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JPH0833260B2 - Absorption cold water heater - Google Patents
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JPH0833260B2 - Absorption cold water heater - Google Patents

Absorption cold water heater

Info

Publication number
JPH0833260B2
JPH0833260B2 JP2080107A JP8010790A JPH0833260B2 JP H0833260 B2 JPH0833260 B2 JP H0833260B2 JP 2080107 A JP2080107 A JP 2080107A JP 8010790 A JP8010790 A JP 8010790A JP H0833260 B2 JPH0833260 B2 JP H0833260B2
Authority
JP
Japan
Prior art keywords
refrigerant liquid
temperature
cold water
evaporator
water outlet
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
JP2080107A
Other languages
Japanese (ja)
Other versions
JPH03279760A (en
Inventor
智之 村山
繁則 舘下
圭司 和田
孝樹 岩谷
敏之 金子
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 Denki Co Ltd
Original Assignee
Sanyo Denki 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 Denki Co Ltd filed Critical Sanyo Denki Co Ltd
Priority to JP2080107A priority Critical patent/JPH0833260B2/en
Publication of JPH03279760A publication Critical patent/JPH03279760A/en
Publication of JPH0833260B2 publication Critical patent/JPH0833260B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/006Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は冷水と温水とを同時に取り出す吸収冷温水機
に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to an absorption chiller-heater for simultaneously extracting cold water and hot water.

(ロ)従来の技術 例えば特公昭55−9620号公報には、発生器に温水器を
付設し、蒸発器と温水器とから冷水と温水とを同時に取
り出すようにすると共に、低温発生器と蒸発器との間に
接続された濃溶液配管(28)に冷媒液配管(31)或いは
(37)を接続し、これらの冷媒液配管にそれぞれ流量制
御弁(32)或いは(36)を設け、暖房負荷が冷房負荷よ
りも大きいときに、蒸発器の冷水出口側温度に応じて流
量制御弁(32)、或いは(36)を制御し、冷媒液が上記
冷媒液配管(31)、或いは(37)を経て濃溶液配管(2
8)の濃溶液に混入され、吸収器に散布される濃溶液の
濃度が変化し、吸収機能を調整して冷房能力を制御する
ようにした吸収式冷暖房装置が開示されている。
(B) Conventional technology For example, in Japanese Patent Publication No. Sho 55-9620, a water heater is attached to the generator so that cold water and hot water can be taken out simultaneously from the evaporator and the water heater, and at the same time, a low temperature generator and an evaporator can be used. The refrigerant solution pipe (31) or (37) is connected to the concentrated solution pipe (28) connected to the reactor, and these refrigerant liquid pipes are provided with flow control valves (32) or (36), respectively, for heating. When the load is larger than the cooling load, the flow rate control valve (32) or (36) is controlled according to the temperature of the cold water outlet of the evaporator, and the refrigerant liquid is the refrigerant liquid pipe (31) or (37). Via concentrated solution piping (2
Disclosed is an absorption type cooling and heating device in which the concentration of the concentrated solution mixed in the concentrated solution of 8) and sprayed on the absorber changes, and the cooling function is controlled by adjusting the absorption function.

(ハ)発明が解決しようとする課題 上記従来の技術において、暖房負荷が冷房負荷より大
きいとき、流量制御弁(32)、或いは(36)を冷水出口
温度、即ち冷房負荷に応じて制御し、冷媒液を濃溶液配
管(28)の濃溶液に混入した場合、冷媒液(例えば4〜
5℃)と濃溶液(例えば40〜50℃)との温度差によっ
て、混入部でフラッシュが発生し、フラッシュ音が発生
するおそれがあった。又、上記フラッシュが冷媒液の濃
溶液への混入の抵抗になり、流量制御弁(32)、或いは
(36)の開度を調節した場合にも、冷房負荷の低下に応
じて冷媒液の濃溶液への混入量が増大せず、冷房能力を
大幅に低下させることができず、冷水出口温度の過低
下、或いは蒸発器の冷媒液の氷結が発生するおそれがあ
った。
(C) Problem to be Solved by the Invention In the above-mentioned conventional technique, when the heating load is larger than the cooling load, the flow rate control valve (32) or (36) is controlled according to the chilled water outlet temperature, that is, the cooling load, When the refrigerant liquid is mixed with the concentrated solution in the concentrated solution pipe (28), the refrigerant liquid (for example, 4 to
Due to the temperature difference between the concentrated solution (for example, 40 to 50 ° C.) and the concentrated solution (for example, 40 to 50 ° C.), a flash may be generated in the mixing part, and a flash noise may be generated. In addition, even if the flash becomes a resistance against the mixture of the refrigerant liquid into the concentrated solution and the opening degree of the flow control valve (32) or (36) is adjusted, the concentration of the refrigerant liquid is reduced according to the decrease of the cooling load. There is a possibility that the amount of mixture in the solution does not increase, the cooling capacity cannot be significantly reduced, the cold water outlet temperature excessively drops, or the refrigerant liquid in the evaporator freezes.

本発明は、暖房負荷(温水負荷)が冷房負荷(冷水負
荷)より大きいとき、即ち温水主制御時の、冷水出口温
度の過低下、或いは冷媒液の氷結を防止することを目的
とする。
It is an object of the present invention to prevent the cold water outlet temperature from excessively decreasing or the refrigerant liquid to freeze when the heating load (hot water load) is larger than the cooling load (cold water load), that is, during hot water main control.

(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(3)、蒸発器(4)、及び吸収器
(5)をそれぞれ接続して蒸発器(4)から冷水を取り
出す冷凍サイクルと、高温発生部(1)に付設された温
水器(35)とから冷水と温水とを同時に取り出すように
構成し、温水主制御の運転時、蒸発器(4)の冷水出口
側の温度に応じて高温発生器(1)から凝縮器(3)へ
流れる冷媒量を調節すると共に、温水器(35)の温水出
口側の温度に応じて高温発生器(1)の加熱量を調節す
る吸収冷温水機において、凝縮器(3)と吸収器(5)
との間に第1冷媒液戻し管(31)を接続し、この第1冷
媒液戻し管(31)に第1開閉弁(33)を設け、かつ、蒸
発器(4)に接続された冷媒液循環管(19)と吸収器
(5)との間に第2冷媒液戻し管(32)を接続し、この
第2冷媒液戻し管(32)に第2開閉弁(34)を設け、温
水主制御時、蒸発器(4)の出口側冷水温度に応じて第
1開閉弁(33)と第2開閉弁(34)とを順次開閉制御す
る制御装置(41)を備えた吸収冷温水機を提供するもの
である。
(D) Means for Solving the Problems In order to solve the above problems, the present invention connects a high temperature generator (1), a condenser (3), an evaporator (4), and an absorber (5), respectively. The refrigeration cycle that takes out cold water from the evaporator (4) and the hot water heater (35) attached to the high temperature generation part (1) are configured to take out cold water and hot water at the same time. The amount of refrigerant flowing from the high temperature generator (1) to the condenser (3) is adjusted according to the temperature of the cold water outlet side of the evaporator (4), and the high temperature is adjusted according to the temperature of the hot water outlet side of the water heater (35). In an absorption chiller-heater for adjusting the heating amount of a generator (1), a condenser (3) and an absorber (5)
And a first refrigerant liquid return pipe (31) connected between the first refrigerant liquid return pipe (31) and the first opening / closing valve (33), and a refrigerant connected to the evaporator (4). A second refrigerant liquid return pipe (32) is connected between the liquid circulation pipe (19) and the absorber (5), and a second opening / closing valve (34) is provided in the second refrigerant liquid return pipe (32), Absorption cold / hot water provided with a control device (41) for sequentially opening / closing the first opening / closing valve (33) and the second opening / closing valve (34) according to the outlet side cold water temperature of the evaporator (4) during hot water main control Machine.

又、凝縮器(3)の冷媒液を吸収器(5)へ導く第1
冷媒液戻し管(31)を設け、この第1冷媒液戻し管(3
1)に蒸発器(4)の冷水出口温度に応じて開閉する第
1開閉弁(33)を設け、かつ、蒸発器(4)の冷媒液を
吸収器(5)へ導く第2冷媒液戻し管(32)を設け、こ
の冷媒液戻し管(32)に上記冷水出口温度に応じて開閉
する第2開閉弁(34)を設けた吸収冷温水機を提供する
ものである。
In addition, the first to guide the refrigerant liquid of the condenser (3) to the absorber (5)
A refrigerant liquid return pipe (31) is provided, and the first refrigerant liquid return pipe (3
A first on-off valve (33) that opens and closes according to the cold water outlet temperature of the evaporator (4) is provided in 1), and a second refrigerant liquid return for guiding the refrigerant liquid of the evaporator (4) to the absorber (5). An absorption chiller-heater having a pipe (32) and a second on-off valve (34) which opens and closes according to the cold water outlet temperature is provided in the refrigerant liquid return pipe (32).

さらに、凝縮器(3)の冷媒液を吸収器(5)へ導く
第1冷媒液戻し管(31)を設け、この第1冷媒液戻し管
(31)に冷水出口温度に応じて開閉する第1開閉弁(3
3)を設け、かつ、蒸発器(4)の冷媒液を吸収器
(5)へ導く第2冷媒液戻し管(32)を設け、この第2
冷媒液戻し管(32)に冷水出口温度に応じて開閉し、閉
から開に切換わる温度を第1開閉弁(33)の温度より低
く設定した第2開閉弁(34)を設けた吸収冷温水機を提
供するものである。
Furthermore, a first refrigerant liquid return pipe (31) for guiding the refrigerant liquid of the condenser (3) to the absorber (5) is provided, and the first refrigerant liquid return pipe (31) is opened / closed according to the cold water outlet temperature. 1 open / close valve (3
3) is provided, and a second refrigerant liquid return pipe (32) for guiding the refrigerant liquid of the evaporator (4) to the absorber (5) is provided.
Absorption cold temperature provided with a second on-off valve (34) that opens and closes the refrigerant liquid return pipe (32) according to the cold water outlet temperature and sets the temperature at which it switches from closed to open lower than the temperature of the first on-off valve (33). It provides a water machine.

(ホ)作用 温水主制御時、冷水負荷が大幅に低下した状態が続
き、冷媒が高温発生器(31)から凝縮器(3)へ流れな
くなった後も、冷水出口温度が低下した場合には第1開
閉弁(33)が開き、凝縮器(3)の冷媒液が吸収器
(5)へ流れ、吸収液が稀釈される。さらに冷水出口温
度が低下した場合には、第2開閉弁(34)が開き、蒸発
器(4)の冷媒液が吸収器(5)へ大量に流れ、吸収液
が大幅に稀釈され、かつ蒸発器(4)での冷媒散布量が
減少し、冷水出口温度の過低下、及び吸収液濃度の上昇
を確実に回避することが可能になる。又、冷水出口温度
に応じて冷却能力が変化して冷水出口温度を安定させる
ことが可能になる。
(E) Action During hot water main control, if the cold water load continues to drop significantly and the cold water outlet temperature drops even after the refrigerant has stopped flowing from the high temperature generator (31) to the condenser (3), The first on-off valve (33) opens, the refrigerant liquid in the condenser (3) flows into the absorber (5), and the absorption liquid is diluted. When the chilled water outlet temperature further decreases, the second opening / closing valve (34) opens, a large amount of refrigerant liquid in the evaporator (4) flows into the absorber (5), and the absorbed liquid is greatly diluted and evaporated. The amount of refrigerant sprayed in the vessel (4) is reduced, and it becomes possible to reliably avoid an excessive decrease in the cold water outlet temperature and an increase in the absorption liquid concentration. Further, the cooling capacity changes depending on the cold water outlet temperature, and the cold water outlet temperature can be stabilized.

又、温水主制御時、冷水負荷が大幅に低下した状態が
続き、冷水出口温度が低下した場合には第1開閉弁(3
3)、及び第2開閉弁(34)が開き、凝縮器(3)の冷
媒液、及び蒸発器(4)の冷媒液が第1,第2冷媒液戻し
管(31),(32)を経て吸収器(5)へ流れ、吸収液の
濃度が大幅に低下すると共に、蒸発器(4)の冷却能力
が大幅に低下して冷水出口温度の過低下、冷媒液の氷結
を確実に回避することが可能になる。
Also, during hot water main control, if the cold water load continues to drop significantly and the cold water outlet temperature drops, the first on-off valve (3
3) and the second opening / closing valve (34) are opened, and the refrigerant liquid in the condenser (3) and the refrigerant liquid in the evaporator (4) pass through the first and second refrigerant liquid return pipes (31), (32). After that, it flows to the absorber (5), the concentration of the absorbing liquid is significantly reduced, and the cooling capacity of the evaporator (4) is also significantly reduced, so that the cold water outlet temperature is prevented from being excessively lowered and the freezing of the refrigerant liquid is surely avoided. It will be possible.

(ヘ)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。
(F) Embodiment Hereinafter, one embodiment of the present invention will be described in detail with reference to the drawings.

第1図に示したものは吸収冷温水機であり、冷媒に水
(H2O)、吸収剤(吸収液)に臭化リチウム(LiBr)水
溶液を使用したものである。
What is shown in FIG. 1 is an absorption chiller-heater, which uses water (H 2 O) as a refrigerant and an aqueous lithium bromide (LiBr) solution as an absorbent (absorption liquid).

第1図において、(1)はガスバーナ(1B)を備えた
高温発生器、(2)は低温発生器、(3)は凝縮器、
(3A)は冷媒液溜め、(4)は蒸発器、(5)は吸収
器、(6)は低温熱交換器、(7)は高温熱交換器、
(8)ないし(14)は吸収液管、(15)は吸収液ポン
プ、(16)及び(17)は冷媒管、(18)は冷媒液下管、
(19)は冷媒液循環管、(19P)は冷媒液ポンプ、(2
0)はバーナ(1B)に接続されたガス配管、(21)は加
熱量制御弁、(22)は冷水配管、(23)は蒸発器熱交換
器であり、それぞれは第1図に示したように配管接続さ
れている。又、(A)は蒸発吸収器胴、(B)は発生凝
縮器胴である。さらに、(25)は冷却水配管であり、こ
の冷却水配管(25)の途中には吸収器熱交換器(26)、
及び凝縮器熱交換器(27)が設けられている。
In FIG. 1, (1) is a high temperature generator equipped with a gas burner (1B), (2) is a low temperature generator, (3) is a condenser,
(3A) is a refrigerant reservoir, (4) is an evaporator, (5) is an absorber, (6) is a low temperature heat exchanger, (7) is a high temperature heat exchanger,
(8) to (14) are absorption liquid pipes, (15) is an absorption liquid pump, (16) and (17) are refrigerant pipes, (18) is a refrigerant liquid lower pipe,
(19) is a refrigerant liquid circulation pipe, (19P) is a refrigerant liquid pump, (2)
(0) is a gas pipe connected to the burner (1B), (21) is a heating control valve, (22) is cold water pipe, and (23) is an evaporator heat exchanger, each of which is shown in FIG. Are connected by pipes. Further, (A) is an evaporative absorber cylinder, and (B) is a generating condenser cylinder. Further, (25) is a cooling water pipe, and in the middle of this cooling water pipe (25), an absorber heat exchanger (26),
And a condenser heat exchanger (27).

又、(30)は冷媒管(17)に設けられた冷媒ドレン制
御弁、(31)は第1冷媒液戻し管であり、第1冷媒液戻
し管(31)の一端は冷媒液流下管(18)に接続され、他
端は吸収器(5)内の気相部に開口している。そして、
第1冷媒液戻し管(31)の途中に電磁弁などの第1開閉
弁(33)が設けられている。
Further, (30) is a refrigerant drain control valve provided in the refrigerant pipe (17), (31) is a first refrigerant liquid return pipe, and one end of the first refrigerant liquid return pipe (31) has a refrigerant liquid flow-down pipe ( 18) and the other end is open to the gas phase in the absorber (5). And
A first opening / closing valve (33) such as a solenoid valve is provided in the middle of the first refrigerant liquid return pipe (31).

さらに、(32)は第2冷媒液戻し管であり、この第2
冷媒液戻し管(32)の一端は冷媒液ポンプ(19P)の吐
出側の冷媒液循環管(19)に接続され、他端は吸収器
(5)の気相部に開口している。又、(34)は第2冷媒
液戻し管(32)の途中に設けられた例えば電磁弁などの
第2開閉弁である。
Further, (32) is a second refrigerant liquid return pipe,
One end of the refrigerant liquid return pipe (32) is connected to the refrigerant liquid circulation pipe (19) on the discharge side of the refrigerant liquid pump (19P), and the other end is open to the gas phase portion of the absorber (5). Further, (34) is a second opening / closing valve such as an electromagnetic valve provided in the middle of the second refrigerant liquid return pipe (32).

(35)は高温発生器(1)に付設された温水器、(3
6)は温水器(35)の下部と高温発生器(1)との間に
接続された冷媒ドレン管であり、この冷媒ドレン管(3
6)の途中に温水ドレン制御弁(37)が設けられてい
る。又、(38)は温水配管であり、この温水配管(38)
の途中に温水器熱交換器(40)が設けられている。
(35) is a water heater attached to the high temperature generator (1), (3
6) is a refrigerant drain pipe connected between the lower part of the water heater (35) and the high temperature generator (1), and this refrigerant drain pipe (3
A hot water drain control valve (37) is provided in the middle of 6). Also, (38) is a hot water pipe, and this hot water pipe (38)
A water heater heat exchanger (40) is provided on the way.

(41)は上記吸収冷温水機の制御装置、(42)は蒸発
器(4)の出口側の冷水配管(22)に取り付けられた冷
水出口温度検出器、(43)は温水器(35)の出口側の温
水配管(38)に取り付けられた温水出口温度検出器であ
り、各温度検出器(42),(43)は制御装置(41)に接
続されている。又、冷媒ドレン制御弁(30)、冷媒ドレ
ン制御弁(37)、加熱量制御弁(21)、第1,第2開閉弁
(33),(34)はそれぞれ制御装置(41)に接続されて
いる。又、制御装置(41)には冷水主制御と温水主制御
とを切換える冷主温主切換装置(41A)が設けられてい
る。そして、切換装置(41A)は第2図に示したように
冷水出口温度と温水出口温度とに応じて冷水主制御と温
水主制御とを切換える。ここで、冷水主制御時には制御
装置(41)が冷水出口温度に応じて加熱量制御弁(21)
へ開度信号を出力すると共に、温水出口温度に応じて温
水ドレン制御弁(37)へ開度信号を出力する。又、温水
主制御時には、制御装置(41)が冷水出口温度に応じて
冷媒ドレン制御弁(30)へ開度信号を出力すると共に、
温水出口温度に応じて加熱量制御弁(21)へ開度信号を
出力する。
(41) is a control device for the absorption chiller-heater, (42) is a chilled water outlet temperature detector attached to the chilled water pipe (22) on the outlet side of the evaporator (4), and (43) is a water heater (35) Is a hot water outlet temperature detector attached to the hot water pipe (38) on the outlet side of each of the temperature detectors (42) and (43) is connected to the control device (41). Further, the refrigerant drain control valve (30), the refrigerant drain control valve (37), the heating amount control valve (21), the first and second opening / closing valves (33) and (34) are respectively connected to the control device (41). ing. Further, the control device (41) is provided with a cold main temperature main switching device (41A) for switching between cold water main control and hot water main control. Then, the switching device (41A) switches between the cold water main control and the hot water main control according to the cold water outlet temperature and the hot water outlet temperature as shown in FIG. Here, during the cold water main control, the control device (41) controls the heating amount control valve (21) according to the cold water outlet temperature.
The opening signal is output to the hot water drain control valve (37) according to the hot water outlet temperature. Further, during hot water main control, the control device (41) outputs an opening signal to the refrigerant drain control valve (30) according to the cold water outlet temperature,
An opening signal is output to the heating amount control valve (21) according to the hot water outlet temperature.

上記のように構成された吸収冷温水機の運転時、例え
ば冷水出口温度が例えば7℃、温水出口温度が例えば60
℃のときには、冷主温主切換装置(41A)が冷水主制御
に切換っており、制御装置(41)にて、冷水主制御の制
御が行われる。ここで、冷水主制御と温水主制御とは上
記のように第2図に示したように冷水出口温度と温水出
口温度とにより決まる。ここで、実線(L1),(L2),
(L3)上は冷水主制御である。冷水主制御の運転が行わ
れているときには、制御装置(41)は冷媒ドレン制御弁
(30)へ全開の信号を出力し、第1,第2開閉弁(33),
(34)へ閉信号を出力する。又、制御装置(41)は冷水
出口温度検出器(42)が検出した温度に応じて加熱量制
御弁(21)へ開度信号を出力し、冷水出口温度が上昇し
たときには加熱量制御弁(21)の開度は大きくなり、冷
水出口温度が低下したときには加熱量制御弁(21)の開
度は小さくなる。又、吸収液ポンプ(15)、及び冷媒液
ポンプ(19P)はそれぞれ運転され、従来の吸収冷温水
機と同様に吸収液、及び冷媒が循環し、蒸発器熱交換器
(23)で温度低下した冷水が負荷へ供給される。
During operation of the absorption chiller-heater configured as described above, for example, the cold water outlet temperature is, for example, 7 ° C., and the hot water outlet temperature is, for example, 60 degrees.
When the temperature is ℃, the cold main temperature main switching device (41A) is switched to the cold water main control, and the control device (41) controls the cold water main control. Here, the cold water main control and the hot water main control are determined by the cold water outlet temperature and the hot water outlet temperature as shown in FIG. 2 as described above. Where the solid lines (L 1 ), (L 2 ),
(L 3 ) Above is the cold water main control. When the operation of the chilled water main control is being performed, the control device (41) outputs a fully open signal to the refrigerant drain control valve (30), and the first and second on-off valves (33),
Output a close signal to (34). Further, the control device (41) outputs an opening signal to the heating amount control valve (21) according to the temperature detected by the cold water outlet temperature detector (42), and when the cooling water outlet temperature rises, the heating amount control valve (21 The opening of 21) becomes large and the opening of the heating amount control valve (21) becomes small when the cold water outlet temperature decreases. Also, the absorption liquid pump (15) and the refrigerant liquid pump (19P) are operated respectively, and the absorption liquid and the refrigerant circulate as in the conventional absorption chiller-heater, and the temperature drops in the evaporator heat exchanger (23). Cold water is supplied to the load.

又、高温発生器(1)で吸収液から分離した冷媒蒸気
の一部は温水器(35)へ流れ、温水器熱交換器(40)を
流れる温水と熱交換して凝縮する。そして、温水器(3
5)にて凝縮した冷媒液は冷媒ドレン管(36)及び温水
ドレン制御弁(37)を経て高温発生器(1)へ戻る。
又、温水器熱交換器(40)にて温度上昇した温水が負荷
へ供給される。ここで、制御装置(41)は温水出口温度
検出器(43)が検出した温度に応じて温水ドレン制御弁
(37)へ開度信号を出力する。そして、温水出口温度が
上昇したときには、温水ドレン制御弁(37)の開度は小
さくなり、温水器(35)の冷媒液面が上昇する。このた
め、温水器熱交換器(40)の熱交換面積が減少し、熱交
換量が減少して温水出口温度は低下する。又、温水出口
温度が低下したときには、温水ドレン制御弁(37)の開
度は大きくなり、温水器(35)の冷媒液面が低下する。
このため、温水器熱交換器(40)の熱交換面積が増大
し、熱交換量が増加して温水出口温度は上昇する。上記
のように冷水主制御が行われているとき、冷水出口温度
に応じて加熱量制御弁(21)の開度が変化し、高温発生
器(1)の冷媒蒸気の発生量が変化して冷水出口温度が
ほぼ設定温度に保たれる。又、温水出口温度に応じて温
水ドレン制御弁(37)の開度が変化し、温水器(35)の
熱交換量が変化して温水出口温度がほぼ設定温度に保た
れる。
Further, a part of the refrigerant vapor separated from the absorbing liquid in the high temperature generator (1) flows into the water heater (35) and exchanges heat with the hot water flowing in the water heater heat exchanger (40) to be condensed. And the water heater (3
The refrigerant liquid condensed in 5) returns to the high temperature generator (1) through the refrigerant drain pipe (36) and the hot water drain control valve (37).
Further, hot water whose temperature has risen in the water heater heat exchanger (40) is supplied to the load. Here, the control device (41) outputs an opening degree signal to the hot water drain control valve (37) according to the temperature detected by the hot water outlet temperature detector (43). Then, when the temperature of the hot water outlet rises, the opening degree of the hot water drain control valve (37) becomes smaller and the liquid level of the refrigerant in the water heater (35) rises. Therefore, the heat exchange area of the water heater heat exchanger (40) decreases, the heat exchange amount decreases, and the hot water outlet temperature decreases. Further, when the temperature of the hot water outlet decreases, the opening degree of the hot water drain control valve (37) increases, and the liquid level of the refrigerant in the water heater (35) decreases.
Therefore, the heat exchange area of the hot water heat exchanger (40) increases, the amount of heat exchange increases, and the hot water outlet temperature rises. When the chilled water main control is performed as described above, the opening degree of the heating amount control valve (21) changes according to the chilled water outlet temperature, and the generation amount of the refrigerant vapor of the high temperature generator (1) changes. The cold water outlet temperature is maintained at about the set temperature. Further, the opening degree of the hot water drain control valve (37) changes according to the hot water outlet temperature, the heat exchange amount of the water heater (35) changes, and the hot water outlet temperature is maintained at a substantially set temperature.

又、冷水負荷が減少し、冷水出口温度が例えば6.2℃
であり、温水出口温度が例えば60℃のときには、冷主温
主切換装置(41A)が温水主制御に切換っており、制御
装置(41)にて温水主制御の制御が行われる。このと
き、制御装置(41)は第1,第2開閉弁(33),(34)へ
閉信号を出力するとともに、温水ドレン制御弁(37)へ
全開の信号を出力する。そして、温水ドレン制御弁(3
7)は全開する。又、制御装置(41)は冷水出口温度検
出器(42)が検出した温度に応じて冷媒ドレン制御弁
(30)へ開度信号を出力し、冷水出口温度が上昇したと
きには、冷媒ドレン制御弁(30)の開度が大きくなる。
そして、高温発生器(1)から冷媒管(16)、低温発生
器(2)、及び冷媒管(17)を経て凝縮器(3)へ流れ
る冷媒の量が増加し、又、低温発生器(2)での冷媒蒸
気の発生量が増える。このため、凝縮器(3)から蒸発
器(4)へ流れる冷媒液の量が増え、冷水出口温度が低
下する。又、冷水出口温度が低下したときには、冷媒ド
レン制御弁(30)の開度が小さくなる。そして、高温発
生器(1)から凝縮器(3)へ流れる冷媒の量が減少
し、又、低温発生器(2)での冷媒蒸気の発生量が減少
する。このため、凝縮器(3)から蒸発器(4)へ流れ
る冷媒液の量が減少し、冷水出口温度が上昇する。上記
のように温水主制御が行われているとき、温水出口温度
に応じて加熱量制御弁(21)の開度が変化し、温水出口
温度がほぼ設定温度に保たれる。又、第3図、及び第4
図に示したように冷水出口温度に応じて冷媒ドレン制御
弁(30)の開度が変化し、冷水出口温度がほぼ設定温度
に保たれる。
Also, the cold water load is reduced, and the cold water outlet temperature is
When the hot water outlet temperature is 60 ° C., for example, the cold main temperature main switching device (41A) is switched to the hot water main control, and the control device (41) controls the hot water main control. At this time, the control device (41) outputs a close signal to the first and second on-off valves (33) and (34) and also outputs a fully open signal to the hot water drain control valve (37). Then, the hot water drain control valve (3
7) fully open. Further, the control device (41) outputs an opening signal to the refrigerant drain control valve (30) according to the temperature detected by the cold water outlet temperature detector (42), and when the cold water outlet temperature rises, the refrigerant drain control valve The opening of (30) becomes large.
Then, the amount of the refrigerant flowing from the high temperature generator (1) to the condenser (3) via the refrigerant pipe (16), the low temperature generator (2), and the refrigerant pipe (17) increases, and the low temperature generator ( The amount of refrigerant vapor generated in 2) increases. Therefore, the amount of the refrigerant liquid flowing from the condenser (3) to the evaporator (4) increases, and the cold water outlet temperature decreases. Further, when the cold water outlet temperature decreases, the opening degree of the refrigerant drain control valve (30) decreases. Then, the amount of refrigerant flowing from the high temperature generator (1) to the condenser (3) decreases, and the amount of refrigerant vapor generated in the low temperature generator (2) decreases. Therefore, the amount of the refrigerant liquid flowing from the condenser (3) to the evaporator (4) is reduced, and the cold water outlet temperature rises. When the hot water main control is performed as described above, the opening degree of the heating amount control valve (21) changes according to the hot water outlet temperature, and the hot water outlet temperature is maintained at a substantially set temperature. Also, FIGS. 3 and 4
As shown in the figure, the opening degree of the refrigerant drain control valve (30) changes according to the cold water outlet temperature, and the cold water outlet temperature is maintained at substantially the set temperature.

以下、第4図に基づいて冷媒液ポンプ(19P)、冷媒
ドレン制御弁(30)、第1,第2開閉弁(33),(34)の
制御について説明する。上記のように温水主制御が行わ
れているとき、例えば温水負荷が大きく冷水負荷が減少
し、冷水出口温度が低下した場合には、冷水出口温度に
応じて冷媒ドレン制御弁(30)の開度が小さくなる。そ
して、冷水出口温度が第1設定温度の例えば6.0℃にな
ると、制御装置(41)が動作し、冷媒ドレン制御弁(3
0)へ閉信号を出力する。このため、冷媒ドレン制御弁
(30)は閉じ、冷媒が冷媒管(16),(17)を経て凝縮
器(3)へ流れなくなる。又、制御装置(41)が第1開
閉弁(33)へ開信号を出力する。このため、第1開閉弁
(33)は開き、凝縮器(3)の冷媒液が流れる。このた
め、低温発生器(2)で吸収液から分離して凝縮器
(3)で凝縮した冷媒液は、凝縮器(3)から冷媒液流
下管(18)、第1冷媒液戻し管(31)を経て吸収器
(5)へ流れる。そして、吸収液が稀釈され、吸収液の
濃度は上昇しない。
The control of the refrigerant liquid pump (19P), the refrigerant drain control valve (30), and the first and second opening / closing valves (33) and (34) will be described below with reference to FIG. When hot water main control is performed as described above, for example, when the hot water load is large and the cold water load decreases, and the cold water outlet temperature decreases, the refrigerant drain control valve (30) is opened according to the cold water outlet temperature. The degree becomes smaller. When the chilled water outlet temperature reaches the first set temperature, for example 6.0 ° C., the control device (41) operates and the refrigerant drain control valve (3
Output a close signal to 0). Therefore, the refrigerant drain control valve (30) is closed, and the refrigerant does not flow to the condenser (3) through the refrigerant pipes (16) and (17). Further, the control device (41) outputs an open signal to the first opening / closing valve (33). Therefore, the first opening / closing valve (33) opens and the refrigerant liquid in the condenser (3) flows. Therefore, the refrigerant liquid separated from the absorbing liquid in the low temperature generator (2) and condensed in the condenser (3) flows from the condenser (3) into the refrigerant liquid downflow pipe (18) and the first refrigerant liquid return pipe (31). ) To the absorber (5). Then, the absorption liquid is diluted and the concentration of the absorption liquid does not rise.

上記のように、第1開閉弁(33)が開き凝縮器(3)
の冷媒液が吸収器(8)へ流れているとき、冷水負荷が
さらに減少した場合、或いは零になった場合には、冷水
出口温度がさらに低下する。そして、冷水出口温度が第
1設定温度より低い第2設定温度の例えば5.7℃になる
と、制御装置(41)が動作して第2開閉弁(34)へ開信
号を出力する。そして、第2開閉弁(34)が開くと、冷
媒液ポンプ(19P)から吐出した冷媒液が冷媒液循環管
(19)及び第2冷媒液戻し管(32)を経て吸収器(5)
へ流れる。このため、吸収液がさらに稀釈されると共
に、蒸発器(4)での冷媒散布量が減少し、蒸発器
(4)の冷却能力が大幅に低下して冷水出口温度の過低
下が回避される。
As described above, the first opening / closing valve (33) opens and the condenser (3)
If the cold water load is further reduced or becomes zero when the refrigerant liquid of (1) is flowing to the absorber (8), the cold water outlet temperature further decreases. Then, when the chilled water outlet temperature reaches a second preset temperature lower than the first preset temperature, for example, 5.7 ° C., the control device (41) operates and outputs an open signal to the second opening / closing valve (34). Then, when the second opening / closing valve (34) is opened, the refrigerant liquid discharged from the refrigerant liquid pump (19P) passes through the refrigerant liquid circulation pipe (19) and the second refrigerant liquid return pipe (32) and then the absorber (5).
Flows to. Therefore, the absorption liquid is further diluted, the amount of the refrigerant sprayed in the evaporator (4) is reduced, the cooling capacity of the evaporator (4) is significantly reduced, and an excessive decrease in the cold water outlet temperature is avoided. .

以後、冷水負荷が増え、冷水出口温度が上昇して例え
ば6.0℃になった場合には、冷水出口温度検出器(42)
から信号を入力した制御装置(41)が動作して第2開閉
弁(34)へ閉信号を出力する。そして、冷媒液ポンプ
(19P)から吐出した冷媒液は総て蒸発器(4)にて散
布され、冷却能力が向上する。さらに、冷水負荷が増加
して冷水出口温度が例えば6.3℃になった場合には、制
御装置(41)が動作して第1開閉弁(33)へ閉信号を出
力すると共に、冷媒ドレン制御弁(30)へ開度信号を出
力する。そして、凝縮器(3)の冷媒液は総て蒸発器
(4)へ流れ、又、冷水出口温度の上昇に伴い高温発生
器(1)で発生した冷媒液が冷媒管(16),(17)及び
冷媒ドレン制御弁(30)を経て凝縮器(3)へ流れるよ
うになり、凝縮器(3)から蒸発器(4)へ流れる冷媒
液の量が増加する。そして、冷媒ドレン制御弁(30)の
開度調節によって、低温発生器(2)での冷媒蒸気の発
生量が変化して、蒸発器(4)への冷媒液の流下量が変
化して冷水出口温度がほぼ設定温度に保たれる。その
後、冷水負荷が例えばゼロになり、冷水出口温度の低下
に伴い第1,第2開閉弁(33),(34)が開いた後も、さ
らに冷水出口温度が低下して例えば5.0℃になったとき
には制御装置(41)が動作して冷媒液ポンプ(19P)は
停止し、冷水出口温度が6.0℃になったときに冷媒液ポ
ンプ(19P)は運転を始める。
After that, when the cold water load increases and the cold water outlet temperature rises to, for example, 6.0 ° C, the cold water outlet temperature detector (42)
The control device (41) which receives the signal from the above operates to output a closing signal to the second on-off valve (34). Then, all the refrigerant liquid discharged from the refrigerant liquid pump (19P) is sprayed by the evaporator (4), and the cooling capacity is improved. Further, when the chilled water load increases and the chilled water outlet temperature reaches, for example, 6.3 ° C., the control device (41) operates to output a close signal to the first opening / closing valve (33) and the refrigerant drain control valve. Output the opening signal to (30). Then, all the refrigerant liquid in the condenser (3) flows to the evaporator (4), and the refrigerant liquid generated in the high temperature generator (1) as the temperature of the chilled water outlet rises causes the refrigerant pipes (16) and (17). ) And the refrigerant drain control valve (30) to flow to the condenser (3), and the amount of the refrigerant liquid flowing from the condenser (3) to the evaporator (4) increases. Then, by adjusting the opening degree of the refrigerant drain control valve (30), the amount of refrigerant vapor generated in the low temperature generator (2) is changed, and the amount of refrigerant liquid flowing into the evaporator (4) is changed, so that cold water is cooled. The outlet temperature is maintained at about the set temperature. After that, the cold water load becomes, for example, zero, and even after the first and second opening / closing valves (33) and (34) are opened due to the decrease in the cold water outlet temperature, the cold water outlet temperature further decreases and reaches, for example, 5.0 ° C. In that case, the control device (41) operates to stop the refrigerant liquid pump (19P), and when the chilled water outlet temperature reaches 6.0 ° C., the refrigerant liquid pump (19P) starts operating.

上記実施例によれば、温水主制御時、冷水負荷が大幅
に減少した状態或いは冷水負荷が零の状態が続き冷水出
口温度が低下したときには、冷媒ドレン制御弁(30)が
閉じ、さらに、第1開閉弁(33)が開き、凝縮器(3)
から流出した冷媒液の一部が第1冷媒液戻し管(31)を
介して吸収器(5)へ流れるようになる。このため、吸
収器(5)の吸収液が稀釈され、冷却能力が大幅に低下
して冷水出口温度の過低下を回避することができる。さ
らに、冷水負荷が減少して冷水出口温度が低下した場合
には、第2開閉弁(34)が開き、冷媒液ポンプ(19P)
から吐出した冷媒液の一部が第2冷媒液戻し管(32)を
介して吸収器(5)へ流れ、吸収液が稀釈されると共に
冷媒液の散布量が減少するので、さらに、蒸発器(4)
での冷却能力を減少させることができ、この結果、冷水
負荷の大幅な減少に対しても、冷水出口温度の過低下を
確実に回避することができ、温水主制御時の吸収冷温水
機の運転を安定させることができる。
According to the above-described embodiment, during the hot water main control, when the cold water load is significantly reduced or the cold water load is continuously zero and the cold water outlet temperature is lowered, the refrigerant drain control valve (30) is closed, and 1 open / close valve (33) opens, condenser (3)
A part of the refrigerant liquid flowing out of the first refrigerant liquid returns to the absorber (5) through the first refrigerant liquid return pipe (31). For this reason, the absorbing liquid in the absorber (5) is diluted, the cooling capacity is significantly lowered, and it is possible to avoid excessive lowering of the cold water outlet temperature. Further, when the cold water load decreases and the cold water outlet temperature decreases, the second opening / closing valve (34) opens and the refrigerant liquid pump (19P)
Part of the refrigerant liquid discharged from the refrigerant flows to the absorber (5) through the second refrigerant liquid return pipe (32), and the absorbed liquid is diluted and the spray amount of the refrigerant liquid is reduced. (4)
As a result, it is possible to reliably avoid an excessive decrease in the chilled water outlet temperature even if the chilled water load is drastically reduced. The driving can be stabilized.

又、上記実施例において、第1冷媒液戻し管(31)を
冷媒液循環管(18)と吸収器(5)の気相部との間に設
けたが、例えば、第1冷媒液戻し管(31)を凝縮器
(3)の冷媒液溜め(3A)の下部と吸収器(5)の気相
部との間に設け、第1冷媒液戻し管(31)の途中に第1
開閉弁を設けた場合にも、上記実施例と同様の作用効果
を得ることができる。
In the above embodiment, the first refrigerant liquid return pipe (31) is provided between the refrigerant liquid circulation pipe (18) and the gas phase part of the absorber (5). (31) is provided between the lower part of the refrigerant liquid reservoir (3A) of the condenser (3) and the gas phase part of the absorber (5), and the first refrigerant liquid return pipe (31) is provided with a first portion.
Even when the on-off valve is provided, the same operational effect as that of the above-described embodiment can be obtained.

又、冷媒液ポンプ(19P)が停止したとき、第1開閉
弁(35)が開いているため、凝縮器(3)の冷媒液が吸
収器(5)へ流れ、吸収液の濃度上昇を回避することが
でき、この結果、蒸発器(4)に溜っている冷媒液の氷
結を回避することができる。
Further, when the refrigerant liquid pump (19P) is stopped, the first opening / closing valve (35) is open, so that the refrigerant liquid in the condenser (3) flows to the absorber (5) and avoids an increase in the concentration of the absorbing liquid. As a result, the freezing of the refrigerant liquid accumulated in the evaporator (4) can be avoided.

さらに、上記実施例において、冷水出口温度の低下に
伴い第1開閉弁(33)を開き、さらに冷水出口温度が低
下したときに、第2開閉弁(34)を開いたが、冷水負荷
が急激に減少して冷水出口温度が急激に低下したとき
に、第2開閉弁(34)を開き吸収器(5)へ大量の冷媒
液を送り、吸収液を大幅に稀釈すると共に、蒸発器
(4)での冷媒液の散布量を減少させ、さらに冷水出口
温度低下したときに第1開閉弁(33)を開き凝縮器
(3)の冷媒液を蒸発器(4)へ送りさらに吸収液を稀
釈するようにすることによって、冷水負荷が急激に減少
した場合にも、冷水出口温度の過低下、及び冷媒液の氷
結を回避することができる。又、冷水負荷が急激に減少
した場合に第1,第2開閉弁(33),(34)を同時に開く
ことによって、上記と同様に冷水出口温度の過低下、及
び冷媒液の氷結を回避することができる。
Furthermore, in the above embodiment, the first opening / closing valve (33) was opened as the cold water outlet temperature decreased, and when the cold water outlet temperature further decreased, the second opening / closing valve (34) was opened. When the outlet temperature of the chilled water drops sharply, the second on-off valve (34) is opened to send a large amount of refrigerant liquid to the absorber (5) to dilute the absorbed liquid significantly, and at the same time, the evaporator (4 ), The first spray valve (33) is opened and the refrigerant liquid in the condenser (3) is sent to the evaporator (4) and the absorption liquid is diluted when the cold water outlet temperature further decreases. By doing so, even when the cold water load is suddenly reduced, it is possible to avoid excessive lowering of the cold water outlet temperature and freezing of the refrigerant liquid. Also, by opening the first and second on-off valves (33) and (34) at the same time when the cold water load sharply decreases, the cold water outlet temperature is prevented from excessively decreasing and the refrigerant liquid is frozen in the same manner as above. be able to.

(ト)発明の効果 本発明は以上のように構成された吸収冷温水機であ
り、凝縮器と吸収器との間に第1冷媒液戻し管を接続
し、この第1冷媒液戻し管に開閉弁を設け、かつ、蒸発
器に接続された冷媒液循環管を吸収器との間に第2冷媒
液戻し管を接続し、この第2冷媒液戻し管に開閉弁を設
け、温水器の温水出口側温度に応じて発生器の加熱量を
制御する温水主制御時には、制御装置が動作して上記各
弁を蒸発器の出口側冷水温度に応じて順次開閉制御する
ので、温水主制御時、冷水負荷が大幅に減少した場合
に、上記各弁を開くことにより凝縮器の冷媒液及び蒸発
器の冷媒液が順次吸収器へ流れ、吸収液を大幅に稀釈す
ることができ、この結果、蒸発器の冷却能力を低減して
冷水出口温度の過低下、及び冷媒液の氷結を確実に回避
することができ、この結果、温水主制御時の吸収冷温水
機の運転を安定させることができる。
(G) Effect of the Invention The present invention is an absorption chiller-heater configured as described above, in which a first refrigerant liquid return pipe is connected between the condenser and the absorber, and the first refrigerant liquid return pipe is connected to the first refrigerant liquid return pipe. An opening / closing valve is provided, and a second refrigerant liquid return pipe is connected between the refrigerant liquid circulation pipe connected to the evaporator and the absorber, and an opening / closing valve is provided to the second refrigerant liquid return pipe to During hot water main control that controls the heating amount of the generator according to the hot water outlet side temperature, the control device operates to sequentially open and close each valve according to the evaporator outlet side cold water temperature. , When the cold water load is significantly reduced, the refrigerant liquid in the condenser and the refrigerant liquid in the evaporator sequentially flow to the absorber by opening the valves, and the absorbed liquid can be greatly diluted. To reduce the cooling capacity of the evaporator to avoid excessive lowering of the cold water outlet temperature and freezing of the refrigerant liquid. As a result, the operation of the absorption chiller-heater during hot water main control can be stabilized.

又、凝縮器の冷媒液を吸収器へ導く冷媒液配管と、蒸
発器の冷媒液を吸収器へ導く冷媒液配管とにそれぞれ開
閉弁を設け、これらの開閉弁を蒸発器の冷水出口側の温
度に応じて開閉制御するので、冷水負荷が大幅に減少し
て冷水出口側の温度が低下した場合に凝縮器、及び蒸発
器の冷媒液を吸収器へ流し、吸収液を大幅に稀釈するこ
とができ、又、蒸発器での冷媒散布量を減少させること
ができ、蒸発器の冷却能力を低減させて、冷水出口温度
の過低下を防止することができ、冷水出口温度を安定さ
せることができ、この結果、吸収冷温水機の運転を安定
させることができる。
Further, opening / closing valves are respectively provided in the refrigerant liquid pipe for guiding the refrigerant liquid of the condenser to the absorber and the refrigerant liquid pipe for guiding the refrigerant liquid of the evaporator to the absorber, and these opening / closing valves are provided on the cold water outlet side of the evaporator. Since the opening / closing control is performed according to the temperature, when the cold water load is significantly reduced and the temperature at the cold water outlet side drops, the refrigerant liquid of the condenser and the evaporator is allowed to flow to the absorber, and the absorption liquid is greatly diluted. In addition, it is possible to reduce the amount of refrigerant sprayed in the evaporator, reduce the cooling capacity of the evaporator, prevent excessive lowering of the cold water outlet temperature, and stabilize the cold water outlet temperature. As a result, the operation of the absorption chiller-heater can be stabilized.

さらに、凝縮器の冷媒液を吸収器へ導く冷媒液配管に
第1開閉弁を設け、蒸発器の冷媒液を吸収器へ導く冷媒
液配管に第2開閉弁を設け、これらの開閉弁を蒸発器の
冷水出口側の温度に応じて作動させると共に、第2開閉
弁が閉から開に切換わる温度を上記第1開閉弁の温度よ
り低くしたので、温水主制御時、冷水負荷が大幅に減少
して冷水出口温度が低下したとき、第1開閉弁と第2開
閉弁とが順次開き、凝縮器及び蒸発器の冷媒液によって
吸収液を冷水出口温度の低下に応じて稀釈することがで
き、蒸発器の冷却能力を冷水負荷の大幅な低下に応じて
調節することができ、冷水出口温度の過低下、及び冷媒
液の氷結を防止することができ、吸収冷温水機の運転を
安定させることができる。
Further, a first opening / closing valve is provided in the refrigerant liquid pipe for guiding the refrigerant liquid in the condenser to the absorber, and a second opening / closing valve is provided in the refrigerant liquid pipe for guiding the refrigerant liquid in the evaporator to the absorber, and these opening / closing valves are evaporated. It operates according to the temperature of the cold water outlet side of the water cooler, and the temperature at which the second on-off valve switches from closed to open is lower than the temperature of the first on-off valve, so the cold water load is greatly reduced during hot water main control. Then, when the cold water outlet temperature decreases, the first opening / closing valve and the second opening / closing valve are sequentially opened, and the absorbing liquid can be diluted according to the decrease in the cold water outlet temperature by the refrigerant liquid of the condenser and the evaporator. The cooling capacity of the evaporator can be adjusted according to a significant decrease in the cold water load, the excessive decrease in the cold water outlet temperature and the freezing of the refrigerant liquid can be prevented, and the operation of the absorption cold / hot water machine can be stabilized. You can

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

第1図は本発明の一実施例を示す吸収冷温水機の回路構
成図、第2図は冷水主制御と温水主制御との切換えの説
明図、第3図は冷水負荷と冷水温度との関係図、第4図
は冷媒液ポンプ、第1,第2開閉弁及び冷媒ドレン制御弁
の冷水出口温度に応じた動作の説明図である。 (1)……高温発生器、(3)……凝縮器、(4)……
蒸発器、(5)……吸収器、(17)……冷媒管、(18)
……冷媒液流下管、(19)……冷媒液循環管、(19P)
……冷媒液ポンプ、(30)……冷媒ドレン制御弁、(3
1),(32)……第1,第2冷媒液戻し管、(33),(3
4)……第1,第2開閉弁、(35)……温水器。
FIG. 1 is a circuit configuration diagram of an absorption chiller-heater showing an embodiment of the present invention, FIG. 2 is an explanatory diagram of switching between cold water main control and hot water main control, and FIG. 3 is a diagram showing cold water load and cold water temperature. FIG. 4 is a diagram for explaining the operation of the refrigerant liquid pump, the first and second opening / closing valves, and the refrigerant drain control valve according to the cold water outlet temperature. (1) …… High temperature generator, (3) …… Condenser, (4) ……
Evaporator, (5) ... Absorber, (17) ... Refrigerant tube, (18)
…… Refrigerant liquid flow down pipe, (19) …… Refrigerant liquid circulation pipe, (19P)
…… Refrigerant liquid pump, (30) …… Refrigerant drain control valve, (3
1), (32) …… First and second refrigerant liquid return pipes, (33), (3
4) …… First and second on-off valves, (35) …… Water heater.

フロントページの続き (72)発明者 岩谷 孝樹 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (72)発明者 金子 敏之 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (56)参考文献 特開 昭62−155478(JP,A) 特開 平3−156261(JP,A)Front page continuation (72) Inventor Takaki Iwatani, 2-18 Keihan Hondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd. (72) Toshiyuki Kaneko 2--18, Keihan Hondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd. (56) References JP 62-155478 (JP, A) JP 3-156261 (JP, A)

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】発生器、凝縮器、蒸発器、及び吸収器をそ
れぞれ接続して蒸発器から冷水を取り出す冷凍サイクル
の高温側に付設された温水器から温水を取り出すように
構成し、冷水主制御の運転時、蒸発器の冷水出口側の温
度に応じて発生器の加熱量を調節すると共に、温水器の
温水出口側の温度に応じて温水器からの冷媒液のドレン
量を調節し、かつ、温水主制御の運転時、上記冷水出口
側の温度に応じて発生器から凝縮器へ流れる冷媒量を調
節すると共に、上記温水出口温度に応じて発生器の加熱
量を調節する吸収冷温水機において、凝縮器と吸収器と
の間に第1冷媒液戻し配管を接続し、この第1冷媒液戻
し配管に第1開閉弁を設け、かつ蒸発器に接続された冷
媒循環管と吸収器との間に第2冷媒液戻し配管を接続
し、この第2冷媒液戻し配管に第2開閉弁を設け、温水
主制御時、上記蒸発器の出口側冷水温度に応じて上記第
1開閉弁と第2開閉弁とを順次開閉制御する制御装置を
備えたことを特徴とする吸収冷温水機。
1. A generator, a condenser, an evaporator, and an absorber are connected to each other, and hot water is taken out from a water heater attached to a high temperature side of a refrigeration cycle for taking cold water from the evaporator. During control operation, while adjusting the heating amount of the generator according to the temperature of the cold water outlet side of the evaporator, and adjusting the drain amount of the refrigerant liquid from the water heater depending on the temperature of the hot water outlet side of the water heater, And, during the operation of the hot water main control, while adjusting the amount of refrigerant flowing from the generator to the condenser according to the temperature of the cold water outlet side, absorption cold hot water that adjusts the heating amount of the generator according to the hot water outlet temperature In a machine, a first refrigerant liquid return pipe is connected between a condenser and an absorber, a first opening / closing valve is provided in the first refrigerant liquid return pipe, and a refrigerant circulation pipe and an absorber connected to an evaporator The second refrigerant liquid return pipe is connected between the A second opening / closing valve is provided in the pipe, and a control device for sequentially opening / closing the first opening / closing valve and the second opening / closing valve in accordance with the outlet side cold water temperature of the evaporator during hot water main control is provided. Absorption chiller / heater.
【請求項2】発生器、凝縮器、蒸発器、及び吸収器をそ
れぞれ接続して蒸発器から冷水を取り出す冷凍サイクル
の高温側に付設された温水器から温水を取り出すように
構成し、温水主制御時、蒸発器の冷水出口側の温度に応
じて発生器から凝縮器へ流れる冷媒量を調節すると共
に、温水器の温水出口側の温度に応じて発生器の加熱量
を調節する吸収冷温水機において、凝縮器の冷媒液を吸
収器へ導く冷媒液配管を設け、この冷媒液配管に上記冷
水出口側の温度に応じて開閉する第1開閉弁を設け、か
つ、蒸発器の冷媒液を吸収器へ導く冷媒液配管を設け、
この冷媒液配管に上記冷水出口側の温度に応じて開閉す
る第2開閉弁を設けたことを特徴とする吸収冷温水機。
2. A hot water main unit configured to connect a generator, a condenser, an evaporator, and an absorber to take hot water from a water heater attached to a high temperature side of a refrigeration cycle for taking cold water from the evaporator. At the time of control, the amount of refrigerant flowing from the generator to the condenser is adjusted according to the temperature of the cold water outlet side of the evaporator, and the absorption cold hot water that adjusts the heating amount of the generator according to the temperature of the hot water outlet side of the water heater In the machine, a refrigerant liquid pipe for guiding the refrigerant liquid of the condenser to the absorber is provided, a first opening / closing valve that opens and closes according to the temperature of the cold water outlet side is provided in the refrigerant liquid pipe, and the refrigerant liquid of the evaporator is Provide a refrigerant liquid pipe leading to the absorber,
An absorption chiller-hot water machine characterized in that a second opening / closing valve that opens and closes according to the temperature of the cold water outlet side is provided in the refrigerant liquid pipe.
【請求項3】発生器、凝縮器、蒸発器、及び吸収器をそ
れぞれ接続して蒸発器から冷水を取り出す冷凍サイクル
の高温側に付設された温水器から温水を取り出すように
構成し、温水主制御時、蒸発器の冷水出口側の温度に応
じて発生器から凝縮器へ流れる冷媒量を調節すると共
に、温水器の温水出口温度に応じて発生器の加熱量を調
節する吸収冷温水機において、凝縮器と冷媒液を吸収器
へ導く冷媒液配管を設け、この冷媒液配管に上記冷水出
口側の温度に応じて作動する第1開閉弁を設け、かつ、
蒸発器の冷媒液を吸収器へ導く冷媒液配管を設け、この
冷媒液配管に上記冷水出口側の温度に応じて作動し、閉
から開に切換わる温度が上記第1開閉弁の温度より低く
設定された第2開閉弁を設けたことを特徴とする吸収冷
温水機。
3. A hot water main unit configured to connect a generator, a condenser, an evaporator and an absorber to take hot water from a water heater attached to a high temperature side of a refrigeration cycle for taking cold water from the evaporator. At the time of control, in an absorption chiller-heater that adjusts the amount of refrigerant flowing from the generator to the condenser according to the temperature on the cold water outlet side of the evaporator, and adjusts the heating amount of the generator according to the hot water outlet temperature of the water heater. A condenser liquid and a refrigerant liquid pipe for guiding the refrigerant liquid to the absorber are provided, and the refrigerant liquid pipe is provided with a first opening / closing valve that operates according to the temperature of the cold water outlet side, and
A refrigerant liquid pipe for guiding the refrigerant liquid of the evaporator to the absorber is provided, and the temperature of the refrigerant liquid pipe that operates according to the temperature of the cold water outlet side and switches from closed to open is lower than the temperature of the first on-off valve. An absorption chiller-heater having a set second opening / closing valve.
JP2080107A 1990-03-28 1990-03-28 Absorption cold water heater Expired - Lifetime JPH0833260B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2080107A JPH0833260B2 (en) 1990-03-28 1990-03-28 Absorption cold water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2080107A JPH0833260B2 (en) 1990-03-28 1990-03-28 Absorption cold water heater

Publications (2)

Publication Number Publication Date
JPH03279760A JPH03279760A (en) 1991-12-10
JPH0833260B2 true JPH0833260B2 (en) 1996-03-29

Family

ID=13708962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2080107A Expired - Lifetime JPH0833260B2 (en) 1990-03-28 1990-03-28 Absorption cold water heater

Country Status (1)

Country Link
JP (1) JPH0833260B2 (en)

Also Published As

Publication number Publication date
JPH03279760A (en) 1991-12-10

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