JP2645824B2 - Double effect absorption refrigerator - Google Patents

Double effect absorption refrigerator

Info

Publication number
JP2645824B2
JP2645824B2 JP15362286A JP15362286A JP2645824B2 JP 2645824 B2 JP2645824 B2 JP 2645824B2 JP 15362286 A JP15362286 A JP 15362286A JP 15362286 A JP15362286 A JP 15362286A JP 2645824 B2 JP2645824 B2 JP 2645824B2
Authority
JP
Japan
Prior art keywords
solution
control valve
temperature
refrigerant liquid
absorber
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 - Fee Related
Application number
JP15362286A
Other languages
Japanese (ja)
Other versions
JPS6314056A (en
Inventor
龍雄 宮城
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 JP15362286A priority Critical patent/JP2645824B2/en
Publication of JPS6314056A publication Critical patent/JPS6314056A/en
Application granted granted Critical
Publication of JP2645824B2 publication Critical patent/JP2645824B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は濃溶液流路にポンプを備える型式の二重効用
吸収冷凍機の改良に関する。
The present invention relates to an improvement in a double effect absorption refrigerator having a pump in a concentrated solution flow path.

(ロ) 従来の技術 上記型式の二重効用吸収冷凍機の従来の技術として、
例えば特公昭53−36174号公報にみられるように、稀溶
液用ポンプの吐出側と濃溶液用ポンプの吸込み側とを制
御弁付きの管路で接続し、この管路の制御弁の開度を蒸
発器の冷水出口温度検出器の信号により調節する制御器
を備えたものが知られている。
(B) Conventional technology As a conventional technology of the above-described double effect absorption refrigerator,
For example, as shown in JP-B-53-36174, the discharge side of the dilute solution pump and the suction side of the concentrated solution pump are connected by a pipe with a control valve, and the opening of the control valve of this pipe is And a controller for adjusting the temperature of the evaporator by a signal from a temperature detector of a chilled water outlet of the evaporator.

(ハ) 発明が解決しようとする問題点 上記した従来の二重効用吸収冷凍機においては、吸収
器へ流す濃溶液を稀溶液で希釈することにより部分負荷
時での吸収器の冷媒吸収能力を弱めて冷え過ぎを防ぎ得
る利点があるものの、稀溶液による濃溶液の希釈には限
度があるため、微小負荷時での冷え過ぎを防ぎきれない
問題点があった。
(C) Problems to be Solved by the Invention In the conventional double-effect absorption refrigerator described above, the concentrated solution flowing to the absorber is diluted with a dilute solution to reduce the refrigerant absorption capacity of the absorber at partial load. Although there is an advantage that the solution can be weakened to prevent overcooling, dilution of the concentrated solution with a dilute solution is limited, so that there is a problem that overcooling under a small load cannot be prevented.

本発明は、この問題点に鑑み、微小負荷時においても
冷え過ぎを防ぐことの可能な二重効用吸収冷凍機の提供
を目的としたものである。
The present invention has been made in view of the above problems, and has as its object to provide a double-effect absorption refrigerator capable of preventing overcooling even under a small load.

(ニ) 問題点を解決するための手段 本発明は、前述の問題点を解決する手段として、上記
型式の二重効用吸収冷凍機における蒸発器の冷水出口温
度検出器の信号により、濃溶液用ポンプ吸込み側と吸収
器の稀溶液溜とを結んだ管路の制御弁の開度調節を行う
と共に稀溶液溜と冷媒液流路とを結んだ冷媒液ブロー用
管路の開閉弁の開閉切替を行う構成としたものである。
(D) Means for Solving the Problems The present invention solves the above-mentioned problems by using a signal from a chilled water outlet temperature detector of an evaporator in a double effect absorption refrigerator of the above-mentioned type to measure a concentrated solution. Controls the opening of the control valve of the line connecting the pump suction side and the dilute solution reservoir of the absorber, and switches the on / off valve of the refrigerant liquid blowing line connecting the dilute solution reservoir and the refrigerant liquid flow path Is performed.

(ホ) 作用 本発明の二重効用吸収冷凍機においては、冷水温度の
下降しやすい微小負荷時に稀溶液と冷媒液とで濃溶液を
稀釈して吸収器の冷媒吸収能力を従来のものよりも弱め
る作用を発揮させることができる。このため、本発明の
二重効用吸収冷凍機においては、従来のものにくらべ、
微小負荷時での冷水温度の降下をより一層軽減すること
ができ、冷え過ぎを効果的に防ぐことが可能となる。
(E) Function In the double effect absorption refrigerator of the present invention, the concentrated solution is diluted with the dilute solution and the refrigerant liquid at a small load when the temperature of the chilled water is apt to decrease, so that the refrigerant absorption capacity of the absorber is higher than that of the conventional one. The effect of weakening can be exhibited. For this reason, in the double effect absorption refrigerator of the present invention,
It is possible to further reduce the drop in the temperature of the chilled water at the time of a minute load, and it is possible to effectively prevent overcooling.

(ヘ) 実施例 第1図は本発明による二重効用吸収冷凍機の一実施例
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)および
凝縮器(4)より成る発生凝縮器、(5)は蒸発器
(6)および吸収器(7)より成る蒸発吸収器、(8)
は低温溶液熱交換器、(9)は高温溶液熱交換器、(P
LA)は稀溶液用ポンプ、(PHA)は濃溶液用ポンプ、(P
R)は冷媒液用ポンプであり、これら機器を冷媒用管路
(10)、(11)、冷媒液流下用管路(12)、冷媒液還流
用管路(13)、(14)、稀溶液用管路(15)、(16)、
(17)、(18)、中間濃度の溶液用管路(19)、(2
0)、濃溶液用管路(21)、(22)、(23)で接続して
冷媒〔水〕と溶液〔臭化リチウム水溶液〕の循環路が形
成されている。
(F) Embodiment FIG. 1 is a schematic structural explanatory view showing an embodiment of a double effect absorption refrigerator according to the present invention. In FIG.
(1) is a high-temperature generator, (2) is a generating condenser composed of a low-temperature generator (3) and a condenser (4), (5) is an evaporator-absorber composed of an evaporator (6) and an absorber (7). , (8)
Is a low-temperature solution heat exchanger, (9) is a high-temperature solution heat exchanger, (P
(LA ) is a dilute solution pump, (P HA ) is a concentrated solution pump, (P
R ) is a refrigerant liquid pump, which connects these devices with refrigerant lines (10) and (11), refrigerant liquid flowing down line (12), refrigerant liquid recirculating lines (13) and (14), Solution conduits (15), (16),
(17), (18), medium concentration solution line (19), (2
0) and a concentrated solution pipe line (21), (22), (23) connected to form a circulation path for the refrigerant [water] and the solution [lithium bromide aqueous solution].

(24)は高温発生器(1)の燃焼加熱室、(25)は低
温発生器(3)の加熱器、(26)は凝縮器(4)の冷却
器、(27)は蒸発器(6)の熱交換器、(28)は吸収器
(7)の冷却器、(29)は蒸発器(6)の冷媒溶溜、
(30)は吸収器(7)の溶液溜、(B)は高温発生器
(1)のバーナー、(31)、(31)…は燃焼ガスの通
路、(32)は燃焼ガス排気路、(33)、(34)は、それ
ぞれ、バーナー(B)への燃料供給路、燃焼用空気供給
路であり、また、(35)、(36)は熱交換器(27)と接
続した冷温水用管路、(37)、(38)、(39)は冷却器
(28)、(26)を直列に接続した冷却水用管路である。
なお、(P)、(F)はそれぞれバーナー(B)の着火
装置、送風機、(40)は冷温切替弁(VCHR)付きの冷媒
蒸気用管路、(41)は冷温切替弁(VCHA)付きの溶液用
管路である。
(24) is a combustion heating chamber of the high-temperature generator (1), (25) is a heater of the low-temperature generator (3), (26) is a cooler of the condenser (4), and (27) is an evaporator (6). ), A heat exchanger (28), a cooler of an absorber (7), (29) a refrigerant distillation of an evaporator (6),
(30) is a solution reservoir of the absorber (7), (B) is a burner of the high-temperature generator (1), (31), (31) ... are combustion gas passages, (32) is a combustion gas exhaust passage, ( 33) and (34) are a fuel supply path and a combustion air supply path to the burner (B), respectively, and (35) and (36) are for cold and hot water connected to the heat exchanger (27). The pipelines (37), (38) and (39) are cooling water pipelines in which the coolers (28) and (26) are connected in series.
In addition, (P) and (F) are the ignition device and the blower of the burner (B), respectively, (40) is a refrigerant vapor line with a cold / hot switching valve (V CHR ), and (41) is a cold / hot switching valve (V CHA). ) Is for the solution.

(42)は吸収器(7)の溶液溜(30)と濃溶液用ポン
プ(PHA)吸込み側の濃溶液用管路(21)とを結んだ溶
液流通用管路で、この管路には流量制御弁(VA)が備え
てある。また、(43)は冷媒液用ポンプ(PR)吐出側の
冷媒液還流用管路(14)と吸込器(7)の溶液溜(30)
とを結んだ冷媒液ブロー用管路で、この管路には開閉弁
(V)が備えてある。
(42) is a solution circulation line connecting the solution reservoir (30) of the absorber (7) and the concentrated solution pump ( PHA ) suction side pipeline (21). Is equipped with a flow control valve (V A ). (43) is a refrigerant liquid recirculation line (14) on the refrigerant liquid pump (P R ) discharge side and a solution reservoir (30) of the suction device (7).
And an on-off valve (V).

(VF)は燃料供給路(33)に備えた燃料制御弁、
(D)は燃料用空気供給路(34)に備えたダンパーであ
り、このダンパーは燃料制御弁(VF)とリンクして開度
調節されるようになっている。また、(ST)は冷温水用
管路(36)に備えた温度検出器である。
(V F ) is a fuel control valve provided in the fuel supply path (33),
(D) is a damper provided in the fuel air supply path (34), and this damper is linked to a fuel control valve (V F ) to adjust the opening. Further, a temperature detector provided in (S T) is hot and cold water conduit (36).

そして、(C)は温度検出器(ST)からの信号を受け
て燃料制御弁(VF)の開度調節信号と流量制御弁(VA
の開度調節信号と開閉弁(V)の開閉切替信号と冷媒液
用ポンプ(PR)の発停信号とを送る制御器であり、この
制御器は、図示していないが、温度設定部やこれにより
設定された温度と温度検出器の感知温度との高低をくら
べる温度比較部や信号入出力部などの電気回路で構成さ
れている。
(C) receives the signal from the temperature detector (S T ) and receives the opening control signal for the fuel control valve (V F ) and the flow control valve (V A )
The controller sends a signal for controlling the opening degree, a signal for switching the opening and closing of the on-off valve (V), and a signal for starting and stopping the pump for refrigerant liquid (P R ). And an electric circuit such as a temperature comparison unit and a signal input / output unit that compares the level of the temperature set by this with the temperature sensed by the temperature detector.

次に、このように構成された二重効用吸収冷凍機(以
下、本機という)の運転動作例について第2図ないし第
4図を参照しつつ説明する。
Next, an operation example of the double effect absorption refrigerator (hereinafter, referred to as this machine) configured as described above will be described with reference to FIG. 2 to FIG.

第2図は流量制御弁(VA)および燃料制御弁(VF)の
開度と蒸発器(6)の冷水出口温度との関係を表わした
線図である。また、第3図は開閉弁(V)の開閉切替動
作と冷水出口温度との関係を表わした線図であり、第4
図は冷媒液用ポンプ(PR)と冷水出口温度との関係を表
わした線図である。
FIG. 2 is a diagram showing the relationship between the opening degree of the flow control valve (V A ) and the fuel control valve (V F ) and the chilled water outlet temperature of the evaporator (6). FIG. 3 is a diagram showing the relationship between the switching operation of the on-off valve (V) and the chilled water outlet temperature.
The figure is a diagram showing the relationship between the coolant pump (P R ) and the chilled water outlet temperature.

本機の冷水取出し運転において、冷水出口温度が定格
値〔例えば7℃〕であるとき、温度検出器(ST)からの
信号を受けた制御器(C)により溶液用の流量制御弁
(VA)の全閉信号、燃料制御弁(VF)の全開信号、冷媒
ブロー用の開閉弁(V)の全閉信号および冷媒液用ポン
プ(PR)の作動信号が送られ定格の運転が行われる。ま
た、冷水出口温度が定格値を越えたときも、制御器
(C)から定格運転時と同様の信号が発信され、運転が
行われる〔第2図〜第4図参照〕。
In the chilled water discharge operation of the present apparatus, when the chilled water outlet temperature is a rated value (for example, 7 ° C.), the controller (C) which receives a signal from the temperature detector (S T ) receives a solution flow control valve (V). All close signal of a), fully open signal of the fuel control valve (V F), the operation of the actuation signal is sent rating of all closing signal and the coolant pump (P R) of the opening and closing valve for refrigerant blow (V) Done. Also, when the chilled water outlet temperature exceeds the rated value, the same signal as in the rated operation is transmitted from the controller (C) and the operation is performed (see FIGS. 2 to 4).

そして、負荷が減りこれに伴ない冷水出口温度が定格
値より低くなったとき、温度検出器(ST)からの信号を
受けた制御器(C)は、第2図に示すように、冷水出口
温度に応じて比例的に燃料制御弁(VF)の開度を減らす
一方で溶液用流量制御弁(VA)の開度を増やす。なお、
ダンパー(D)の開度は燃料制御弁(VF)と連動して減
じられる。
Then, when the load decreases and the chilled water outlet temperature falls below the rated value, the controller (C) receiving the signal from the temperature detector ( ST ), as shown in FIG. The opening of the fuel flow control valve (V F ) is increased while the opening of the solution flow control valve (V A ) is increased in proportion to the outlet temperature. In addition,
The opening of the damper (D) is reduced in conjunction with the fuel control valve (V F ).

このように制御されることにより、吸収器(7)の冷
却器(28)に散布される濃溶液への稀溶液の混入量言い
代えれば散布濃溶液の濃度と高温発生器(1)の加熱量
とが負荷に応じて同時に調節されるため、部分負荷時に
おける冷凍能力制御の追従性が向上する。
With such control, the amount of the dilute solution mixed into the concentrated solution sprayed on the cooler (28) of the absorber (7), in other words, the concentration of the sprayed concentrated solution and the heating of the high-temperature generator (1) Since the amount and the load are simultaneously adjusted according to the load, the followability of the refrigeration capacity control at the time of the partial load is improved.

さらに負荷が減り冷水出口温度が低温設定値〔例えば
5℃〕に達したとき、燃料制御弁(VF)は全閉されると
共に流量制御弁(VA)は全開され、かつ、第3図に示す
ように制御器(C)は冷媒液ブロー用の開閉弁(V)の
全開信号を送り、冷媒液が冷媒液用ポンプ(PR)により
吸収器(7)の溶液溜(30)内の稀溶液にブローされ、
この稀溶液が希釈される。そして、希釈された稀溶液に
より濃溶液がうすめられつつ吸収器(7)内に散布され
てその冷媒吸収能力がさらに弱められるため、微小負荷
における冷凍能力制御の追従性も良くなる。
When the load further decreases and the chilled water outlet temperature reaches the low-temperature set value (for example, 5 ° C.), the fuel control valve (V F ) is fully closed, the flow control valve (V A ) is fully opened, and FIG. As shown in (1), the controller (C) sends a fully open signal of the on-off valve (V) for blowing the refrigerant liquid, and the refrigerant liquid is pumped into the solution reservoir (30) of the absorber (7) by the refrigerant liquid pump (P R ). Blown into a dilute solution of
This dilute solution is diluted. Then, the concentrated solution is dispersed in the absorber (7) while being diluted by the diluted diluted solution, and the refrigerant absorption capacity is further weakened, so that the follow-up performance of the refrigeration capacity control under a small load is improved.

また、なお一層の負荷の減少や本機に供給される冷却
水の温度降下などにより冷水出口温度が下限設定値〔例
えば4.5℃〕まで低下したとき、第4図に示すように、
制御器(C)は冷媒液用ポンプ(PR)の作動停止信号を
発信し、蒸発器(6)の熱交換器(27)への冷媒液の散
布が断たれて冷媒の気化作用が止められている。その結
果、微小負荷時における冷水の過度の温度降下すなわち
負荷側の冷え過ぎが防止され、かつ、冷水の凍結も防止
される。
Further, when the chilled water outlet temperature falls to the lower limit set value (for example, 4.5 ° C.) due to a further reduction in load or a drop in the temperature of the cooling water supplied to the unit, as shown in FIG.
The controller (C) sends an operation stop signal of the refrigerant liquid pump (P R ), and the spraying of the refrigerant liquid to the heat exchanger (27) of the evaporator (6) is cut off to stop the vaporization of the refrigerant. Have been. As a result, an excessive temperature drop of the cold water at the time of a minute load, that is, excessive cooling of the load side is prevented, and freezing of the cold water is also prevented.

一方、減少していた負荷が増え始めて冷水出口温度が
上昇し始めた場合、制御器(C)は冷水出口温度の低温
設定値〔5℃〕への復帰時に冷媒液用ポンプ(PR)の作
動復帰信号と、燃料制御弁(VF)の開度の増大制御信号
と溶液用流量制御弁(VA)の開度の減少制御信号とを発
し、かつ、冷水出口温度が低温設定値〔5℃〕よりも所
定温度〔例えば0.5℃〕高い値〔5.5℃〕まで上昇した
時、制御器(C)は冷媒液ブロー用の開閉弁(V)にそ
の閉止信号を送り、かつまた、冷水出口温度の定格値へ
の復帰時に制御器(C)は燃料制御弁(VF)の全開信号
と流量制御弁(VA)の全閉信号とを発して本機の定格運
転が再開される。
On the other hand, if the chilled water outlet temperature starts to increase due to the decrease in the load, the controller (C) switches the refrigerant liquid pump (P R ) when the chilled water outlet temperature returns to the low temperature set value [5 ° C.]. An operation return signal, a control signal for increasing the opening of the fuel control valve (V F ) and a control signal for decreasing the opening of the solution flow control valve (V A ), and the chilled water outlet temperature is set to a low temperature set value [ When the temperature rises to a value [5.5 ° C.] higher than the predetermined temperature [0.5 ° C.] than the temperature [5 ° C.], the controller (C) sends a signal to close the on-off valve (V) for blowing the refrigerant liquid, and When the outlet temperature returns to the rated value, the controller (C) issues a fully open signal of the fuel control valve (V F ) and a fully closed signal of the flow control valve (V A ) to resume the rated operation of the machine. .

なお、本機より温水を取出すときには、冷温切替弁
(VCHR)、(VCHR)を全開する一方で開閉弁(V)およ
び流量制御弁(VA)を全閉し、冷媒液用ポンプ(PR)お
よび濃溶液用ポンプ(PHA)の作動を止める一方で稀溶
液用ポンプ(PLA)を作動させ、吸収器(7)と凝縮器
(4)への冷却水の供給を断ち、かつ温度検出器(ST
の信号により制御器(C)を介して燃料制御弁(VF)の
開度を温水負荷に応じて制御しつつ運転する。なおま
た、本機の冷水取出し運転から温水取出し運転への切替
時に冷媒液ブロー用の開閉弁(V)を開いて予め溶液の
希釈運転を行い、その後温水取出し運転へ移行させるよ
うにしても良い。
When taking out hot water from the machine, the cold / hot switching valves (V CHR ) and (V CHR ) are fully opened while the on-off valve (V) and the flow control valve (V A ) are fully closed, and the refrigerant liquid pump ( While the operation of the P R ) and the concentrated solution pump (P HA ) is stopped, the dilute solution pump (P LA ) is activated, and the supply of the cooling water to the absorber (7) and the condenser (4) is cut off. And temperature detector (S T )
Is operated while controlling the opening degree of the fuel control valve (V F ) according to the hot water load through the controller (C) in response to the signal (1). In addition, when switching from the cold water discharging operation to the hot water discharging operation of the present apparatus, the on-off valve (V) for blowing the refrigerant liquid may be opened to perform the solution dilution operation in advance, and then the operation may be shifted to the hot water discharging operation. .

また、本機において、図示していないが、凝縮器
(4)内の冷媒液を溶液溜(30)の溶液中にブローする
ようにしても良いことは勿論である。
Although not shown in the drawings, the refrigerant liquid in the condenser (4) may be blown into the solution in the solution reservoir (30).

(ト) 発明の効果 以上のとおり、本発明によれば、稀溶液と冷媒液とで
濃溶液を希釈して吸収器の冷媒吸収能力を迅速に弱める
作用を二重効用吸収冷凍機に発揮させ得るので、負荷の
急減における冷凍能力制御の追従性の向上効果と冷え過
ぎ防止の効果とを二重効用吸収冷凍機にもたらすことが
できる。
(G) Effects of the Invention As described above, according to the present invention, the double effect absorption refrigerator has the effect of diluting the concentrated solution with the dilute solution and the refrigerant liquid to quickly weaken the refrigerant absorption capacity of the absorber. Therefore, the effect of improving the followability of the refrigeration capacity control when the load suddenly decreases and the effect of preventing overcooling can be provided to the double effect absorption refrigerator.

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

第1図は本発明にする二重効用吸収冷凍機の一実施例を
示した概略構成説明図、第2図は燃料制御弁と溶液用流
量制御弁の動作説明図、第3図は冷媒液ブロー用の開閉
弁の動作説明図、第4図は冷媒液用ポンプの動作説明図
である。 (1)……高温発生器、(2)……低温発生器、(4)
……凝縮器、(6)……蒸発器、(7)……吸収器、
(8)、(9)……低温、高温溶液熱交換器、(PR)…
…冷媒液用ポンプ、(PLA)……稀溶液用ポンプ、
(PHA)……濃溶液用ポンプ、(13)、(14)……冷媒
液還流用管路、(21)、(22)、(23)……濃溶液用管
路、(27)……熱交換器、(28)……冷却器、(29)…
…冷媒液溜、(30)……溶液溜、(42)……溶液流通用
管路、(43)……冷媒液ブロー用管路、(C)……制御
器、(VA)……流量制御弁、(VF)……燃料制御弁、
(V)……開閉弁、(ST)……温度検出器。
FIG. 1 is a schematic diagram illustrating an embodiment of a double effect absorption refrigerator according to the present invention, FIG. 2 is a diagram illustrating the operation of a fuel control valve and a solution flow control valve, and FIG. FIG. 4 is an operation explanatory view of the on-off valve for blowing, and FIG. 4 is an operational explanatory view of the refrigerant liquid pump. (1) High temperature generator, (2) Low temperature generator, (4)
... condenser, (6) ... evaporator, (7) ... absorber,
(8), (9) ... Low temperature, high temperature solution heat exchanger, (P R ) ...
… Refrigerant liquid pump, (P LA ) …… Dilute solution pump,
(P HA ) ... Pump for concentrated solution, (13), (14) ... Refrigerant liquid reflux pipe, (21), (22), (23) ... Pipe for concentrated solution, (27) ... ... heat exchanger, (28) ... cooler, (29) ...
... Refrigerant liquid reservoir, (30) ... Solution reservoir, (42) ... Solution distribution pipeline, (43) ... Refrigerant liquid blow pipeline, (C) ... Controller, ( VA ) ... Flow control valve, (V F ) …… Fuel control valve,
(V): On-off valve, (S T ): Temperature detector.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】低温発生器から低温溶液熱交換器を経て吸
収器へ至る濃溶液流路に濃溶液用ポンプの備えられた二
重効用吸収冷凍機において、濃溶液用ポンプの吸込み側
と吸収器の溶液溜とを制御弁付きの管路で結ぶと共に冷
媒液流路と吸収器の溶液溜とを開閉弁付きの冷媒液ブロ
ー用管路で結び、かつ、蒸発器の冷水出口温度を感知す
る検出器の信号により前記制御弁の開度調節と開閉弁の
開閉切替とを行う制御器を備えていることを特徴とした
二重効用吸収冷凍機。
In a double effect absorption refrigerator having a concentrated solution pump provided in a concentrated solution flow path from a low temperature generator to a absorber through a low temperature solution heat exchanger, a suction side of the concentrated solution pump and an absorber are connected. Connects the solution reservoir of the evaporator with a pipe with a control valve, connects the refrigerant liquid flow path and the solution reservoir of the absorber with a refrigerant liquid blow pipe with an on-off valve, and senses the chilled water outlet temperature of the evaporator. A double-effect absorption refrigerator comprising a controller that controls the opening of the control valve and switches the opening and closing of the on-off valve in accordance with a signal from a detector that performs the operation.
JP15362286A 1986-06-30 1986-06-30 Double effect absorption refrigerator Expired - Fee Related JP2645824B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15362286A JP2645824B2 (en) 1986-06-30 1986-06-30 Double effect absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15362286A JP2645824B2 (en) 1986-06-30 1986-06-30 Double effect absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS6314056A JPS6314056A (en) 1988-01-21
JP2645824B2 true JP2645824B2 (en) 1997-08-25

Family

ID=15566515

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15362286A Expired - Fee Related JP2645824B2 (en) 1986-06-30 1986-06-30 Double effect absorption refrigerator

Country Status (1)

Country Link
JP (1) JP2645824B2 (en)

Also Published As

Publication number Publication date
JPS6314056A (en) 1988-01-21

Similar Documents

Publication Publication Date Title
KR920003906B1 (en) Absorption system hot and cold water supply apparatus
JP2645824B2 (en) Double effect absorption refrigerator
JP3075944B2 (en) Absorption chiller / heater
JPS602584B2 (en) Absorption chiller safety device
KR100193750B1 (en) Absorption Cooling Unit
JP3086594B2 (en) Single double effect absorption refrigerator
JP2918665B2 (en) Operation stop method and stop control device for absorption chiller / chiller / heater
JP2895974B2 (en) Absorption refrigerator
JPH02140564A (en) Controlling method for absorption refrigerator
JP3157668B2 (en) Absorption chiller / heater
JPH0627591B2 (en) Absorption refrigerator
JP2883372B2 (en) Absorption chiller / heater
JPS6021721Y2 (en) Absorption chiller control device
JP3434280B2 (en) Absorption refrigerator and its operation method
JPH08233392A (en) Absorption type refrigerating machine
JP3824441B2 (en) Absorption refrigeration equipment
JPS6113547B2 (en)
JP2567662B2 (en) Air-cooled double-effect absorption refrigerator
JPH07849Y2 (en) Air-cooled absorption chiller / heater
JPH04313652A (en) Absorption refrigerating machine
JPS6117319Y2 (en)
KR20000006027A (en) Absorptive refrigerator
JP2592014B2 (en) Absorption chiller / heater
JPS6149586B2 (en)
JPH0448454Y2 (en)

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees