μEZO
(e),μENS(e),μENM(e),μENB(e)を示
したものであり、第4図(b)は冷媒過熱度の偏差の時
間変化Δeに対するフアジー変数E′PB,E′PM,E′PS,
E′ZO,E′NS,E′NM,E′NBのメンバシツプ関数μE′PB
(Δe),μE′PM(Δe),μE′PS(Δe),μ
E′ZO(Δe),μE′NS(Δe),μE′NM(Δ
e),μE′NB(Δe)を示したものである。第4図
(c)は電動膨張弁の開度変化ΔUに対するフアジー変
数UPB,UPM,UPS,UZO,UNS,UNM,UNBのメンバシツプ関数μU
PB(ΔU),μUPM(ΔU),μUPS(ΔU),μUZO
(ΔU),μUNS(ΔU),μUNM(ΔU),μUNB(Δ
U)を示したものである。FIG. 4A shows the membership functions μEPB (e), μEPM (e), μEPS (e), μEZO of the fuzzy variables EPB, EPM, EPS, EZO, ENS, ENM, ENB with respect to the deviation e of the refrigerant superheat degree.
4 (e), μENS (e), μENM (e), μENB (e). FIG. 4 (b) shows a fuzzy variable E′PB, E ′ with respect to a time change Δe of the deviation of the refrigerant superheat degree. PM, E′PS,
Membership functions μE'PB of E'ZO, E'NS, E'NM, E'NB
(Δe), μE′PM (Δe), μE′PS (Δe), μ
E′ZO (Δe), μE′NS (Δe), μE′NM (Δ
e), μE′NB (Δe). FIG. 4 (c) shows the membership function μU of the fuzzy variables UPB, UPM, UPS, UZO, UNS, UNM and UNB with respect to the change ΔU of the opening of the electric expansion valve.
PB (ΔU), μUPM (ΔU), μUPS (ΔU), μUZO
(ΔU), μUNS (ΔU), μUNM (ΔU), μUNB (Δ
U).
第1図に示すフアジー推論プロセツサ10で実行するフ
アジー推論は、前記制御ルールR1〜R13と第4図
(a),(b),(c)のメンバシツプ関数とを用いて
フアジー推論演算を行つて、電動膨張弁の開度操作量の
演算を行う。The fuzzy inference executed by the fuzzy inference processor 10 shown in FIG. 1 is performed by performing a fuzzy inference operation using the control rules R1 to R13 and the membership functions of FIGS. 4 (a), (b) and (c). Then, the operation amount of the opening degree of the electric expansion valve is calculated.
以下に推論の手順を示す。 The procedure of inference is shown below.
ステツプ1: 冷媒過熱度の偏差eおよび冷媒過熱度の偏差の時間変
化Δeに対するメンバシツプ関数を用いて、検知された
冷媒過熱度の偏差eおよび偏差の時間変化Δeのメンバ
シツプ値の算出を行う。Step 1: Using the membership function for the deviation e of the refrigerant superheat degree and the time change Δe of the deviation of the refrigerant superheat degree, the detected membership e of the deviation e of the refrigerant superheat degree and the temporal change Δe of the deviation are calculated.
ステツプ2: ステツプ1で得られた冷媒過熱度の偏差eおよび偏差
の時間変化Δeのメンバシツプ値が、前記13の各制御ル
ールの前件部をどの程度満たしているかの度合を次のよ
うにフアジー論理積で算出する。Step 2: The degree to which the membership values of the deviation e of the refrigerant superheat degree and the time change Δe of the deviation obtained in Step 1 satisfy the antecedents of the above-mentioned 13 control rules is as follows. Calculate with AND.
R1:W1=μENB(e)∧μE′ZO(Δe) =MIN{μNB(e),μE′ZO(Δe)}…(1) R2:W2=μEZO(e)∧μE′PB(Δe) =MIN{μEZO(e),μE′PB(Δe)} …(2) …… 式(1)は、冷媒過熱度の偏差eがENBに入る割合と
偏差の時間変化ΔeがE′ZOに入る割合のうち、小さい
値としての割合で成立することを示している。つまり、
冷媒過熱度の偏差がeで、偏差の時間変化がΔeの時、
制御ルールR1の前件部は、W1の割合で成立することを示
している。R1: W 1 = μENB (e) ∧μE'ZO (Δe) = MIN {μNB (e), μE'ZO (Δe)} ... (1) R2: W 2 = μEZO (e) ∧μE'PB (Δe ) = MIN {μEZO (e), μE′PB (Δe)} (2) Equation (1) shows that the ratio of the deviation e of the refrigerant superheat degree into the ENB and the time change Δe of the deviation become E′ZO. This indicates that the ratio is satisfied as a small value among the ratios included. That is,
When the deviation of the refrigerant superheat degree is e and the time change of the deviation is Δe,
Antecedent of control rules R1 shows that established at a rate of W 1.
式(2)についても同様に、制御ルールR2がW2の割合
で成立することを示している。Similarly, the equation (2) shows that the control rule R2 is established in a ratio of W 2.
ステツプ3: 一つの制御ルールの前件部が割合Wnで成立すれば、そ
の制御ルールの実行部(THEN部)もWnの割合で成立する
ので、各制御ルール毎の前件部が成立する割合Wnを実行
部におけるフアジー変数(UPB,UPM,UPS,UZO,UNS,UNM,UN
B)のメンバシツプ関数に乗じて、実行部のメンバシツ
プ関数の修正を次のように行う。Step 3: if satisfied with the antecedents proportion W n of one control rule, therefore established at a rate of execution unit (THEN part) is also W n of the control rules, established antecedent of each control rule Fuaji variable in the execution unit the ratio W n to (UPB, UPM, UPS, UZO , UNS, UNM, UN
The membership function of the execution unit is modified by multiplying the membership function of B) as follows.
R1:μUNB*(C)=W1×μUNB(C) R2:μUPB*(C)=W2×μUPB(C) …… ステツプ4: ステツプ3で修正された制御ルールの実行部のメンバ
シツプ関数によつて、検出された冷媒過熱度の偏差e、
偏差の時間変化Δeに対する電動膨張弁の開度操作量の
総合メンバシツプ関数は、以下のように論理和の形で求
められる。R1: μUNB * (C) = W 1 × μUNB (C) R2: μUPB * (C) = W 2 × μUPB (C) ...... step 4: Menbashitsupu function executing unit of the modified control rules in step 3 Thus, the deviation e of the detected superheat degree of the refrigerant,
The total membership function of the opening degree operation amount of the electric expansion valve with respect to the time change Δe of the deviation is obtained in the form of a logical sum as follows.
μ*(C)=μUNB*(C)UμNM*(C)U… …UμPB*(C) …(3) 式(3)は、電動膨張弁の各開度に対する発生度合
を、電動膨張弁の開度に対する関数として表したもので
ある。μ * (C) = μUNB * (C) UμNM * (C) U... UμPB * (C) (3) Equation (3) shows the degree of occurrence for each opening of the electric expansion valve. It is expressed as a function of the opening.
ステツプ5: 総合メンバシツプ関数のフアジー変数の電動膨張弁の
開度を総合メンバシツプ関数に属す度合で重み付け平均
することによつて、電動膨張弁の開度操作量C*を求め
る。Step 5: The degree of opening of the electric expansion valve, which is a fuzzy variable of the total membership function, is weighted and averaged based on the degree of belonging to the total membership function, thereby obtaining the opening operation amount C * of the electric expansion valve.
C*=∫C×μ*(C)dC/∫μ*(C)dC 前述のようにステツプ1〜ステツプ5までのフアジー
推論により求められた電動膨張弁の開度操作量が、膨張
弁制御器12を通じて、電動膨張弁3に出力される。C * = ΔC × μ * (C) dC / Δμ * (C) dC As described above, the opening operation amount of the electric expansion valve obtained by the fuzzy inference from step 1 to step 5 is determined by the expansion valve control. Is output to the electric expansion valve 3 through the device 12.
この第1の実施例では、第4図(a)〜(c)に示す
ような冗長性のあるメンバシツプ関数と、経験則に基づ
いて得られた制御ルールを用いて、冷媒過熱度の制御を
行うことができるので、運転条件が変化しても制御の結
果が変わることはなく、幅広い運転範囲にわたつて安定
した冷媒流量制御を行うことができる結果、冷媒装置の
性能向上と信頼性向上を図り得る効果がある。In the first embodiment, the control of the degree of superheat of the refrigerant is performed using a redundant membership function as shown in FIGS. 4 (a) to 4 (c) and a control rule obtained based on empirical rules. As a result, even if the operating conditions change, the control result does not change, and stable refrigerant flow rate control can be performed over a wide operating range, thereby improving the performance and reliability of the refrigerant device. There is a plausible effect.
次に、第5図は本発明の第2の実施例を示す系統図で
ある。Next, FIG. 5 is a system diagram showing a second embodiment of the present invention.
この第2の実施例では、センサ6′は圧縮機1の出口
の吐出配管に取り付けられており、他のセンサ7′は凝
縮器2の出口部に取り付けられており、吐出ガス冷媒過
熱度を設定値に制御する構成となつている。In this second embodiment, the sensor 6 'is attached to the discharge pipe at the outlet of the compressor 1, and the other sensor 7' is attached to the outlet of the condenser 2 to determine the degree of superheat of the discharged gas refrigerant. It is configured to control to the set value.
この第2の実施例において、フアジー推論等、他の構
成は第1の実施例と全く同様である。なお、吐出ガス冷
媒過熱度をさらに正確に検知するためには、センサ7′
を圧力センサとし、高圧側の圧力を検知して飽和温度に
変換してから、吐出ガス冷媒過熱度を算出するようにす
ればよい。In the second embodiment, other configurations such as fuzzy inference are exactly the same as those in the first embodiment. In order to more accurately detect the degree of superheat of the discharged gas refrigerant, the sensor 7 '
May be used as a pressure sensor, the pressure on the high pressure side may be detected and converted to the saturation temperature, and then the superheat degree of the discharged gas refrigerant may be calculated.
この第2の実施例の場合には、吐出ガス冷媒過熱度を
設定値に制御できるため、特に冷凍装置の信頼性向上を
図り得る効果がある。In the case of the second embodiment, since the superheat degree of the discharge gas refrigerant can be controlled to the set value, there is an effect that the reliability of the refrigerating apparatus can be particularly improved.
ついで、第6図は本発明の第3の実施例を示す系統図
である。FIG. 6 is a system diagram showing a third embodiment of the present invention.
この第3の実施例では、センサ6″は凝縮器2の中間
部に設けられており、凝縮温度を検知する構成となつて
いる。一方、センサ7″は凝縮器2の出口に設けられて
おり、過冷却した液冷媒の温度を検知する構成となつて
いる。これら二つのセンサ6″,7″によつて検知された
温度より、凝縮器2での冷媒過冷却度が求められ、この
第3の実施例では冷媒過冷却度が設定値に保たれる。In the third embodiment, the sensor 6 "is provided at an intermediate portion of the condenser 2 to detect the condensing temperature. On the other hand, the sensor 7" is provided at the outlet of the condenser 2. Thus, the temperature of the supercooled liquid refrigerant is detected. From the temperatures detected by these two sensors 6 ", 7", the degree of subcooling of the refrigerant in the condenser 2 is obtained, and in the third embodiment, the degree of subcooling of the refrigerant is maintained at a set value.
前記第2の実施例と同様に、センサ6″に圧力センサ
を用いれば、さらに正確に冷媒過冷却度を検知すること
ができる。As in the second embodiment, if a pressure sensor is used as the sensor 6 ", the degree of subcooling of the refrigerant can be detected more accurately.
この第3の実施例では、凝縮器2の過冷却度を制御す
るので、冷凍装置の高圧圧力の過度の上昇を防止できる
とともに、電動膨張弁3の上流側を常に液冷媒の状態に
して、定圧側への安定した冷媒供給を確保できるので、
よい一層信頼性向上と性能向上の効果が期待できる。In the third embodiment, since the degree of supercooling of the condenser 2 is controlled, it is possible to prevent an excessive increase in the high pressure of the refrigerating apparatus, and to always keep the upstream side of the electric expansion valve 3 in a liquid refrigerant state. Since stable refrigerant supply to the constant pressure side can be secured,
The effects of better reliability and performance can be expected.
以上の各実施例では、冷媒温度差を設定値として制御
することを説明したが、この設定値は一定値でなくとも
よく、他の冷凍装置の信号に連動して変化するものであ
つてもよい。In each of the embodiments described above, the refrigerant temperature difference is controlled as a set value. However, the set value may not be a constant value, and may be changed in conjunction with a signal of another refrigeration apparatus. Good.
続いて、第7図は本発明の第4の実施例を示す系統
図、第8図は第4の実施例における制御ルールのメモリ
装置の内容を示す説明図である。Next, FIG. 7 is a system diagram showing a fourth embodiment of the present invention, and FIG. 8 is an explanatory diagram showing the contents of a control rule memory device in the fourth embodiment.
この第4の実施例において、第1図,第5図に示す第
1,第2の実施例と同じ部分には同じ符号を付けて示して
いる。In the fourth embodiment, the third embodiment shown in FIGS.
1, the same parts as those in the second embodiment are denoted by the same reference numerals.
この第4の実施例では、制御装置5の他に、もう一つ
の制御装置5′を備えて構成されている。In the fourth embodiment, in addition to the control device 5, another control device 5 'is provided.
その制御装置5′は、前記制御装置5′と同様、冷媒
温度差設定器8′と、温度差演算器9′と、フアジー推
論プロセツサ10′と、制御ルールのメモリ装置11′と、
膨張弁制御器12′とを有して構成されている。前記温度
差演算器9′には、圧縮機1の出口の吐出配管に取り付
けられたセンサ6′と、凝縮器2の出口部に取り付けら
れたセンサ7′とが接続されている。The controller 5 'includes a refrigerant temperature difference setting device 8', a temperature difference calculator 9 ', a fuzzy inference processor 10', a control rule memory device 11 ', and a control rule memory device 11'.
And an expansion valve controller 12 '. The temperature difference calculator 9 ′ is connected to a sensor 6 ′ attached to the discharge pipe at the outlet of the compressor 1 and a sensor 7 ′ attached to the outlet of the condenser 2.
また、前記制御装置5,5′の膨張弁制御器12,12′は、
別設置のフアジー推論プロセツサ16に接続されている。
さらに、このフアジー推論プロセツサ16には、前記セン
サ6′と、別設置の制御ルールのメモリ装置15および膨
張弁制御器17とが接続されている。そして、前記膨張弁
制御器17は、電動膨張弁3に接続されている。Further, the expansion valve controllers 12, 12 'of the control devices 5, 5'
It is connected to a separately installed fuzzy inference processor 16.
Further, the fuzzy inference processor 16 is connected to the sensor 6 ', a memory device 15 for separately installed control rules, and an expansion valve controller 17. The expansion valve controller 17 is connected to the electric expansion valve 3.
この第4の実施例では、制御装置5は蒸発器過熱度制
御のための制御部であり、蒸発器出入口温度を検知する
センサ6,7の検知信号を受け取り、前記第1の実施例の
ようにフアジー推論により、膨張弁制御器12から膨張弁
操作信号13が出力される。また、制御装置5′は吐出ガ
ス過熱度のための制御器であり、吐出ガス温度を検知す
るセンサ6′と、凝縮液温度を検知するセンサ7′から
検知信号を受け取り、フアジー推論プロセツサ10′で制
御装置5のフアジー推論プロセツサ10と同様の演算を行
い、膨張弁制御器12′から膨張弁操作信号13′が出力さ
れる。In the fourth embodiment, the control device 5 is a control unit for controlling the degree of superheat of the evaporator, and receives the detection signals of the sensors 6 and 7 for detecting the inlet and outlet temperatures of the evaporator, as in the first embodiment. The expansion valve operation signal 13 is output from the expansion valve controller 12 by fuzzy inference. The control device 5 'is a controller for the degree of superheat of the discharge gas. The control device 5' receives a detection signal from a sensor 6 'for detecting the discharge gas temperature and a sensor 7' for detecting the condensate temperature, and receives a fuzzy inference processor 10 '. The same operation as that of the fuzzy inference processor 10 of the control device 5 is performed, and an expansion valve operation signal 13 'is output from the expansion valve controller 12'.
この第4の実施例で新たに組み込まれているフアジー
推論プロセツサ16には、第8図にその内容を示す制御ル
ールのメモリ装置15が接続されており、二つの制御器5
および5′からの膨張弁操作信号13,13′および吐出ガ
ス温度のセンサ6′からの検知信号14が入力されてい
る。A fuzzy inference processor 16 newly incorporated in the fourth embodiment is connected to a memory device 15 for control rules whose contents are shown in FIG.
And 5 'and the detection signal 14 from the discharge gas temperature sensor 6'.
この実施例では、第8図に示した制御ルールに基づい
て、冷凍サイクルの吐出ガス温度の絶対値が高い場合に
は、二つの制御ルールのうち、吐出ガス過熱度制御の重
みを大きくし、吐出ガス温度が高くなければ蒸発器過熱
度制御を行うべく、膨張弁制御器17から電動膨張弁3へ
推論結果が出力される。これらの重み付けは、フアジー
推論プロセツサ16で行われる。In this embodiment, based on the control rule shown in FIG. 8, when the absolute value of the discharge gas temperature of the refrigeration cycle is high, the weight of the discharge gas superheat degree control is increased among the two control rules, If the discharge gas temperature is not high, the inference result is output from the expansion valve controller 17 to the electric expansion valve 3 in order to perform the evaporator superheat control. These weightings are performed by the fuzzy inference processor 16.
この第4の実施例によれば、吐出ガス温度の絶対値が
高くなりそうな時は、信頼性を重視して、吐出ガス過熱
度制御を行い、そうでない時は、性能向上を重視して、
蒸発器4の過熱度制御を行うことができる。According to the fourth embodiment, when the absolute value of the discharge gas temperature is likely to be high, discharge gas superheat control is performed with an emphasis on reliability, and otherwise, performance improvement is emphasized. ,
The superheat degree of the evaporator 4 can be controlled.
本発明は、以上説明したように、冗長性のあるメンバ
シツプ関係と経験則に基づいて得られた制御ルールに基
づいて、フアジー推論によつて、電動膨張弁の開度を操
作して、冷凍サイクル中の冷媒温度差の制御を行うよう
にしているので、運転条件が変化しても、幅広い運転範
囲にわたつて、安定した冷媒流量制御を行い得る効果が
あり、ひいては冷凍装置の性能向上と信頼性向上を図り
得る効果がある。As described above, according to the present invention, the refrigeration cycle is operated by controlling the opening degree of the electric expansion valve by fuzzy inference based on a redundant membership relationship and a control rule obtained based on empirical rules. The refrigerant temperature difference inside is controlled, so that even if the operating conditions change, there is an effect that stable refrigerant flow control can be performed over a wide operating range, and as a result, the performance of the refrigeration system is improved and reliability is improved. This has the effect of improving the performance.
第1図は本発明の第1の実施例を示す系統図、第2図お
よび第3図はフアジー推論における制御ルールおよび制
御状況想定図、第4図(a)〜(c)はフアジー推論に
おけるメンバシツプ関数を示す図、第5図,第6図およ
び第7図は本発明の第2,第3および第4の実施例を示す
系統図、第8図は第4の実施例における制御ルールのメ
モリ装置の内容の説明図である。 1……圧縮機、2……凝縮器、3……電動膨張弁、4…
…蒸発器、5,5′……制御装置、6,7;6′,7′;6″,7″…
…センサ、8,8′……冷媒温度差設定器、9,9′……温度
差演算器、10,10′……フアジー推論プロセツサ、11,1
1′……制御ルールのメモリ装置、12,12′……膨張弁制
御器、15……制御ルールのメモリ装置、16……フアジー
推論プロセツサ、17……膨張弁制御器。1 is a system diagram showing a first embodiment of the present invention, FIGS. 2 and 3 are control rule and control situation assumption diagrams in fuzzy inference, and FIGS. 4 (a) to 4 (c) are diagrams in fuzzy inference. FIGS. 5, 6, and 7 are diagrams showing the membership functions, FIGS. 5, 6, and 7 are system diagrams showing the second, third, and fourth embodiments of the present invention, and FIG. 8 is a diagram showing control rules in the fourth embodiment. FIG. 3 is an explanatory diagram of the contents of a memory device. 1 ... Compressor, 2 ... Condenser, 3 ... Electric expansion valve, 4 ...
... Evaporator, 5,5 '... Control device, 6,7; 6', 7 '; 6 ", 7" ...
... Sensor, 8,8 '... Refrigerant temperature difference setting device, 9,9' ... Temperature difference calculator, 10,10 '... Fuzzy inference processor, 11,1
1 ': Control rule memory device, 12, 12': Expansion valve controller, 15: Control rule memory device, 16: Fuzzy inference processor, 17: Expansion valve controller.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 中山 進 茨城県土浦市神立町502番地 株式会社 日立製作所機械研究所内 (72)発明者 南方 留美 茨城県土浦市神立町502番地 株式会社 日立製作所機械研究所内 (72)発明者 千秋 隆雄 静岡県清水市村松390番地 株式会社日 立製作所清水工場内 (72)発明者 多賀 義明 静岡県清水市村松390番地 株式会社日 立製作所清水工場内 (72)発明者 高木 啓史 静岡県清水市村松390番地 株式会社日 立製作所清水工場内 (56)参考文献 特開 昭62−158953(JP,A) 実開 平2−85960(JP,U) 実開 平3−34564(JP,U) (58)調査した分野(Int.Cl.7,DB名) F25B 1/00 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Susumu Nakayama 502 Kandate-cho, Tsuchiura-shi, Ibaraki Pref. Machinery Research Laboratory, Hitachi, Ltd. (72) Inventor Rumi 502-Kandate-cho, Tsuchiura-City, Ibaraki Hitachi, Ltd. In-house (72) Inventor Takao Chiaki 390 Muramatsu, Shimizu-shi, Shizuoka Prefecture Inside Shimizu Plant, Hitachi Ltd. (72) Inventor Yoshiaki Taga 390 Muramatsu, Shimizu-shi, Shizuoka Prefecture Inside Shimizu Plant, Hitachi Ltd. (72) Inventor Keishi Takagi 390 Muramatsu, Shimizu-shi, Shizuoka Prefecture Inside the Shimizu Plant of Hitachi Ltd. (56) References JP-A-62-158953 (JP, A) JP-A-2-85960 (JP, U) JP-A-3-34564 (JP, U) (58) Field surveyed (Int. Cl. 7 , DB name) F25B 1/00
Claims (1)
弁とを備えた冷凍サイクルにおいて、前記冷凍サイクル
中の冷媒温度差を検知する検知手段と、冷媒温度差の情
報に対応させて、経験則に基づき電動膨張弁の開度操作
量に関する制御ルールを記憶したメモリ装置と、前記検
知手段から冷媒温度差に関する情報を取り込み、前記メ
モリ装置から前記情報に対応する制御ルールを取り込
み、電動膨張弁の開示操作量を演算して出力するフアジ
ー推論プロセツサとを有する制御装置を配備したことを
特徴とする冷凍装置。In a refrigeration cycle including a compressor, a condenser, an evaporator, and an electric expansion valve, a detecting means for detecting a refrigerant temperature difference in the refrigeration cycle, and corresponding to information on the refrigerant temperature difference. Then, a memory device storing a control rule regarding the opening degree operation amount of the electric expansion valve based on an empirical rule, and information regarding the refrigerant temperature difference are fetched from the detection unit, and a control rule corresponding to the information is fetched from the memory device. A refrigeration system comprising a controller having a fuzzy inference processor for calculating and outputting a disclosed operation amount of the electric expansion valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1321434A JP3039941B2 (en) | 1989-12-13 | 1989-12-13 | Refrigeration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1321434A JP3039941B2 (en) | 1989-12-13 | 1989-12-13 | Refrigeration equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03186154A JPH03186154A (en) | 1991-08-14 |
| JP3039941B2 true JP3039941B2 (en) | 2000-05-08 |
Family
ID=18132510
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1321434A Expired - Fee Related JP3039941B2 (en) | 1989-12-13 | 1989-12-13 | Refrigeration equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3039941B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5165391B2 (en) * | 2008-01-07 | 2013-03-21 | ホシザキ電機株式会社 | Cooling storage |
| JP5634081B2 (en) * | 2010-03-01 | 2014-12-03 | 三菱電機株式会社 | Air conditioner |
-
1989
- 1989-12-13 JP JP1321434A patent/JP3039941B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03186154A (en) | 1991-08-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6854285B2 (en) | Controller and a method for controlling an expansion valve of a refrigeration system | |
| CN107036256B (en) | Exhaust temperature control method, exhaust temperature control device, and air conditioner | |
| US8996141B1 (en) | Adaptive predictive functional controller | |
| CN102748906B (en) | Control algolithm for electronic expansion valve regulation | |
| KR850008208A (en) | Operation method and control system for refrigeration system | |
| JPS61175458A (en) | Refrigerant flow control device | |
| JP2006266533A (en) | Valve control system and valve control method | |
| US7290402B1 (en) | Expansion valve control system and method and refrigeration unit employing the same | |
| JP3039941B2 (en) | Refrigeration equipment | |
| KR100201645B1 (en) | Fuzzy control of branch flow rate and combustion of a multi-type absorption type air conditioner and its method | |
| JPH09159284A (en) | Expansion valve control device for air conditioner | |
| KR950033343A (en) | Control Unit of Absorption Chiller | |
| JP3489281B2 (en) | Air conditioner expansion valve controller | |
| JP3059534B2 (en) | Control method of reversible proportional expansion valve | |
| KR20180053181A (en) | Proportional integral derivative controller for high-precision temperature control of cooler | |
| JP2646917B2 (en) | Refrigeration equipment | |
| JPS6353454B2 (en) | ||
| JPS6356465B2 (en) | ||
| JPH0550666B2 (en) | ||
| JP2002106915A (en) | Control method and control device for heat pump | |
| JP2785546B2 (en) | Refrigeration equipment | |
| JPH07234001A (en) | Air conditioner control method and device | |
| JPH0670537B2 (en) | Heat source steam flow controller for absorption refrigerator | |
| JPH0686961B2 (en) | Refrigerant flow controller | |
| JPH087314Y2 (en) | refrigerator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080303 Year of fee payment: 8 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313113 |
|
| S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080303 Year of fee payment: 8 |
|
| R371 | Transfer withdrawn |
Free format text: JAPANESE INTERMEDIATE CODE: R371 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080303 Year of fee payment: 8 |
|
| S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
| S111 | Request for change of ownership or part of ownership |
Free format text: JAPANESE INTERMEDIATE CODE: R313113 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080303 Year of fee payment: 8 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080303 Year of fee payment: 8 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090303 Year of fee payment: 9 |
|
| LAPS | Cancellation because of no payment of annual fees |