JPH0486462A - Controller for absorption type freezer - Google Patents
Controller for absorption type freezerInfo
- Publication number
- JPH0486462A JPH0486462A JP20201490A JP20201490A JPH0486462A JP H0486462 A JPH0486462 A JP H0486462A JP 20201490 A JP20201490 A JP 20201490A JP 20201490 A JP20201490 A JP 20201490A JP H0486462 A JPH0486462 A JP H0486462A
- Authority
- JP
- Japan
- Prior art keywords
- water outlet
- control
- value
- temperature
- fuzzy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000006096 absorbing agent Substances 0.000 claims description 5
- 238000005057 refrigeration Methods 0.000 claims description 4
- 239000000446 fuel Substances 0.000 abstract description 15
- 230000004044 response Effects 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 239000003507 refrigerant Substances 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 4
- 230000005484 gravity Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】
(イ)産業上の利用分野
本発明はファジィ制御により吸収式冷凍機を制御する吸
収式冷凍機の制御装置に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a control device for an absorption refrigerating machine that controls the absorption refrigerating machine by fuzzy control.
(ロ)従来の技術
従来、吸収冷温水機、冷凍機においては、冷水出口温度
を検出し設定値からの偏差に基すき、吸収冷温水機、冷
凍機への入熱の制御を行う比例制御、あるいは冷水出口
温度によるPID制御が一般的であった。(B) Conventional technology Conventionally, in absorption chiller/heaters and refrigerators, proportional control detects the chilled water outlet temperature and controls the heat input to the absorption chiller/heater and refrigerator based on the deviation from the set value. , or PID control based on the cold water outlet temperature was common.
これらの制御は冷水出口温度という単一の物理量に対し
て一義的に吸収式冷凍機への入熱を制御するため、起動
、停止、緩急の負荷変動などあらゆる条件変化に対して
熟練オペレーターが行う制御に比べると即応性に難点が
あった。その改善のため、吸収冷温水機、吸収冷凍機の
外的条件を表す複数の物理量(冷水出口温度の設定値か
らの偏差、その時間的変化割合など)、及び冷温水機。These controls uniquely control the heat input to the absorption chiller based on a single physical quantity, the chilled water outlet temperature, and are therefore performed by skilled operators in response to all kinds of condition changes, such as start-up, stop, and slow and sudden load fluctuations. Compared to control, there was a problem in quick response. To improve this, we developed an absorption chiller/heater, a number of physical quantities representing the external conditions of the absorption chiller (deviation of the chilled water outlet temperature from a set value, its rate of change over time, etc.), and a water chiller/heater.
冷凍機の内部条件を表す複数の物理1(高温再生器温度
、その時間的変化割合など)と吸収冷温水機、冷凍機へ
の入熱量、吸収液の循環量との間にファジィルール及び
メンバーシップ関数を構成して、それに基ずき吸収式冷
凍機の制御を行う制御方式が提案されている。Fuzzy rules and members are created between multiple physical conditions representing the internal conditions of the refrigerator (high-temperature regenerator temperature, rate of change over time, etc.) and the amount of heat input to the absorption chiller/heater, the amount of heat input to the refrigerator, and the amount of circulation of the absorption liquid. A control method has been proposed in which a ship function is configured and an absorption chiller is controlled based on the ship function.
その制御方式によると、冷水出口温度のみによるPID
制御方式に比べ、吸収冷温水機、吸収冷凍機の内部及び
外部状態とその変化を検知し、それらを統合的に判断し
制御を行うことができるため、熟練オペレーターが行う
制御と同等の即応性のよい制御性能が得られる。According to the control method, PID based only on the cold water outlet temperature
Compared to control methods, it is possible to detect the internal and external conditions of the absorption chiller/heater and absorption chiller, as well as changes in these conditions, and perform control based on integrated judgment, resulting in the same level of responsiveness as control performed by a skilled operator. Good control performance can be obtained.
しかしながら、吸収冷温水機、吸収冷凍機が安定に運転
制御されている状!!(冷水出口温度が設定値近傍に制
御できている状態)では、ファジィ制御で一般的に言わ
れている設定値追従性能に問題がある。すなわち、
■設定値とのオフセットが残る、
■外乱の影響を受けやすい、
などである。However, the absorption chiller/heater and absorption chiller are operating stably! ! (In a state where the chilled water outlet temperature is controlled close to the set value), there is a problem in the set value follow-up performance, which is generally said to be the case with fuzzy control. In other words, ① An offset from the set value remains, ② It is susceptible to disturbances, etc.
(ハ)発明が解決しようとする課題
本発明のは、前述の従来方式において難点のあった設定
値近傍の°制御性能について改善を行うものである。(c) Problems to be Solved by the Invention The present invention improves the degree control performance near the set value, which was a problem in the conventional method described above.
(ニ)課題を解決するための手段
本発明では、蒸発器、吸収器、発生器、凝縮器などを接
続して冷凍サイクルを形成し、発生器の加熱量を冷水出
口温度を含む外的条件によってファジィ推論を用いて制
御する吸収式冷凍機の制御装置に於て、冷温水出口温度
が設定値近傍で、冷温水出口温度の設定値との偏差を有
限一定時間分積算してその平均値をとり、その値により
加熱量との間にファジィルール及びメンバー・シップ関
数を構成している。(d) Means for Solving the Problems In the present invention, a refrigeration cycle is formed by connecting an evaporator, an absorber, a generator, a condenser, etc., and the heating amount of the generator is determined by external conditions including the chilled water outlet temperature. In a control device for an absorption chiller that uses fuzzy reasoning to control the cold and hot water outlet temperature, when the cold and hot water outlet temperature is close to the set value, the deviations from the cold and hot water outlet temperature from the set value are integrated over a finite period of time, and the average value is calculated. A fuzzy rule and a membership function are constructed between the heating amount and the heating amount based on the value.
(ホ)作用
積算するサンプルの回数を:A整することにより冷水出
口温度の設定値への追従性が向上し、夕1乱の影響も受
けにくくなる。(E) By adjusting the number of samples to be integrated, the followability of the cold water outlet temperature to the set value is improved, and it is less susceptible to the effects of evening disturbances.
(へ)実施例
第1図は冷媒に水、吸収剤(溶液)に臭化リチュウム(
LiBr)水溶液を利用した二重効用吸収式冷凍機を示
し、1はバーナIB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、】0は箱板収液配管、11は中間吸収液配管、12
は濃縮液配管、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fiii’1
5の途中に冷媒ポンプ15Pが設けられている。また、
】6はバーナIB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)1
7が設けられている。(f) Example Figure 1 shows water as the refrigerant and lithium bromide as the absorbent (solution).
(LiBr) A double-effect absorption refrigerator using an aqueous solution, 1 is a high temperature generator equipped with burner IB, 2 is a low temperature generator, 3 is a condenser, 4 is an evaporator, 5 is an absorber, and 6 is a Absorption liquid pump, 7 and 8 are a low temperature heat exchanger and a high temperature heat exchanger, respectively, ] 0 is a box plate liquid collection pipe, 11 is an intermediate absorption liquid pipe, 12
is a concentrated liquid pipe, 13 is a refrigerant pipe, 14 is a refrigerant liquid down pipe,
15 is a refrigerant liquid circulation pipe, each of which is connected as shown in FIG. And refrigerant liquid circulation fiii'1
A refrigerant pump 15P is provided in the middle of 5. Also,
] 6 is a fuel supply pipe connected to burner IB, and a fuel control valve (heat amount control valve) 1 is installed in the middle of this fuel supply pipe 16.
7 is provided.
また、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。Further, 20 is a cold water pipe, and an evaporator heat exchanger 21 is provided in the middle of this cold water pipe 20.
さらに、22は冷却水配管である。Furthermore, 22 is a cooling water pipe.
23は制御部、24は上記冷水配管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25はファジィ推論プロッセサ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
推論プロッセサ27は燃料制御弁17への操作量KQを
論理演算し、得た操作量KQを制御装置26へ出力する
。制御装置26は上記操作量KQに基すいて燃料制御弁
17の開度を補正する。具体的には、この制御部726
は弁23の開度情報Qを保持していて、この開度情報Q
に応じて燃料制御弁17の開度を調整する。そして、操
作量KQ、を受けるごとに、今まで設定されていた開度
情報Q、−1と操作量KQ、とにより新たな開度情報Q
、=Q、−1+KQ、を設定する。即ち、この実施例で
はファジィ推論プロッセサ27からの操作量KQで燃料
制御弁17の開度が変更される。また制御ルールの記憶
装置28はファジィ推論プロッセサ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
)、条件部及び結論部メンバ・シップ関数を記憶する。Reference numeral 23 denotes a control unit, and 24 denotes a cold water outlet temperature detector provided in the cold water pipe 20. This cold water temperature detector 24 and the fuel control valve 17 are connected to the control panel 23. 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 27 and a control rule storage device 28. The fuzzy inference processor 27 performs a logical operation on the manipulated variable KQ to the fuel control valve 17 and outputs the obtained manipulated variable KQ to the control device 26 . The control device 26 corrects the opening degree of the fuel control valve 17 based on the manipulated variable KQ. Specifically, this control section 726
holds the opening degree information Q of the valve 23, and this opening degree information Q
The opening degree of the fuel control valve 17 is adjusted accordingly. Then, each time the manipulated variable KQ is received, new opening information Q is created using the previously set opening information Q, -1 and the manipulated variable KQ.
, =Q, -1+KQ, are set. That is, in this embodiment, the opening degree of the fuel control valve 17 is changed by the manipulated variable KQ from the fuzzy inference processor 27. Further, the control rule storage device 28 stores control rules (fuzzy rules), conditional parts, and conclusion part membership functions necessary for fuzzy logic operations executed by the fuzzy inference processor 27.
また、30は演算装置、31は蒸発器4の入口側の冷水
配管20に設けられた冷水入口温度検出器である。32
は高温再生器温度を検出する高温再生器温度検出器、3
3は冷却水入口温度を検出する冷却水入口温度検出器で
ある。演算装置30は上記冷水出口温度検出器24、冷
水入口温度検出器31、高温再生器温度検出器32、及
び冷却水入口温度検出器33の温度データを取り込み次
のデータを算出する。Further, 30 is a calculation device, and 31 is a cold water inlet temperature detector provided in the cold water pipe 20 on the inlet side of the evaporator 4. 32
is a high temperature regenerator temperature detector that detects the high temperature regenerator temperature, 3
3 is a cooling water inlet temperature detector that detects the cooling water inlet temperature. The arithmetic unit 30 takes in the temperature data of the cold water outlet temperature detector 24, the cold water inlet temperature detector 31, the high temperature regenerator temperature detector 32, and the cooling water inlet temperature detector 33, and calculates the following data.
■冷水出口温度の偏差(e t o)
e t、 o =現在値−目標値
■冷水出口温度の偏差の変化率(dto)dto−現在
値−前の値
■冷却水入口温度の変化率(dtci)dtci=現在
値−前の値
■冷水入口温度の変化率(dti)
dti=現在値−前の値
0etOの過去40サンプルの平均値(e)e、=(Σ
e t o + ) / 40■高温再生器温度変化
率(d t g)c!tg=現在値−前の値
次に、マイクロプロッセサ25の機能ブロック図を第2
図に示す。同図において、34は上記演算装置30から
のデータeto、dto、dtci、dti、e、dt
gを受けて、制御ルール記憶装置28ないに記憶されて
いる条件部メンバーシップ関数と制御ルールから、各制
御ルールの適合度を求める適合度算出部であり、複数の
条件部メンバーシップ関数で定義が為されているときは
最小の適合度をその適合度とする。ここで、条件部メン
バーシップ関数として、eto、dto、dti、dt
ci、dtg、eについてそれぞれNB、NS、ZR,
PS、PBを用いて第3図乃至第8図のように定義する
。これから分かるように、clti、dtci、eにつ
いては影響度合い小さくするため、それぞれ0.4.0
.5.0゜5の重み付けを行っている。■ Deviation of chilled water outlet temperature (e t o) e t, o = current value - target value ■ Rate of change of deviation of chilled water outlet temperature (dto) dto - current value - previous value ■ Rate of change of cooling water inlet temperature ( dtci) dtci = Current value - Previous value ■ Rate of change in cold water inlet temperature (dti) dti = Current value - Previous value Average value of the past 40 samples of 0etO (e) e, = (Σ
e t o + ) / 40 ■ High temperature regenerator temperature change rate (d t g) c! tg = current value - previous value Next, the functional block diagram of the microprocessor 25 is shown in the second section.
As shown in the figure. In the figure, 34 is data eto, dto, dtci, dti, e, dt from the arithmetic unit 30.
This is a suitability calculation unit which calculates the suitability of each control rule from the condition part membership function and control rule stored in the control rule storage device 28 in response to g, and is defined by a plurality of condition part membership functions. is done, the minimum degree of conformity is taken as the degree of conformity. Here, as the conditional membership functions, eto, dto, dti, dt
NB, NS, ZR, for ci, dtg, and e, respectively.
It is defined as shown in FIGS. 3 to 8 using PS and PB. As you can see, clti, dtci, and e are each 0.4.0 to reduce the degree of influence.
.. A weighting of 5.0°5 is performed.
制御ルールとしてはeto、dto、dtgについては
第9図のようにしている。即ち、ここでは隣り合う制御
ルールについて、ルールの定義を行わず、適合度の演算
時間の短縮を図っている。The control rules for eto, dto, and dtg are as shown in FIG. That is, here, rules are not defined for adjacent control rules, thereby reducing the time required to calculate the degree of suitability.
また、eto、dtoについては第10図のように定義
している。ここでは、後述のNZやPZを結論部メンパ
ン−シップ関数に加え、etoが設定値に近付いたとき
の制御量KQの収束度合いを良くしている。dtciに
ついては第11図、dtiについては第12図、eにつ
いては第13図はのものが定義されている。なお、この
eについてはetoがZHの近傍の時のみ、上記■で示
すようにetoの過去40サンプルの平均を採ることで
制御性能、収束性を向上させている。Furthermore, eto and dto are defined as shown in FIG. Here, NZ and PZ, which will be described later, are added to the conclusion section membership function to improve the degree of convergence of the control amount KQ when eto approaches the set value. dtci is defined in FIG. 11, dti in FIG. 12, and e in FIG. 13. Regarding e, control performance and convergence are improved by taking the average of the past 40 samples of eto only when eto is in the vicinity of ZH, as shown in (2) above.
35は上記制御ルール記憶装置28内の結論部メンバー
シップ関数を上記適合度算出部34で得られた適合度に
応じて、その上部をカットするように、修正する修正部
である。なお、この結論部メンバーシップ関数のとして
は第14図のものが定義される。この図から分かるよう
にZR近傍においてはNZ及びPZを定義して制御を良
くしている。Reference numeral 35 denotes a modification unit that modifies the conclusion part membership function in the control rule storage device 28 so as to cut the upper part of the conclusion part membership function in accordance with the degree of fitness obtained by the degree of fitness calculation unit 34. Note that the conclusion section membership function shown in FIG. 14 is defined. As can be seen from this figure, NZ and PZ are defined in the vicinity of ZR to improve control.
36はこの修正部35で修正された各メンバー・シップ
関数を重ね合わせて論理和を採る論理和部、37はこの
論理和部36で生成された関数の重心を演算する重心演
算部であって、この演算値が弁の操作量KQとして制御
装置26へ与えられる。Reference numeral 36 denotes a disjunctive unit that superimposes the membership functions modified by the correcting unit 35 and calculates a logical sum; and 37 a centroid calculation unit that computes the centroid of the function generated by the disjunctive unit 36. , this calculated value is given to the control device 26 as the valve operation amount KQ.
このような装置において、吸収式冷凍機の動作中、演算
装置30は冷水出口温度検出器24、冷水入口温度検出
器31、高温再生器温度検出器32、及び冷却水入口温
度検出器33より温度信号を例えば、5秒周期で取り入
れる。そして、こうして得られた温度信号から、上記冷
水出口温度の偏差(eto)、冷水出口温度の偏差の変
化率(dto)、冷却水入口温度の変化率(dtci)
、冷水入口温度の変化率(dti)、etoの過去40
サンプルの平均値(e)、高温再生器温度変化率(d
t g)を演算してマイクロコンピュタ25へ送る。In such a device, during operation of the absorption chiller, the arithmetic unit 30 detects the temperature from the chilled water outlet temperature detector 24, the chilled water inlet temperature detector 31, the high temperature regenerator temperature detector 32, and the chilled water inlet temperature detector 33. The signal is taken in, for example, every 5 seconds. From the temperature signal thus obtained, the deviation of the chilled water outlet temperature (eto), the rate of change of the deviation of the chilled water outlet temperature (dto), and the rate of change of the chilled water inlet temperature (dtci) are calculated.
, rate of change of chilled water inlet temperature (dti), past 40 of eto
Sample average value (e), high temperature regenerator temperature change rate (d
tg) and sends it to the microcomputer 25.
このマイクロコンピュータ25内の適合度演算部34で
は全ての制御ルールの条件部の適合度を調べる。そして
、この適合度をもちいて修正部35で第14図で示す対
応する結論部のメンバー・シンプ関数を修正する。即ち
、各メンバー・シップ関数の適合度より上の部分をカッ
トする。こうして修正されたメンバー・シップ関数の論
理和が論理和部36で採られ、そのメンバー・シップ関
数の重心を重・01演算部37で求める。この重心演算
部37の出力が燃料制御弁17の操作量KQ。The suitability calculation section 34 in the microcomputer 25 examines the suitability of the condition parts of all control rules. Then, using this goodness of fit, the modification unit 35 modifies the member simp function of the corresponding conclusion section shown in FIG. 14. That is, the portion above the fitness level of each membership function is cut. The logical sum of the membership functions thus modified is taken by the logical sum section 36, and the center of gravity of the membership function is determined by the gravity/01 calculation section 37. The output of this center of gravity calculating section 37 is the manipulated variable KQ of the fuel control valve 17.
とじて出力される。The output is closed.
弁の制御装置26はこの操作量KQ、、:今までの開度
情報Q、−,に基ずし1て新たな開度情報Q、=Q 、
−、+ K Qヨを算出する。そして、この間度情報Q
、応じて燃料制御弁】7を調整する。The valve control device 26 generates new opening information Q,=Q based on the previous opening information Q,-,
−, +K Calculate Qyo. And during this time, the degree information Q
, adjust the fuel control valve]7 accordingly.
こうした動作は上述した5秒周期で繰り返される。These operations are repeated at the above-mentioned 5 second period.
(ト)発明の効果
以上述べた如く、本発明吸収式冷凍機の制御装置は、蒸
発器、吸収器、発生器、凝縮器などを接続して冷凍サイ
クルを形成し、発生器の加熱量を冷水出口温度を含む外
的条件によってファジィ推論を用いて制御する吸収式冷
凍機の制御装置に於て、冷温水出口温度が設定値近傍で
、冷温水出口温度の設定値との偏差を有限一定時間分積
算してその値により加熱量との間にファジィルール及び
メンバー・シップ関数を構成しているので、冷水出口温
度の設定値への追従性が向上し、外乱の影響も受けにく
くなり、制御の安定性が向上する。(G) Effects of the Invention As described above, the control device for the absorption refrigerator of the present invention connects the evaporator, absorber, generator, condenser, etc. to form a refrigeration cycle, and controls the heating amount of the generator. In an absorption chiller control device that uses fuzzy reasoning to control external conditions including the chilled water outlet temperature, when the chilled and hot water outlet temperature is close to the set value, the deviation from the set value of the chilled and hot water outlet temperature is kept constant at a finite value. Fuzzy rules and membership functions are created between the accumulated value over time and the amount of heating, which improves the followability of the cold water outlet temperature to the set value and makes it less susceptible to external disturbances. Control stability is improved.
第1図は本発明制御装置が適用された吸収式冷凍機のブ
ロック図、第2図は本発明装置に使用されるマイクロコ
ンピュータの機能ブロック図、第3図乃至第8図は本発
明に用いられる条件部メンバー・シップ関数の特性図、
第9図乃至第13図は制御ルールの説明図、第14図は
結論部のメンバー・シップ関数の特性図である。
1・高温発生器、2・・・低温発生器、3・・・凝縮器
、4・・蒸発器、5・・吸収器、17・・・燃料制御弁
、23・・・制御部、24・・・冷水出口温度検出器、
25・・・マイクロプロッセサ、26・・制御装置、2
7・・・ファジィ推論プロッセサ、28・・・制御ルー
ルの記憶装置、30・・・演算装置31・・・冷水入口
温度検出器、32・・・高温再生器温度検出器、33・
・・冷水入口温度検出器34・・・適合度演算部、35
・・・修正部、36・・論理和部、37・・重心演算部
。Fig. 1 is a block diagram of an absorption chiller to which the control device of the present invention is applied, Fig. 2 is a functional block diagram of a microcomputer used in the device of the present invention, and Figs. Characteristic diagram of the conditional membership function,
9 to 13 are explanatory diagrams of the control rules, and FIG. 14 is a characteristic diagram of the membership function of the conclusion part. DESCRIPTION OF SYMBOLS 1. High temperature generator, 2... Low temperature generator, 3... Condenser, 4... Evaporator, 5... Absorber, 17... Fuel control valve, 23... Control part, 24...・・Cold water outlet temperature detector,
25...Microprocessor, 26...Control device, 2
7... Fuzzy inference processor, 28... Control rule storage device, 30... Arithmetic device 31... Chilled water inlet temperature detector, 32... High temperature regenerator temperature detector, 33...
...Cold water inlet temperature detector 34...Compatibility calculating section, 35
...correction section, 36.. logical sum section, 37.. centroid calculation section.
Claims (1)
冷凍サイクルを形成し、発生器の加熱量を冷水出口温度
を含む外的条件によってファジィ推論を用いて制御する
吸収式冷凍機の制御装置に於て、冷温水出口温度が設定
値近傍で、冷温水出口温度の設定値との偏差を有限一定
時間分積算してその平均値をとり、その値により加熱量
との間にファジィルール及びメンバー・シップ関数を構
成したことを特徴とした吸収式冷凍機の制御装置。(1) Absorption refrigeration, in which an evaporator, absorber, generator, condenser, etc. are connected to form a refrigeration cycle, and the amount of heat generated by the generator is controlled using fuzzy reasoning according to external conditions including the chilled water outlet temperature. In the control device of the machine, when the cold and hot water outlet temperature is close to the set value, the deviation from the cold and hot water outlet temperature from the set value is integrated over a finite fixed period of time, the average value is taken, and the difference between the heating amount and the heating amount is determined by that value. A control device for an absorption refrigerator, characterized in that a fuzzy rule and a membership function are configured.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20201490A JP2815993B2 (en) | 1990-07-30 | 1990-07-30 | Absorption chiller control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20201490A JP2815993B2 (en) | 1990-07-30 | 1990-07-30 | Absorption chiller control device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0486462A true JPH0486462A (en) | 1992-03-19 |
| JP2815993B2 JP2815993B2 (en) | 1998-10-27 |
Family
ID=16450497
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20201490A Expired - Fee Related JP2815993B2 (en) | 1990-07-30 | 1990-07-30 | Absorption chiller control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2815993B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109588782A (en) * | 2018-12-18 | 2019-04-09 | 绿烟实业(深圳)有限公司 | Temperature control equipment, temprature control method and the non-burning smoking set of heating |
| CN112002853A (en) * | 2020-07-14 | 2020-11-27 | 华瑞矿业科技有限公司 | Explosion-proof battery |
-
1990
- 1990-07-30 JP JP20201490A patent/JP2815993B2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109588782A (en) * | 2018-12-18 | 2019-04-09 | 绿烟实业(深圳)有限公司 | Temperature control equipment, temprature control method and the non-burning smoking set of heating |
| CN112002853A (en) * | 2020-07-14 | 2020-11-27 | 华瑞矿业科技有限公司 | Explosion-proof battery |
| CN112002853B (en) * | 2020-07-14 | 2023-07-25 | 华瑞矿业科技有限公司 | Explosion-proof battery |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2815993B2 (en) | 1998-10-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5156013A (en) | Control device for absorption refrigerator | |
| JPH0486460A (en) | Controller for absorption type freezer | |
| US20210116160A1 (en) | Refrigeration appliance and method for the operation thereof | |
| KR960012321B1 (en) | Absorption Chiller Control | |
| KR100201645B1 (en) | Fuzzy control of branch flow rate and combustion of a multi-type absorption type air conditioner and its method | |
| JPH07225061A (en) | Controller for absorption type chilled and warm water machine | |
| JP2815993B2 (en) | Absorption chiller control device | |
| JP3138004B2 (en) | Absorption refrigerator control device | |
| JP2823338B2 (en) | Absorption chiller control device | |
| JP4227476B2 (en) | Control method and apparatus for absorption chiller / heater | |
| JP2557722B2 (en) | Absorption refrigerator control method | |
| JP2823335B2 (en) | Control device for absorption refrigerator | |
| JP2517454B2 (en) | Absorption refrigerator control device | |
| JP2517455B2 (en) | Absorption refrigerator control device | |
| JPH0486463A (en) | Controller for absorption type freezer | |
| JP2517450B2 (en) | Absorption chiller control method and absorption chiller control device | |
| JP2708809B2 (en) | Control method of absorption refrigerator | |
| JPH0486461A (en) | Controller for absorption type freezer | |
| JP2517447B2 (en) | Absorption chiller control method and absorption chiller control device | |
| JP2517446B2 (en) | Absorption chiller control method and absorption chiller control device | |
| KR960012320B1 (en) | Absorption Chiller Control | |
| JP2816007B2 (en) | Control device for absorption refrigerator | |
| JP2725883B2 (en) | Control device for absorption refrigerator | |
| JPH04240360A (en) | Controller for absorption type refrigerator | |
| JPH04225760A (en) | Controller of absorption type refrigerating machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |