JP2517446B2 - Absorption chiller control method and absorption chiller control device - Google Patents
Absorption chiller control method and absorption chiller control deviceInfo
- Publication number
- JP2517446B2 JP2517446B2 JP2149578A JP14957890A JP2517446B2 JP 2517446 B2 JP2517446 B2 JP 2517446B2 JP 2149578 A JP2149578 A JP 2149578A JP 14957890 A JP14957890 A JP 14957890A JP 2517446 B2 JP2517446 B2 JP 2517446B2
- Authority
- JP
- Japan
- Prior art keywords
- change
- rate
- water outlet
- outlet temperature
- control valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 49
- 238000000034 method Methods 0.000 title claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 98
- 230000006870 function Effects 0.000 claims description 54
- 238000010438 heat treatment Methods 0.000 claims description 35
- 239000006096 absorbing agent Substances 0.000 claims description 8
- 238000005057 refrigeration Methods 0.000 claims description 7
- 239000000446 fuel Substances 0.000 description 41
- 239000007788 liquid Substances 0.000 description 11
- 239000003507 refrigerant Substances 0.000 description 11
- 230000007423 decrease Effects 0.000 description 10
- 238000010586 diagram Methods 0.000 description 8
- 230000005484 gravity Effects 0.000 description 6
- 230000003247 decreasing effect Effects 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】 (イ)産業上の利用分野 本発明は吸収冷凍機(吸収冷温水機を含む)に関し、
特に吸収冷凍機の制御装置に関する。The present invention relates to an absorption refrigerator (including an absorption chiller / heater),
In particular, it relates to a control device for an absorption refrigerator.
(ロ)従来の技術 例えば特開昭58−160778号公報には、冷水出口温度を
検出して再生器への加熱量を制御し、かつ、再生器内の
吸収液レベルを検出して吸収器から再生器へ流れる稀吸
収液の量を制御すると共に、冷水入口温度を検出してこ
の温度に対する再生器の加熱量、或いは再生器へ流れる
稀吸収液の量のうちいずれか一方の適正値を求め、この
値により加熱量或いは稀吸収液の量のうちいずれか一方
を制御する吸収冷凍機の制御装置が開示されている。(B) Prior art In Japanese Patent Laid-Open No. 58-160778, for example, the cold water outlet temperature is detected to control the amount of heat to the regenerator, and the level of the absorbing liquid in the regenerator is detected to detect the absorber. Control the amount of rare absorbent flowing from the regenerator to the regenerator, and detect the cold water inlet temperature to determine the appropriate value of either the heating amount of the regenerator for this temperature or the amount of rare absorbent flowing to the regenerator. There is disclosed a control device for an absorption refrigerating machine which controls one of the heating amount and the amount of the rare absorption liquid based on this value.
(ハ)発明が解決しようとする課題 上記従来の技術において、冷水出口温度を検出して再
生器の加熱量の制御を行う比例制御、或いはPID制御が
一般的であった。(C) Problem to be Solved by the Invention In the above-mentioned conventional technique, proportional control or PID control for detecting the cold water outlet temperature to control the heating amount of the regenerator is general.
又、吸収冷凍機では冷水出口温度と冷凍能力(冷凍容
量)との関係は一般に第9図に示したようになる。そし
て、第9図から明らかなように、冷水出口温度が定格点
より高い場合には冷水出口温度の上昇に伴い冷凍能力は
緩やかに増加し、定格点より低い場合には、冷水出口温
度の低下に伴い冷凍能力は急激に減少する。Further, in the absorption refrigerator, the relationship between the cold water outlet temperature and the refrigerating capacity (refrigerating capacity) is generally as shown in FIG. As is clear from FIG. 9, when the cold water outlet temperature is higher than the rated point, the refrigerating capacity gradually increases as the cold water outlet temperature rises, and when it is lower than the rated point, the cold water outlet temperature decreases. As a result, the refrigerating capacity decreases sharply.
上記冷凍能力の増加及び減少を冷水出口温度の変化率
と冷凍能力との関係で考えると、冷水出口温度の正の変
化に対しては冷凍能力を緩やかに増加させ、負の変化に
対しては急激に減少させる必要がある。しかしながら、
上記従来のPID制御、又は比例制御では、冷水出口温度
の変化率に対する燃料制御弁の操作量がリニアであるた
め、冷水出口温度の正の変化及び負の変化の場合も、即
ち、冷水出口温度の上昇時及び低下時に燃料制御弁が同
様に制御される。そして、例えば変化率が正の側で操作
量を設定した場合には、冷水出口温度の低下に対して燃
料制御弁の操作が遅れ、冷水出口温度が設定温度より大
幅に低くなる下方行き過ぎが発生するおそれがある。
又、変化率が負の側で操作量を設定した場合には冷水出
口温度の上昇に対して燃料制御弁の操作が早過ぎ、冷水
出口温度が設定温度より大幅に低くなる下方行き過ぎが
発生するおそれがある。Considering the increase and decrease of the refrigerating capacity in the relationship between the change rate of the cold water outlet temperature and the refrigerating capacity, the refrigerating capacity is gradually increased for a positive change of the cold water outlet temperature and for a negative change. It needs to be sharply reduced. However,
In the above conventional PID control or proportional control, since the operation amount of the fuel control valve with respect to the rate of change of the cold water outlet temperature is linear, even in the case of positive change and negative change of the cold water outlet temperature, that is, the cold water outlet temperature The fuel control valve is controlled in the same manner when the pressure rises and falls. Then, for example, when the manipulated variable is set on the side where the rate of change is positive, the operation of the fuel control valve is delayed with respect to the decrease in the chilled water outlet temperature, and there is an overshoot downward where the chilled water outlet temperature is significantly lower than the set temperature. May occur.
Further, when the manipulated variable is set on the negative side of the rate of change, the fuel control valve is operated too early with respect to the rise of the chilled water outlet temperature, and the chilled water outlet temperature is significantly lower than the set temperature, resulting in excessive downward movement. There is a risk.
又、吸収冷凍機の制御にファジィ制御を採用するとき
に、冷水出口温度の変化率をdToとし、燃料制御弁、或
いは蒸気制御弁の操作量をKQとした場合、従来のファジ
ィ制御では変化率(dTo)のメンバー・シップ関数は第
5図で表される。又、燃料制御弁、或いは蒸気制御弁の
操作量(KQ)のメンバー・シップ関数は第6図で表され
る。さらに、上記変化率に対する操作量のファジィ・ル
ールは第3図で表される。ここで、第3図のファジィ・
ルールと第5図のメンバー・シップ関数とは変化率の正
側と負側とで差を設けていないため、冷水出口温度の変
化率と各メンバー・シップ関数とファジィ・ルールとに
よってファジィ推論して上記制御弁の操作量を制御した
場合には、上記のPID制御などのときと同様に冷水出口
温度に下方行き過ぎが発生するおそれがある。尚、第3
図、第5図、及び第6図でPB(Positive Big)は正に
大、PM(Positive Medium)は正に中、PS(Positive Sm
all)は正に小、ZRはゼロ、NS(Negative Small)は負
に小、NM(Nega−tive Medium)は負に中、NB(Negativ
e Big)は負に大のことである。Also, when fuzzy control is adopted for control of the absorption refrigerator, if the rate of change of the chilled water outlet temperature is dTo and the manipulated variable of the fuel control valve or steam control valve is KQ, the rate of change in conventional fuzzy control is The membership function of (dTo) is represented in Figure 5. The membership function of the manipulated variable (KQ) of the fuel control valve or steam control valve is shown in FIG. Further, the fuzzy rule of the manipulated variable with respect to the above change rate is shown in FIG. Here, the fuzzy
Since there is no difference between the rule and the membership function in Fig. 5 on the positive side and the negative side of the rate of change, fuzzy reasoning is performed based on the rate of change of the chilled water outlet temperature, each membership function and the fuzzy rule. When the operation amount of the control valve is controlled by the above, there is a possibility that the cold water outlet temperature may excessively go downward as in the case of the above PID control. The third
In Figures 5, 5 and 6, PB (Positive Big) is positively large, PM (Positive Medium) is positively medium, PS (Positive Sm)
all) is positively small, ZR is zero, NS (Negative Small) is negatively small, NM (Nega-tive Medium) is negatively medium, NB (Negativ)
e Big) is a negative big thing.
本発明は冷水出口温度が変化したときの冷水出口温度
の下方行き過ぎを回避し、冷水出口温度を安定させるこ
とを目的とする。An object of the present invention is to prevent the cold water outlet temperature from overshooting when the cold water outlet temperature changes and to stabilize the cold water outlet temperature.
(ニ)課題を解決するための手段 本発明は上記課題を解決するために、蒸発器(4)、
吸収器(5)、高温発生器(1)、及び凝縮器(3)な
どを接続して冷凍サイクルを形成し、高温発生器(1)
の加熱量を外的条件によって制御する吸収冷凍機の制御
方法において、上記外的条件に冷水出口温度の変化率を
用い、この変化率とと高温発生器(1)の加熱量との間
にメンバー・シップ関数及びファジィ・ルールを定め、
このファジィ・ルール及びメンバー・シップ関数に基づ
いてファジィ推論し、上記変化率に対する高温発生器
(1)の加熱量を冷水出口温度の変化率が正の場合には
緩やかに変化させ、負の場合には急速に変化させる吸収
冷凍機の制御方法を提供するものである。(D) Means for Solving the Problems In order to solve the above problems, the present invention provides an evaporator (4),
The absorber (5), the high temperature generator (1), the condenser (3), etc. are connected to form a refrigeration cycle, and the high temperature generator (1)
In a method of controlling an absorption chiller in which the heating amount of is controlled according to an external condition, the rate of change of the chilled water outlet temperature is used as the external condition, and between the rate of change and the heating amount of the high temperature generator (1). Define membership function and fuzzy rules,
Fuzzy inference is performed based on this fuzzy rule and membership function, and the heating amount of the high temperature generator (1) with respect to the above change rate is gently changed when the change rate of the chilled water outlet temperature is positive, and when it is negative. Provides a control method for an absorption refrigerator that changes rapidly.
又、冷水出口温度の変化率と燃料制御弁(17)の操作
量との間にメンバー・シップ関数を設け、上記変化率に
対する高温発生器(1)の燃料制御弁(17)の操作量を
上記変化率が正の場合には緩やかに変化させ、上記変化
率が負の場合には急速に変化させるように構成したメン
バー・シップ関数を記憶した記憶装置(28)と、冷水出
口温度と上記記憶装置のメンバー・シップ関数に基づい
てファジィ推論して燃料制御弁(17)の操作量を演算す
るファジィ推論プロセッサ(演算装置)(27)とを備え
た吸収冷凍機の制御装置を提供するものである。In addition, a membership function is provided between the rate of change of the chilled water outlet temperature and the manipulated variable of the fuel control valve (17) to determine the manipulated variable of the fuel control valve (17) of the high temperature generator (1) with respect to the above rate of change. A storage device (28) storing a membership function configured to change gently when the rate of change is positive and to change rapidly when the rate of change is negative; A fuzzy inference processor (arithmetic device) (27) for fuzzy inference based on a membership function of a memory device to compute the manipulated variable of a fuel control valve (17), and to provide a control device for an absorption refrigerator. Is.
又、冷水出口温度の変化率に対する高温発生器(1)
の燃料制御弁(17)の操作量を上記変化率が正の場合に
は緩やかに変化させ、上記変化率が負の場合には急速に
変化させるように構成したファジィ・ルールを記憶した
記憶装置(28)と、冷水出口温度と上記記憶装置のファ
ジィ・ルールに基づいてファジィ推論して燃料制御弁
(17)の操作量を演算するファジィ推論プロセッサ(演
算装置)(27)とを備えた吸収冷凍機の制御装置を提供
するものである。Also, a high temperature generator for the rate of change of the cold water outlet temperature (1)
A storage device for storing a fuzzy rule configured such that the manipulated variable of the fuel control valve (17) is gently changed when the rate of change is positive and is rapidly changed when the rate of change is negative. (28) and a fuzzy inference processor (arithmetic device) (27) that calculates the manipulated variable of the fuel control valve (17) by fuzzy inference based on the cold water outlet temperature and the fuzzy rules of the storage device. A control device for a refrigerator is provided.
さらに、冷水出口温度の変化率に対する高温発生器
(1)の加熱量を変化率が正の場合には緩やかに変化さ
せ、変化率が負の場合には急速に変化させるように構成
したメンバー・シップ関数及びファジィ・ルールを記憶
する記憶装置(28)と、上記変化率と記憶装置(28)の
メンバー・シップ関数及びファジィ・ルールとに基づい
てファジィ推論して上記操作量を演算するファジィ推論
プロセッサ(演算装置)(27)とを備えた吸収冷凍機の
制御装置を提供するものである。Further, a member configured to gradually change the heating amount of the high temperature generator (1) with respect to the change rate of the chilled water outlet temperature when the change rate is positive and to change rapidly when the change rate is negative. A storage device (28) for storing a ship function and a fuzzy rule, and a fuzzy inference for calculating the manipulated variable by fuzzy inference based on the rate of change and the membership function and fuzzy rule of the storage device (28). The present invention provides a control device for an absorption chiller, which includes a processor (arithmetic device) (27).
(ホ)作用 吸収冷凍機の運転時、冷水出口温度が上昇した場合、
即ち変化率が正の場合にはファジィ・ルール及びメンバ
ー・シップ関数に基づいたファジィ推論によって高温発
生器(1)の加熱量が緩やかに増加し、冷凍能力が増加
し、又、冷水出口温度が低下した場合、即ち変化率が負
の場合には、ファジィ・ルール及びメンバー・シップ関
数に基づいたファジィ推論によって高温発生器(1)の
加熱量が急速に減少し、冷凍能力が減少し、冷水出口温
度の下方行き過ぎを回避して冷水出口温度を安定させる
ことが可能になる。(E) Action When the cold water outlet temperature rises during operation of the absorption refrigerator,
That is, when the rate of change is positive, the heating amount of the high temperature generator (1) gradually increases by the fuzzy reasoning based on the fuzzy rule and the membership function, the refrigerating capacity increases, and the chilled water outlet temperature increases. When it is decreased, that is, when the rate of change is negative, the heating amount of the high temperature generator (1) is rapidly decreased by the fuzzy reasoning based on the fuzzy rule and the membership function, the refrigerating capacity is decreased, and the cold water is reduced. It becomes possible to stabilize the cold water outlet temperature by avoiding the outlet temperature from overshooting downward.
又、冷水出口温度が上昇した場合及び低下した場合
に、記憶装置(28)に記憶されたファジィ・ルール或い
はメンバー・シップ関数に基づいてファジィ推論プロセ
ッサ(27)でファジィ推論が行われ、吸収冷凍機の特性
に合った加熱量制御弁(17)の制御が行われ、冷水出口
温度の変化率が負の場合には燃料制御弁(17)の操作量
を急速に減少させ、かつ、上記変化率が正の場合には燃
料制御弁(17)の操作量を緩やかに増加させ、冷水出口
温度の下方行き過ぎを回避することが可能になる。Further, when the chilled water outlet temperature rises or falls, fuzzy inference is performed by the fuzzy inference processor (27) based on the fuzzy rule or the membership function stored in the storage device (28), and absorption refrigeration is performed. The heating amount control valve (17) is controlled according to the characteristics of the machine, and when the rate of change of the chilled water outlet temperature is negative, the operation amount of the fuel control valve (17) is rapidly reduced and When the ratio is positive, it is possible to gradually increase the operation amount of the fuel control valve (17) and avoid excessive downward passage of the cold water outlet temperature.
(ヘ)実施例 以下、本発明の第1の実施例を図面に基づいて詳細に
説明する。(F) Embodiment Hereinafter, a first embodiment of the present invention will be described in detail with reference to the drawings.
第1図は冷媒に水、吸収剤(溶液)に臭化リチウム
(LiBr)水溶液を使用した二重効用吸収冷凍機を示し、
(1)はバーナー(1B)を備えた高温発生器、(2)は
低温発生器、(3)は凝縮器、(4)は蒸発器、(5)
は吸収器、(6)は吸収液ポンプ、(7),(8)はそ
れぞれ低温熱交換器及び高温熱交換器、(10)は稀吸収
液配管、(11)は中間吸収配管、(12)は濃吸収液配
管、(13)は冷媒配管、(14)は冷媒液流下管、(15)
は冷媒液循環管であり、それぞれは第1図に示したよう
に接続されている。そして、冷媒液循環管(15)の途中
に冷媒ポンプ(15P)が設けられている。又、(16)は
バーナー(1B)に接続された燃料供給管であり、この燃
料供給管(16)の途中に燃料制御弁(加熱量制御弁)
(17)が設けられている。又、(20)は冷水配管であ
り、この冷水配管(20)の途中に蒸発器熱交換器(21)
が設けられている。さらに(22)は冷却水配管である。Figure 1 shows a dual-effect absorption refrigerator that uses water as the refrigerant and lithium bromide (LiBr) solution as the absorbent (solution).
(1) is a high temperature generator equipped with a burner (1B), (2) is a low temperature generator, (3) is a condenser, (4) is an evaporator, (5)
Is an absorber, (6) is an absorption pump, (7) and (8) are a low temperature heat exchanger and a high temperature heat exchanger, respectively, (10) is a rare absorption liquid pipe, (11) is an intermediate absorption pipe, (12) ) Is a concentrated absorption liquid pipe, (13) is a refrigerant pipe, (14) is a refrigerant liquid flow pipe, (15)
Are refrigerant liquid circulation pipes, which are connected as shown in FIG. A refrigerant pump (15P) is provided in the refrigerant liquid circulation pipe (15). Further, (16) is a fuel supply pipe connected to the burner (1B), and a fuel control valve (heating amount control valve) is provided in the middle of this fuel supply pipe (16).
(17) is provided. Further, (20) is a cold water pipe, and an evaporator heat exchanger (21) is provided in the middle of this cold water pipe (20).
Is provided. Further, (22) is a cooling water pipe.
(23)は制御盤、(24)は冷水配管(20)に設けられ
た冷水出口温度検出器であり、この冷水出口温度検出器
(24)、及び燃料制御弁(17)が制御盤(23)に接続さ
れている。そして、制御盤(23)にはマイクロプロセッ
サ(25)及び燃料制御弁(17)の制御装置(26)が設け
られている。そして、マイクロプロセッサ(25)はファ
ジィ推論プロセッサ(演算装置)(27)と制御ルールの
記憶装置(28)とから構成されている。ファジィ推論プ
ロセッサ(27)は冷水出口温度の設定値からの偏差及び
冷水出口温度の変化率と後述する制御ルール及びメンバ
ー・シップ関数とに基づいてファジィ論理演算を行い燃
料制御弁(17)の操作量(開度)を求め、この操作量を
制御装置(26)へ出力する。制御装置(26)は上記操作
量に基づいて燃料制御弁(17)の開度を制御する。又、
制御ルールの記憶装置(28)はファジィ推論プロセッサ
(27)で実行されるファジィ論理演算に必要な制御ルー
ル(ファジィ・ルール)及びメンバー・シップ関数を記
憶する。又、(30)は演算装置であり、この演算装置は
冷水出口温度検出器(24)の温度データに基づいて冷水
出口温度の設定値からの偏差及び冷水出口温度の例えば
1分毎の変化率を演算する。(23) is a control panel, (24) is a cold water outlet temperature detector provided in the cold water pipe (20), and the cold water outlet temperature detector (24) and the fuel control valve (17) are the control panel (23 )It is connected to the. The control panel (23) is provided with a microprocessor (25) and a control device (26) for the fuel control valve (17). The microprocessor (25) is composed of a fuzzy inference processor (arithmetic device) (27) and a control rule storage device (28). The fuzzy inference processor (27) performs a fuzzy logic operation based on the deviation from the set value of the cold water outlet temperature and the rate of change of the cold water outlet temperature, and the control rule and membership function described later, and operates the fuel control valve (17). The amount (opening) is obtained, and this manipulated variable is output to the control device (26). The control device (26) controls the opening degree of the fuel control valve (17) based on the operation amount. or,
A control rule storage device (28) stores control rules (fuzzy rules) and membership functions required for fuzzy logic operations executed by the fuzzy inference processor (27). Further, (30) is an arithmetic unit, which is based on the temperature data of the cold water outlet temperature detector (24) and shows the deviation from the set value of the cold water outlet temperature and the rate of change of the cold water outlet temperature, for example, every minute. Is calculated.
上記燃料制御弁(17)の開度を求めるファジィ論理演
算は制御ルール及びメンバー・シップ関数に基づいて行
われる。そして、上記制御ルールについては、人間の経
験に基づいて第7図に示したような冷水出口温度の設定
値からの偏差(eTo)と燃料制御弁(17)の操作量(K
Q)との間に制御ルールを構成し、この制御ルールが記
憶装置(28)に記憶されている。さらに、制御ルールに
ついて、第2図に示したような冷水出口温度の変化率と
燃料制御弁(17)の操作量との間に制御ルールを構成
し、この制御ルールが記憶装置(28)に記憶されてい
る。第2図から明らかなように変化率がPB、即ち正に大
のとき操作量はPM(Positive Medium)の正に中にして
操作量を抑えている。又、変化率がNS、即ち負に小のと
き、操作量をNSにせずNM(Negative Medium)の負に中
にして操作量を増やしている。即ち、冷水出口温度の正
側と負側とで操作量に差を設けている。The fuzzy logic operation for obtaining the opening of the fuel control valve (17) is performed based on the control rule and the membership function. Regarding the above control rule, based on human experience, the deviation (eTo) from the set value of the cold water outlet temperature as shown in FIG. 7 and the operation amount (K of the fuel control valve (17)
A control rule is formed between the control rule and Q), and this control rule is stored in the storage device (28). Further, regarding the control rule, a control rule is configured between the rate of change of the chilled water outlet temperature and the operation amount of the fuel control valve (17) as shown in FIG. 2, and this control rule is stored in the storage device (28). Remembered As is apparent from FIG. 2, when the rate of change is PB, that is, when it is positively large, the manipulated variable is set to the positive medium of PM (Positive Medium) to suppress the manipulated variable. Further, when the rate of change is NS, that is, a small negative value, the operation amount is increased to the negative value of NM (Negative Medium) without setting the operation amount to NS. That is, there is a difference in the operation amount between the positive side and the negative side of the cold water outlet temperature.
又、冷水出口温度の設定値からの偏差に対するファジ
ィ変数PB,PS,ZR,NS,NBのメンバー・シップ関数は第8図
に示したものである。又、冷水出口温度の変化率に対す
るファジィ変数PB,PS,ZR,NS,NBのメンバー・シップ関数
は第5図に示したものである。さらに、燃料制御弁(1
7)の開度に対するファジィ変数PB,PM,PS,ZR,NS,NM,NB
のメンバー・シップ関数は第6図に示したものである。
第8図、及び第5図から明らかなように、上記偏差及び
変化率に対するメンバー・シップ関数には設定値からの
偏差の正側と負側、及び変化率の正側と負側とで差は設
けていない。The membership function of the fuzzy variables PB, PS, ZR, NS, and NB with respect to the deviation from the set value of the cold water outlet temperature is shown in FIG. The membership function of the fuzzy variables PB, PS, ZR, NS and NB with respect to the rate of change of the cold water outlet temperature is shown in FIG. In addition, the fuel control valve (1
Fuzzy variables PB, PM, PS, ZR, NS, NM, NB for the opening of 7)
The membership function of is shown in FIG.
As is clear from FIG. 8 and FIG. 5, the membership functions for the deviation and the change rate are different between the positive side and the negative side of the deviation from the set value and the positive side and the negative side of the change rate. Is not provided.
そして、上記の制御ルールとメンバー・シップ関数と
により冷水出口温度に基づいてファジィ論理演算がファ
ジィ推論プロセッサ(27)にて行われる。Then, a fuzzy logic operation is performed in the fuzzy inference processor (27) based on the cold water outlet temperature according to the above control rule and the membership function.
以下、上記吸収冷凍機の動作について説明する。吸収
冷凍機の運転時、高温発生器(1)が燃焼すると共に、
吸収液ポンプ(6)及び冷媒ポンプ(15P)が運転す
る。このため、従来の吸収冷凍機と同様に吸収液が循環
する。又、冷媒蒸気が低温発生器(2)で凝縮して凝縮
器(3)へ流れ、かつ、低温発生器(2)で発生した冷
媒蒸気が凝縮器(3)で凝縮する。そして冷媒液が凝縮
器(3)から蒸発器(4)へ流れる。そして、冷媒液が
蒸発器熱交換器(21)に散布され、温度低下した冷水が
蒸発器(4)から負荷へ供給される。The operation of the absorption refrigerator will be described below. During operation of the absorption refrigerator, the high temperature generator (1) burns,
The absorption liquid pump (6) and the refrigerant pump (15P) operate. Therefore, the absorption liquid circulates as in the conventional absorption refrigerator. Further, the refrigerant vapor is condensed in the low temperature generator (2) and flows to the condenser (3), and the refrigerant vapor generated in the low temperature generator (2) is condensed in the condenser (3). The refrigerant liquid then flows from the condenser (3) to the evaporator (4). Then, the refrigerant liquid is sprinkled on the evaporator heat exchanger (21), and the cold water whose temperature has dropped is supplied from the evaporator (4) to the load.
又、冷水出口温度の設定値からの偏差に基づいて上記
第8図の偏差に対するメンバー・シップ関数と第7図の
ファジィ・ルールと第6図の操作量に対するメンバー・
シップ関数とによりファジィ推論が行われ、燃料制御弁
(17)の操作量のメンバー・シップ値が求められる。こ
こで、上記偏差が例えば−1.4℃の場合には、第10図に
示したようにファジィ推論が行われ、冷水出口温度の設
定値からの偏差に対するメンバー・シップ値(A)が求
められる。又、このときの、負荷が減少して上記変化率
が例えば−0.6℃/minの場合には、第11図に示したよう
にファジィ推論が行われ、変化率NSに対して操作量はNS
より大きいNMに決まる。そして、上記偏差に対するメン
バー・シップ値(B)が求められる。このメンバー・シ
ップ値(B)と上記メンバー・シップ値(A)との論理
和の重心、即ち第12図に示した操作量に対するメンバー
・シップ値(C)の重心(G1)により操作量が決定す
る。そして、燃料制御弁(17)が開度が急速に小さくな
り、冷凍能力は減少する。Further, based on the deviation of the chilled water outlet temperature from the set value, the membership function for the deviation in FIG. 8 above, the fuzzy rule in FIG. 7 and the member quantity for the manipulated variable in FIG.
Fuzzy inference is performed with the ship function, and the membership value of the manipulated variable of the fuel control valve (17) is obtained. Here, if the deviation is, for example, −1.4 ° C., fuzzy inference is performed as shown in FIG. 10 to obtain the membership value (A) for the deviation from the set value of the cold water outlet temperature. At this time, when the load is reduced and the rate of change is, for example, −0.6 ° C./min, fuzzy inference is performed as shown in FIG. 11, and the manipulated variable is NS with respect to the rate of change NS.
Determined by a larger NM. Then, the membership value (B) for the deviation is obtained. The operation amount is determined by the centroid of the logical sum of the membership value (B) and the membership value (A), that is, the centroid (G 1 ) of the membership value (C) with respect to the operation amount shown in FIG. Will be decided. Then, the opening of the fuel control valve (17) rapidly decreases, and the refrigerating capacity decreases.
又、上記偏差が上記の例と同様に−1.4℃であり、負
荷が増加して冷水出口温度の変化率が例えば0.8℃/min
の場合には、第10図及び第13図に示したようにファジィ
推論が行われる。そして、上記偏差に対するメンバー・
シップ値(A)が求められると共に、上記変化率に対す
るメンバー・シップ値(D)が求められる。ここで、フ
ァジィ・ルールでは変化率PBに対し操作量はPBより小さ
いPMに決まる。さらに、これらのメンバー・シップ値
(A)と(D)との論理和の重心、即ち、第14図に示し
た操作量に対するメンバー・シップ値(F)の重心
(G2)により操作量が決定される。そして、燃料制御弁
(17)の開度が緩やかに大きくなり、冷凍能力は増加す
る。Further, the deviation is −1.4 ° C. as in the above example, the load increases and the chilled water outlet temperature change rate is, for example, 0.8 ° C./min.
In this case, fuzzy inference is performed as shown in FIGS. 10 and 13. And the members for the above deviation
The ship value (A) is calculated, and the membership value (D) for the change rate is calculated. Here, in the fuzzy rule, the manipulated variable is determined to be PM smaller than PB with respect to the change rate PB. Further, the operation amount is determined by the center of gravity of the logical sum of these membership values (A) and (D), that is, the center of gravity (G 2 ) of the membership value (F) with respect to the operation amount shown in FIG. It is determined. Then, the opening degree of the fuel control valve (17) gradually increases, and the refrigerating capacity increases.
上記実施例によれば、冷水出口温度の変化率に対する
操作量のファジィ・ルールが第2図に示したように決め
られ、冷水出口温度の変化率がPB(正に大)のときは操
作量がPM(正に中)、変化率がNS(負に小)のときは操
作量がNM(負に中)に設定されているので、変化率が正
側は冷水出口温度の変化が大きくてもファジィ推論によ
って操作量が小さく決まり、燃料制御弁(17)を緩やか
に操作することができ、かつ、変化率が負側は冷水出口
温度が小さくてもファジィ推論によって操作量が大きく
決まり、燃料制御弁(17)を急速に操作することができ
る。この結果、冷水出口温度の上昇及び低下に対して吸
収冷凍機の特性、即ち、冷水負荷の増加に対しては冷水
出口温度が緩やかに上昇し、冷水負荷の減少に対しては
冷水出口温度が急速に低下する特性を考慮した燃料制御
弁(17)の制御を行うことができ、吸収冷凍機の運転を
安定させることができる。According to the above embodiment, the fuzzy rule of the manipulated variable with respect to the change rate of the cold water outlet temperature is determined as shown in FIG. 2, and when the change rate of the cold water outlet temperature is PB (just large), the manipulated variable is set. Is PM (positively medium) and the rate of change is NS (negatively small), the manipulated variable is set to NM (negatively medium), so if the rate of change is positive, the change in the chilled water outlet temperature is large. Also, the amount of operation is determined by fuzzy reasoning, the fuel control valve (17) can be operated gently, and on the negative side of the rate of change, the amount of operation is greatly determined by fuzzy reasoning even if the chilled water outlet temperature is small. The control valve (17) can be operated rapidly. As a result, the characteristics of the absorption chiller against the rise and fall of the chilled water outlet temperature, that is, the chilled water outlet temperature gradually rises as the chilled water load increases, and the chilled water outlet temperature rises as the chilled water load decreases. The fuel control valve (17) can be controlled in consideration of the characteristic of rapidly decreasing, and the operation of the absorption refrigerator can be stabilized.
以下、燃料制御弁(17)の変化率に対するメンバー・
シップ関数に変化率の正側と負側とで差を設けた第2の
実施例について説明する。Below are the members for the rate of change of the fuel control valve (17).
A second embodiment in which the ship function is provided with a difference between the positive side and the negative side of the rate of change will be described.
第4図に示したように、変化率に対するメンバー・シ
ップ関数には変化率が正側と負側とで差が設けられ、こ
のメンバー・シップ関数が記憶装置(28)に記憶されて
いる。即ち、NB,NS,及びZRのメンバー・シップ値を変化
率ゼロに近付けている。又、ファジィ・ルール及び操作
量に対するメンバー・シップ関数はそれぞれ、第3図及
び第6図に示したものであり、それぞれは記憶装置(2
8)に記憶されている。このため、変化率の絶対値の評
価が正側が大きくても小さく、負側は小さくても大きく
評価する。As shown in FIG. 4, the membership function with respect to the rate of change is provided with a difference between the positive side and the negative side in the rate of change, and this membership function is stored in the storage device (28). That is, the membership values of NB, NS, and ZR are approaching zero rate of change. The membership functions for the fuzzy rules and the manipulated variables are those shown in FIGS. 3 and 6, respectively.
It is stored in 8). Therefore, the evaluation of the absolute value of the change rate is large or small on the positive side and large or small on the negative side.
以下、上記のような変化率に対するメンバー・シップ
関数が記憶装置(28)に記憶された制御装置による吸収
冷凍機の制御について説明する。Hereinafter, the control of the absorption refrigerating machine by the control device in which the membership function with respect to the change rate as described above is stored in the storage device (28) will be described.
吸収冷凍機の運転時、冷水出口温度の変化率が例え
ば、−0.4℃/minの場合には、第15図に一点鎖線で示し
たようにファジィ推論が行われ、各メンバー・シップ値
及びファジィ・ルールから操作量に対するメンバー・シ
ップ値(H)が求められる。又、冷水出口温度の設定値
から偏差が例えば上記実施例と同様に例えば−1.4℃の
場合には、第10図に示したようにファジィ推論が行われ
操作量に対するメンバー・シップ値(A)が求められ
る。そして、メンバー・シップ値(H),(A)の論理
和の重心から操作量が決まる。When the chilled water outlet temperature change rate is, for example, −0.4 ° C / min during operation of the absorption chiller, fuzzy inference is performed as indicated by the dashed line in Fig. 15, and each membership value and fuzzy・ The membership value (H) for the operation amount is calculated from the rule. When the deviation from the set value of the cold water outlet temperature is, for example, −1.4 ° C. as in the above embodiment, fuzzy reasoning is performed as shown in FIG. 10 and the membership value (A) for the manipulated variable is calculated. Is required. Then, the operation amount is determined from the centroid of the logical sum of the membership values (H) and (A).
又、上記偏差が例えば−1.4℃であり、変化率が例え
ば0.4℃/minの場合には、変化率について第15図に二点
鎖線で示したようにファジィ推論が行われる。そして、
各メンバー・シップ関数及びファジィ・ルールによって
操作量に対するメンバー・シップ値(I)が求められ
る。そして、このメンバー・シップ値(I)と偏差につ
いての上記メンバー・シップ値(A)との論理和の重心
から操作量が決まる。この操作量の絶対値は変化率が−
0.4℃/minのときの操作量の絶対値より小さい。When the deviation is, for example, −1.4 ° C. and the rate of change is, for example, 0.4 ° C./min, fuzzy inference is performed on the rate of change as indicated by the chain double-dashed line in FIG. And
The membership value (I) with respect to the manipulated variable is obtained by each membership function and fuzzy rule. The operation amount is determined from the center of gravity of the logical sum of the membership value (I) and the membership value (A) for the deviation. The absolute value of this manipulated variable has a change rate of −
It is smaller than the absolute value of the manipulated variable at 0.4 ° C / min.
又、上記変化率が例えば−0.7℃/minの場合には第16
図に一点鎖線にて示したようにファジィ推論が行われ
る。そして、各メンバー・シップ関数、及びファジィ・
ルールによって操作量に対するメンバー・シップ値
(J)が求められる。又、このとき、偏差が上記実施例
と等しい−1.4℃である場合には、上記と同様にメンバ
ー・シップ値(A)が求められる。そして、このメンバ
ー・シップ値(A)と上記メンバー・シップ値(J)と
の論理和の重心から操作量が決まる。If the rate of change is, for example, -0.7 ° C / min, the 16th
Fuzzy inference is performed as indicated by the chain line in the figure. And each membership function and fuzzy
A membership value (J) with respect to the operation amount is obtained by the rule. At this time, if the deviation is −1.4 ° C., which is the same as in the above embodiment, the membership value (A) is obtained in the same manner as above. Then, the operation amount is determined from the center of gravity of the logical sum of the membership value (A) and the membership value (J).
上記実施例によれば、冷水出口温度の変化率のメンバ
ー・シップ関数が第4図に示したように決められ、メン
バー・シップ値(NB),(NS),(ZR)を0(ゼロ)に
近付け、変化率の正側と負側とで差を設け、変化率の正
側では変化率の絶対値の評価が大きくてもファジィ推論
によって操作量が小さく決まるので、燃料制御弁(17)
を緩やかに操作することができる。又、変化率の負側で
は変化率が小さくてもファジィ推論によって操作量が大
きく決まるので、燃料制御弁(17)を急速に操作するこ
とができ、この結果冷水出口温度の変化に対して燃料制
御弁(17)を吸収冷凍機の特性、即ち負荷の増加に対し
ては冷水出口温度が緩やかに上昇し、負荷の減少に対し
て冷水出口温度が急速に低下するという特性に合った燃
料制御弁(17)の制御を行うことができ、冷水出口温度
を安定させることができる。According to the above embodiment, the membership function of the rate of change of the chilled water outlet temperature is determined as shown in FIG. 4, and the membership values (NB), (NS), (ZR) are set to 0 (zero). , The difference between the positive side and the negative side of the rate of change is set. On the positive side of the rate of change, the manipulated variable is determined to be small by fuzzy reasoning even if the absolute value of the rate of change is large, so the fuel control valve (17)
Can be operated gently. On the negative side of the rate of change, the amount of operation is largely determined by fuzzy reasoning even if the rate of change is small, so the fuel control valve (17) can be operated rapidly, and as a result, the fuel control valve (17) can be operated with respect to changes in chilled water outlet temperature. Fuel control that matches the characteristics of the absorption chiller with the control valve (17), that is, the chilled water outlet temperature gradually rises as the load increases and the chilled water outlet temperature rapidly decreases as the load decreases. The valve (17) can be controlled, and the cold water outlet temperature can be stabilized.
以下、燃料制御弁(17)の変化率に対するメンバー・
シップ関数に第4図に示したように変化率の正側と負荷
とで差を設け、かつ、上記変化率と操作量との間のファ
ジィ・ルールに第2図に示したように変化率の正側と負
荷とで差を設けた第3の実施例について説明する。記憶
装置には第6図及び第8図に示したメンバー・シップ関
数と第7図に示したファジィ・ルールとが記憶されてい
る。Below are the members for the rate of change of the fuel control valve (17).
As shown in FIG. 4, the ship function is provided with a difference between the positive side of the rate of change and the load, and the fuzzy rule between the rate of change and the manipulated variable is the rate of change as shown in FIG. A third embodiment in which a difference is provided between the positive side and the load will be described. The memory stores the membership functions shown in FIGS. 6 and 8 and the fuzzy rules shown in FIG. 7.
以下、上記のようなメンバー・シップ値及びファジィ
・ルールが記憶装置(28)に記憶された吸収冷凍機の制
御について説明する。Hereinafter, the control of the absorption refrigerator in which the membership value and the fuzzy rule as described above are stored in the storage device (28) will be described.
吸収冷凍機の運転時、冷水出口温度の偏差が例えば上
記実施例と同様に例えば−1.4℃の場合には、第10図に
示したようにファジィ推論が行われ、操作量に対するメ
ンバー・シップ値(A)が求められる。このとき、変化
率が例えば−0.4℃/minのときには、第15図に示したよ
うにファジィ推論が行われ、操作量に対するメンバー・
シップ値(H)が求められる。そして、このメンバー・
シップ値(H)とメンバー・シップ値(A)との論理和
の重心から操作量が求まる。During operation of the absorption chiller, when the deviation of the chilled water outlet temperature is, for example, −1.4 ° C. as in the above embodiment, fuzzy inference is performed as shown in FIG. 10, and the membership value for the manipulated variable is calculated. (A) is required. At this time, when the rate of change is, for example, −0.4 ° C./min, fuzzy inference is performed as shown in FIG.
The ship value (H) is required. And this member
The operation amount is obtained from the center of gravity of the logical sum of the ship value (H) and the membership value (A).
又、冷水出口温度の偏差が例えば−1.4℃であり、か
つ変化率が0.4℃/minのときには、第10図に示したよう
にファジィ推論が行われ、偏差についてのメンバー・シ
ップ値(A)が求められ、さらに、第15図に示したよう
にファジィ推論が行われ、操作量(I)が求められる。
そして、このメンバー・シップ値(I)とメンバー・シ
ップ値(A)との論理和の重心から操作量が求まる。Further, when the deviation of the cold water outlet temperature is, for example, −1.4 ° C. and the rate of change is 0.4 ° C./min, fuzzy inference is performed as shown in FIG. 10, and the membership value (A) for the deviation is shown. Is calculated, and fuzzy reasoning is performed as shown in FIG. 15 to calculate the manipulated variable (I).
Then, the operation amount is obtained from the center of gravity of the logical sum of the membership value (I) and the membership value (A).
ここで、変化率が−0.4℃/minのときと0.4℃/minのと
きとの操作量の絶対値とを比較すると、−0.4℃/minの
ときの操作量の絶対値が0.4℃/minのときよりも大き
い。Here, comparing the absolute value of the manipulated variable when the rate of change is −0.4 ° C./min and 0.4 ° C./min, the absolute value of the manipulated variable at −0.4 ° C./min is 0.4 ° C./min. Bigger than when.
上記実施例によれば、冷水出口温度の変化率のメンバ
ー・シップ関数及びファジィ・ルールがそれぞれ第4図
及び第2図に示したように決められ、変化率の正側と負
側とでメンバー・シップ関数及びファジィ・ルールに差
を設ける。そして、変化率の正側では変化率の絶対値の
評価が大きくてもファジィ推論によって操作量が小さく
決まり、変化率の負側では変化率の絶対値の評価が小さ
くてもファジィ推論によって操作量が大きく決まる。こ
のため、変化率の正側では燃料制御弁(17)を緩やかに
操作することができ、負側では燃料制御弁(17)を急速
に操作することができ、この結果吸収冷凍機の特性に合
った燃料制御弁(17)の制御を行うことができ、吸収冷
凍機の運転を安定させることができる。According to the above-described embodiment, the membership function and the fuzzy rule of the change rate of the chilled water outlet temperature are determined as shown in FIGS. 4 and 2, respectively, and the member is determined on the positive side and the negative side of the change rate.・ Providing a difference in the ship function and fuzzy rules. On the positive side of the rate of change, even if the absolute value of the rate of change is large, the amount of operation is determined by fuzzy reasoning. On the negative side of the rate of change, even if the absolute value of the rate of change is small, the amount of operation is determined by fuzzy reasoning. Is largely determined. Therefore, the fuel control valve (17) can be gently operated on the positive side of the rate of change, and the fuel control valve (17) can be rapidly operated on the negative side, resulting in the characteristics of the absorption refrigerator. The matched fuel control valve (17) can be controlled, and the operation of the absorption refrigerator can be stabilized.
尚、本発明は上記実施例に限定されるものではなく、
メンバー・シップ関数及びファジィ・ルールは吸収冷凍
機の能力などに応じて変化率の正側と負側とで任意に設
定される。The present invention is not limited to the above embodiment,
The membership function and the fuzzy rule are arbitrarily set on the positive side and the negative side of the rate of change according to the capacity of the absorption refrigerator.
又、上記各実施例において、バーナー(1B)を備えた
高温発生器(1)を有した吸収冷凍機について説明した
が、加熱源に高温蒸気を利用した高温発生器を有し、高
温発生器への高温蒸気の供給量を制御する制御弁の開度
を上記燃料制御弁(17)の制御と同様にファジィ推論に
基づいて制御した場合にも同様の作用効果を得ることが
できる。Further, in each of the above embodiments, the absorption refrigerator having the high temperature generator (1) equipped with the burner (1B) has been described. However, the high temperature generator using high temperature steam is used as a heating source, and the high temperature generator is used. Similar effects can be obtained when the opening degree of the control valve that controls the supply amount of high-temperature steam to the fuel cell is controlled based on fuzzy reasoning as in the control of the fuel control valve (17).
(ト)発明の効果 本発明は以上のように構成された吸収冷凍機の制御方
法或いは制御装置であり、冷水出口温度の変化率と発生
器の加熱量との間にメンバー・シップ関数及びファジィ
・ルールを定め、このファジィ・ルール及びメンバー・
シップ関数に基づいてファジィ推論し、冷水出口温度の
上昇時には上記加熱量を緩やかに変化させ、冷水出口温
度の低下時には上記加熱量を急速に変化させるので、冷
水出口温度が変化したときに吸収冷凍機の特性に合った
高温発生器の加熱量制御を行うことができ、この結果、
冷水出口温度を安定させることができる。(G) Effect of the Invention The present invention is a control method or a control apparatus for an absorption refrigerating machine configured as described above, wherein a membership function and a fuzzy function are provided between the rate of change of the chilled water outlet temperature and the heating amount of the generator.・ Define the rules, this fuzzy rule and members ・
Fuzzy inference is performed based on the Ship function, the heating amount is gently changed when the cold water outlet temperature rises, and the heating amount is rapidly changed when the cold water outlet temperature falls, so absorption refrigeration is performed when the cold water outlet temperature changes. It is possible to control the heating amount of the high temperature generator that matches the characteristics of the machine.
The cold water outlet temperature can be stabilized.
又、冷水出口温度の変化率が正の場合には加熱量制御
弁の操作量を緩やかに変化させ、変化率が負の場合には
操作量を急速に変化させるように構成されたメンバー・
シップ関数或いはファジィ・ルールを記憶装置が記憶
し、演算装置は記憶装置に記憶されたファジィ・ルール
或いはメンバー・シップ関数に基づいてファジィ推論し
て加熱量制御弁を制御するので、冷水出口温度が上昇或
いは低下したときに、吸収冷凍機の特性に合った加熱量
制御弁の制御を行うことができ、冷水出口温度の過低下
を回避して冷水出口温度を安定させることができる。Further, when the rate of change of the chilled water outlet temperature is positive, the operation amount of the heating amount control valve is gently changed, and when the rate of change is negative, the operation amount is changed rapidly.
The storage device stores the ship function or the fuzzy rule, and the arithmetic device controls the heating amount control valve by performing fuzzy inference based on the fuzzy rule or the membership function stored in the storage device. When the temperature rises or falls, it is possible to control the heating amount control valve that matches the characteristics of the absorption chiller, avoid excessive lowering of the cold water outlet temperature, and stabilize the cold water outlet temperature.
さらに、冷水出口温度の変化率に対する発生器の加熱
量を変化率が正の場合は緩やかに変化させ、変化率が負
の場合は急速に変化させるように構成したメンバー・シ
ップ関数及びファジィ・ルールを記憶した記憶装置と、
上記変化率とメンバー・シップ関数とファジィ・ルール
とに基づいてファジィ推論して加熱量制御弁の操作量を
演算する演算装置とを備えているので、冷水出口温度が
変化したとき、演算装置にてメンバー・シップ関数及び
ファジィ・ルールに基づいてファジィ推論が行われ、吸
収冷凍機の特性に合った加熱量制御弁の制御を行うこと
ができ、この結果、冷水出口温度の過低下を回避して冷
水出口温度を安定させることができる。Furthermore, the membership function and the fuzzy rule are configured so that the amount of heating of the generator with respect to the rate of change of the chilled water outlet temperature is gradually changed when the rate of change is positive and is rapidly changed when the rate of change is negative. A storage device that stores
It has a computing device that computes the manipulated variable of the heating amount control valve by fuzzy inference based on the rate of change, the membership function and the fuzzy rule, so when the chilled water outlet temperature changes, the computing device Fuzzy inference is performed based on the membership function and fuzzy rules, and the heating amount control valve can be controlled according to the characteristics of the absorption refrigerator, and as a result, excessive decrease in the chilled water outlet temperature can be avoided. It is possible to stabilize the cold water outlet temperature.
【図面の簡単な説明】 第1図は本発明の一実施例を示す吸収冷凍機の回路構成
図、第2図及び第3図はそれぞれ変化率に対する操作量
のファジィ・ルールを示す図、第4図及び第5図はそれ
ぞれ変化率のメンバー・シップ関数を示す図、第6図は
操作量のメンバー・シップ関数を示す図、第7図は偏差
に対する操作量のファジィ・ルールを示す図、第8図は
偏差のメンバー・シップ関数を示す図、第9図は冷水出
口温度と冷凍容量(冷凍能力)との関係図、第10図ない
し第16図はそれぞれファジィ推論の説明図である。 (1)……高温発生器、(3)……凝縮器、(4)……
発生器、(5)……吸収器、(17)……燃料制御弁(加
熱量制御弁)、(27)……ファジィ推論プロセッサ(演
算装置)、(28)……記憶装置。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a circuit configuration diagram of an absorption chiller showing an embodiment of the present invention, and FIGS. 2 and 3 are diagrams showing fuzzy rules of manipulated variables with respect to change rates, respectively. 4 and 5 are diagrams showing the membership function of the rate of change, FIG. 6 is a diagram showing the membership function of the manipulated variable, and FIG. 7 is a diagram showing a fuzzy rule of the manipulated variable with respect to the deviation. FIG. 8 is a diagram showing a membership function of deviation, FIG. 9 is a relational diagram between the chilled water outlet temperature and refrigerating capacity (refrigerating capacity), and FIGS. 10 to 16 are explanatory diagrams of fuzzy reasoning. (1) …… High temperature generator, (3) …… Condenser, (4) ……
Generator, (5) ... absorber, (17) ... fuel control valve (heating amount control valve), (27) ... fuzzy inference processor (arithmetic device), (28) ... storage device.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 人見 和弘 大阪府守口市京阪本通2丁目18番地 三 洋電機株式会社内 (56)参考文献 特開 昭62−77567(JP,A) 特開 平2−140564(JP,A) 特開 昭63−131942(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazuhiro Hitomi 2-18 Keihan Hondori, Moriguchi City, Osaka Sanyo Electric Co., Ltd. (56) Reference JP 62-77567 (JP, A) JP Flat 2-140564 (JP, A) JP-A-63-131942 (JP, A)
Claims (4)
続して冷凍サイクルを形成し、発生器の加熱量を外的条
件によって制御する吸収冷凍機の制御方法において、上
記外的条件に冷水出口温度の変化率を用い、この変化率
と発生器の加熱量との間にメンバー・シップ関数、及び
ファジィ・ルールを定め、このファジィ・ルール及びメ
ンバー・シップ関数に基づいてファジィ推論し、上記変
化率に対する発生器の加熱量を冷水出口温度の変化率が
正の場合には緩やかに変化させ、冷水出口温度の変化率
が負の場合には急速に変化させることを特徴とする吸収
冷凍機の制御方法。1. A method for controlling an absorption refrigerator, wherein an evaporator, an absorber, a generator, a condenser, etc. are connected to form a refrigeration cycle, and a heating amount of the generator is controlled by an external condition. Using the rate of change of the cold water outlet temperature as the condition, define a membership function and a fuzzy rule between this rate of change and the heating amount of the generator, and perform fuzzy reasoning based on this fuzzy rule and the membership function. However, the heating amount of the generator with respect to the rate of change is gently changed when the rate of change of the cold water outlet temperature is positive, and is rapidly changed when the rate of change of the cold water outlet temperature is negative. Control method of absorption refrigerator.
続して冷凍サイクルを形成し、発生器の加熱量制御弁を
外的条件によって制御する吸収冷凍機の制御装置におい
て、上記外的条件に冷水出口温度の変化率を用い、この
変化率に対する加熱量制御弁の操作量を上記変化率が正
の場合には緩やかに変化させ、上記変化率が負の場合に
は急速に変化させるように構成したメンバー・シップ関
数を記憶した記憶装置と、冷水出口温度と上記記憶装置
のメンバー・シップ関数とに基づいてファジィ推論して
加熱量制御弁の操作量を演算する演算装置とを備えたこ
とを特徴とする吸収冷凍機の制御装置。2. A control device for an absorption refrigerating machine, wherein an evaporator, an absorber, a generator, a condenser, etc. are connected to form a refrigeration cycle, and a heating amount control valve of the generator is controlled by an external condition. The change rate of the chilled water outlet temperature is used as an external condition, and the operation amount of the heating amount control valve with respect to this change rate is gently changed when the change rate is positive, and rapidly when the change rate is negative. A storage device that stores a membership function that is configured to change, and a computing device that performs fuzzy inference based on the cold water outlet temperature and the membership function of the storage device to compute the manipulated variable of the heating control valve. An absorption refrigerating machine control device comprising:
続して冷凍サイクルを形成し、発生器の加熱量制御弁を
外的条件によって制御する吸収冷凍機の制御装置におい
て、上記外的条件に冷水出口温度の設定値からの偏差を
用い、この変化率に対する加熱量制御弁の操作量を上記
変化率が正の場合には緩やかに変化させ、上記変化率が
負の場合には急速に変化させるように構成したファジィ
・ルールを記憶した記憶装置と、冷水出口温度と上記記
憶装置のファジィ・ルールとに基づいてファジィ推論し
て加熱量制御弁の操作量を演算する演算装置とを備えた
ことを特徴とする吸収冷凍機の制御装置。3. A control device for an absorption refrigerating machine, wherein an evaporator, an absorber, a generator, a condenser, etc. are connected to form a refrigeration cycle, and a heating amount control valve of the generator is controlled by an external condition. The deviation from the set value of the chilled water outlet temperature is used as the external condition, and the operation amount of the heating amount control valve with respect to this change rate is gently changed when the above change rate is positive, and when the above change rate is negative. Is a storage device that stores a fuzzy rule configured to change rapidly, and an arithmetic device that calculates the manipulated variable of the heating amount control valve by fuzzy inference based on the cold water outlet temperature and the fuzzy rule of the storage device. An absorption refrigerating machine control device comprising:
続して冷凍サイクルを形成し、発生器の加熱量制御弁を
外的条件によって制御する吸収冷凍機の制御装置におい
て、上記外的条件に冷水出口温度の変化率を用い、この
変化率に対する加熱量制御弁の操作量を冷水出口温度の
変化率が正の場合には緩やかに変化させ、上記変化率が
負の場合には急速に変化させるように構成したメンバー
・シップ関数及びファジィ・ルールを記憶した記憶装置
と、冷水出口温度の変化率と上記記憶装置のメンバー・
シップ関数及びファジィ・ルールとに基づいてファジィ
推論して加熱量制御弁の操作量を演算する演算装置とを
備えたことを特徴とする吸収冷凍機の制御装置。4. A control device for an absorption refrigerating machine, wherein an evaporator, an absorber, a generator, a condenser, etc. are connected to form a refrigeration cycle, and a heating amount control valve of the generator is controlled by an external condition. The rate of change of the cold water outlet temperature is used as an external condition, and the manipulated variable of the heating amount control valve with respect to this rate of change is gradually changed when the rate of change of the cold water outlet temperature is positive, and when the rate of change is negative. Is a storage device that stores membership functions and fuzzy rules that are configured to change rapidly, and the rate of change of the chilled water outlet temperature and the membership of the storage device.
A control device for an absorption chiller, comprising: a fuzzy inference based on a ship function and a fuzzy rule to calculate a manipulated variable of a heating amount control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2149578A JP2517446B2 (en) | 1990-06-07 | 1990-06-07 | Absorption chiller control method and absorption chiller control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2149578A JP2517446B2 (en) | 1990-06-07 | 1990-06-07 | Absorption chiller control method and absorption chiller control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0443265A JPH0443265A (en) | 1992-02-13 |
| JP2517446B2 true JP2517446B2 (en) | 1996-07-24 |
Family
ID=15478263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2149578A Expired - Fee Related JP2517446B2 (en) | 1990-06-07 | 1990-06-07 | Absorption chiller control method and absorption chiller control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2517446B2 (en) |
-
1990
- 1990-06-07 JP JP2149578A patent/JP2517446B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0443265A (en) | 1992-02-13 |
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