JPS62166271A - Absorption refrigerator - Google Patents

Absorption refrigerator

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Publication number
JPS62166271A
JPS62166271A JP666086A JP666086A JPS62166271A JP S62166271 A JPS62166271 A JP S62166271A JP 666086 A JP666086 A JP 666086A JP 666086 A JP666086 A JP 666086A JP S62166271 A JPS62166271 A JP S62166271A
Authority
JP
Japan
Prior art keywords
liquid
gas
absorption
generator
liquid separator
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
JP666086A
Other languages
Japanese (ja)
Inventor
雅裕 古川
大能 正之
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 JP666086A priority Critical patent/JPS62166271A/en
Publication of JPS62166271A publication Critical patent/JPS62166271A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は、発生器で沸1112!キせた吸収液を冷媒の
気泡によって気液分離器へ揚液する型式の吸収冷凍機や
吸収ヒートポンプ(以下、この種の吸収冷凍機という)
の改良に係り、特にこの種の吸収冷凍機の発生器の空焚
きや気液分離器から凝縮器への吸収液の溢流などを防止
するものに関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention provides a method for boiling 1112! Absorption refrigerators and absorption heat pumps (hereinafter referred to as this type of absorption refrigerator) that pump the quenched absorption liquid to a gas-liquid separator using refrigerant bubbles.
In particular, the present invention relates to improvements in this type of absorption refrigerating machine that prevent dry firing of the generator and overflow of absorption liquid from the gas-liquid separator to the condenser.

(ロ)従来の技術 この種の吸収冷凍機は、稀吸収液を加熱濃縮する燃焼室
とその上位に配列した多数の煙管とから成る炉筒煙管ボ
イラーと同様の構造の満液式発生器を組込んだ吸収冷凍
機にくらべ、高価な吸収液を少量で済まし得てその分燃
費も少なくできる等の利点をもち、例えば実公昭46−
6702号公報、実公昭46−7955号公報、実公昭
56−218号公報、実公昭58−52466号公報な
どでみられるように、以前から主として小型の吸収冷凍
機に多く採用されている。
(B) Conventional technology This type of absorption refrigerator uses a flooded generator with a structure similar to a furnace tube boiler, which consists of a combustion chamber that heats and concentrates the dilute absorption liquid and a number of smoke tubes arranged above the combustion chamber. Compared to a built-in absorption refrigerator, it has the advantage of requiring a small amount of expensive absorption liquid and reducing fuel consumption accordingly.
As seen in Japanese Utility Model Publication No. 6702, Japanese Utility Model Publication No. 46-7955, Japanese Utility Model Publication No. 56-218, and Japanese Utility Model Publication No. 58-52466, it has been widely used mainly in small-sized absorption refrigerators.

(ハ)発明が解決しようとする問題点 この種の吸収冷凍機は、上述のような利点を有している
ものの、その始動時に気液分離器内の吸収液の凝縮器側
への侵入[キ〜り一オーバー]を引起しやすい問題点を
有している。このため、この種の吸収冷凍機においては
、例えば特開昭57−169569号公報にみられるよ
うに、発生器へ稀吸収液を送るポンプに可逆転ポンプを
用いて始動時に発生器内の吸収液が所定温度に高まるま
でポンプを逆回転させることにより、稀吸収液の送り量
を減らしてキャリーオーバーを防ぐ手段が提案されてい
る。しかし、この手段は発生器内の液温か外気温に近い
始動時には有用であるものの、液温か所定温度に近い部
分負荷時にはほとんど有効に働かない。
(c) Problems to be solved by the invention Although this type of absorption refrigerator has the above-mentioned advantages, the absorption liquid in the gas-liquid separator enters the condenser side at the time of startup. This has the problem that it is easy to cause over-keying. For this reason, in this type of absorption refrigerator, a reversible pump is used as the pump for feeding the diluted absorption liquid to the generator, as seen in Japanese Patent Application Laid-Open No. 57-169569, and a reversible pump is used to supply the diluted absorption liquid to the generator. A method has been proposed in which the pump is rotated in reverse until the liquid reaches a predetermined temperature, thereby reducing the amount of dilute absorption liquid fed and preventing carryover. However, although this method is useful at startup when the temperature of the liquid in the generator is close to the outside temperature, it hardly works effectively at partial loads when the temperature of the liquid is close to the predetermined temperature.

そして、この種の吸収冷凍機においては、発生器の加熱
を止めずにその加熱量を減らす部分負荷時、気液分離器
から吸収器側へ流出する吸収液量よりも発生器で生じた
気泡の揚液作用によって気液分離器に流入する吸収液量
の方が多くなりやすいため、キャリーオーバーを引起し
やすい問題点がある。かつまた、発生器の加熱量を減ら
す部分負荷時には、通常、発生器への稀吸収液の送り量
も減らすため、この種の吸収冷凍機においては気液分離
器での吸収液の偏在に伴なって発生器の空焚きを引起し
やすい問題点もある。
In this type of absorption refrigerator, when the heating amount is reduced without stopping the heating of the generator during partial load, the amount of bubbles generated in the generator is larger than the amount of absorbed liquid flowing from the gas-liquid separator to the absorber side. Because the amount of absorbed liquid that flows into the gas-liquid separator tends to increase due to the liquid pumping action, there is a problem that carryover tends to occur. Furthermore, during partial load to reduce the heating amount of the generator, the amount of diluted absorption liquid sent to the generator is also reduced, so in this type of absorption refrigerator, absorption liquid is unevenly distributed in the gas-liquid separator. There is also the problem that the generator tends to run dry.

本発明は、これらの問題点に鑑み、発生器の加熱量を減
じる部分負荷時におけるキャリーオーバーや空焚きなど
の弊害を確実に防ぎ得るこの種の吸収冷凍機の提供を目
的としたものである。
In view of these problems, it is an object of the present invention to provide an absorption refrigerator of this type that can reliably prevent harmful effects such as carryover and dry firing during partial loads that reduce the heating amount of the generator. .

(ニ)問題点を解決するための手段 本発明は、上記の問題点を解決する手段として、稀吸収
液用ポンプに可逆転ポンプを用い、かつ、気液分離器と
発生器との間に逆止弁その他の弁付きの液戻し管路を設
け、気液分離器に備えた液面検出器の感知液位が設定値
まで上昇すると可逆転ポンプを逆転させて稀吸収液の送
り量を減らし、感知液位が上限値まで上昇すると可逆転
ポンプを止め弁を開いて気液分離器の液を発生器へ戻す
ようにこの種の吸収冷凍機を構成したものである。
(d) Means for Solving the Problems The present invention, as a means for solving the above problems, uses a reversible pump as a pump for dilute absorption liquid, and also uses a reversible pump between the gas-liquid separator and the generator. A liquid return line with a check valve or other valve is provided, and when the liquid level sensed by the liquid level detector installed in the gas-liquid separator rises to a set value, the reversible pump is reversed to reduce the amount of dilute absorption liquid sent. This type of absorption refrigerator is configured so that when the detected liquid level rises to the upper limit, the reversible pump is stopped and the valve is opened to return the liquid in the gas-liquid separator to the generator.

(ホ)作用 本発明によるこの種の吸収冷凍機においては、その始動
時や部分負荷時などに気液分離器内の液面が設定値以上
に上昇した場合には発生器および気液分離器への吸収液
を減らし、さらに上限値まで上昇した場合には気液分離
器内の吸収液を戻す一方で所定の液面まで降下した場合
には再び発生器および気液分離器へ吸収液を送り、気液
分離器内の液面位を所定の範囲内に調整する機能(作用
)を発揮する。この機能により、部分負荷時にこの種の
吸収冷凍機において生じやすかったキャリーオーバーや
発生器の空焚きなどの弊害を確実に防止することができ
る。
(E) Function In this type of absorption refrigerator according to the present invention, if the liquid level in the gas-liquid separator rises above a set value during startup or partial load, the generator and gas-liquid separator If the absorption liquid reaches the upper limit, the absorption liquid in the gas-liquid separator is returned, but if the liquid level drops to a predetermined level, the absorption liquid is returned to the generator and the gas-liquid separator. The liquid level within the gas-liquid separator is adjusted within a predetermined range. This function makes it possible to reliably prevent adverse effects such as carryover and dry firing of the generator, which tend to occur in this type of absorption refrigerator during partial loads.

くべ)実施例 図面は本発明によるこの種の吸収冷凍機の一実施例を示
した概略構成説明図である。図において、(1)はガス
や油などの燃焼ガスを用いて稀吸収液を加熱する高温発
生器、(2)は高温発生器(1)で加熱され揚液管(3
)を冷媒蒸気の気泡と共に上昇してきた吸収液からこれ
と冷媒とを分離する気液分離器、(4)は気液分離器(
2)で分離された冷媒蒸気を熱源として中間濃度の吸収
液をさらに加熱して冷媒を分離する低温発生器、(5)
は発生器(1)(4)から流入する冷媒を冷却器(6)
で冷却して液化きせる凝縮器、(7)は凝縮器(5)か
らの冷媒液を散布し気化させる際の潜熱を利用して熱交
換器(8)から冷水を得るようにした蒸発器、(9)は
気液分離器(2)内の吸収液を低温発生器(4)へ溢流
させるオーバーフロー管に備えたトラップ、(10)は
、発生器(1)、(4)において冷媒の分離された濃吸
収液を散布して器内の気状冷媒を吸収しつつ蒸発器(7
)内を低圧に維持することにより、連続して冷水の供給
を行なえるようにした吸収器、(11)は開閉弁(12
)を有してこの開閉弁を暖房時に開くことにより気液分
離器(2)内の高温の冷媒を蒸発吸収胴(13)へ導き
つつ熱交換器(8)から温水を取り出し得るようにした
バイパス管、(14)は冷暖房時において吸収器(10
)からの稀吸収液を発生器(1)へ戻す可逆転の吸収液
用ポンプ、(15)、(16)は低温、高温溶液熱交換
器であり、これらは冷媒用の管路(17)、(18)、
吸収液用の管路(19)、(20)、(21)、揚液管
(3〉、バイパス管(11)などで接続されて従来のこ
の種の吸収冷凍機と同様の冷媒[水]および吸収液[臭
化リチウム水溶液]の循環路を構成している。なお、 
(22)は高温発生器(1)に備えたバーナーであり、
(23)は冷媒液用ポンプである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS (1) Embodiment The drawings are schematic structural explanatory diagrams showing one embodiment of this type of absorption refrigerator according to the present invention. In the figure, (1) is a high-temperature generator that heats the dilute absorption liquid using combustion gas such as gas or oil, and (2) is a high-temperature generator heated by the high-temperature generator (1) and a liquid pump (3).
) is a gas-liquid separator that separates refrigerant from the absorption liquid that has risen together with refrigerant vapor bubbles; (4) is a gas-liquid separator (
(5) a low-temperature generator that uses the refrigerant vapor separated in step 2) as a heat source to further heat the intermediate concentration absorption liquid and separate the refrigerant;
The refrigerant flowing from the generators (1) and (4) is transferred to the cooler (6).
(7) is an evaporator that obtains cold water from a heat exchanger (8) by using latent heat when the refrigerant liquid from the condenser (5) is dispersed and vaporized; (9) is a trap installed in the overflow pipe that causes the absorption liquid in the gas-liquid separator (2) to overflow to the low-temperature generator (4); The separated concentrated absorption liquid is sprayed to absorb the gaseous refrigerant in the evaporator (7).
) The absorber can continuously supply cold water by maintaining a low pressure inside the absorber. (11) is the on-off valve (12).
), and by opening this on-off valve during heating, hot water can be taken out from the heat exchanger (8) while guiding the high-temperature refrigerant in the gas-liquid separator (2) to the evaporative absorption shell (13). The bypass pipe (14) is used to connect the absorber (10) during heating and cooling.
) is a reversible absorption liquid pump that returns the dilute absorption liquid from the generator (1) to the generator (1), (15) and (16) are low temperature and high temperature solution heat exchangers, which are connected to the refrigerant line (17). ,(18),
The refrigerant [water] is connected with the absorption liquid pipes (19), (20), (21), the liquid pumping pipe (3), the bypass pipe (11), etc., and is the same as in the conventional absorption refrigerator of this type. and constitutes a circulation path for the absorption liquid [lithium bromide aqueous solution].
(22) is a burner provided in the high temperature generator (1),
(23) is a refrigerant liquid pump.

そして、(24)は気液分離器(2)と高温発生器(1
)を結んだ液戻し用管路で、この管路には*滋弁や電動
弁などの開閉弁(■)が備えである。
(24) is a gas-liquid separator (2) and a high temperature generator (1).
), and this pipe is equipped with an on-off valve (■) such as a water valve or an electric valve.

また、(LS)は気液分離器(2)内の液面位を検知す
る液面検出器で、この検出器にはそれぞれ上限液面、設
定液面、下限液面を感知する電極(PI>、(P2)、
(P、)が内蔵されている。(C)は制御器で、これに
は液面検出器(LS)の信号が入力されるようになって
いる。そして、気液分離器(2)内の液面位が高くなっ
て電極(P2)端の設定液面まで上昇したときには制御
器(C)により吸収液用ポンプ(14)のモーターへの
通電が逆方向に切換えられてこのモーターを逆回転させ
るマグネット(M2)が励磁され、さらに電極〈P、)
端の上限液面まで上昇したときにはモーターへの通電が
断たれてポンプ(14)が停止きれると同時に開閉弁(
V)が開かれ、一方、液面位が低くなり始めて電極(P
I)端の下限液面まで降下したときには制御器(C)に
より開閉弁(Vンが再び閉じられると同時にポンプ〈1
4〉のモーターを正回転きせるマグネット(Ml)が励
磁きれるようになっている。なお、逆回転時のポンプ(
14)の吐出量は正回転時のそれの40〜60%である
In addition, (LS) is a liquid level detector that detects the liquid level in the gas-liquid separator (2), and this detector has electrodes (PI) that sense the upper limit liquid level, set liquid level, and lower limit liquid level, respectively. >, (P2),
(P,) is built-in. (C) is a controller to which a signal from a liquid level detector (LS) is input. When the liquid level in the gas-liquid separator (2) rises to the set liquid level at the end of the electrode (P2), the controller (C) stops energizing the motor of the absorption liquid pump (14). The magnet (M2), which is switched in the opposite direction and rotates this motor in the opposite direction, is energized, and the electrode <P,)
When the liquid level rises to the upper limit at the end, the power to the motor is cut off, the pump (14) stops, and at the same time the on-off valve (
V) is opened, while the liquid level begins to drop and the electrode (P
I) When the liquid level drops to the lower limit of the end, the controller (C) closes the on-off valve (V-n) again and at the same time the pump <1
The magnet (Ml) that rotates the motor in 4> in the forward direction can be energized. In addition, when the pump rotates in reverse (
14) The discharge amount is 40 to 60% of that during forward rotation.

また、(TS)は熱交換器(8)出口側の冷温水温度を
検出するセンサーで、このセンサーの信号により調節器
(R)を介して燃料制御弁(V、)の開度を制御するこ
とによって従来のこの種の吸収冷凍機と同様に高温発生
器(1)の加熱量を調節する構造となっている。
In addition, (TS) is a sensor that detects the cold/hot water temperature on the outlet side of the heat exchanger (8), and the opening degree of the fuel control valve (V,) is controlled by the signal from this sensor via the regulator (R). As a result, the structure is such that the heating amount of the high temperature generator (1) is adjusted in the same manner as the conventional absorption refrigerator of this type.

次に、このように構成された吸収冷凍機(以下、本機と
いう)の動作例を説明する。
Next, an example of the operation of the absorption refrigerating machine (hereinafter referred to as the present machine) configured as described above will be explained.

今、本機の運転中、例えば冷房を必要とする部屋数が半
減して冷房負荷が100%から50%へ変化したとき、
センサー(Is)の信号により調節器(R)を介して燃
料制御弁(V、)の開度が50%に制御きれ、高温発生
器(1)の加熱量がほぼ子分に減らきれる。加熱量が半
減きれることによって高温発生器(1)および気液分熱
器(2)内の蒸気圧が降下し始め、この気液分離器と低
温発生器(4)間の圧力差が不要くなって気液分離器(
2)からの吸収液の流出量が減り始める。一方、高温発
生器(1〉から気液分熱器(2)への揚液作用は衰える
ものの、吸収器(10)から高温発生器(1)および気
液分離器(2)側への吸収液の送り量は冷房負荷の変化
前と殆んど変わらないためこの気液分離器における液の
出入量のバランスが崩れて液面が上昇し始める。そして
、液面検出器(LS)の電極(P2)下端まで液面が上
昇した際、吸収液用ポンプ(14)のモーターが正回転
から逆回転へ切換えられて高温発生器(1)への吸収液
の送り量がほぼ半分に減らされる。
Now, while the machine is operating, for example, if the number of rooms that require cooling is halved and the cooling load changes from 100% to 50%,
The opening degree of the fuel control valve (V,) can be controlled to 50% by the signal from the sensor (Is) via the regulator (R), and the heating amount of the high temperature generator (1) can be reduced to almost the same amount. As the amount of heating is halved, the vapor pressure in the high temperature generator (1) and the gas-liquid heat separator (2) begins to drop, and the pressure difference between the gas-liquid separator and the low-temperature generator (4) is no longer necessary. Gas-liquid separator (
2) The amount of absorbent flowing out from 2) begins to decrease. On the other hand, although the liquid pumping effect from the high-temperature generator (1) to the gas-liquid heat divider (2) declines, the absorption from the absorber (10) to the high-temperature generator (1) and gas-liquid separator (2) side decreases. Since the amount of liquid sent is almost the same as before the cooling load change, the balance between the amount of liquid in and out of this gas-liquid separator is disrupted and the liquid level begins to rise.Then, the electrode of the liquid level detector (LS) (P2) When the liquid level rises to the lower end, the motor of the absorption liquid pump (14) is switched from forward rotation to reverse rotation, and the amount of absorption liquid sent to the high temperature generator (1) is reduced by approximately half. .

吸収液の送り量がほぼ半減されることによって高温発生
器(1)の熱量不足が解消され、再びこの発生器および
気液分熱器(2)内の蒸気圧が上昇し始めて気液分離器
(2)からの吸収液の流出量も増え始め、かつまた、高
温発生器(1)から気液分離器(2)への揚液作用も活
発となる。しかし、この種の吸収冷凍機においては、揚
液作用による気液分離器(2)への吸収液の流入量と圧
力上昇による気液分離器(2)からの吸収液の流出量と
が必ずしもバランス良く増えないため、気液分離器(2
)内に吸収液が偏在して凝縮器(5)側へしばしばキャ
リーオーバーしやすくなる。さらにまた、気液分離器(
2)内での吸収液の偏在に伴ない高温発生器(1)への
吸収液の送り量の減少時にはこの発生器の貯液不足を引
起して空焚きに近い状態に陥いる場合もある。
By reducing the amount of absorption liquid sent by almost half, the lack of heat in the high-temperature generator (1) is resolved, and the vapor pressure in this generator and the gas-liquid heat separator (2) begins to rise again, causing the gas-liquid separator to rise. The amount of absorption liquid flowing out from (2) also begins to increase, and the liquid pumping action from the high temperature generator (1) to the gas-liquid separator (2) also becomes active. However, in this type of absorption refrigerator, the amount of absorption liquid flowing into the gas-liquid separator (2) due to liquid pumping and the amount of absorption liquid flowing out from the gas-liquid separator (2) due to pressure increase are not necessarily equal. Since it does not increase in a well-balanced manner, a gas-liquid separator (2
), the absorbing liquid is unevenly distributed in the condenser (5) and tends to often carry over to the condenser (5) side. Furthermore, a gas-liquid separator (
2) When the amount of absorption liquid sent to the high-temperature generator (1) decreases due to the uneven distribution of absorption liquid within the generator, this generator may not be able to store enough liquid, resulting in a situation close to dry firing. .

このような場合、本機においては、気液分離器(2)の
液面が検出器(LS)の電極(P、)端まで上昇した時
点で、吸収液用ポンプ(14)の稼動が止められると同
時に弁(V)が開かれて気液分離器(2)内の吸収液が
管路(24)経由で高温発生器(1)へ戻される。その
結果、気液分離器(2)での吸収液の偏在が解消符れ、
吸収液のキャリーオーバーや高温発生器(1〉の空焚き
が確実に防止される。なお、弁(V)は電磁弁や電動弁
その他の開閉弁を用いる代りに破線で示した逆止弁(■
c)を用いるようにしても良い。逆止弁(VC)を用い
た際には、ポンプ(14)を停止させることによって逆
止弁(VC)の閉止力となるポンプ吐出圧が解除されて
弁が開き、気液分離器(2)内の吸収液が高温発生器(
1)へ戻される。このため、制御器(C)と逆止弁(V
、l:)とを電気的に接続する必要がなく、制御回路を
簡略化できる利点がある。
In such a case, in this machine, the absorption liquid pump (14) stops operating when the liquid level in the gas-liquid separator (2) rises to the electrode (P,) end of the detector (LS). At the same time, the valve (V) is opened and the absorption liquid in the gas-liquid separator (2) is returned to the high temperature generator (1) via the pipe (24). As a result, the uneven distribution of the absorption liquid in the gas-liquid separator (2) is eliminated,
Carry-over of the absorption liquid and dry firing of the high temperature generator (1) are reliably prevented.Instead of using a solenoid valve, electric valve or other shut-off valve, the valve (V) is a check valve (shown with a broken line). ■
c) may also be used. When a check valve (VC) is used, by stopping the pump (14), the pump discharge pressure that acts as the closing force of the check valve (VC) is released, the valve opens, and the gas-liquid separator (2 ) is absorbed into the high temperature generator (
Returned to 1). For this reason, the controller (C) and the check valve (V
, l:), which has the advantage of simplifying the control circuit.

上記の動作例の説明から分かるように、炉筒煙管ボイラ
ーと同様の構造の満液式発生器を組み込んだ吸収冷凍機
においては殆んど問題とならない弊害すなわち発生器の
加熱量と吸収液の送り量の減らされる部分負荷時に生じ
やすい気液分離器(2)内の吸収液のキャリーオーバー
や発生器(1)の空焚きなどこの種の吸収冷凍機に特有
の弊害を本機では確実に防ぐことができる。
As can be seen from the explanation of the operation example above, an absorption chiller incorporating a flooded generator with a structure similar to that of a fire tube boiler has a problem that is hardly a problem, that is, the heating amount of the generator and the absorption liquid This machine reliably eliminates the problems peculiar to this type of absorption refrigerator, such as carryover of absorbent liquid in the gas-liquid separator (2) and dry firing of the generator (1), which tend to occur during partial loads when the feed rate is reduced. It can be prevented.

また、本機においては、気液分離器(2)の液面が検出
器(LS>の電極(P、)端まで降下すると吸収液用ポ
ンプ(14)が再び稼動されると同時に弁(v)が閉じ
られて気液分離器(2)内の液面位が電極(P、)端と
電極(P、)端との間に保たれる。
In addition, in this machine, when the liquid level of the gas-liquid separator (2) falls to the end of the electrode (P,) of the detector (LS>), the absorption liquid pump (14) is operated again and at the same time the valve (v ) is closed and the liquid level in the gas-liquid separator (2) is maintained between the electrode (P, ) ends and the electrode (P, ) ends.

なお、本機において、検出器(LS)の信号で制御器(
C)によりポンブク14)を再び稼動させる際に、セン
サー(I’S)の信号を制御器(C)へ送ってカスケー
ド制御することにより、部分負荷時にはマグネット(L
)を働かせてポンプ(14)のモーターを逆回転させる
ようにしても良い。
In addition, in this machine, the controller (
When the pump 14) is operated again by C), the signal from the sensor (I'S) is sent to the controller (C) for cascade control, so that the magnet (L) is activated at partial load.
) may be activated to rotate the pump (14) motor in the reverse direction.

(ト)発明の効果 以上のとおり、本発明によるこの種の吸収冷凍機におい
ては、発生器の加熱量と発生器への吸収液の送り量を減
らされる部分負荷時に生じやすい気液分離器での吸収液
の偏在とこれに伴なう吸収液の凝縮器側へのキャリーオ
ーバーおよび発生器の空焚きとを確実に防ぎ得る効果が
もたらされる。
(G) Effects of the Invention As described above, in this type of absorption refrigerator according to the present invention, the gas-liquid separator that tends to occur during partial load when the heating amount of the generator and the amount of absorption liquid sent to the generator are reduced. This brings about the effect of reliably preventing the uneven distribution of the absorption liquid, the accompanying carryover of the absorption liquid to the condenser side, and the dry firing of the generator.

なお、本発明を一重効用のこの種の吸収冷凍機に適用し
得ることは無論である。
It goes without saying that the present invention can be applied to this type of single-effect absorption refrigerator.

揚液管、 (4)・・・低温発生器、 (5)・・・凝
縮器、(7)・・・蒸発器、 (8〉・・・熱交換器、
 (10〉・・・吸収器、(14)・・・吸収液用ポン
プ、 (17)、(18)、(19)、(20)、(2
1)・・・管路、 (22)・・・バーナー、  (2
4)・・・液戻し用管路、(C)・・・制御器、 (L
S)・・・液面検出器、 (Ml)、(シ)・・・マグ
ネット、 (R)・・・調節器、(I’S)・・・セン
サー、 (V)・・・開閉弁、(VC)・・・逆止弁、
(VF)・・・燃料制御弁。
Lifting pipe, (4)...low temperature generator, (5)...condenser, (7)...evaporator, (8>...heat exchanger,
(10>...Absorber, (14)...Absorption liquid pump, (17), (18), (19), (20), (2
1)...Pipe line, (22)...Burner, (2
4)...liquid return pipe line, (C)...controller, (L
S)...liquid level detector, (Ml), (shi)...magnet, (R)...regulator, (I'S)...sensor, (V)...open/close valve, (VC)...Check valve,
(VF)...Fuel control valve.

Claims (1)

【特許請求の範囲】[Claims] (1)発生器で濃縮した吸収液と発生した冷媒蒸気とを
管路経由で気液分離器へ上昇させこの気液分離器で分離
した吸収液を吸収器側へ導くと共に分離した冷媒を凝縮
器、蒸発器側へ導くよう構成した吸収冷凍機において、
吸収器から発生器側へ吸収液を送る管路には逆通電時に
正常通電時よりも吐出液量の少なくなる可逆転ポンプが
配設されると共に気液分離器と発生器との間には逆止弁
その他の弁付きの液戻し用管路が配設され、かつ、気液
分離器内の複数の液面位を検知する液面検出器の信号に
より可逆転ポンプの正逆通電の切換えあるいはポンプの
発停や弁の開閉を行なって気液分離器内の液面位を所定
の範囲内に調整する制御器が備えられていることを特徴
とした吸収冷凍機。
(1) The absorbed liquid concentrated in the generator and the refrigerant vapor generated rise to a gas-liquid separator via a pipe, and the absorbed liquid separated by this gas-liquid separator is guided to the absorber side, and the separated refrigerant is condensed. In an absorption refrigerator configured to lead to the evaporator side,
A reversible pump, which discharges less liquid during reverse energization than during normal energization, is installed in the pipeline that sends the absorption liquid from the absorber to the generator side, and a reversible pump is installed between the gas-liquid separator and the generator. A liquid return line with check valves and other valves is installed, and the reversible pump can be switched between forward and reverse energization based on signals from a liquid level detector that detects multiple liquid levels in the gas-liquid separator. Alternatively, an absorption refrigerating machine characterized by being equipped with a controller that adjusts the liquid level within a gas-liquid separator to within a predetermined range by starting and stopping a pump and opening and closing a valve.
JP666086A 1986-01-16 1986-01-16 Absorption refrigerator Pending JPS62166271A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP666086A JPS62166271A (en) 1986-01-16 1986-01-16 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP666086A JPS62166271A (en) 1986-01-16 1986-01-16 Absorption refrigerator

Publications (1)

Publication Number Publication Date
JPS62166271A true JPS62166271A (en) 1987-07-22

Family

ID=11644533

Family Applications (1)

Application Number Title Priority Date Filing Date
JP666086A Pending JPS62166271A (en) 1986-01-16 1986-01-16 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS62166271A (en)

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