JPH04136666A - Controller for absorbing freezer - Google Patents

Controller for absorbing freezer

Info

Publication number
JPH04136666A
JPH04136666A JP25918590A JP25918590A JPH04136666A JP H04136666 A JPH04136666 A JP H04136666A JP 25918590 A JP25918590 A JP 25918590A JP 25918590 A JP25918590 A JP 25918590A JP H04136666 A JPH04136666 A JP H04136666A
Authority
JP
Japan
Prior art keywords
liquid pump
absorption liquid
controller
generator
absorbing liquid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP25918590A
Other languages
Japanese (ja)
Inventor
Yasuo Sakata
坂田 泰雄
Hideaki Oana
秀明 小穴
Naoki Sakamoto
直樹 坂本
Hiroshi Sakamoto
弘 坂本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP25918590A priority Critical patent/JPH04136666A/en
Publication of JPH04136666A publication Critical patent/JPH04136666A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To easily change over the operation of an absorbing liquid pump corresponding to heating volume of a generator and to control properly circulation volume of absorbing liquid by providing a heating volume controller to change over the heating volume of the generator corresponding to load and an absorbing liquid pump controller to operate the absorbing liquid pump under delta connecting system or star connecting system corresponding to the heating. volume of the generator. CONSTITUTION:At the time of operation of an absorbing freezer, for example, if freezing load is small, burning volume of a high temperature generator 1 is controlled by a burning controller 31 to be small. At this time, an absorbing liquid pump 20 is operated by an absorbing liquid pump controller 32 under star connecting system to decrease discharging volume of the absorbing liquid pump 20 is decreased corresponding to the heating volume. On the other hand, if the freezing load is large, the heating volume of the high temperature generator 1 is controlled by the burning controller 31 to be large, and the absorbing liquid pump 20 is operated by the absorbing liquid pump controller 32 under delta connecting system, so that the discharging volume of the absorbing liquid pump 20 is increased corresponding to the heating volume. Accordingly, without using an inverter controlling device of the like, circulating volume of absorbing liquid can be controlled.

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に関し、特に、吸収冷凍機の制御装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to an absorption refrigerator, and particularly to a control device for an absorption refrigerator.

(ロ)従来の技術 例えば特開昭62−77567号公報には、発生器の加
熱量を蒸発器の冷水出口温度により制御する加熱量調節
装置と釉液用ポンプの吐出量を発生器の溶液温度により
制御する稀溶液流量調節装置とを備えた吸収冷凍機が開
示されている。そして、この吸収冷凍機において、稀溶
液流量調節装置の制御動作が比例動作であり、加熱量調
節装置の制御動作がPID動作、或いはPI動作である
(b) Conventional technology For example, Japanese Patent Application Laid-Open No. 62-77567 discloses a heating amount adjusting device that controls the heating amount of the generator by the cold water outlet temperature of the evaporator, and a heating amount adjusting device that controls the amount of heating from the generator based on the temperature of the cold water outlet of the evaporator. An absorption refrigerator is disclosed that includes a temperature-controlled dilute solution flow rate regulator. In this absorption refrigerator, the control operation of the dilute solution flow rate adjustment device is a proportional operation, and the control operation of the heating amount adjustment device is a PID operation or a PI operation.

ここで、発生器の加熱量、即ち発生器の運転を冷水出口
温度によって高燃焼運転と低燃焼運転とに切換える加熱
量調節装置を備えた吸収冷凍機では、釉液用ポンプ(以
下吸収液ポンプという)の運転を発生器の溶液温度によ
り制御するとき、例えば吸収液ポンプに極数変換用特殊
吸収液ポンプを用い、極数変換制御装置によって吸収液
ポンプの極数を変換して吸収液ポンプの吐出量を制御す
る方法、或いはインバータ制御装置を用いて吸収液ポン
プに供給される電力の周波数を制御して吸収液ポンプの
吐出量を制御する方法が用いられている。
Here, in an absorption chiller equipped with a heating amount adjustment device that switches the heating amount of the generator, that is, the operation of the generator, between high combustion operation and low combustion operation depending on the cold water outlet temperature, the glaze pump (hereinafter referred to as absorption liquid pump When controlling the operation of the absorbent pump by the solution temperature of the generator, for example, a special absorbent pump for pole number conversion is used as the absorbent pump, and the pole number of the absorbent pump is changed by the pole number converter control device. A method of controlling the discharge amount of the absorption liquid pump, or a method of controlling the discharge amount of the absorption liquid pump by controlling the frequency of the electric power supplied to the absorption liquid pump using an inverter control device is used.

(ハ)発明が解決しようとする課題 例えば発生器を負荷、即ち冷水出口温度によって高燃焼
運転と低燃焼運転とに切換え、それに応じて吸収液の循
環量を適量に制御するときに、上記従来の技術に示した
ように極数変換制御装置、或いはインバータ制御装置を
用いた場合には、制御装置が非常に複雑になるという問
題が発生していた。又、極数変換用特殊吸収液ポンプ、
或いはインバータ制御装置を使用した場合には、吸収冷
凍機の制御装置のコストが上昇する。
(c) Problems to be Solved by the Invention For example, when switching the generator between high combustion operation and low combustion operation depending on the load, that is, the cold water outlet temperature, and controlling the circulating amount of absorption liquid to an appropriate amount accordingly, the above-mentioned conventional When a pole number conversion control device or an inverter control device is used as shown in the above technique, a problem arises in that the control device becomes extremely complicated. In addition, special absorption liquid pump for pole number conversion,
Alternatively, if an inverter control device is used, the cost of the absorption refrigerator control device increases.

本発明は発生器の高燃焼運転及び低燃焼運転に対して容
易に吸収液ポンプを制御でき、安価な吸収冷凍機の制御
装置を提供するものである。
The present invention provides an inexpensive control device for an absorption refrigerator that can easily control an absorption liquid pump for high combustion operation and low combustion operation of a generator.

(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、高温発生器(1)
、凝縮器(4)、蒸発器(6)、吸収器(7)、及び吸
収器(7)から高温発生器<1)へ吸収液を送る吸収液
ポンプ(20)などを配管接続して冷凍サイクルを形成
した吸収冷凍機において、負荷に応じて高温発生器(1
)の加熱量を切換える燃焼制御器(加熱量制御器)(3
1)と、高温発生器(1)の加熱量によって吸収液ポン
プ(20〉をデルタ結線運転及びスター結線運転させる
吸収液ポンプ制御器(32)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。
(d) Means for Solving the Problems In order to solve the above problems, the present invention provides a high temperature generator (1).
, condenser (4), evaporator (6), absorber (7), and an absorption liquid pump (20) that sends the absorption liquid from the absorber (7) to the high temperature generator <1), etc., are connected via piping for refrigeration. In the absorption refrigerator that forms the cycle, a high temperature generator (1
) Combustion controller (heating amount controller) (3
1) and an absorption liquid pump controller (32) that operates the absorption liquid pump (20) in delta connection operation and star connection operation according to the heating amount of the high temperature generator (1). It is something.

又、負荷に応じて高温発生器(1)を高燃焼運転と低燃
焼運転とに切換える燃焼制御器(31)と、高燃焼運転
及び低燃焼運転に対して吸収液ポンプ(20)と三相交
流電源との間の結線をデルタ結線及びスター結線に切換
える吸収液ポンプ制御器(32)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。
Additionally, there is a combustion controller (31) that switches the high temperature generator (1) between high combustion operation and low combustion operation according to the load, and an absorption liquid pump (20) and three-phase controller for high combustion operation and low combustion operation. The present invention provides a control device for an absorption refrigerating machine that includes an absorption liquid pump controller (32) that switches connection to an AC power source between delta connection and star connection.

(ホ)作用 吸収冷凍機の運転時、例えば冷凍負荷が小きいときには
燃焼制御器(31)によって高温発生器(1)の燃焼量
は7ノ1さく制御され加熱量は小さく、このとき、吸収
液ポンプ制御器(32)によって吸収液ポンプ(20)
はスター結線運転され、吸収液ポンプ(20)の吐出量
を上記加熱量に合せて/JSさくすることができる。又
、冷凍負荷が大きいときには、燃焼制御器(31)によ
って高温発生器(1)の加熱量は大きく制御され、かつ
、吸収液ポンプ制御器(32〉によって吸収液ポンプ(
20)はデルタ結線運転され、吸収液ポンブク20)の
吐出量を上記加熱量に合せて大きくすることができ、イ
ンバータ制御装置などを使用せずに、吸収液の循環量を
適量に制御することが可能になる。
(e) Effect When the absorption refrigerator is operating, for example, when the refrigeration load is small, the combustion amount of the high temperature generator (1) is controlled by 7 times less by the combustion controller (31), and the heating amount is small. Absorption liquid pump (20) by liquid pump controller (32)
is operated in star connection, and the discharge amount of the absorption liquid pump (20) can be reduced according to the above heating amount. Furthermore, when the refrigeration load is large, the amount of heating of the high temperature generator (1) is largely controlled by the combustion controller (31), and the absorption liquid pump (32) is controlled by the absorption liquid pump controller (32>).
20) is operated with a delta connection, and the discharge amount of the absorption liquid pump 20) can be increased in accordance with the above heating amount, and the circulation amount of the absorption liquid can be controlled to an appropriate amount without using an inverter control device or the like. becomes possible.

又、吸収冷凍機の運転時、高温発生器(1)は燃焼制御
器(31)によって負荷に応じて高燃焼運転と低燃焼運
転とに切換えられると共に、高燃焼運転及び低燃焼運転
に対して吸収液ポンプ(2o)と三相交流電源との間の
結線が吸収液ポンプ制御器(32)によってデルタ結線
及びスター結線に切換えられ、インバータ制御装置など
を使用せずに上記高燃焼運転及び低燃焼運転に合せて、
吸収液の循環量を適量に制御することが可能になる。
Furthermore, when the absorption chiller is operating, the high temperature generator (1) is switched between high combustion operation and low combustion operation by the combustion controller (31) according to the load, and also is switched between high combustion operation and low combustion operation. The connection between the absorption liquid pump (2o) and the three-phase AC power supply is switched to delta connection and star connection by the absorption liquid pump controller (32), and the above-mentioned high combustion operation and low combustion operation are performed without using an inverter control device or the like. In line with combustion operation,
It becomes possible to control the circulation amount of the absorption liquid to an appropriate amount.

くべ)実施例 以下、本発明の一実施例を図面に基づいて詳細に説明す
る。
Example) An example of the present invention will be described in detail below with reference to the drawings.

第1図は冷媒に水(H,O)、吸収剤(溶液)に臭化リ
チウム(LiBr)水溶液を用いた吸収冷凍機の回路構
成図である。
FIG. 1 is a circuit diagram of an absorption refrigerator using water (H, O) as a refrigerant and a lithium bromide (LiBr) aqueous solution as an absorbent (solution).

第1図において、(1)はバーナ〈IB)を備えた高温
発生器、(2)は分離器、(3)は低温発生器、(4)
は凝縮器、(5)は凝縮器(4)及び低温発生器(3)
を収納した上胴、(6)は蒸発器、(7)は吸収器、(
8)は吸収器(7)及び蒸発器(6)を収納した下胴、
(10)は低温熱交換器、(11〉は高温熱交換器であ
り、それぞれは稀吸収液配管(12)、揚液管(13)
、中間吸収液配管(14)、濃吸収液配管(15)、冷
媒管(16) 。
In Figure 1, (1) is a high temperature generator equipped with a burner (IB), (2) is a separator, (3) is a low temperature generator, (4) is a separator, and (4) is a separator.
is the condenser, (5) is the condenser (4) and the low temperature generator (3)
(6) is the evaporator, (7) is the absorber, (
8) is a lower shell housing an absorber (7) and an evaporator (6);
(10) is a low-temperature heat exchanger, (11> is a high-temperature heat exchanger, and each has a dilute absorption liquid pipe (12) and a liquid lift pipe (13).
, intermediate absorption liquid piping (14), concentrated absorption liquid piping (15), and refrigerant pipe (16).

(17)、冷媒液流下管(18)などによって配管接続
されている。又、(20)は稀吸収液配管(12)に設
けられた吸収液ポンプ、(21)は分離器(2〉から下
胴(8)へ至り開閉弁(22)を有した冷媒配管、(2
2A)は分離器(2)から低温発生器(3)に至り、ス
チームトラップ(22a)を有した側路配管、(23)
は蒸発器(6)に付設され冷媒ポンプ(24)を途中に
備えた冷媒循環配管、(25)は蒸発器熱交換器(26
)に接続された冷温水配管、(27)は吸収器熱交換器
<28)及び凝縮器熱交換器(29)に接続された冷却
水配管である。
(17), and a refrigerant liquid flow down pipe (18). In addition, (20) is an absorption liquid pump installed in the dilute absorption liquid pipe (12), (21) is a refrigerant pipe that runs from the separator (2> to the lower shell (8)) and has an on-off valve (22); 2
2A) is a bypass pipe from the separator (2) to the low temperature generator (3) with a steam trap (22a), (23)
(25) is a refrigerant circulation pipe attached to the evaporator (6) and equipped with a refrigerant pump (24), and (25) is an evaporator heat exchanger (26).
), and (27) is a cooling water pipe connected to the absorber heat exchanger <28) and the condenser heat exchanger (29).

ここで、上記側路配管(22A)には、吸収冷凍機の運
転停止のときの稀釈運転時に吸収液が分離器(2)から
低温発生器(3)へ流れる。
Here, the absorption liquid flows into the side pipe (22A) from the separator (2) to the low temperature generator (3) during dilution operation when the absorption refrigerator is stopped.

又、(30)は吸収冷凍機の制御盤であり、(31)は
加熱量制御器(燃焼制御器)、(32)は吸収液ポンプ
制御器である。(33)は蒸発器(6)の出口側の冷温
水配管(25〉に設けられた冷水出口温度検出器であり
、この温度検出器(33)から加熱量制御器(31)は
温度信号を入力して、冷水出口温度に応じてバーナ(I
B〉へ高燃焼信号或いは低燃焼信号を出力し、バーナ(
IB)の運転を高燃焼運転と低燃焼運転とに制御する。
Further, (30) is a control panel for the absorption refrigerator, (31) is a heating amount controller (combustion controller), and (32) is an absorption liquid pump controller. (33) is a cold water outlet temperature detector installed in the cold/hot water pipe (25) on the outlet side of the evaporator (6), and the heating amount controller (31) receives a temperature signal from this temperature detector (33). input and set the burner (I) according to the cold water outlet temperature.
A high combustion signal or a low combustion signal is output to the burner (
The operation of IB) is controlled into high combustion operation and low combustion operation.

又、加熱量制御器り31)は、バーナ(IB〉へ低燃焼
信号を出力しているときには吸収液ポンプ制御器(32
)へ同様に低燃焼信号を出力し、バーナ(IB)へ高燃
焼信号を出力しているときには吸収液ポンプ制御器(3
2)へ同様に高燃焼信号を出力する。
Also, when the heating amount controller 31) is outputting a low combustion signal to the burner (IB>), the absorption liquid pump controller (32)
), and when outputting a high combustion signal to the burner (IB), the absorbent pump controller (3
Similarly, a high combustion signal is output to 2).

第2図は吸収液ポンプ制御器(32)の概略回路図であ
り、(34)は加熱量制御器(31)からの低燃焼信号
によってONする第1接点、(35)は加熱量制御器(
31)からの高燃焼信号によってONする第2接点であ
る。又、(36)はスター運転用の!離開閉器(以下第
1電磁開閉器という)、(37)は常開の第1電磁開閉
器主接点(以下第1主接点という)。
Figure 2 is a schematic circuit diagram of the absorption liquid pump controller (32), where (34) is the first contact that is turned ON by the low combustion signal from the heating amount controller (31), and (35) is the heating amount controller. (
This is the second contact that is turned ON by the high combustion signal from 31). Also, (36) is for star operation! A separation switch (hereinafter referred to as a first electromagnetic switch), (37) is a normally open first electromagnetic switch main contact (hereinafter referred to as a first main contact).

(38)は常閉の第1電磁開閉器補助接点(以下第1補
助接点という)であり、第1主接点(37)がONした
とき、吸収液ポンプ(20)は例えば三相200ボルト
電源とスター結線され、スター結線運転(以下スター運
転という)が行われる。(40)はデルタ運転用の電磁
開閉器(以下第2電磁開閉器という)、(41)は常開
の第2電磁開閉器主接点(以下第2主接点という)、(
42)は常閉の第2電磁開閉器補助接点(以下第2補助
接点という)であり、第2主接点(41)がONしたと
き、吸収液ポンプ(20)は三相200ポルト電源とデ
ルタ結線され、デルタ結線運転(以下デルタ運転という
)が行われる。
(38) is the normally closed first electromagnetic switch auxiliary contact (hereinafter referred to as the first auxiliary contact), and when the first main contact (37) is turned on, the absorption liquid pump (20) is powered by, for example, a three-phase 20V power source. A star connection is made with the terminal, and a star connection operation (hereinafter referred to as star operation) is performed. (40) is the electromagnetic switch for delta operation (hereinafter referred to as the second electromagnetic switch), (41) is the normally open second electromagnetic switch main contact (hereinafter referred to as the second main contact), (
42) is a normally closed second electromagnetic switch auxiliary contact (hereinafter referred to as the second auxiliary contact), and when the second main contact (41) is turned on, the absorption liquid pump (20) is connected to the three-phase 200 port power supply and the delta The wires are connected and delta connection operation (hereinafter referred to as delta operation) is performed.

以下、第3図のタイムチャートに基づいて、上記吸収冷
凍機の運転について説明する。
Hereinafter, the operation of the absorption refrigerator will be explained based on the time chart shown in FIG.

吸収冷凍機が運転を始めたとき、冷水出口温度が低い場
合には、温度検出器(33)から温度信号を入力した加
熱量制御器(31)はバーナ(IB)へ低燃焼信号を出
力し、バーナ(IB)は例えば30%の低燃焼運転を行
う。さらに、加熱量制御器(31)は吸収液ポンプ制御
器(32)へ低燃焼信号を出力し、第1接点(34)は
ONする。そして、第1電磁開閉器く36)が通電され
、第1主接点(37)がONL、、第1補助接点(38
)がOFFする。第1主接点のONによルトの電圧が印
加され、吸収液ポンプ(20〉はスター運転を始める。
When the absorption chiller starts operating, if the chilled water outlet temperature is low, the heating amount controller (31) which receives the temperature signal from the temperature detector (33) outputs a low combustion signal to the burner (IB). , the burner (IB) performs a low combustion operation of, for example, 30%. Further, the heating amount controller (31) outputs a low combustion signal to the absorption liquid pump controller (32), and the first contact (34) is turned ON. Then, the first electromagnetic switch (36) is energized, the first main contact (37) is ONL, and the first auxiliary contact (38) is energized.
) turns off. When the first main contact is turned on, the rut voltage is applied, and the absorption liquid pump (20) starts star operation.

そして、吸収液ポンプ(20〉の吸収液吐出量はデルタ
運転時の30%になる。
Then, the absorption liquid discharge amount of the absorption liquid pump (20>) becomes 30% of that of the delta operation.

又、冷媒ポンプ(24)も運転され、従来の吸収冷凍機
と同様に吸収液、及び冷媒が循環し、蒸発器〈6〉から
冷水が負荷へ供給される。
Further, the refrigerant pump (24) is also operated, the absorption liquid and refrigerant are circulated in the same manner as in a conventional absorption refrigerator, and cold water is supplied from the evaporator <6> to the load.

その後、冷水負荷が増加し、冷水出口温度が上昇し、所
定の温度になると、温度検出器(33)から温度信号を
入力した加熱量制御器(31)が動作し、バーナ(IB
)へ低燃焼信号に代わり高燃焼信号を出力し、バーナ(
IB)は100%の高燃焼運転を行う。さらに、加熱量
制御器(31)は吸収液ポンプ制御器(32)への低燃
焼信号に代わり高燃焼信号を出力し、第1接点(34)
はOFFすると共に、第2接点(35)がONする。そ
して、第1電磁開閉器(36)が非通電になり、第1主
接点(37)が0FFL、第1補助接点(38)がON
する。そして、第2電磁開閉器(41)が通電され、第
2主接点(41)がONL、第2補助接点(42)がO
FFする。このため、吸収液ポンプ(20〉の各コイル
には200ボルトの電圧が印加きれ、吸収液ポンプ(2
0)はデルタ運転を始める。そして、吸収液ポンプ(2
0)の吸収液吐出量は100%になる。
Thereafter, the chilled water load increases, the chilled water outlet temperature rises, and when it reaches a predetermined temperature, the heating amount controller (31) that inputs the temperature signal from the temperature detector (33) operates, and the burner (IB)
) outputs a high combustion signal instead of a low combustion signal to the burner (
IB) performs 100% high combustion operation. Furthermore, the heating amount controller (31) outputs a high combustion signal instead of the low combustion signal to the absorption liquid pump controller (32), and the first contact (34)
is turned off, and the second contact (35) is turned on. Then, the first electromagnetic switch (36) is de-energized, the first main contact (37) is 0FFL, and the first auxiliary contact (38) is ON.
do. Then, the second electromagnetic switch (41) is energized, the second main contact (41) is ONL, and the second auxiliary contact (42) is OFF.
FF. Therefore, a voltage of 200 volts is applied to each coil of the absorption liquid pump (20), and a voltage of 200 volts is applied to each coil of the absorption liquid pump (20).
0) starts delta operation. Then, absorb liquid pump (2
The amount of absorption liquid discharged in case 0) is 100%.

以後、冷水負荷が減少して冷水出口温度が所定温度まで
低下したときには加熱量制御器(31)が動作してバー
ナ(IB)は低燃焼運転を行い、かつ、吸収液ポンプ制
御器(32)が動作し、吸収液ポンプ(20)はスター
運転を始める。以後、同様に、バーナ(IB)が高燃焼
運転を行っているときには、吸収液ポンプ(20)はデ
ルタ運転を行い、吸収液の循環量は100%に制御され
、バーナ(IB)が低燃焼運転を行っているときには、
吸収液ポンプ(20)はスター運転を行い、吸収液の循
環量はほぼ30%に制御される。又、吸収冷凍機の温水
供給時には、開閉弁(22)が開き冷媒蒸気が下胴(8
)へ流れ蒸発器(6)から温水が供給される。このとき
も、上記冷水供給時と同様に温水出口温度に応じて高温
発生器(1)の加熱量が制御され、それに応じて吸収液
ポンプ(20)はデルタ運転又はスター運転される。
Thereafter, when the chilled water load decreases and the chilled water outlet temperature falls to a predetermined temperature, the heating amount controller (31) operates and the burner (IB) performs low combustion operation, and the absorption liquid pump controller (32) operates. operates, and the absorption liquid pump (20) starts star operation. Thereafter, similarly, when the burner (IB) is performing high combustion operation, the absorption liquid pump (20) performs delta operation, the circulation amount of absorption liquid is controlled to 100%, and the burner (IB) is in low combustion operation. When you are driving,
The absorption liquid pump (20) performs star operation, and the circulation amount of the absorption liquid is controlled to approximately 30%. Also, when hot water is supplied to the absorption chiller, the on-off valve (22) opens and refrigerant vapor flows into the lower shell (8).
) is supplied with hot water from the evaporator (6). At this time as well, the heating amount of the high temperature generator (1) is controlled according to the hot water outlet temperature, as in the case of cold water supply, and the absorption liquid pump (20) is operated in delta operation or star operation accordingly.

上記実施例によれば、冷凍負荷或いは温水負荷に応じて
バーナ(IB〉が高燃焼運転、或いは低燃焼運転を行う
とき、吸収液ポンプ(20〉の結線をデルタ結線、又は
スター結線に切換えることによって、吸収液ポンプ(2
0)をデルタ運転又はスター運転させるので、制御装置
を複雑にすることなく吸収液の循環量を適量に制御する
ことができる。
According to the above embodiment, when the burner (IB) performs high combustion operation or low combustion operation depending on the refrigeration load or hot water load, the connection of the absorption liquid pump (20) can be switched to delta connection or star connection. The absorption liquid pump (2
0) is operated in delta or star mode, the circulation amount of the absorption liquid can be controlled to an appropriate amount without complicating the control device.

又、吸収冷凍機の制御装置のコストを抑えることができ
る。
Furthermore, the cost of the control device for the absorption refrigerator can be reduced.

尚、吸収液ポンプ制御器(32)の回路は第2図に示し
た回路に限定されるものではなく、例えば吸収液ポンプ
(20〉の運転を正転又は逆転させる回路と組合せた場
合には、バーナ(IB)の例えば高燃焼、中燃焼、低燃
焼の状態に応じて吸収液ボンブク20〉の運転を制御す
ることができる。
Note that the circuit of the absorption liquid pump controller (32) is not limited to the circuit shown in FIG. The operation of the absorption liquid bomb 20> can be controlled depending on the state of the burner (IB), for example, high combustion, medium combustion, or low combustion.

又、上記実施例においてバーナ(IB)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、例
えば高温高圧の蒸気を加熱源とする高温発生器を有した
吸収冷凍機においても、加熱量の切換えに応して吸収液
ポンプ(20)と三相交流電源との結線をデルタ結線と
スター結線とに切換えて、吸収液ポンプ(20)をデル
タ運転又はスター運転させることによって、上記実施例
と同様の作用効果を得ることができる。
Further, in the above embodiment, an absorption refrigerator having a high temperature generator (1) equipped with a burner (IB) has been described, but for example, in an absorption refrigerator having a high temperature generator using high temperature and high pressure steam as a heating source, Also, by switching the connection between the absorption liquid pump (20) and the three-phase AC power supply between delta connection and star connection in accordance with the switching of the heating amount, and operating the absorption liquid pump (20) in delta operation or star operation. , it is possible to obtain the same effects as in the above embodiment.

(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装置
であり、負荷に応じて発生器の加熱量を切換える加熱量
制御器と、発生器の加熱量に応じて吸収液ポンプをデル
タ結線運転及びスター結線運転させる吸収液ポンプ制御
器とを備えているので、加熱量制御器で発生器の加熱量
を切換えるとともに、従来のインバータ制御装置のよう
な制御装置を用いることなく吸収液ポンプ制御器によっ
て発生器の加熱量に応じて吸収液ポンプの運転を容易に
切換え吸収液の循環量を適切に制御することができ、又
、吸収冷凍機の制御装置のコストを抑えることができる
(G) Effects of the Invention The present invention is a control device for an absorption refrigerator configured as described above, which includes a heating amount controller that switches the heating amount of the generator according to the load, and a heating amount controller that switches the heating amount of the generator according to the load. Since it is equipped with an absorption liquid pump controller that operates the absorption liquid pump in delta connection operation and star connection operation, the heating amount controller can be used to switch the heating amount of the generator, and a control device such as a conventional inverter control device can be used. The operation of the absorption liquid pump can be easily switched according to the heating amount of the generator using the absorption liquid pump controller to appropriately control the amount of absorption liquid circulation, and the cost of the absorption chiller control system can be reduced. It can be suppressed.

又、燃焼制御器によって負荷に応じて発生器を高燃焼運
転と低燃焼運転に切換えるとともに、高燃焼運転と低燃
焼運転に対して吸収液ポンプ制御器によって吸収液ポン
プと三相交流電源との結線をデルタ結線及びスター結線
に切換えるので、発生器の燃焼量の大小に応じて吸収液
ポンプの能力を容易に切換え、吸収液の循環量を適切に
制御することができる。
In addition, the combustion controller switches the generator between high combustion operation and low combustion operation according to the load, and the absorption liquid pump controller switches between the absorption liquid pump and the three-phase AC power supply for high combustion operation and low combustion operation. Since the connection is switched between a delta connection and a star connection, the capacity of the absorption liquid pump can be easily changed according to the magnitude of the combustion amount of the generator, and the circulation amount of the absorption liquid can be appropriately controlled.

【図面の簡単な説明】[Brief explanation of the drawing]

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図は第1図に示した吸収液ポンプ制御器の概略
回路図、第3図は発生器、及び吸収液ポンプの運転状態
を説明するタイムチャートである。 (1)・・・高温発生器、 (4)・・・凝縮器、 (
6)・・・蒸発器、 り7)・・・吸収器、 (20)
・・・吸収液ポンプ、(31)・・・加熱量制御器、 
(32)・・・吸収液ポンプ制御器。
Fig. 1 is a circuit configuration diagram of an absorption refrigerator showing an embodiment of the present invention, Fig. 2 is a schematic circuit diagram of the absorption liquid pump controller shown in Fig. 1, and Fig. 3 is a generator and absorption liquid diagram. It is a time chart explaining the operating state of a pump. (1)...High temperature generator, (4)...Condenser, (
6)...Evaporator, 7)...Absorber, (20)
... Absorption liquid pump, (31) ... Heating amount controller,
(32)...Absorption liquid pump controller.

Claims (1)

【特許請求の範囲】 1、発生器、凝縮器、蒸発器、吸収器、及び吸収器から
発生器へ吸収液を送る吸収液ポンプなどを配管接続して
冷凍サイクルを形成した吸収冷凍機において、負荷に応
じて発生器の加熱量を切換える加熱量制御器と、発生器
の加熱量に応じて吸収液ポンプをデルタ結線運転及びス
ター結線運転させる吸収液ポンプ制御器とを備えたこと
を特徴とする吸収冷凍機の制御装置。 2、発生器、凝縮器、蒸発器、吸収器、及び三相交流電
源から電力が供給され吸収器から発生器へ吸収液を送る
吸収液ポンプなどを配管接続して冷凍サイクルを形成し
た吸収冷凍機において、負荷に応じて発生器を高燃焼運
転と低燃焼運転とに切換える燃焼制御器と、上記高燃焼
運転及び低燃焼運転に対して吸収液ポンプと三相交流電
源との間の結線をデルタ結線及びスター結線に切換える
吸収液ポンプ制御器とを備えたことを特徴とする吸収冷
凍機の制御装置。
[Scope of Claims] 1. In an absorption refrigerator in which a generator, a condenser, an evaporator, an absorber, an absorption liquid pump for sending absorption liquid from the absorber to the generator, etc. are connected via piping to form a refrigeration cycle, It is characterized by being equipped with a heating amount controller that switches the heating amount of the generator according to the load, and an absorption liquid pump controller that operates the absorption liquid pump in delta connection operation and star connection operation according to the heating amount of the generator. A control device for an absorption chiller. 2. Absorption refrigeration, in which a refrigeration cycle is formed by connecting a generator, condenser, evaporator, absorber, and an absorption liquid pump that is supplied with power from a three-phase AC power source and sends absorption liquid from the absorber to the generator, etc. In the machine, the generator is equipped with a combustion controller that switches the generator between high combustion operation and low combustion operation according to the load, and a connection between the absorption liquid pump and the three-phase AC power source for the high combustion operation and low combustion operation. 1. A control device for an absorption refrigerating machine, comprising: an absorption liquid pump controller that switches between delta connection and star connection.
JP25918590A 1990-09-27 1990-09-27 Controller for absorbing freezer Pending JPH04136666A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25918590A JPH04136666A (en) 1990-09-27 1990-09-27 Controller for absorbing freezer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25918590A JPH04136666A (en) 1990-09-27 1990-09-27 Controller for absorbing freezer

Publications (1)

Publication Number Publication Date
JPH04136666A true JPH04136666A (en) 1992-05-11

Family

ID=17330553

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25918590A Pending JPH04136666A (en) 1990-09-27 1990-09-27 Controller for absorbing freezer

Country Status (1)

Country Link
JP (1) JPH04136666A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0763436A (en) * 1993-08-24 1995-03-10 Yazaki Corp Absorption refrigerating machine

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62262690A (en) * 1986-05-08 1987-11-14 Satake Eng Co Ltd Induction motor
JPH0198864A (en) * 1987-10-09 1989-04-17 Kawasaki Heavy Ind Ltd Method of controlling quantity of absorbing solution circulated in absorption refrigerator

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62262690A (en) * 1986-05-08 1987-11-14 Satake Eng Co Ltd Induction motor
JPH0198864A (en) * 1987-10-09 1989-04-17 Kawasaki Heavy Ind Ltd Method of controlling quantity of absorbing solution circulated in absorption refrigerator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0763436A (en) * 1993-08-24 1995-03-10 Yazaki Corp Absorption refrigerating machine

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