JPS5824706B2 - Control device for dual effect absorption chiller - Google Patents
Control device for dual effect absorption chillerInfo
- Publication number
- JPS5824706B2 JPS5824706B2 JP3021979A JP3021979A JPS5824706B2 JP S5824706 B2 JPS5824706 B2 JP S5824706B2 JP 3021979 A JP3021979 A JP 3021979A JP 3021979 A JP3021979 A JP 3021979A JP S5824706 B2 JPS5824706 B2 JP S5824706B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- evaporator
- high temperature
- separator
- solenoid 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
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は二重効用吸収冷凍機の制御装置に関するもので
、特に部分負荷時の効率を高めて冷水温度の安定化をは
かると共に起動時の立ち上シ時間を短縮し、同時に液循
環を良好にすることを目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a control device for a dual-effect absorption chiller, which improves efficiency particularly at partial loads, stabilizes chilled water temperature, and shortens start-up time at startup. At the same time, the purpose is to improve liquid circulation.
一般に20冷凍トン以下の比較的小容量の吸収冷凍機に
おいては、燃焼量が小さく、また構造を簡単で安価なも
のとするために0N−OFF制御方式のバーナが使用さ
れ、冷水温度によってこのバーナが制御されている。In general, in relatively small capacity absorption chillers of 20 refrigeration tons or less, burners with 0N-OFF control are used in order to have a small amount of combustion and to keep the structure simple and inexpensive. is controlled.
したがって冷房時部分負荷となシ冷水温度が低下すると
バーナがOFFとなるが、燃焼が停止すると、冷媒及び
吸収液の散布も停止する。Therefore, when there is a partial load during cooling, the burner is turned off when the chilled water temperature drops, but when combustion stops, the spraying of the refrigerant and absorption liquid also stops.
そのために冷媒能力が零となり部分負荷期間の効率は全
負荷時に比べ低下するという欠点があった。Therefore, there was a drawback that the refrigerant capacity became zero and the efficiency during the partial load period was lower than that during the full load period.
本発明は上記の点に鑑みてなされたもので以下図に示す
実施例について説明する。The present invention has been made in view of the above points, and an embodiment shown in the drawings will be described below.
1は燃焼器2によシ槽液を沸騰せしめて冷媒蒸気を発生
せしめる高温発生器、3は前記高温発生器1から冷媒蒸
気の気泡と共に揚液された槽液よシ冷媒を分離する分離
器、4は前記分離器3から送出された冷媒蒸気を熱源と
して中間液を再熱し更に冷媒を分離する低温発生器、5
は冷却器6によシ前記分離器3及び低温発生器4から流
入する冷媒を冷却し且つ凝縮する凝縮器、7は前記凝縮
器5からの液冷媒を散布し気化させる際の潜熱を利用し
て冷水器8から冷房用冷水を得るようにした蒸発器、9
は前記低温発生器4で中間液から冷媒を分離した後の濃
液を散布して器内の冷媒蒸気を吸収することによシ前記
蒸発器7の内部を低圧に維持し連続した冷水の供給を行
なえるようにした吸収器、10及び11は低温熱交換器
と高温熱交換器、12はレベルタンクでこれらは揚液t
13、冷媒蒸気配管14、冷媒液流下管15、気泡ポン
プ16を有した冷媒循環路17、吸収液ポンプ18を有
した槽液管19,20,21、中間液管22及び濃液管
23によシ配管接続して冷凍サイクルを構成すると共に
前記分離器3とレベルタンク12は均圧管24によシ連
通している。1 is a high-temperature generator that boils the tank liquid in the combustor 2 to generate refrigerant vapor, and 3 is a separator that separates the tank liquid and refrigerant pumped up from the high-temperature generator 1 together with refrigerant vapor bubbles. , 4 is a low temperature generator that reheats the intermediate liquid using the refrigerant vapor sent out from the separator 3 as a heat source and further separates the refrigerant; 5
7 is a condenser that cools and condenses the refrigerant flowing into the cooler 6 from the separator 3 and the low temperature generator 4; an evaporator configured to obtain cold water for cooling from a water cooler 8;
After separating the refrigerant from the intermediate liquid in the low-temperature generator 4, the concentrated liquid is dispersed to absorb the refrigerant vapor in the container, thereby maintaining the inside of the evaporator 7 at a low pressure and continuously supplying cold water. 10 and 11 are low-temperature heat exchangers and high-temperature heat exchangers, 12 is a level tank, and these are pumped liquid t
13, refrigerant vapor pipe 14, refrigerant liquid down-flow pipe 15, refrigerant circulation path 17 with bubble pump 16, tank liquid pipes 19, 20, 21 with absorption liquid pump 18, intermediate liquid pipe 22 and concentrated liquid pipe 23. The separator 3 and the level tank 12 are connected through a pressure equalization pipe 24 to form a refrigeration cycle.
而して前記冷媒液流下管15は蒸発器7の上方に位置す
る冷媒散布器25に接続すると共に該散布器の上流側に
冷媒タンク26を形成し該タンクと前記冷媒散布器25
は冷媒流出管27と並例に電磁弁Sv1を有した側路管
28で接続している。The refrigerant liquid down-flow pipe 15 is connected to a refrigerant dispersion device 25 located above the evaporator 7, and a refrigerant tank 26 is formed on the upstream side of the dispersion device.
is connected to the refrigerant outflow pipe 27 by a side pipe 28 which similarly has a solenoid valve Sv1.
また分離器3と吸収器9の上方に位置する吸収液散布器
29は電磁弁S■2を有した溶液導管30で接続してい
る。Further, the separator 3 and the absorption liquid dispersion device 29 located above the absorber 9 are connected through a solution conduit 30 having a solenoid valve S2.
THlは冷水器8の出口温度を検出するサーモスタット
で該サーモスタットからの信号で高温発生器1の燃料制
御弁31を開閉すると共に前記両電磁弁SV0.SV2
を開閉する。THl is a thermostat that detects the outlet temperature of the water cooler 8, and a signal from the thermostat opens and closes the fuel control valve 31 of the high temperature generator 1, and also opens and closes the fuel control valve 31 of the high temperature generator 1, and also opens and closes the fuel control valve 31 of the high temperature generator 1. SV2
Open and close.
また高温発生器1の液温を検出するサーモスタットTH
2からの信号によっても前記両電磁弁S■1.Sv2を
開閉することが出来る。Additionally, a thermostat TH detects the liquid temperature of the high temperature generator 1.
2 also causes both of the solenoid valves S■1. Sv2 can be opened and closed.
上記の構成において通常運転中は燃料制御弁31は開、
電磁弁SV1及びSV2はいずれも閉となっておシ、凝
縮器5から冷媒散布器25に流下する冷媒液は途中の冷
媒タンク26に貯溜されタンクの上部より冷媒流出管2
7を通シ前記冷媒散布器25に流入して蒸発器8に散布
されて気化する。In the above configuration, during normal operation, the fuel control valve 31 is open;
Both electromagnetic valves SV1 and SV2 are closed, and the refrigerant liquid flowing down from the condenser 5 to the refrigerant spargeer 25 is stored in the refrigerant tank 26 on the way, and then flows from the upper part of the tank into the refrigerant outflow pipe 2.
The refrigerant 7 flows through the refrigerant dispersion device 25, is dispersed in the evaporator 8, and is vaporized.
これによシ冷水器8から冷房負荷に供給される冷水の温
度は次第に低下し設定値に達し部分負荷となる。As a result, the temperature of the cold water supplied from the water cooler 8 to the cooling load gradually decreases until it reaches the set value and becomes a partial load.
この時冷水温度が低下するとサーモスタツ)THlから
の信号によシ燃焼制御弁31が閉となシ燃焼器2の加燃
動作が停止する。At this time, when the cold water temperature decreases, the combustion control valve 31 is closed in response to a signal from the thermostat THL, and the combustion operation of the combustor 2 is stopped.
そして前記サーモスタツ)THlの信号又は高温発生器
1の液温を検出するサーモスタットTH2の信号によシ
ミ磁弁S■1 とS■2を開くと蒸発器8へは冷媒タン
ク26に貯溜されている冷媒が側路管28を通シ流入す
ると共に吸収器9へは分離器3からの中間吸収液が溶液
導管30を通シ流入するために冷凍能力の維持が可能と
なシ同時に冷水温度の上昇が防止できる。When the magnetic valves S1 and S2 are opened in response to the signal from the thermostat THl or the signal from the thermostat TH2 which detects the liquid temperature of the high temperature generator 1, the refrigerant is stored in the tank 26 and sent to the evaporator 8. Since the refrigerant flows into the absorber 9 through the side pipe 28 and the intermediate absorption liquid from the separator 3 flows into the absorber 9 through the solution conduit 30, it is possible to maintain the refrigeration capacity, and at the same time, the temperature of the chilled water increases. can be prevented.
また電磁弁Sv2の開によシ部分負荷時には分離器3の
液面上昇及び吸収液ポンプ18のキャビテーショントラ
ブルを防止することができる。Furthermore, by opening the solenoid valve Sv2, it is possible to prevent a rise in the liquid level in the separator 3 and cavitation troubles in the absorption liquid pump 18 during partial load.
また吸収冷凍機の運転停止時に別の電気回路によす電磁
弁SV1を閉、Sv2を開となるように操作し、次の運
転再開時に備えるようにすれば、起動待電磁弁SV1及
びS■2を開とすると、運転開始と同時に蒸発器7と吸
収器9に冷媒と吸収液が散布されるので起動時間が著し
く短縮され、吸収液循環不良のトラブルも同時に解消さ
れる。In addition, if the solenoid valve SV1 connected to another electric circuit is closed and the solenoid valve Sv2 is opened when the operation of the absorption chiller is stopped, in preparation for the next restart of operation, the start-up standby solenoid valves SV1 and S If 2 is opened, the refrigerant and absorption liquid are sprayed into the evaporator 7 and absorber 9 at the same time as the start of operation, so the start-up time is significantly shortened and the problem of poor circulation of the absorption liquid is also solved at the same time.
尚冷水器8よシ温水を得る場合は、配管32゜33に設
けた開閉弁■1.■2をいずれも開として吸収器9と冷
却器6に対する冷却水の流通を停止すれば高温発生器1
で加熱された補液は分離器3で冷媒を分離して中間液と
なシ配管33よシ吸収器9に流入すると共に冷媒蒸気は
配管32、低温発生器4の上部空間及びUシール管34
を通シ蒸発器7に流入し水との熱交換により凝縮して吸
収液に吸収される。In addition, when obtaining hot water from the water cooler 8, use the on-off valves installed in the pipes 32 and 33■1. ■If both 2 are opened and the flow of cooling water to the absorber 9 and the cooler 6 is stopped, the high temperature generator 1
The refrigerant heated in the separator 3 separates the refrigerant and becomes an intermediate liquid.The refrigerant vapor flows through the pipe 33 into the absorber 9, and the refrigerant vapor flows through the pipe 32, the upper space of the low temperature generator 4, and the U-seal pipe 34.
It flows into the evaporator 7, condenses through heat exchange with water, and is absorbed into the absorption liquid.
これによシ暖房用温水が得られる。This provides hot water for heating.
本発明は上述の如く、高温発生器、分離器、低温発生器
、凝縮器、蒸発器、吸収器、低温熱交換器及び高温熱交
換器等を接続して冷凍サイクルを構成し、前記蒸発器で
熱交換した冷水を負荷に供給するようにした二重効用吸
収冷凍機において、前記凝縮器と蒸発器の上方に位置す
る冷媒散布器を電磁弁S■1 を有した側路管で接続す
ると共に分離器と吸収器の上方に位置する吸収液散布器
を電磁弁Sv2を有した溶液導管で接続し、前記蒸発器
よシ供給される冷水の温度をサーモスタットTH1で検
出して部分負荷時に高温発生器の加熱制御弁を閉じると
共に前記サーモスタツ1−TH1或は前記高温発生器の
液温を検出するサーモスタットTH2のいずれかによシ
前記両電磁弁S■1SV2を開くようにしたものである
から、部分負荷時においても冷凍能力の維持ができ効率
を高めると共に冷水温度の上昇ギ防止して安定化をはか
ることができる。As described above, the present invention configures a refrigeration cycle by connecting a high temperature generator, a separator, a low temperature generator, a condenser, an evaporator, an absorber, a low temperature heat exchanger, a high temperature heat exchanger, etc. In a double-effect absorption refrigerator that supplies chilled water heat exchanged with a load to a load, the refrigerant distribution device located above the condenser and evaporator is connected by a side pipe having a solenoid valve S1. At the same time, the separator and the absorption liquid distribution device located above the absorber are connected by a solution conduit having a solenoid valve Sv2, and the temperature of the cold water supplied from the evaporator is detected by a thermostat TH1, and the temperature of the cold water supplied from the evaporator is detected by a thermostat TH1, and the high temperature is adjusted at partial load. This is because the heating control valve of the generator is closed and both the electromagnetic valves S1SV2 are opened by either the thermostat 1-TH1 or the thermostat TH2 that detects the liquid temperature of the high temperature generator. The refrigerating capacity can be maintained even under partial load, increasing efficiency and stabilizing the chilled water temperature by preventing it from rising.
また分離器の液面上昇、吸収液ポンプのキャビテーショ
ントラブルも防止出来るなど実用上有益な効果がある。It also has practical effects such as preventing the rise in liquid level in the separator and cavitation problems in the absorption pump.
図面は本発明装置を備えた二重効用吸収冷凍機の一実施
例を示す回路構成図である。
1・・・高温発生器、3・・・分離器、7・・・蒸発器
、8・・・冷水器、25・・・冷媒散布器、29・・・
吸収液散布器、THl・・・サーモスタット、TH2・
・・サーモスタット、Svl・・・電磁弁、S■2・・
・電磁弁。The drawing is a circuit diagram showing an embodiment of a dual-effect absorption refrigerator equipped with the device of the present invention. 1... High temperature generator, 3... Separator, 7... Evaporator, 8... Water cooler, 25... Refrigerant distribution device, 29...
Absorption liquid sprayer, THL... thermostat, TH2...
・・Thermostat, Svl・Solenoid valve, S■2・・
·solenoid valve.
Claims (1)
、吸収器、低温熱交換器及び高温熱交換器等を接続して
冷凍サイクルを構成し、前記蒸発器で熱交換した冷水を
負荷に供給するようにした二重効用吸収冷凍機において
、前記凝縮器と蒸発器の上方に位置する冷媒散布器の間
に冷媒タンクを設け、該タンクと冷媒散布器を電磁弁S
V1を有した側路管で接続すると共に分離器と吸収器の
上方に位置する吸収液散布器を電磁弁S■2を有した溶
液導管で接続し、前記蒸発器よシ供給される冷水の温度
をサーモスタツ)THlで検出して部分負荷時に高温発
生器の加熱制御弁を閉じると共に前記サーモスタツ)T
Hl或は前記高温発生器の液温を検出するサーモスタッ
トTH2のいずれかによシ前記両電磁弁S■1.S■2
を開くようにしたことを特徴とする二重効用吸収冷凍機
の制御装置。1 A refrigeration cycle is constructed by connecting a high temperature generator, a separator, a low temperature generator, a condenser, an evaporator, an absorber, a low temperature heat exchanger, a high temperature heat exchanger, etc., and the cold water heat exchanged with the evaporator is In a dual-effect absorption refrigerating machine configured to supply a load, a refrigerant tank is provided between the condenser and the refrigerant spreader located above the evaporator, and the tank and the refrigerant spreader are connected to each other by a solenoid valve S.
At the same time, the separator and the absorption liquid distribution device located above the absorber are connected by a side pipe having a solenoid valve S2, and the cold water supplied from the evaporator is connected by a side pipe having a solenoid valve S2. The temperature is detected by the thermostat) THL and the heating control valve of the high temperature generator is closed at partial load.
Both the solenoid valves S1. S■2
A control device for a dual-effect absorption refrigerator, characterized in that the device is configured to open.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3021979A JPS5824706B2 (en) | 1979-03-14 | 1979-03-14 | Control device for dual effect absorption chiller |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3021979A JPS5824706B2 (en) | 1979-03-14 | 1979-03-14 | Control device for dual effect absorption chiller |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55121360A JPS55121360A (en) | 1980-09-18 |
JPS5824706B2 true JPS5824706B2 (en) | 1983-05-23 |
Family
ID=12297600
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3021979A Expired JPS5824706B2 (en) | 1979-03-14 | 1979-03-14 | Control device for dual effect absorption chiller |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5824706B2 (en) |
-
1979
- 1979-03-14 JP JP3021979A patent/JPS5824706B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS55121360A (en) | 1980-09-18 |
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