JPH0718618B2 - Cold temperature switching absorption refrigerator - Google Patents
Cold temperature switching absorption refrigeratorInfo
- Publication number
- JPH0718618B2 JPH0718618B2 JP1864086A JP1864086A JPH0718618B2 JP H0718618 B2 JPH0718618 B2 JP H0718618B2 JP 1864086 A JP1864086 A JP 1864086A JP 1864086 A JP1864086 A JP 1864086A JP H0718618 B2 JPH0718618 B2 JP H0718618B2
- Authority
- JP
- Japan
- Prior art keywords
- machine
- liquid
- absorbing liquid
- gas
- 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 - Lifetime
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 本発明は吸収液を用いて吸収器内の不凝縮ガスを抽気し
てこれを機外へ排気するガス排出装置の備えられた冷温
切換型吸収冷凍機(以下、この種の吸収冷凍機という)
の改良に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a cold / temperature switching equipped with a gas discharge device for extracting uncondensed gas in an absorber using an absorbing liquid and discharging the extracted gas to the outside of the machine. Type absorption refrigerator (hereinafter referred to as this type of absorption refrigerator)
Regarding the improvement of.
(ロ)従来の技術 この種の吸収冷凍機の従来の技術として、ポンプから噴
射される吸収液のエゼクタ作用により吸収器内の不凝縮
ガスを抽気しつつガス貯留部に留めてこれを真空ポンプ
で機外へ排気するもの〔例えば特開昭58−26976号公
報〕が知られている。また、別の従来の技術として、吸
収液の冷媒吸収作用により吸収器内の不凝縮ガスを冷媒
蒸気と共に抽気しつつこれらを分離して不凝縮ガスを貯
室に溜めこれをパラジウム金属製のガス放出管で機外へ
排気するもの〔例えば特開昭60−71866号公報〕が知ら
れている。(B) Conventional technology As a conventional technology of this type of absorption refrigerator, the non-condensed gas in the absorber is extracted by the ejector action of the absorbing liquid injected from the pump, and is retained in the gas storage section to be vacuum pumped. There is known one that exhausts to the outside of the machine [for example, JP-A-58-26976]. Further, as another conventional technique, the non-condensable gas in the absorber is extracted together with the refrigerant vapor by the refrigerant absorbing action of the absorbing liquid, and these are separated to store the non-condensed gas in the storage chamber. There is known an exhaust pipe that exhausts the air to the outside of the machine [for example, Japanese Patent Laid-Open No. 60-71866].
(ハ)発明が解決しようとする問題点 この種の吸収冷凍機において、冷水取出し運転時での蒸
発器および吸収器内の圧力は高くてもせいぜい10mmHg程
度であるが、温水取出し運転時でのそれは200mmHg程度
まで高まることもある。このため、温水取出し運転時に
は蒸発器および吸収器の圧力で吸収液がガス貯室など不
凝縮ガス排出装置側へ必要量以上に押し出されて機内を
循環する吸収液が不足気味となり、吸収液用ポンプのキ
ャビテーションや発生器の空焚きを引起しやすい問題点
があった。また、場合によっては、吸収液が真空ポンプ
やパラジウム金属製のガス放出管にまで流れ込みこれら
を傷めるおそれもあるなど、種々の問題点があった。(C) Problems to be solved by the invention In this type of absorption refrigerator, the pressure inside the evaporator and the absorber during cold water extraction operation is at most about 10 mmHg at the highest, but during the hot water extraction operation It may increase up to about 200 mmHg. Therefore, during the hot water extraction operation, the pressure of the evaporator and the absorber pushes the absorbing liquid to the side of the non-condensable gas discharging device such as the gas storage chamber more than necessary, and the absorbing liquid circulating in the machine tends to be insufficient. There is a problem that it is easy to cause cavitation of the pump and emptying of the generator. In addition, depending on the case, there are various problems that the absorbing liquid may flow into the vacuum pump or the gas discharge pipe made of palladium metal and damage them.
本発明は、これらの問題点を確実に解消でき、温水取出
し運転を安全に続け得るこの種の吸収冷凍機の提供を目
的としたものである。The present invention aims to provide an absorption refrigerator of this type that can reliably solve these problems and can safely continue the hot water extraction operation.
(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、不凝縮
ガス排出装置の流路の途中に吸収液の流れを止める遮断
装置を備えると共にこの遮断装置を温水取出し運転時に
自動的に稼働させる駆動装置を備えてこの種の吸収冷凍
機を構成したものである。(D) Means for Solving the Problems As a means for solving the above problems, the present invention includes a blocking device for stopping the flow of the absorbing liquid in the middle of the flow path of the non-condensable gas discharging device and the blocking device. This type of absorption refrigerating machine is provided with a drive device that automatically operates during the hot water extraction operation.
(ホ)作用 本発明のこの種の吸収冷凍機は、その温水取出し運転時
に不凝縮ガス排出装置側への吸収液の流れを断つ機能
〔作用〕を発揮するので、機内の吸収液不足の発生を防
ぎ得て吸収液用ポンプのキャビテーションや発生器の空
焚きなどを防止でき、温水取出し運転を安全に続き得
る。かつまた、真空ポンプやパラジウム金属管などへの
吸収液の侵入を断ってこれらの損傷を防止できる。(E) Action This type of absorption refrigerating machine of the present invention exerts a function [action] of cutting off the flow of the absorbing liquid to the side of the non-condensable gas discharging device during the hot water take-out operation, so that a shortage of absorbing liquid in the machine occurs. It is possible to prevent the cavitation of the absorption liquid pump and the water heating of the generator, so that the hot water extraction operation can be safely continued. In addition, it is possible to prevent the absorption liquid from entering the vacuum pump, the palladium metal tube, etc., and prevent the damage.
(ヘ)実施例 図面は本発明によるこの種の吸収冷凍機の一実施例を示
した概略構成説明図である。図において、(1)は高温
発生器、(2)は低温発生器、(3)は凝縮器、(4)
は蒸発器(5)および吸収器(6)より成る蒸発吸収
器、(7)、(8)は低温、高温溶液熱交換器、(PA)
は吸収液用ポンプ、(9)は分離器であり、これらを冷
媒の流れる管(10)、(11)、冷媒液の流下する管(1
2)、稀吸収液の送られる管(13)、(14)、(15)、
(16)、揚液管(17)、中間濃度の吸収液の流れる管
(18)、(19)、濃吸収液の流れる管(20)、(21)、
冷温切換弁(VCH)付きの管(22)で接続して従来のこ
の種の吸収冷凍機〔以下、従来機という〕と同様の冷媒
〔水〕および吸収液〔臭化リチウム水溶液〕の循環路を
形成することにより、冷温切換型吸収冷凍機〔以下、本
機という〕が構成されている。(F) Embodiments The drawings are schematic configuration diagrams showing an embodiment of an absorption refrigerator of this type according to the present invention. In the figure, (1) is a high temperature generator, (2) is a low temperature generator, (3) is a condenser, and (4).
Is an evaporative absorber comprising an evaporator (5) and an absorber (6), (7) and (8) are low temperature and high temperature solution heat exchangers, (P A ).
Is a pump for absorbing liquid, (9) is a separator, and these are pipes (10), (11) through which the refrigerant flows, and pipes (1) through which the refrigerant liquid flows.
2), pipes (13), (14), (15), through which rare absorbent is sent
(16), pumping pipe (17), pipes (18), (19) where intermediate concentration absorption liquid flows, pipes (20), (21) where concentrated absorption liquid flows,
Circulation of refrigerant [water] and absorption liquid [lithium bromide aqueous solution] similar to a conventional absorption refrigerator of this type [hereinafter referred to as a conventional machine] by connecting with a pipe (22) equipped with a cold temperature switching valve (V CH ). By forming the passage, a cold / temperature switching type absorption refrigerator (hereinafter referred to as this machine) is configured.
(B)は高温発生器(1)のバーナー、(23)は低温発
生器(2)の加熱器、(24)は凝縮器(3)の冷却器、
(25)は蒸発器(5)の熱交換器であり、(26)は吸収
器(6)の冷却器である。また、(SWCH)は冷温切換ス
イッチである。(B) is a burner of the high temperature generator (1), (23) is a heater of the low temperature generator (2), (24) is a cooler of the condenser (3),
(25) is a heat exchanger of the evaporator (5), and (26) is a cooler of the absorber (6). Further, (SW CH ) is a cold / hot changeover switch.
そして、本機の冷水取出し運転時には、従来機と同様に
冷媒および吸収液の循環による吸収冷凍サイクルを生成
させ、蒸発器(5)の熱交換器(25)での冷媒の気化潜
熱で熱交換器(25)内の水を6〜8℃程度に降温させて
取出すようになっている。また、本機の温水取出し運転
時には、従来機と同様に冷却器(26)、(24)への冷却
水の供給を止める一方で冷温切換スイッチ(SWCH)によ
り冷温切換弁(VCH)を開いて高温の吸収液および冷媒
蒸気を管(22)経由で蒸発吸収器(4)へ導き、熱交換
器(25)での冷媒の凝縮潜熱〔あるいはこの熱と吸収液
の顕熱〕で熱交換器(25)内の水を昇温させて取出すよ
うになっている。Then, during the cold water take-out operation of this machine, an absorption refrigeration cycle is generated by circulating the refrigerant and the absorbing liquid as in the conventional machine, and heat is exchanged by latent heat of vaporization of the refrigerant in the heat exchanger (25) of the evaporator (5). The water in the vessel (25) is cooled to about 6-8 ° C and taken out. In addition, during the hot water extraction operation of this machine, the cooling water supply to the coolers (26) and (24) is stopped in the same way as the conventional machine, while the cold / hot switching valve (V CH ) is turned on by the cold / hot switching switch (SW CH ). Open and guide the high-temperature absorption liquid and refrigerant vapor to the evaporation absorber (4) via the pipe (22), and heat by the latent heat of condensation of the refrigerant (or this heat and the sensible heat of the absorption liquid) in the heat exchanger (25). The water in the exchanger (25) is heated and taken out.
かつまた、(29)、(27)は吸収器(6)内に配備した
抽気管、(28)は抽気用トラップ、(29)は抽気用トラ
ップ(28)へ吸収液を流下させるための管路、(30)は
管路(29)の途中に配備した吸収液用降温器、(31)は
下部に管路(29)を接続する一方で上部に蒸発吸収器
(4)への液溢流口を形成した液溜め、(32)は吸収液
用ポンプ(PA)から吐出される吸収液の一部を液溜め
(31)へ送るための管路、(33)は抽気用トラップ(2
8)で抽気した不凝縮ガスを吸収液と共にサイホン作用
により気液分離器(34)へ導く管路、(35)は気液分離
器(34)で分離した吸収液を吸収器(6)へ戻す管路、
(36)は気液分離器(34)で分離した不凝縮ガスをタン
ク(T)へ導くための管路、(37)はタンク(T)内の
ガスをパラジウム金属製の水素放出管(38)へ導くため
の管路であり、これら管路および機器により本機のガス
排出装置が従来のガス排出装置と同様に構成されてい
る。そして、(V)は管路(32)に配備した電動弁で、
この電動弁は冷温切換弁(VCH)の開動作に連動して閉
止されるよう冷温切換スイッチ(SWCH)と電気的に接続
されている。なお、(39)は管路(32)に設けたオリフ
ィスである。Moreover, (29) and (27) are bleeding pipes arranged in the absorber (6), (28) is a bleeding trap, and (29) is a pipe for flowing the absorbing liquid into the bleeding trap (28). A channel, (30) is a temperature lowering device for absorbing liquid arranged in the middle of the pipe line (29), and (31) is a pipe line (29) connected to the lower part, while the liquid overflows to the evaporation absorber (4) at the upper part. A liquid reservoir having a flow outlet, (32) is a conduit for sending a part of the absorbing liquid discharged from the absorbing liquid pump (P A ) to the liquid reservoir (31), and (33) is an extraction trap ( 2
A conduit for guiding the non-condensable gas extracted in 8) to the gas-liquid separator (34) by siphon action together with the absorbing liquid, and (35) to the absorbing liquid separated in the gas-liquid separator (34) to the absorber (6). Return conduit,
(36) is a conduit for guiding the non-condensable gas separated by the gas-liquid separator (34) to the tank (T), (37) is a hydrogen release pipe (38) made of palladium metal for the gas in the tank (T). ), And the gas discharge device of this machine is constructed in the same manner as the conventional gas discharge device by these pipes and equipment. And (V) is a motor-operated valve arranged in the pipeline (32),
This motor-operated valve is electrically connected to the cold / hot changeover switch (SW CH ) so as to be closed in conjunction with the opening operation of the cold / hot changeover valve (V CH ). In addition, (39) is an orifice provided in the conduit (32).
このようなガス排出装置を備えた本機においては、冷水
取出し運転時、冷温切換スイッチ(SWCH)により電動弁
(V)が開かれてガス排出装置内を吸収液が循環し、従
来のガス排出装置と同様に蒸発吸収器(4)内よりも抽
気用トラップ(28)の内圧が低く保たれ、これに不凝縮
ガスが抽気されつつ管路(33)経由で気液分離器(34)
へ流れ、ガスはタンク(T)に溜められる一方で吸収液
は吸収器(6)へ戻される。そして、ガスは水素放出管
(38)を通して大気中へ排出される。なお、不凝縮ガス
の大部分は水素ガスである。また、本機の冷水取出し運
転時には蒸発吸収器(4)内圧は10mmHg以下に保たれて
おり、この蒸発吸収器とタンク(T)との間の圧力差が
小さいので吸収液の液面は管路(36)内にある。このた
め、吸収液用ポンプ(PA)によりガス排出装置へ送られ
る吸収液が、従来機の場合と同様、タンク(T)に溜め
られることはなく、機内の液不足を生じることもない。In this machine equipped with such a gas discharge device, during the cold water extraction operation, the motor-operated valve (V) is opened by the cold / hot changeover switch (SW CH ) so that the absorbing liquid circulates in the gas discharge device. Like the discharge device, the internal pressure of the extraction trap (28) is kept lower than that in the evaporative absorber (4), and the non-condensable gas is extracted into this, and the gas-liquid separator (34) is passed through the pipe line (33).
Flow into the tank (T) while the absorbing liquid is returned to the absorber (6). Then, the gas is discharged into the atmosphere through the hydrogen discharge pipe (38). Most of the non-condensable gas is hydrogen gas. In addition, the internal pressure of the evaporative absorber (4) is maintained at 10 mmHg or less during the cold water extraction operation of this machine, and the pressure difference between this evaporative absorber and the tank (T) is small, so the liquid level of the absorbing liquid is Located on road (36). Therefore, the absorbing liquid sent to the gas discharge device by the absorbing liquid pump (P A ) is not stored in the tank (T) as in the case of the conventional machine, and the liquid shortage in the machine does not occur.
一方、温水取出し運転時においては、蒸発吸収器(4)
内圧は150〜200mmHgに保たれるので、管路(36)の液面
が冷水取出し運転時よりも高くなり、タンク(T)まで
達する。そして、管路(32)に弁を有しない従来機の場
合、ガス排出装置へ送られる吸収液がタンク(T)へ供
給されることになり、これをそのまま放置していると機
内の液不足を生じて吸収液用ポンプ(PA)のキャビテー
ションや高温発生器(1)の空焚きを引起すことにな
る。On the other hand, during the hot water extraction operation, the evaporative absorber (4)
Since the internal pressure is maintained at 150 to 200 mmHg, the liquid level in the pipe line (36) becomes higher than during the cold water extraction operation and reaches the tank (T). In the case of a conventional machine that does not have a valve in the pipe line (32), the absorption liquid sent to the gas discharge device is supplied to the tank (T). If this is left as it is, the liquid in the machine will be insufficient. dry frying would be cause of the resulting by absorbing liquid pump (P a) of the cavitation and high temperature generator (1).
これに対し、本機の場合、温水取出し運転の開始と同時
に冷温切換スイッチ(SWCH)により電動弁(V)が閉じ
られてガス排出装置への吸収液の供給が断たれるので、
タンク(T)への吸収液の供給も止まり、機内の液不足
の発生を確実に防止でき、運転を安全に続けることがで
きる。また、本機において、電動弁(V)を管路(29)
や管路(36)に配備しても良い。かつまた、電動弁の代
わりに、液の流れを止める遮断装置として電磁弁や逆止
弁を用いても良い。なお、本機において、管路(35)の
吸収器(6)側開口端を蒸発吸収器(4)の気相部に配
置していることを無論である。On the other hand, in the case of this machine, the motor-operated valve (V) is closed by the cold / hot changeover switch (SW CH ) at the same time as the start of the hot water extraction operation, and the supply of the absorbing liquid to the gas discharge device is cut off.
The supply of the absorbing liquid to the tank (T) is also stopped, the occurrence of liquid shortage in the machine can be reliably prevented, and the operation can be continued safely. In addition, in this machine, the electric valve (V) is connected to the pipe (29).
It may also be deployed in the pipeline (36). Moreover, instead of the motor-operated valve, a solenoid valve or a check valve may be used as a shutoff device for stopping the flow of the liquid. In this machine, it goes without saying that the absorber (6) side opening end of the pipe (35) is arranged in the vapor phase portion of the evaporation absorber (4).
また、図示していないが、本機に吸収液のエゼクタ作用
で不凝縮ガスを抽気するガス排出装置を備えた場合に
も、この装置の流路の途中に電動弁(V)などの遮断装
置を備えることにより、温水取出し運転を安全に接続で
きる。かつまた、本機においては、ガス排出装置に用い
る水素放出管(38)や真空ポンプへの液の侵入を防止で
きることも無論である。さらにまた、図示していない
が、本発明を一重効用のこの種の吸収冷凍機に適用でき
ることは勿論である。Although not shown in the figure, even when this machine is equipped with a gas discharge device for extracting the non-condensable gas by the ejector action of the absorbing liquid, a shutoff device such as an electric valve (V) is provided in the middle of the flow path of this device. With the provision of, the hot water extraction operation can be safely connected. In addition, it is needless to say that the present apparatus can prevent the liquid from entering the hydrogen discharge pipe (38) used in the gas discharge device and the vacuum pump. Furthermore, although not shown, it goes without saying that the present invention can be applied to this type of absorption refrigerator having a single effect.
(ト)発明の効果 以上のとおり、本発明によるこの種の吸収冷凍機は、蒸
発吸収器内の蒸気圧の高まる温水取出し運転時に不凝縮
ガス排出装置への吸収液の供給を自動的に断つようにし
たものであるから、装置側への多量の吸収液の流出を阻
止して機内の液不足の発生を防止でき、吸収液用ポンプ
のキャビテーションや発生器の空焚きを確実に防ぎ得る
と共に真空ポンプやパラジウム金属管などへの液の侵入
を阻止してこれらの損傷を防ぎ得、温水取出し運転を安
全に続け得るという実用的効果を発揮する。(G) Effect of the Invention As described above, the absorption refrigerator of the present invention according to the present invention automatically cuts off the supply of the absorption liquid to the non-condensable gas discharge device during the hot water extraction operation in which the vapor pressure in the evaporation absorber increases. As a result, it is possible to prevent the outflow of a large amount of absorbing liquid to the device side and prevent the occurrence of liquid shortage inside the machine, and it is possible to reliably prevent cavitation of the absorbing liquid pump and emptying of the generator. It can prevent the liquid from entering the vacuum pump, the palladium metal pipe, etc. to prevent these damages, and has a practical effect that the hot water extraction operation can be safely continued.
図面は本発明によるこの種の吸収冷凍機の一実施例を示
した概略構成説明図である。 (1)……高温発生器、(2)……低温発生器、(3)
……凝縮器、(4)……蒸発吸収器、(5)……蒸発
器、(6)……吸収器、(PA)……吸収液用ポンプ、
(28)……抽気用トラップ、(T)……タンク、(2
9)、(32)、(33)、(36)……管路、(38)……水
素放出管、(VCH)……冷温切換弁、(SWCH)……冷温
切換スイッチ、(V)……電動弁。The drawings are schematic explanatory views showing an embodiment of an absorption refrigerator of this type according to the present invention. (1) …… High temperature generator, (2) …… Low temperature generator, (3)
...... Condenser, (4) …… Evaporation absorber, (5) …… Evaporator, (6) …… Absorber, (P A ) …… Absorbing liquid pump,
(28) …… Bleed trap, (T) …… Tank, (2
9), (32), (33), (36) ... Pipe line, (38) ... Hydrogen release pipe, (V CH ) ... Cold / hot switching valve, (SW CH ) ... Cold / hot switching switch, (V ) …… Motor operated valve.
Claims (1)
器内の不凝縮ガスを抽気して機外へ排気するガス排出装
置の備えられた冷温切換型吸収冷凍機において、ガス排
出装置の流路の途中に吸収液の流れを止める遮断装置が
備えられ、かつ、この遮断装置を温かい流体の取出し運
転時に自動的に働かせる駆動装置が備えられていること
を特徴とした冷温切換型吸収冷凍機。1. A cold-temperature switching absorption refrigerating machine equipped with a gas discharge device for extracting non-condensable gas in an evaporator and the outside of the device while using an absorbing liquid in the machine, A cooling / cooling-type absorption refrigeration system characterized in that a shutoff device for stopping the flow of the absorbing liquid is provided in the middle of the flow path, and a drive device for automatically operating the shutoff device during the operation of taking out warm fluid is provided. Machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1864086A JPH0718618B2 (en) | 1986-01-30 | 1986-01-30 | Cold temperature switching absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1864086A JPH0718618B2 (en) | 1986-01-30 | 1986-01-30 | Cold temperature switching absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62175566A JPS62175566A (en) | 1987-08-01 |
| JPH0718618B2 true JPH0718618B2 (en) | 1995-03-06 |
Family
ID=11977195
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1864086A Expired - Lifetime JPH0718618B2 (en) | 1986-01-30 | 1986-01-30 | Cold temperature switching absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0718618B2 (en) |
-
1986
- 1986-01-30 JP JP1864086A patent/JPH0718618B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62175566A (en) | 1987-08-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |