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JPH0623627B2 - Cold water flow controller for absorption refrigerator - Google Patents
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JPH0623627B2 - Cold water flow controller for absorption refrigerator - Google Patents

Cold water flow controller for absorption refrigerator

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Publication number
JPH0623627B2
JPH0623627B2 JP20106085A JP20106085A JPH0623627B2 JP H0623627 B2 JPH0623627 B2 JP H0623627B2 JP 20106085 A JP20106085 A JP 20106085A JP 20106085 A JP20106085 A JP 20106085A JP H0623627 B2 JPH0623627 B2 JP H0623627B2
Authority
JP
Japan
Prior art keywords
cold water
flow rate
water flow
refrigerant
evaporator
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 - Lifetime
Application number
JP20106085A
Other languages
Japanese (ja)
Other versions
JPS6262163A (en
Inventor
雅裕 古川
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 JP20106085A priority Critical patent/JPH0623627B2/en
Publication of JPS6262163A publication Critical patent/JPS6262163A/en
Publication of JPH0623627B2 publication Critical patent/JPH0623627B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、ポンプの吐出量制御もしくは台数制御によ
り、吸収冷凍機への冷水の供給量を調節する装置(以
下、この種の装置という)の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a device for controlling the supply amount of cold water to an absorption refrigerator by controlling the discharge amount of pumps or the number of pumps (hereinafter referred to as this type of device). ) Regarding the improvement.

(ロ) 従来の技術 この種の装置の従来の技術として、例えば特公昭53−
2216号公報にみられるように、50%負荷時に2台
の冷却水ポンプのうちの1台を停止すると共に冷媒ポン
プの運転および発生器の加熱を一時中断し、冷水温度の
所定の上昇により2台の冷水ポンプのうちの1台を停止
し冷媒ポンプの運転および発生器の加熱を復帰させて吸
収冷凍機の低負荷運転を維持するものが知られている。
(B) Conventional technology As a conventional technology of this type of apparatus, for example, Japanese Patent Publication No. 53-
As disclosed in Japanese Patent No. 2216, at the time of 50% load, one of the two cooling water pumps is stopped, the operation of the refrigerant pump and the heating of the generator are temporarily stopped, and 2 It is known that one of the chilled water pumps is stopped to resume the operation of the refrigerant pump and the heating of the generator to maintain the low load operation of the absorption refrigerator.

(ハ) 発明が解決しようとする問題点 上記した従来のこの種の装置においては、吸収冷凍機に
対する負荷が100%から50%へ急変した際に発生器
の加熱を一時中断し冷水温度の所定の上昇を待って2台
の冷水ポンプのうちの1台を停止するため、負荷の急減
時における冷水凍結を確実に防ぐことができる。しか
し、負荷の急減時に冷媒ポンプの運転が一時休止される
のに対し吸収液ポンプの運転は継続されていて吸収器で
冷媒が吸収されるため、例えば冷媒散布器に滞留してい
る少量の冷媒液や蒸発器の冷媒液溜めの上層部の冷媒液
が凍結する場合がある。この場合、冷媒ポンプの過負荷
防止やキャビテーション防止のための安全装置が働き、
冷水が所定温度まで上昇しても冷媒ポンプの運転および
発生器の加熱が復帰されないことになる。このため、吸
収冷凍機の運転が休止されたままとなり、冷水温度が必
要以上に上昇してしまう問題点があった。
(C) Problems to be solved by the invention In the above-mentioned conventional device of this type, when the load on the absorption refrigerator is suddenly changed from 100% to 50%, the heating of the generator is temporarily stopped to set the chilled water temperature to a predetermined level. Since one of the two cold water pumps is stopped after waiting for the rise of the cold water, it is possible to surely prevent the freezing of the cold water when the load suddenly decreases. However, while the operation of the refrigerant pump is temporarily stopped when the load suddenly decreases, the operation of the absorption liquid pump is continued and the refrigerant is absorbed by the absorber, so that, for example, a small amount of refrigerant that remains in the refrigerant spreader. The liquid or the liquid refrigerant in the upper layer of the liquid refrigerant reservoir of the evaporator may freeze. In this case, a safety device works to prevent overload and cavitation of the refrigerant pump,
Even if the cold water rises to a predetermined temperature, the operation of the refrigerant pump and the heating of the generator are not restored. Therefore, there is a problem that the operation of the absorption chiller remains stopped and the cold water temperature rises more than necessary.

また、発生器の加熱を一時中断するため、運転再開に立
上り時間を要し、運転が不安定になりやすい問題点もあ
った。
Further, since the heating of the generator is temporarily interrupted, it takes a rise time to restart the operation, and there is a problem that the operation tends to be unstable.

本発明は、ポンプの台数制御や吐出量制御により吸収冷
凍機への冷水供給量を急減させる際に生じやすい問題点
すなわち冷媒や冷水の凍結を未然に防ぎ、吸収冷凍機の
運転を安定的に継続させ得るこの種の装置の提供を目的
としたものである。
The present invention prevents problems, such as refrigerant and cold water freezing, that occur easily when the cold water supply amount to the absorption refrigerator is sharply reduced by controlling the number of pumps and the discharge amount control, and stabilizes the operation of the absorption refrigerator. The purpose is to provide a device of this kind that can be continued.

(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、吸収冷
凍機に供給する冷水の流量を急減させた際に蒸発器を流
れる冷水の流量の変化に応じて変化する蒸発器内の冷媒
温度や蒸気圧などの物理量が設定値に達した場合、この
物理量を感知する検出器の信号を受けて冷水流量の増加
補正信号を発する調整器をこの種の装置に備える構成と
したものである。
(D) Means for solving the problem The present invention, as a means for solving the above problems, changes in the flow rate of the cold water flowing through the evaporator when the flow rate of the cold water supplied to the absorption refrigerator is sharply reduced. When a physical quantity such as refrigerant temperature or vapor pressure in the evaporator that changes in accordance with it reaches a set value, a controller that receives a signal from a detector that senses this physical quantity and issues an increase correction signal of the chilled water flow rate The configuration is provided for the device.

(ホ) 作用 本発明のこの種の装置によれば、蒸発器内の冷媒液温度
や蒸気圧が過度に低下する前の設定値に達すると蒸発器
における冷水流量を増加補正して冷媒液の温度とその飽
和蒸気圧を再び上昇させる作用〔働き〕を吸収冷凍機に
もたらすので、冷媒の冷凍延いては冷水の凍結を未然に
防ぐことができる。
(E) Action According to this kind of device of the present invention, when the refrigerant liquid temperature or vapor pressure in the evaporator reaches a set value before excessive reduction, the flow rate of the cold water in the evaporator is corrected to increase and Since the absorption refrigerator has the function of increasing the temperature and its saturated vapor pressure again, it is possible to prevent freezing of the refrigerant and freezing of cold water.

そして、従来のこの種の装置を備えた吸収冷凍機にくら
べ、その運転をより安定させて続けることができる。
And, compared with the conventional absorption refrigerator having this kind of device, the operation can be continued more stably.

(ヘ) 実施例 第1図は本発明によるこの種の装置の一実施例を示した
概略構成説明図である。第1図において、(1)は高温発
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)、(7)はそれぞれ低温、高温溶液熱交
換器、(PR)は冷媒液用ポンプ、(PA)は吸収液用ポン
プで、これらを冷媒の流れる管(8)、(9)、冷媒後の流下
する管(10)、冷媒液の還流する管(11)、(12)、稀吸収液
の送られる管(13)、(14)、中間濃度の吸収液の流れる管
(15)、(16)、濃吸収液の流れる管(17)、(18)により接続
して従来の二重効用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〕の循環路が構成されて
いる。
(F) Embodiment FIG. 1 is a schematic configuration explanatory view showing an embodiment of this type of apparatus according to the present invention. In FIG. 1, (1) is a high temperature generator, (2) is a low temperature generator, (3) is a condenser, (4) is an evaporator,
(5) is an absorber, (6) and (7) are low-temperature and high-temperature solution heat exchangers, (P R ) is a refrigerant liquid pump, and (P A ) is an absorption liquid pump, through which the refrigerant flows. Pipes (8), (9), pipes (10) that flow down after the refrigerant, pipes (11), (12) that flow back the refrigerant liquid, pipes (13), (14) to which the dilute absorption liquid is sent, intermediate concentration Absorption liquid flow tube
(15), (16), the pipes (17), (18) through which the concentrated absorbing liquid flows, and the same refrigerant (water) and absorbing liquid (lithium bromide aqueous solution) as in the conventional double-effect absorption refrigerator are connected. A circuit is constructed.

(19)は高温発生器(1)の燃焼加熱室、(20)、(20)…は燃
焼ガスの流れる吸収液加熱用の管、(21)は低温発生器
(2)の加熱器、(22)は凝縮器(3)の冷却器、(23)は蒸発器
(4)の冷水器、(24)は吸収器(5)の冷却器である。(25)、
(26)は冷水器(23)と負荷側熱交換ユニット〔図示せず〕
とを結ぶ冷水用管路で、この管路には吐出量可変の冷水
用ポンプ(PW)が設けてある。また、(27)、(28)、(29)
は冷却器(24)、(22)を直列に結んだ冷却水流路であり、
この流路には吐出量可変の冷却水用ポンプ(PC)が設け
てある。なお、(30)は燃焼加熱室(19)への燃料供給路
で、これには燃料制御弁(VF)が設けてある。
(19) is a combustion heating chamber of the high temperature generator (1), (20), (20) ... are tubes for heating the absorbing liquid through which the combustion gas flows, and (21) is a low temperature generator.
(2) heater, (22) condenser (3) cooler, (23) evaporator
(4) is a water cooler, and (24) is a cooler of the absorber (5). (twenty five),
(26) is a water cooler (23) and a load side heat exchange unit (not shown)
This is a chilled water pipe that connects with and is equipped with a chilled water pump (P W ) with a variable discharge rate. Also, (27), (28), (29)
Is a cooling water flow path in which coolers (24) and (22) are connected in series,
A cooling water pump (P C ) with a variable discharge rate is provided in this flow path. Note that (30) in the fuel supply passage to the combustion heating chamber (19), This is provided a fuel control valve (V F) is.

そして、(Scal)は管路(25)、(26)のそれぞれの冷水温
度および冷水流量を感知するカロリー検出器であり、こ
のカロリー検出器の信号により冷水流量コントローラー
(CW)を介して冷水用ポンプ(PW)の吐出量が制御され
ると共に冷却水流量コントローラー(CC)を介して冷却
水用ポンプ(PC)の吐出量が制御されるようになってい
る。また、(RC)は冷却水流量コントローラー(CCに内
蔵されている冷却水流量調整器で、この調整器は、高温
発生器(1)に設けた液面検出器(SL)の信号を受けつ
つ、液面検出器(SL)の感知液位が設定値以下になる
と、冷却水流量コントローラー(CC)によって減じられ
たポンプ(PC)吐出量を例えば元の量に戻すなど、コン
トローラー(CC)に対してポンプ(PC)吐出量の増加補
正の指令信号を発するようになっている。なお、冷却水
流量調整器(RC)には高温発生器(1)内の液面の降下速
度に応じて吐出量を増加補正する機能も具備させ得る。
この機能を具備させる場合には、長さの異なる多数の電
極の内蔵されている液面検出器を用いると好都合であ
る。また、圧力検出器(SPC)、(SPG)、温度検出器
(STC)のいずれかの信号を冷却水流量調整器(RC)に
インプットさせるようにしても良い。これら検出器のい
ずれかを用いた場合にはその感知物理量が設定値以上に
高くなったとき調整器(RC)からコントローラー(CC
へ補正信号をアウトプットする。
And (Scal) is a calorie detector that senses the cold water temperature and the cold water flow rate of each of the pipelines (25) and (26), and the cold water flow controller (C W ) is used to send cold water by the signal of this calorie detector. The discharge amount of the cooling water pump (P W ) is controlled and the discharge amount of the cooling water pump (P C ) is controlled via the cooling water flow rate controller (C C ). Further, (R C ) is a cooling water flow controller (cooling water flow controller built into CC , which is a signal of the liquid level detector (S L ) provided in the high temperature generator (1). When the level sensed by the liquid level detector (S L ) falls below the set value while receiving, the pump (P C ) discharge amount reduced by the cooling water flow controller (C C ) is returned to the original amount, for example. , the controller (C C) is adapted to emit a command signal of the pump (P C) discharge amount increase correction for. the cooling water flow rate regulator (R C) in the high temperature generator (1) in A function of increasing and correcting the ejection amount according to the descending speed of the liquid surface may be provided.
When this function is provided, it is convenient to use a liquid level detector having a large number of electrodes having different lengths. Further, any one of the pressure detector (S PC ), (S PG ), and temperature detector (S TC ) signals may be input to the cooling water flow rate regulator (R C ). When any of these detectors is used, when the sensed physical quantity becomes higher than the set value, the regulator ( RC ) to controller ( CC )
Output the correction signal to.

また、(RW)は冷水流量コントローラー(CW)に内蔵さ
れている冷水流量調整器で、この調整器は、蒸発器(4)
の液溜め(31)に設けた温度検出器(STR)もしくは蒸発
器(4)の気相部に設けた圧力検出器(SPE)の信号を受け
つつ、その感知物理量が設定値以下になるとコントロー
ラー(CW)に対してポンプ(PW)吐出量の増加補正の指
令信号を発するようになっている。
Furthermore, (R W) is in a cold water flow regulator incorporated in the coolant flow rate controller (C W), the regulator, the evaporator (4)
While receiving the signal from the temperature detector (S TR ) provided in the liquid reservoir (31) or the pressure detector (S PE ) provided in the vapor phase part of the evaporator (4), the detected physical quantity falls below the set value. Then, the controller (C W ) sends a command signal to the pump (P W ) to increase the discharge amount.

また、(STW)は管路(26)に設けた冷水温度検出器で、
この検出器の信号により温度調節器(TC)を介して燃料
制御弁(VF)の開度が調節されるようになっている。
In addition, (S TW ) is a cold water temperature detector installed in the pipeline (26),
Opening of the temperature controller by the signal of the detector (T C) via a fuel control valve (V F) is adapted to be adjusted.

次に、このように構成された冷水流量調節装置(以下、
本装置という)の動作例を吸収冷凍機の動作と併せて説
明する。
Next, the cold water flow rate control device configured as described above (hereinafter,
An operation example of this device) will be described together with the operation of the absorption refrigerator.

今、吸収冷凍機の運転中に、例えば負荷が100%から
50%に減ったとき負荷に対して吸収冷凍機の冷凍出力
が過大となるので、冷凍出力を負荷に釣合せるための動
作が先ず開始される。すなわち、燃料制御弁(VF)が冷
水温度検出器(STW)の信号で温度調節器(TC)を介し
て全開からほぼ半開に減じられる一方、冷水用ポンプ
(PW)の吐出量がカロリー検出器(Scal)の信号により
冷水流量コントローラー(CW)を介して定格値のほぼ半
分に減らされると共に冷却水用ポンプ(PC)の吐出量が
カロリー検出器(Scal)の信号により冷却水流量コント
ロール(CC)を介して定格値のほぼ半分に減らされる。
Now, during operation of the absorption chiller, for example, when the load is reduced from 100% to 50%, the refrigeration output of the absorption chiller becomes excessive with respect to the load, so the operation for balancing the refrigeration output with the load is first performed. Be started. That is, while the fuel control valve (V F) is reduced to approximately half open from the fully open via the temperature controller (T C) with a signal of a cold water temperature detector (S TW), the discharge amount of chilled water pump (P W) Is reduced to almost half of the rated value via the cold water flow controller (C W ) by the calorie detector (Scal) signal, and the discharge amount of the cooling water pump (P C ) is changed by the calorie detector (Scal) signal. It is reduced to almost half of the rated value via the cooling water flow control (C C ).

しかし、このような動作が行なわれても高温発生器(1)
や低温発生器(2)に余熱があってこれら発生器での冷媒
の発生量は直ちに減らず、吸収器(5)に散布される濃吸
収液の濃度がしばらくの間ほとんど変わらないので、そ
の間、実際には負荷に対してやゝ過大な冷凍出力が続く
ことになる。このため、冷水器(23)内の冷水の温度が降
下し始めると共に蒸発器(4)内の冷媒液の温度およびそ
の飽和蒸気圧が降下し始める。そして、これをそのまま
放置していると冷水および冷媒液が凍結し、ポンプ
(PW)、(PR)の過負荷あるいはキャビテーションを生
じてこれらが故障してしまう場合がある。このような場
合、本装置においては、蒸発器(4)および吸収器(5)内の
蒸気圧あるいは冷媒液溜め(31)の冷媒液温が設定値まで
降下した時に、温度検出器(STR)もしくは圧力検出器
(SPE)の信号を受ける冷水流れ量調整器(RW)が冷水
流量コントローラー(CW)に対して冷水用ポンプ(PW
の吐出量を増加させるよう補正指令信号を発し、蒸発器
(4)への冷水供給量を増やすので、冷媒液の凍結や冷水
の凍結が未然に防止される。そして、冷媒液の温度、飽
和蒸気圧が設定値よりも上昇すると冷水流量コントロー
ラー(CW)に対する調整器(RW)の補正指令信号が解除
される。
However, even if such an operation is performed, the high temperature generator (1)
Since there is residual heat in the low temperature generators (2) and the amount of refrigerant generated in these generators does not immediately decrease, and the concentration of the concentrated absorbing liquid sprinkled in the absorber (5) remains almost unchanged for a while. Actually, the refrigeration output that is too large for the load will continue. Therefore, the temperature of the cold water in the water cooler (23) starts to drop, and the temperature of the refrigerant liquid in the evaporator (4) and its saturated vapor pressure also start to drop. If this is left as it is, the cold water and the refrigerant liquid may freeze, causing overload or cavitation of the pumps (P W ) and (P R ) and causing them to fail. In such a case, in this device, when the vapor pressure in the evaporator (4) and the absorber (5) or the refrigerant liquid temperature of the refrigerant liquid reservoir (31) drops to a set value, a temperature detector (S TR ) or pressure detector (S PE) cold water flow quantity regulator which receives a signal (R W) is cold water pump in cold water flow controller (C W) (P W)
A correction command signal is issued to increase the discharge amount of
Since the amount of cold water supplied to (4) is increased, the freezing of the refrigerant liquid and the freezing of cold water are prevented in advance. Then, the temperature of the refrigerant liquid, the correction command signal when the saturated vapor pressure also rises than the set value coolant flow rate controller regulator for (C W) (R W) is released.

なお、温度検出器(STR)は冷媒液の散布器や管(11)に
備えても良く、圧力検出器(SPE)は吸収器(5)の気相部
に備えても良い。なおまた、図示していないが、温度検
出器(STR)や圧力検出器(SPE)の代りに管(11)、(12)
の冷媒液流量や冷媒液溜め(31)の液位などを感知する検
出器を用いることも可能である。
The temperature detector (S TR ) may be provided in the refrigerant liquid sprayer or the pipe (11), and the pressure detector (S PE ) may be provided in the vapor phase part of the absorber (5). Further, although not shown, pipes (11) and (12) are used instead of the temperature detector (S TR ) and the pressure detector (S PE ).
It is also possible to use a detector that senses the flow rate of the refrigerant liquid and the liquid level of the refrigerant liquid reservoir (31).

第2図は本発明によるこの種の装置の他の実施例を示し
た概略構成説明図で、この図においては冷水用ポンプお
よび冷却水用ポンプの台数制御が行なわれる例を示して
いる。なお、第2図において、第1図に示した構成機器
と同様のものには同一の符号が付されており、
(STW1)、(STW2)は温度検出器で、これらは第1図に
示したカロリー検出器(Scal)に代ってコントローラー
(CW)、(CC)に信号を発するものである。この実施例
においては、温度検出器(STW1)、(STW2)の信号によ
り冷水流量コントローラー(CW)を介して停止させた冷
水用ポンプ(PW)が温度検出器(STR)もしくは圧力検
出器(SPE)の信号により冷水流量調整器(RW)および
冷水流量コントローラー(CW)を介して再び運転される
のである。そして、蒸発器(4)内の冷媒液の温度および
その飽和蒸気圧が正常な範囲内に復帰すると冷水流量コ
ントローラー(CW)への調整器(RW)の補正指令信号が
解除されてポンプ(PW)が再停止されるのである。第2
図において、説明の便宜上、2台の冷水用ポンプ(PW
と冷水用ポンプ(PC)を図示したが、これらを多数設置
しても良いことは勿論である。
FIG. 2 is a schematic configuration explanatory view showing another embodiment of this type of apparatus according to the present invention, and in this figure, an example in which the number of chilled water pumps and cooling water pumps is controlled is shown. Incidentally, in FIG. 2, the same components as those shown in FIG. 1 are designated by the same reference numerals,
(S TW1 ), (S TW2 ) are temperature detectors, and these emit signals to the controllers (C W ) and (C C ) instead of the calorie detector (Scal) shown in FIG. . In this embodiment, the chilled water pump (P W ) stopped via the chilled water flow controller (C W ) by the signal of the temperature detectors (S TW1 ) and (S TW2 ) is the temperature detector (S TR ) or We are again operated via the cold-water flow regulator (R W) and cold water flow controller (C W) by the signal of the pressure detector (S PE). Then, the evaporator (4) in the temperature and the regulator (R W) of the correction command signal is canceled pump of the the saturation vapor pressure is restored to within the normal range coolant flow rate controller (C W) of the refrigerant fluid (P W ) is stopped again. Second
In the figure, two chilled water pumps (P W ) are provided for convenience of explanation.
The cold water pump (P C ) is shown in the figure, but it goes without saying that a large number of these may be installed.

なお、第1図および第2図に示した実施例において、吸
収冷凍機に供給される冷却水の流量が半減することによ
り一時的に高温発生器(1)や凝縮器(3)内の蒸気圧、温度
が上昇すると共に高温発生器(1)内の液面が降下する。
そして、これらが設定値に達すると温度検出器
(STC)、圧力検出器(SPC)、(SPG)、液面検出器(S
L)のいずれかの信号により冷却水流量調整器(RC)、
冷却水流量コントローラー(CC)を介して冷却水用ポン
プ(PC)の吐出量もしくは運転台数が増加補正され、高
温発生器(1)の過度の液面降下や圧力上昇などが防止さ
れる。なおまた、これら実施例においては、本発明の冷
水流量調節装置を二重効用吸収冷凍機に適用した場合に
ついて説明したが、これを一重効用吸収冷凍機に適用で
きることは勿論である。
In the embodiment shown in FIG. 1 and FIG. 2, steam in the high temperature generator (1) and the condenser (3) is temporarily reduced by halving the flow rate of the cooling water supplied to the absorption refrigerator. As the pressure and temperature rise, the liquid level in the high temperature generator (1) falls.
When these reach the set values, the temperature detector (S TC ), pressure detector (S PC ), (S PG ), liquid level detector (S
Cooling water flow rate regulator by either of the signals L) (R C),
The discharge amount of the cooling water pump (P C ) or the number of operating pumps is increased and corrected via the cooling water flow controller (C C ) to prevent excessive liquid level drop and pressure rise of the high temperature generator (1). . Further, in these embodiments, the case where the cold water flow rate control device of the present invention is applied to the double-effect absorption refrigerator is explained, but it is needless to say that this can be applied to the single-effect absorption refrigerator.

(ト) 発明の効果 以上のとおり、本発明の装置によれば、吸収冷凍機への
冷水供給量の急減に伴なって蒸発器内の冷媒液の温度や
飽和蒸気圧が降下し始めた際にこれらが過度に降下する
前の設定値に達すると冷水の供給量を増やすよう調整し
て冷水器内の冷水温度を上昇させると共に蒸発器の冷水
器に散布された冷媒液の温度およびその飽和蒸気圧を上
昇させ、冷水および冷媒の凍結を未然に防止でき、安全
装置が働くのを防いで吸収冷凍機の運転を安定させて継
続できる効果が発揮される。
(G) Effect of the Invention As described above, according to the device of the present invention, when the temperature of the refrigerant liquid in the evaporator or the saturated vapor pressure starts to drop with the rapid decrease in the amount of cold water supplied to the absorption refrigerator. When they reach the set values before they drop excessively, the cold water temperature in the water cooler is adjusted by increasing the supply amount of cold water and the temperature of the refrigerant liquid sprinkled in the water cooler of the evaporator and its saturation. The vapor pressure can be increased to prevent freezing of cold water and the refrigerant, the safety device can be prevented from working, and the operation of the absorption refrigerator can be stabilized and continued.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明によるこの種の装置の一実施例を示した
概略構成説明図であり、第2図は本発明によるこの種の
装置の他の実施例を示した概略構成説明図である。 (1)……高温発生器、(2)……低温発生器、(3)……凝縮
器、(4)……蒸発器、(5)……吸収器、(11)、(12)……
管、(23)……冷水器、(25)、(26)……冷水流路、(31)…
…冷媒液溜め、(PW)……冷水用ポンプ、(PR)……冷
媒液用ポンプ、(PA)……吸収液用ポンプ、(CW)……
冷水流量コントローラー、(RW)……冷水流量調整器、
(STR)……温度検出器、(SPE)……圧力検出器。
FIG. 1 is a schematic configuration explanatory view showing an embodiment of this type of device according to the present invention, and FIG. 2 is a schematic configuration explanatory view showing another embodiment of this type of device according to the present invention. . (1) …… High temperature generator, (2) …… Low temperature generator, (3) …… Condenser, (4) …… Evaporator, (5) …… Absorber, (11), (12)… …
Pipe, (23) …… Chiller, (25), (26) …… Chilled water flow path, (31)…
… Refrigerant liquid reservoir, (P W ) …… Cold water pump, (P R ) …… Refrigerant liquid pump, (P A ) …… Absorbing liquid pump, (C W ) ……
Cold water flow controller, (R W ) …… Cold water flow controller,
(S TR ) …… Temperature detector, (S PE ) …… Pressure detector.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】発生器,凝縮器、蒸発器及び吸収器などの
機器を配管接続して冷媒流路および吸収液流路を形成す
るとともに蒸発器に冷水流路を接続し、この冷水流路に
設けた冷水用ポンプの吐出量制御もしくは運転台数の制
御により冷水流量を調節する装置において、冷水流路を
流れる冷水の流量の変化に関連して変化する物理量を感
知する検出器と、この検出器の信号を入力し、上記装置
により吸収冷凍機に供給する冷水の流量を減らした際に
上記検出器の感知物理量が設定値に達すると上記信号に
基づいて上記冷水用ポンプに信号を出力して冷水流量を
増加補正する調節機構とが備えられていることを特徴と
する吸収冷凍機の冷水流量調節装置。
1. A generator, a condenser, an evaporator, an absorber, and other devices are connected by piping to form a refrigerant flow path and an absorption liquid flow path, and a cold water flow path is connected to the evaporator. In a device that adjusts the flow rate of cold water by controlling the discharge rate of the cold water pump or the number of operating units, the detector that senses the physical quantity that changes in relation to the change in the flow rate of cold water that flows through the cold water flow path, and this detection If the physical quantity sensed by the detector reaches a set value when the flow rate of the cold water supplied to the absorption chiller is reduced by inputting the signal from the cooling device, the signal is output to the chilled water pump based on the signal. And an adjusting mechanism for increasing and correcting the cold water flow rate.
【請求項2】前記物理量が蒸発器内の冷媒液温度である
特許請求の範囲第1項に記載の吸収冷凍機の冷水流量調
節装置。
2. The chilled water flow rate control device for an absorption chiller according to claim 1, wherein the physical quantity is a temperature of the refrigerant liquid in the evaporator.
【請求項3】前記物理量が蒸発器内の蒸気圧である特許
請求の範囲第1項に記載の吸収冷凍機の冷水流量調節装
置。
3. The chilled water flow rate control device for an absorption chiller according to claim 1, wherein the physical quantity is vapor pressure in the evaporator.
JP20106085A 1985-09-11 1985-09-11 Cold water flow controller for absorption refrigerator Expired - Lifetime JPH0623627B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20106085A JPH0623627B2 (en) 1985-09-11 1985-09-11 Cold water flow controller for absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20106085A JPH0623627B2 (en) 1985-09-11 1985-09-11 Cold water flow controller for absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS6262163A JPS6262163A (en) 1987-03-18
JPH0623627B2 true JPH0623627B2 (en) 1994-03-30

Family

ID=16434716

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20106085A Expired - Lifetime JPH0623627B2 (en) 1985-09-11 1985-09-11 Cold water flow controller for absorption refrigerator

Country Status (1)

Country Link
JP (1) JPH0623627B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5097593B2 (en) * 2008-03-28 2012-12-12 三洋電機株式会社 Absorption heat pump

Also Published As

Publication number Publication date
JPS6262163A (en) 1987-03-18

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