JPH04295558A - Absorption refrigerator - Google Patents

Absorption refrigerator

Info

Publication number
JPH04295558A
JPH04295558A JP6036291A JP6036291A JPH04295558A JP H04295558 A JPH04295558 A JP H04295558A JP 6036291 A JP6036291 A JP 6036291A JP 6036291 A JP6036291 A JP 6036291A JP H04295558 A JPH04295558 A JP H04295558A
Authority
JP
Japan
Prior art keywords
solution
refrigerant
tank
circulation pump
regenerator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP6036291A
Other languages
Japanese (ja)
Inventor
Masayuki Fujimoto
正之 藤本
Yasuo Murata
村田 恭夫
Kiyoto Kobayashi
清人 小林
Hiroyuki Takada
浩行 高田
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
Tokyo Gas Co Ltd
Original Assignee
Sanyo Electric Co Ltd
Tokyo Gas 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, Tokyo Gas Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP6036291A priority Critical patent/JPH04295558A/en
Publication of JPH04295558A publication Critical patent/JPH04295558A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To provide an absorption refrigerator of a small capacity for domestic use or the like in which even dilution can obtained. CONSTITUTION:A refrigerant tank 7 ranging with a vaporizer 6, a regenerator 1 and float sensors 15 and 25 are provided, and a solution tank 18 is connected to the refrigerant tank 7 through a refrigerant circulation pump 16 and a main dilution valve 17. In addition, in a piping between the solution tank 18 and a solution heat exchanger 13, a solution circulation pump 20, a diluted solution valve 21 and a subsidiary dilution valve 22 are provided. The subsidiary dilution valve 22, the solution circulation pump 20, the refrigerant circulation pump 16, the main dilution valve 17, the float sensors 15 and 25 and an outdoor temperature sensor 23 are all communicated with a controller 24 so as to obtain a correct dilution.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】この発明は家庭用若しくはその近
辺の小容量の吸収式冷凍機に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a small-capacity absorption refrigerating machine for domestic or nearby use.

【0002】0002

【従来の技術】従来用いられている吸収器,再生器,凝
縮器,蒸発器からなる10冷凍トン相当の吸収式冷凍機
にあっては、停止後、一定時間溶液循環ポンプ,冷媒循
環ポンプを継続運転して吸収器での冷媒蒸気吸収による
濃度低下と濃溶液と稀溶液の混合攪拌により稀釈してい
る場合が多い。
[Prior Art] In a conventionally used absorption refrigerating machine consisting of an absorber, a regenerator, a condenser, and an evaporator, which is equivalent to 10 refrigeration tons, the solution circulation pump and refrigerant circulation pump are operated for a certain period of time after stopping. In many cases, the solution is diluted by continuing operation, reducing the concentration by absorbing refrigerant vapor in the absorber, and mixing and stirring a concentrated solution and a dilute solution.

【0003】0003

【発明が解決しようとする課題】しかし、この場合濃液
側の流れは残存する圧力差に依存しているが、小容量の
吸収式冷凍機では熱容量も小さいため、停止操作でガス
燃焼を止めると再生器の圧力はすぐ低下し、残存しにく
い。このため、十分な稀釈を期待できないうえ、稀釈後
の濃度もばらつく欠点をもっている。なお、従来の異常
運転防止手段として、運転中に蒸発器,吸収器,再生器
の液面検出器の信号により結晶が発生しやすい状況にな
った場合、冷媒或いは稀溶液を濃溶液系統内に導入して
結晶を誘発しない状況にするものも知られている(特公
昭43ー17338号参照)。
[Problem to be solved by the invention] However, in this case, the flow on the concentrated liquid side depends on the residual pressure difference, but in a small-capacity absorption refrigerator, the heat capacity is also small, so gas combustion is stopped by the shutdown operation. The pressure in the regenerator will drop quickly and it will be difficult for it to remain. For this reason, sufficient dilution cannot be expected, and the concentration after dilution also varies. In addition, as a conventional means of preventing abnormal operation, if the signal from the liquid level detector of the evaporator, absorber, or regenerator indicates that crystals are likely to occur during operation, the refrigerant or dilute solution is injected into the concentrated solution system. It is also known that a substance can be introduced to create a situation in which crystallization is not induced (see Japanese Patent Publication No. 17338-1973).

【0004】本発明は上記実情に鑑み、停止中に溶液が
結晶しないように、冷媒タンクの所定の冷媒液面まで冷
媒を吸収液中に放出し稀釈後の濃度を一定値とし、停止
後一定時間は従来と同じ方法にて混合攪拌により稀釈し
、更に所定時間は再生器,溶液熱交換器内で稀釈すると
共に、全吸収液がほぼ均一濃度になるよう攪拌すること
で、前記課題を解決する吸収式冷凍機を提供することを
目的としたものである。
In view of the above circumstances, the present invention has been developed by discharging the refrigerant into the absorption liquid up to a predetermined level of the refrigerant in the refrigerant tank so that the solution does not crystallize during the stoppage, and keeping the concentration after dilution at a constant value. The above problem is solved by diluting the liquid by mixing and stirring in the same way as before, and then diluting it in the regenerator and solution heat exchanger for a predetermined period of time, and stirring so that the entire absorption liquid has a nearly uniform concentration. The purpose of this invention is to provide an absorption refrigerator that

【0005】[0005]

【課題を解決するための手段】本発明は、吸収器と再生
器と凝縮器と蒸発器とから成る吸収式冷凍機において、
吸収器から導出された稀溶液を貯溜する溶液タンクと、
蒸発器内の冷媒を貯溜する冷媒タンクとを有し、この冷
媒タンクから溶液タンクに至る稀釈管路には冷媒循環ポ
ンプと主稀釈弁とを設け、前記溶液タンクから再生器に
至る稀溶液管路には溶液ポンプを設け、再生器から溶液
タンクに至る濃溶液管路には副稀釈弁を設け、冷房運転
の停止中に冷媒タンクと再生器内の液面の高さと外気温
度に応じて冷媒循環ポンプと主稀釈弁と溶液ポンプと副
稀釈弁とを作動させるための制御器とを備えたものであ
る。
[Means for Solving the Problems] The present invention provides an absorption refrigerator comprising an absorber, a regenerator, a condenser, and an evaporator.
a solution tank that stores the dilute solution derived from the absorber;
It has a refrigerant tank that stores the refrigerant in the evaporator, and a dilution pipe line from the refrigerant tank to the solution tank is provided with a refrigerant circulation pump and a main dilution valve, and a dilution pipe line from the solution tank to the regenerator is provided. A solution pump is installed in the condensed solution line from the regenerator to the solution tank, and an auxiliary dilution valve is installed in the concentrated solution conduit from the regenerator to the solution tank. It is equipped with a controller for operating a refrigerant circulation pump, a main dilution valve, a solution pump, and a sub-dilution valve.

【0006】[0006]

【作用】上記のような構成のため、運転終了にて運転停
止信号が入ると、冷媒タンクの液面が所定値a以上であ
れば(通常はa以上)、冷媒循環ポンプは運転を継続し
主稀液弁が開となり、冷媒は溶液タンクに送られ稀釈す
る。また、冷媒タンクの液面がa以下になると冷媒循環
ポンプは停止し、主稀釈弁が閉となる。一方、吸収液側
では停止後S1 分間は燃焼装置のみ停止し、溶液循環
ポンプ及び他はそのまま運転を継続する。溶液タンクで
稀薄になった液は溶液循環ポンプにより送られて溶液熱
交換器,再生器,溶液熱交換器,吸収器,溶液タンク内
を順次稀釈する。但し、この間、再生器フロートセンサ
ーがHi信号の時に稀溶液弁を閉とし、Lo信号の時は
開として流量を制御する。この溶液循環ポンプはHi運
転を継続する。
[Operation] Due to the above configuration, when the operation stop signal is input at the end of operation, the refrigerant circulation pump continues operation if the liquid level in the refrigerant tank is above a predetermined value a (usually above a). The main dilute valve is opened and the refrigerant is sent to the solution tank and diluted. Furthermore, when the liquid level in the refrigerant tank falls below a, the refrigerant circulation pump stops and the main dilution valve closes. On the other hand, on the absorption liquid side, only the combustion device is stopped for S1 minutes after the stop, and the solution circulation pump and others continue to operate. The diluted solution in the solution tank is sent by a solution circulation pump and is sequentially diluted in the solution heat exchanger, regenerator, solution heat exchanger, absorber, and solution tank. However, during this time, the dilute solution valve is closed when the regenerator float sensor is a Hi signal, and opened when it is a Lo signal to control the flow rate. This solution circulation pump continues Hi operation.

【0007】停止後S1 〜S2 分間は副稀釈弁を開
とする。吸収液は溶液循環ポンプにより溶液タンク,溶
液熱交換器,再生器,溶液熱交換器,副稀釈弁,溶液タ
ンクと循環し、更に濃度の均一化をなし稀釈する。S2
 分後は副稀釈弁は開状態になるため再生器,溶液熱交
換器,配管中の吸収液は全て溶液タンクの内に落とし込
む。冷房シーズン以外の時期の稀釈(例えば冬期)、冷
房シーズンの稀釈は外気温度が高いため結晶しづらいこ
と、次回冷房運転の起動を早くすることなどのため比較
的高い濃度であるが、結晶を起こさない程度しか稀釈を
実施しない。即ち、この濃度のままで冬期になると結晶
を起こすため、冬期に近づくと外気温度により自動的に
更に稀釈を実施する。
[0007] The sub-dilution valve is kept open for S1 to S2 minutes after stopping. The absorption liquid is circulated through a solution tank, a solution heat exchanger, a regenerator, a solution heat exchanger, an auxiliary dilution valve, and a solution tank by a solution circulation pump to further equalize the concentration and dilute it. S2
After a few minutes, the sub-dilution valve will be open, so all the absorbent in the regenerator, solution heat exchanger, and piping will fall into the solution tank. Dilutions made during times other than the cooling season (for example, winter) and dilutions made during the cooling season have relatively high concentrations because the outside air temperature is high, making it difficult to crystallize, and to start the cooling operation sooner the next time. Perform dilution only to the extent that That is, since crystals will occur in winter if the concentration remains unchanged, further dilution is automatically performed as winter approaches, depending on the outside temperature.

【0008】この場合、外気温度センサーにより外気温
度t℃を感知すると冷媒循環ポンプが運転し主稀釈弁を
開として冷媒液面lになるまで冷媒を溶液タンク内に放
出稀釈する。一方、吸収液側は溶液循環ポンプがHi運
転し副稀釈弁を開のまま上述と同様濃度均一化のためS
3 分間運転して停止する。一度この操作を行うと記憶
されて二度と実施しない。
In this case, when the outside air temperature t° C. is detected by the outside air temperature sensor, the refrigerant circulation pump is operated, the main dilution valve is opened, and the refrigerant is discharged and diluted into the solution tank until the refrigerant liquid level reaches l. On the other hand, on the absorption liquid side, the solution circulation pump is operated in Hi mode and the sub-dilution valve is left open to make the concentration uniform as described above.
Run for 3 minutes and then stop. Once you perform this operation, it will be remembered and you will never perform it again.

【0009】[0009]

【実施例】以下、本発明を実施例の図面に基づい説明す
れば、次の通りである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be explained below based on drawings of embodiments.

【0010】図1は家庭用などの小容量の水−リチウム
塩系吸収式冷凍機で、吸収器,凝縮器は空気又は水空冷
方式の構造をもつ冷凍サイクル系統図を示し、1はバー
ナー等の燃焼装置2を下部に配設した濃溶液と冷媒蒸気
を発生させる再生器で,該再生器1には冷媒蒸気を冷媒
液とする凝縮器3を配管4にて連設し、該凝縮器3の下
部に取付けた配管5の先端を蒸発器6の下部に有する冷
媒タンク7に接続すると共に、蒸発器6には配管8をも
って吸収器9を連設する。一方、前記再生器1で生じた
濃溶液を導く濃溶液配管10は並列配置した濃溶液弁1
1とオリフィス12を介して溶液熱交換器13に接続し
、該溶液熱交換器13から前記吸収器9へは濃溶液分配
装置14をもって接続する。15は前記冷媒タンク7に
設けた冷媒フロートセンサーで、液面a>h>lを検知
する。冷媒循環系統には冷媒循環ポンプ16と主稀釈弁
17を介して前記吸収器9からの稀溶液を導く稀溶液溜
りとなる溶液タンク18に接続し、該溶液タンク18よ
り接続の稀溶液配管19は溶液循環ポンプ20と稀溶液
弁21と前記溶液熱交換器13を経て再生器1に戻る配
管としている。22は溶液熱交換器13と溶液タンク1
8間の配管に設けた副稀釈弁であり、該副稀釈弁22と
前記冷媒フロートセンサー15と冷媒循環ポンプ16と
主稀釈弁17と溶液循環ポンプ20及び凝縮器3に臨む
配管4に取付けた外気温度センサー23を制御器24に
夫々連絡し、全体として吸収式冷凍機となる。25は再
生器1の側部に設けた再生器フロートセンサーである。
FIG. 1 shows a refrigeration cycle system diagram of a small-capacity water-lithium salt absorption refrigerating machine for household use, in which the absorber and condenser are air-cooled or water-cooled. This is a regenerator that generates a concentrated solution and refrigerant vapor, with a combustion device 2 disposed at the bottom thereof, and a condenser 3 that uses refrigerant vapor as a refrigerant liquid is connected to the regenerator 1 via a pipe 4. The tip of a pipe 5 attached to the lower part of the evaporator 3 is connected to a refrigerant tank 7 provided at the lower part of the evaporator 6, and an absorber 9 is connected to the evaporator 6 through a pipe 8. On the other hand, a concentrated solution pipe 10 that guides the concentrated solution generated in the regenerator 1 has a concentrated solution valve 1 arranged in parallel.
1 and an orifice 12 to a solution heat exchanger 13, and the solution heat exchanger 13 is connected to the absorber 9 through a concentrated solution distribution device 14. 15 is a refrigerant float sensor provided in the refrigerant tank 7, which detects the liquid level a>h>l. The refrigerant circulation system includes a refrigerant circulation pump 16 and a main dilution valve 17 connected to a solution tank 18 serving as a dilute solution reservoir for guiding the dilute solution from the absorber 9, and a dilute solution piping 19 connected from the solution tank 18. The piping returns to the regenerator 1 via the solution circulation pump 20, the dilute solution valve 21, and the solution heat exchanger 13. 22 is a solution heat exchanger 13 and a solution tank 1
This is a sub-dilution valve installed in the pipe between the sub-dilution valve 22, the refrigerant float sensor 15, the refrigerant circulation pump 16, the main dilution valve 17, the solution circulation pump 20, and the pipe 4 facing the condenser 3. The outside air temperature sensors 23 are connected to a controller 24, and the whole becomes an absorption refrigerator. 25 is a regenerator float sensor provided on the side of the regenerator 1.

【0011】次にこの作用を説明すると、先ず再生器1
にて冷媒を吸収して稀薄になった稀溶液は燃焼装置2に
より加熱されて沸騰し濃溶液と冷媒蒸気を生ずる。この
濃溶液は濃溶液配管10と同配管中に並列に配置した濃
溶液弁11とオリフィス12を通って溶液熱交換器13
に入る。更に、濃溶液配管10を通って濃溶液分配装置
14により吸収器9の伝熱管内に分配される。吸収器9
内で濃溶液は蒸発器6で蒸発し、配管8を通って導入さ
れた冷媒蒸気を吸収し、稀溶液となって配管26を通っ
て稀溶液溜りである溶液タンク18に入る。稀溶液は稀
溶液配管19とその途中に設置された溶液循環ポンプ2
0,稀溶液弁21,溶液熱交換器13を通って再び再生
器1に戻る。
Next, to explain this effect, first, the regenerator 1
The diluted solution absorbed the refrigerant in the combustion device 2 is heated and boiled to produce a concentrated solution and refrigerant vapor. This concentrated solution passes through the concentrated solution piping 10 and the concentrated solution valve 11 and orifice 12 arranged in parallel in the same piping to the solution heat exchanger 13.
to go into. Further, the concentrated solution is distributed through the concentrated solution pipe 10 into the heat exchanger tube of the absorber 9 by the concentrated solution distribution device 14 . Absorber 9
The concentrated solution is evaporated in the evaporator 6, absorbs the refrigerant vapor introduced through the pipe 8, becomes a dilute solution, and enters the solution tank 18, which is a dilute solution reservoir, through the pipe 26. The dilute solution is passed through the dilute solution piping 19 and the solution circulation pump 2 installed in the middle.
0, passes through the dilute solution valve 21 and solution heat exchanger 13 and returns to the regenerator 1 again.

【0012】一方、冷媒は再生器1で蒸発し、配管4を
通って凝縮器3にて冷却され液化して冷媒液となる。こ
の冷媒液は配管5により冷媒液溜りである冷媒タンク7
に入る。冷媒タンク7内の冷媒液は配管27を通って冷
媒循環ポンプ16より冷媒分散装置28から蒸発器6の
伝熱管上に分散される。冷媒液はこの伝熱管上で蒸発し
て冷水入口管29より入ってくる冷水を冷やし冷水出口
管30より送り出す。この冷水を室内の冷房に用いる。 蒸発した冷媒蒸気は配管8を通って吸収器9に入り、吸
収される。
On the other hand, the refrigerant is evaporated in the regenerator 1, passes through the pipe 4, is cooled in the condenser 3, and is liquefied to become a refrigerant liquid. This refrigerant liquid is transferred through a pipe 5 to a refrigerant tank 7 which is a refrigerant liquid reservoir.
to go into. The refrigerant liquid in the refrigerant tank 7 passes through the pipe 27 and is dispersed onto the heat transfer tubes of the evaporator 6 from the refrigerant distribution device 28 by the refrigerant circulation pump 16 . The refrigerant liquid evaporates on this heat transfer tube, cools the cold water coming in from the cold water inlet pipe 29, and sends it out from the cold water outlet pipe 30. This cold water is used for indoor air conditioning. The evaporated refrigerant vapor enters the absorber 9 through the pipe 8 and is absorbed.

【0013】吸収器9と凝縮器3の冷却は空冷若しくは
水空冷方式にて行う。冷却ファン31により吸収器9,
凝縮器3を冷却する。また、水空冷方式の場合は、冷却
タンク32内の冷却水を冷却水ポンプ33により冷却水
配管34を通って冷却水散布装置35から吸収器9或い
は凝縮器3に散布し冷却を行う。
The absorber 9 and condenser 3 are cooled by air cooling or water/air cooling. The absorber 9,
Cool the condenser 3. In the case of a water-air cooling system, the cooling water in the cooling tank 32 is sprayed by the cooling water pump 33 through the cooling water piping 34 from the cooling water distribution device 35 to the absorber 9 or the condenser 3 for cooling.

【0014】この場合、■冷房シーズンの停止稀釈は、
冷媒タンク75にあって液面aまで冷媒循環ポンプ16
を運転し主稀釈弁17を開として稀釈する(溶液は平均
57%まで稀釈)。濃度が下がり過ぎないようにして次
の冷房運転の起動を早くする。但し、液面位aは冷房シ
ーズン稀釈停止位置、液面位hは冷媒循環ポンプ運転開
始液面、液面位lは冷媒循環ポンプ停止液面を示す。
[0014] In this case, ■ Stop dilution in the cooling season is
The refrigerant circulation pump 16 in the refrigerant tank 75 reaches the liquid level a.
The main dilution valve 17 is opened to dilute the solution (the solution is diluted to an average of 57%). To prevent the concentration from dropping too much and start the next cooling operation quickly. However, the liquid level a indicates the cooling season dilution stop position, the liquid level h indicates the liquid level at which the refrigerant circulation pump starts operating, and the liquid level l indicates the liquid level at which the refrigerant circulation pump stops.

【0015】冷房シーズン以外の時期では、■冷房シー
ズン時に停止したままなので(濃度57%)、更に自動
稀釈する。外気温度がt℃(例えば5℃)に低下した時
、液面lまで冷媒循環ポンプ16を運転し主稀釈弁17
を開として稀釈する。
[0015] In times other than the cooling season, (1) Since it remains stopped during the cooling season (concentration 57%), it is further automatically diluted. When the outside air temperature drops to t°C (for example, 5°C), the refrigerant circulation pump 16 is operated until the liquid level l and the main dilution valve 17 is opened.
Dilute as diluted.

【0016】■停電時の停止なども含めて全ての停止後
は各配管,経路中の稀溶液,濃溶液を全て溶液タンク1
8内に自然落下にて戻す。 ■停止の場合の制御(冷房シーズン) 冷媒液面〜aまで冷媒循環ポンプ16を運転し、主稀釈
弁17を開く。停止後S1 分間は溶液循環ポンプ20
をHi運転し、再生器フロートセンサー25がHi信号
を発した時は稀溶液弁21を閉じ、再生器フロートセン
サー25がLo信号を発した時は稀溶液弁21を開く。 停止後S1 〜S2 分間、再生器フロートセンサー2
5がHi信号を発した時は溶液循環ポンプ20をLo運
転し、再生器フロートセンサー25がLo信号を発した
時は溶液循環ポンプ20をHi運転し、副稀釈弁22と
稀溶液弁21が開き、停止後S2 分間を経て停止する
■After all stops, including stops due to power outages, drain all the dilute and concentrated solutions in each pipe and route into the solution tank 1.
Return by natural fall within 8. ■Control in case of stoppage (cooling season) The refrigerant circulation pump 16 is operated until the refrigerant liquid level ~a, and the main dilution valve 17 is opened. Solution circulation pump 20 for S1 minute after stopping
When the regenerator float sensor 25 issues a Hi signal, the dilute solution valve 21 is closed, and when the regenerator float sensor 25 issues a Lo signal, the dilute solution valve 21 is opened. For S1 to S2 minutes after stopping, regenerator float sensor 2
When the regenerator float sensor 25 issues a Hi signal, the solution circulation pump 20 is operated at Lo, and when the regenerator float sensor 25 issues a Lo signal, the solution circulation pump 20 is operated at Hi. It opens and stops after S2 minutes.

【0017】[0017]

【発明の効果】上記のように、本発明の吸収式冷凍機で
は冷房運転の停止中に冷媒タンクと再生器内の液面の高
さと外気温度に応じて冷媒循環ポンプと主稀釈弁と溶液
ポンプと副稀釈弁とを作動させるようにしたので、稀釈
後の濃度にバラツキがなく稀釈時間を短縮できると共に
過度の稀釈が避けられ、全体的な効率向上を図ることが
できる。
Effects of the Invention As described above, in the absorption chiller of the present invention, the refrigerant circulation pump, the main dilution valve, and the liquid Since the pump and the sub-dilution valve are operated, there is no variation in the concentration after dilution, the dilution time can be shortened, excessive dilution can be avoided, and the overall efficiency can be improved.

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

【図1】本発明の実施例を示す概略図。FIG. 1 is a schematic diagram showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1    再生器 3    凝縮器 6    蒸発器 7    冷媒タンク 9    吸収器 13    溶液熱交換器 15    冷媒フロートセンサー 16    冷媒循環ポンプ 17    主稀釈弁 18    溶液タンク 19    稀溶液配管 20    溶液循環ポンプ 21    稀溶液弁 22    副稀釈弁 23    外気温度センサー 25    再生器フロートセンサー 1 Regenerator 3. Condenser 6 Evaporator 7 Refrigerant tank 9 Absorber 13 Solution heat exchanger 15 Refrigerant float sensor 16 Refrigerant circulation pump 17 Main dilution valve 18 Solution tank 19 Dilute solution piping 20 Solution circulation pump 21 Dilute solution valve 22 Sub-dilution valve 23 Outside temperature sensor 25 Regenerator float sensor

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  吸収器と再生器と凝縮器と蒸発器とか
ら成る吸収式冷凍機において、吸収器から導出された稀
溶液を貯溜する溶液タンクと、蒸発器内の冷媒を貯溜す
る冷媒タンクとを有し、この冷媒タンクから溶液タンク
に至る稀釈管路には冷媒循環ポンプと主稀釈弁とを設け
、前記溶液タンクから再生器に至る稀溶液管路には溶液
ポンプを設け、再生器から溶液タンクに至る濃溶液管路
には副稀釈弁を設け、冷房運転の停止中に冷媒タンクと
再生器内の液面の高さと外気温度に応じて冷媒循環ポン
プと主稀釈弁と溶液ポンプと副稀釈弁とを作動させるた
めの制御器とを備えたことを特徴とする吸収式冷凍機。
Claim 1: An absorption refrigerator comprising an absorber, a regenerator, a condenser, and an evaporator, comprising: a solution tank for storing a dilute solution derived from the absorber; and a refrigerant tank for storing refrigerant in the evaporator. A dilution pipe line from the refrigerant tank to the solution tank is provided with a refrigerant circulation pump and a main dilution valve, a solution pump is provided in the dilute solution pipe line from the solution tank to the regenerator, and a regenerator A sub-dilution valve is installed in the concentrated solution pipeline leading from to the solution tank, and when cooling operation is stopped, the refrigerant circulation pump, main dilution valve, and solution pump are activated depending on the height of the liquid level in the refrigerant tank and regenerator and the outside air temperature. and a controller for operating the auxiliary dilution valve.
JP6036291A 1991-03-25 1991-03-25 Absorption refrigerator Pending JPH04295558A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6036291A JPH04295558A (en) 1991-03-25 1991-03-25 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6036291A JPH04295558A (en) 1991-03-25 1991-03-25 Absorption refrigerator

Publications (1)

Publication Number Publication Date
JPH04295558A true JPH04295558A (en) 1992-10-20

Family

ID=13139958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6036291A Pending JPH04295558A (en) 1991-03-25 1991-03-25 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JPH04295558A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07133967A (en) * 1993-11-09 1995-05-23 Tokyo Gas Co Ltd Air conditioner using absorption freezer
JPH0828998A (en) * 1994-07-15 1996-02-02 Rinnai Corp Absorption type air conditioner

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07133967A (en) * 1993-11-09 1995-05-23 Tokyo Gas Co Ltd Air conditioner using absorption freezer
JPH0828998A (en) * 1994-07-15 1996-02-02 Rinnai Corp Absorption type air conditioner

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