JPS62166272A - Double-effect absorption refrigerator - Google Patents

Double-effect absorption refrigerator

Info

Publication number
JPS62166272A
JPS62166272A JP61006254A JP625486A JPS62166272A JP S62166272 A JPS62166272 A JP S62166272A JP 61006254 A JP61006254 A JP 61006254A JP 625486 A JP625486 A JP 625486A JP S62166272 A JPS62166272 A JP S62166272A
Authority
JP
Japan
Prior art keywords
detector
temperature
cooling water
solution
generator
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.)
Granted
Application number
JP61006254A
Other languages
Japanese (ja)
Other versions
JPH0478903B2 (en
Inventor
隆 青山
正和 藤本
孝 安田
修行 井上
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP61006254A priority Critical patent/JPS62166272A/en
Priority to KR1019870000317A priority patent/KR960002565B1/en
Publication of JPS62166272A publication Critical patent/JPS62166272A/en
Publication of JPH0478903B2 publication Critical patent/JPH0478903B2/ja
Granted 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
    • F25B15/00Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、運転停止時の操作を行なう制御装置を有する
二重効用吸収冷凍機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a dual-effect absorption refrigerator having a control device for operating during shutdown.

〔従来の技術〕[Conventional technology]

従来の吸収冷凍機においては、運転停止時に、溶液の結
晶化を防止するために、発生器加熱源の制御弁を閉じて
冷凍機の運転を停止した後も溶液ポンプは運転を続け、
溶液径路中のン農度を均一化する希釈運転を行なった後
溶液ポンプを停止しているのであるが、冷却水ポンプも
溶液ポンプと共に運転を続け、溶液ポンプの停止と共に
停止するようになっていた。
In conventional absorption refrigerators, in order to prevent solution crystallization when the operation is stopped, the solution pump continues to operate even after the control valve of the generator heating source is closed and the refrigerator operation is stopped.
The solution pump is stopped after performing dilution operation to equalize the concentration in the solution path, but the cooling water pump also continues to operate along with the solution pump, and stops when the solution pump stops. Ta.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところが、通常は溶液ポンプの出力(例えば1〜2 V
)に比べ冷却水ポンプの出力は大きく (例えば6〜1
0kW)、冷却水ポンプを必要以上に運転するために動
力の損失を招いた。
However, usually the output of the solution pump (for example, 1 to 2 V
), the output of the cooling water pump is larger (e.g. 6 to 1
0kW), causing a loss of power because the cooling water pump was operated more than necessary.

また、冷却水の通水を必要以上に行なうと、高温発生器
の内圧が低下して溶液の循環が行なわれに(くなり、濃
度の均一化が十分なされず結晶を招くおそれがあった。
Furthermore, if the cooling water is passed more than necessary, the internal pressure of the high temperature generator will drop and the solution will not be circulated, which may prevent the concentration from being sufficiently uniform and may lead to crystallization.

このような支障を避けるために、冷凍機の停止時に冷却
水ポンプを直ちに停止すると冷却されない高温のままの
スプレー?B液が降りかかり、冷却水チューブ内の冷却
水の温度が上がり、チューブの熱膨張に基づ(過大応力
によりチューブが#員傷したり、再起動の際に、冷却塔
内のプラスチックの充填材を損傷する、という支障を招
いた。
In order to avoid such problems, if you stop the cooling water pump immediately when the refrigerator stops, the spray remains at a high temperature and is not cooled down. Liquid B falls on the cooling water tube, and the temperature of the cooling water in the cooling water tube rises, and due to thermal expansion of the tube (the tube may be damaged due to excessive stress, or the plastic filling material in the cooling tower may be damaged during restart). This caused problems such as damage to the

本発明は従来のものの上記の如き問題点を解決し、動力
の損失を軽減し、溶液の希釈を促進し、熱応力によるチ
ューブの損傷を防ぎ、かつ再起動時に冷却塔内の充填材
を損傷することのない二重効用吸収冷凍機を提供するこ
とを目的とするものである。
The present invention solves the above-mentioned problems of the conventional ones, reduces power loss, promotes solution dilution, prevents damage to tubes due to thermal stress, and damages packing material in cooling tower during restart. The purpose of this invention is to provide a dual-effect absorption refrigerating machine that does not

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上記の問題点を解決するための手段として 
芸発器、吸収器、高温発生器、低温発生器、凝縮器、こ
れらの機器を接続する78液経路、冷媒経路、これらの
経路に設けられた溶液ポンプ、冷媒ポンプ、前記吸収器
及び凝縮器に通している冷却水経路、該冷却水経路に設
けられた冷却水ポンプ、前記蒸発器に通じている冷水径
路、該冷水経路に設けられた冷水ポンプを備えている二
重効用吸収冷凍機において、 運転停止前の負荷状態を検出する負荷検出器と、運転停
止後所定の設定時間後に前記冷却水ポンプの運転を停止
せしめる信号を発する時限機構と、前記負荷検出器によ
って検出された運転停止前の負荷状態に応じて前記所定
の設定時間を選択する制御機構とを備えたことを特徴と
する二重効用吸収冷凍機を提供せんとするものである。
The present invention is a means for solving the above problems.
generator, absorber, high temperature generator, low temperature generator, condenser, 78 liquid paths connecting these devices, refrigerant path, solution pumps provided in these paths, refrigerant pump, the absorber and condenser In a dual-effect absorption chiller comprising a cooling water path leading to the evaporator, a cooling water pump provided in the cooling water path, a cold water path leading to the evaporator, and a cold water pump provided in the cold water path. , a load detector that detects the load state before the operation is stopped; a timer mechanism that issues a signal to stop the operation of the cooling water pump after a predetermined set time after the operation is stopped; It is an object of the present invention to provide a dual-effect absorption refrigerating machine characterized by comprising a control mechanism that selects the predetermined set time according to a load state of the refrigerating machine.

〔作 用〕[For production]

本発明により、吸収冷凍機停止時に、冷却水ポンプを直
ちに停止するのではなく、停止前の負荷状態に応じてし
ばらく運転を続行せしめることにより、冷却水の循環が
引続き行なわれる。溶液ポンプは希釈運転のため引続き
運転され、溶液の循環が行なわれているが、発生器での
加熱は既に停止されているので冷却水により冷却されて
溶液温度は次第に低下し、冷却水温度も次第に低下する
According to the present invention, when the absorption refrigerating machine is stopped, the cooling water pump is not immediately stopped, but is allowed to continue operating for a while depending on the load condition before stopping, thereby continuing to circulate the cooling water. The solution pump continues to operate for dilution, and the solution is circulated, but since heating in the generator has already been stopped, it is cooled by the cooling water, and the solution temperature gradually decreases, and the cooling water temperature also decreases. It gradually decreases.

冷却塔に用いられる充填材には、例えば硬質塩化ビニー
ル(PVC)などが用いられ、それらの実用的な耐熱限
度はおよそ60〜80℃程度であ従って、冷凍機の運転
停止後、冷却水の温度が次第に低下し、冷却水の通水を
止めて停留状態となる冷却水チューブ内の冷却水が、比
較的高温の?8液(既に成る程度温度降下している)が
降りかかっても上記の耐熱限度に到達しない程度(例え
ば25〜30゛c)以下になったときに冷却水ポンプを
停止すればよいが、この冷却水温度の低下状態は、停止
時点或いはその直前の負荷の状態に関係する。
The filling material used in cooling towers is, for example, hard vinyl chloride (PVC), and the practical heat resistance limit of these materials is approximately 60 to 80°C. Is the cooling water in the cooling water tube at a relatively high temperature as the temperature gradually decreases and the cooling water stops flowing and becomes stagnant? The cooling water pump can be stopped when the temperature drops to a level below (e.g. 25-30°C) that does not reach the above heat resistance limit even if the liquid 8 (the temperature has already dropped to a certain degree) falls on it. The state of decrease in cooling water temperature is related to the state of the load at or just before the stop.

即ち、停止時点において高負荷で運転している場合には
、発生器内の圧力が高(、溶液温度も高く、従って吸収
器への戻り78液の温度も高くなり、j1転停止後の冷
却水の温度低下の速度も遅くなる。
That is, if the operation is under high load at the time of stopping, the pressure inside the generator will be high (and the solution temperature will also be high, so the temperature of the liquid 78 returning to the absorber will also be high, and the cooling after stopping the J1 rotation will be high). The rate at which the water temperature drops also slows down.

そのため、冷凍機の運転停止後、冷却水温度が所定の許
容温度にまで低下するのに要する時間は、高負荷運転後
の場合は長く、低負荷運転後の場合は短かい。
Therefore, the time required for the cooling water temperature to drop to a predetermined allowable temperature after the refrigerator stops operating is long after high-load operation, and short after low-load operation.

運転停止時点又はその直前(直前の時点或いは停止時の
10分子7度萌から停止時までの平均)の負荷状態を溶
液の温度などにより検出し、一方、運転停止時から所定
の設定時間後に冷却水ポンプを停止せしめる時限機構を
設け、この時限機構の設定時間を予め検出した負荷状態
に応じて選択し、冷却水温度が所定の許容温度以下とな
るべき時点以降に冷却水ポンプを停止せしめるようにす
る。
The load condition at the time of stopping operation or just before that (the average from the time immediately before or the time of stopping 10 molecules at 7 degrees until stopping) is detected by the temperature of the solution, etc., and on the other hand, cooling is performed after a predetermined set time from the time of stopping operation. A time limit mechanism is provided to stop the water pump, and the set time of this time limit mechanism is selected according to the pre-detected load condition, and the coolant pump is stopped after the point when the coolant temperature should fall below a predetermined allowable temperature. Make it.

本発明では、このように時限機構の設定時間を停止時点
或いはそれ以前の負荷状態に応じて選択して冷却水ポン
プを停止するようにしたことにより、冷却水の通水停止
後比較的高温(既に成る程度温度降下している)の溶液
が降りかかっても、チューブ内に停留して(・る冷却水
が前記の限度の60〜80℃に達することはなく、チュ
ーブの熱膨張による損傷も防ぎ、その後冷凍機を再起動
しても、冷却塔には十分低温となった冷却水が送られる
ので充填材を損傷することがない。しかも冷却水ポンプ
を必要以上に長く運転して動力の損失を招いたり、高温
発生器内圧力を低下させ過ぎて希釈運転に支障を来すこ
ともない。
In the present invention, the cooling water pump is stopped by selecting the set time of the timer mechanism according to the load condition at or before the stop time, so that the relatively high temperature ( Even if the solution (which has already cooled down to a certain degree) falls on the solution, it will remain in the tube and the cooling water will not reach the above-mentioned limit of 60-80℃, and the tube will not be damaged due to thermal expansion. Even if the chiller is restarted after the chiller is restarted, the cooling water will be sent to the cooling tower at a sufficiently low temperature and will not damage the filling material. It does not cause loss or reduce the pressure inside the high-temperature generator too much, thereby hindering the dilution operation.

なお、負荷状態を検出する負荷検出器として、溶液の温
度を検出する温度検出器を用いる場合には、溶液経路中
のなるべく高温、高圧の部分(低温発生器GLの圧力程
度以上の部分、例えば裔温発生器GH内、高温発生器G
H出口など)における温度を検出するのが好ましい。そ
のほか負荷検出器としては、高温発生器GHの加熱量を
検出するものとして加熱源流体(薄黒、熱水或いは直火
式の場合の燃料ガス、燃料油)の流量検出器、又は流量
制御弁の開度検出器を用いてもよい。さらに、負荷検出
器としては、高温発生器GH内の圧力又は飽和温度を検
出する圧力検出器、温度検出器を用いてもよい。また、
以上の温度、圧力に関連している冷却水温度を検出する
温度検出器を用いてもよい。
In addition, when using a temperature detector that detects the temperature of the solution as a load detector that detects the load state, it is necessary to use a temperature sensor that detects the temperature of the solution as much as possible at a high temperature and high pressure part (a part where the pressure is equal to or higher than that of the low temperature generator GL, for example). Inside the hot generator GH, high temperature generator G
Preferably, the temperature at the H outlet, etc.) is detected. Other load detectors that detect the heating amount of the high-temperature generator GH include a flow rate detector for the heating source fluid (light black, hot water, or fuel gas or fuel oil in the case of a direct-fired type), or a flow rate control valve. An opening detector may also be used. Further, as the load detector, a pressure detector or a temperature detector that detects the pressure or saturation temperature within the high temperature generator GH may be used. Also,
A temperature detector that detects the cooling water temperature related to the above temperature and pressure may be used.

〔実施例〕〔Example〕

本発明の実施例につき図面を用いて説明する。 Embodiments of the present invention will be described with reference to the drawings.

第1図においてAは吸収器、Eは蒸発器、G Hは高温
発生器、CLは低温発生器、Cは凝縮器、XHは高温溶
液熱交換器、XLば低温溶液熱交換器、SPは溶液ポン
プ、RPは冷媒ポンプ、■は減圧弁である。
In Figure 1, A is an absorber, E is an evaporator, GH is a high temperature generator, CL is a low temperature generator, C is a condenser, XH is a high temperature solution heat exchanger, XL is a low temperature solution heat exchanger, and SP is a The solution pump, RP is a refrigerant pump, and ■ is a pressure reducing valve.

これらの機器の間を溶液経路3.4.5、冷媒経路6.
7.8が接続され、吸収溶液及び冷媒が循環されている
A solution path 3.4.5 and a refrigerant path 6.
7.8 is connected and the absorption solution and refrigerant are circulated.

■は蒸気などの加熱源流体が流れる加熱源経路であり、
流量制御弁2により加熱源流体の流量を;bll 1f
ft1して吸収冷凍機の容量を制御するようになってい
る。
■ is the heating source path through which the heating source fluid such as steam flows;
The flow rate of the heating source fluid is controlled by the flow rate control valve 2; bll 1f
ft1 to control the capacity of the absorption refrigerator.

9は冷水経路であり、負荷10と蒸発器Eとの間に冷水
ポンプ1■により冷水を循環するようになっている。
Reference numeral 9 denotes a cold water path, through which cold water is circulated between the load 10 and the evaporator E by a cold water pump 1.

12は冷却水経路であり、冷却水が冷却水ポンプ13に
より冷却塔14、吸収器A、凝縮器Cを循環するように
なっている。
12 is a cooling water path, in which cooling water is circulated through a cooling tower 14, an absorber A, and a condenser C by a cooling water pump 13.

15は容量制御装置であり、冷水出口温度を検出する温
度検出器1Gからの冷水温度信号を受け、冷水温度が一
定になるように流量制御弁2を操作するようになってい
る。
Reference numeral 15 denotes a capacity control device, which receives a cold water temperature signal from a temperature detector 1G that detects the cold water outlet temperature and operates the flow rate control valve 2 so that the cold water temperature is constant.

■8は制御装置であり、冷凍殿の運転停止時から、時限
機構22から与えられる設定時間経iM後冷却水ポンプ
13を停止する信号が発せられるようになっている。し
かして時限機構22における設定時間は、負荷検出器で
ある高温発生器GH内の溶液温度を検出する温度検出器
23により検出された運転停止時或いはその直前の溶液
温度に応じて選択される。
(2) 8 is a control device which is configured to issue a signal to stop the cooling water pump 13 after a set time iM given by the timer mechanism 22 has elapsed since the operation of the freezing chamber is stopped. Thus, the set time in the timer mechanism 22 is selected depending on the solution temperature at or just before the stoppage of operation detected by the temperature detector 23 which is a load detector that detects the solution temperature in the high temperature generator GH.

負荷検出器としては、高温発生器GHの出口における溶
液温度を検出する温度検出器21を用いてもよく、加熱
量に基づいて負荷を検出するために加熱源流体の流星を
検出する流量検出器や、その流量制御弁2の開度を検出
する開度検出器24を用いてもよく、高温発生器G )
Iの内圧を検出する圧力検出器25を用いてもよく、ま
たこれらの温度、圧力に関連する冷却水温度を検出する
l、μ度検出器を用いてもよい。
As the load detector, a temperature detector 21 that detects the solution temperature at the outlet of the high temperature generator GH may be used, and a flow rate detector that detects meteors in the heating source fluid to detect the load based on the amount of heating. Alternatively, an opening detector 24 that detects the opening of the flow rate control valve 2 may be used, and the high temperature generator G)
A pressure detector 25 may be used to detect the internal pressure of I, or a degree detector may be used to detect the cooling water temperature related to these temperatures and pressures.

第2図は、運転停止時のフローチャートである。FIG. 2 is a flowchart when the operation is stopped.

〔発明の効果〕〔Effect of the invention〕

本発明により、吸収冷凍機の運転停止に当たり、無駄な
動力の損失を防ぐと共に、溶液の希釈を促進し、熱応力
による吸収器の冷加水チユーブの[貝傷を防ぎ、かつ再
起動に当たり冷却塔の充填材の損傷を招くおそれのない
二重効用吸収冷凍機を提供することができ、実用上極め
て大なる効果を奏する。
The present invention prevents wasted power loss when shutting down an absorption chiller, promotes solution dilution, prevents damage to the chilled water tube of the absorber due to thermal stress, and prevents damage to the cooling tower when restarting the absorption chiller. It is possible to provide a dual-effect absorption refrigerator that does not cause damage to the filling material, which is extremely effective in practice.

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

第1図は本発明の実施例のフロー図、第2図はそのフロ
ーチャートである。 l・・・加熱源経路、2・・・流量制御弁、3・・・溶
液経路、4・・・溶液経路、5・・・溶液経路、6・・
・冷媒経路、7・・・冷媒経路、8・・・冷媒経路、9
・・・冷水経路、10・・・負荷、11・・・冷水ポン
プ、12・・・冷却水経路、13・・・冷却水ポンプ、
14・・・冷却塔、15・・・容量制御AA置、16・
・・温度検出器、1日・・・制御装置、21・・・温度
検出器、22・・・時限機構、23・・・温度検出器、
24・・・開度検出器、25・・・圧力検出器、A・・
・吸収器、E・・・蒸発器、GH・・・高温発生器、G
L・・・低温発生器、C・・・凝縮器、XH・・・高温
熱交換器、XL・・・低温熱交換器、SP・・・溶液ポ
ンプ、RP・・・冷媒ポンプ、■・・・減圧弁。 第1図
FIG. 1 is a flowchart of an embodiment of the present invention, and FIG. 2 is a flowchart thereof. l... Heat source path, 2... Flow rate control valve, 3... Solution path, 4... Solution path, 5... Solution path, 6...
- Refrigerant route, 7... Refrigerant route, 8... Refrigerant route, 9
...Cold water route, 10...Load, 11...Cold water pump, 12...Cooling water route, 13...Cooling water pump,
14... Cooling tower, 15... Capacity control AA position, 16.
...Temperature detector, 1 day...Control device, 21...Temperature detector, 22...Time limit mechanism, 23...Temperature detector,
24...Opening degree detector, 25...Pressure detector, A...
・Absorber, E... Evaporator, GH... High temperature generator, G
L...Low temperature generator, C...Condenser, XH...High temperature heat exchanger, XL...Low temperature heat exchanger, SP...Solution pump, RP...Refrigerant pump, ■... ·Pressure reducing valve. Figure 1

Claims (1)

【特許請求の範囲】 1、蒸発器、吸収器、高温発生器、低温発生器、凝縮器
、これらの機器を接続する溶液経路、冷媒経路、これら
の経路に設けられた溶液ポンプ、冷媒ポンプ、前記吸収
器及び凝縮器に通じている冷却水経路、該冷却水経路に
設けられた冷却水ポンプ、前記蒸発器に通じている冷水
経路、該冷水経路に設けられた冷水ポンプを備えている
二重効用吸収冷凍機において、 運転停止前の負荷状態を検出する負荷検出 器と、 運転停止後所定の設定時間後に前記冷却水 ポンプの運転を停止せしめる信号を発する時限機構と、 前記負荷検出器によって検出された運転停 止前の負荷状態に応じて前記所定の設定時間を選択する
制御機構と、 を備えたことを特徴とする二重効用吸収冷 凍機。 2、前記負荷検出器が、高温部における溶液温度を検出
する温度検出器である特許請求の範囲第1項記載の冷凍
機。 3、前記負荷検出器が、前記発生器における加熱源流体
の流量検出器である特許請求の範囲第1項記載の冷凍機
。 4、前記負荷検出器が、前記発生器の加熱源流体の流量
制御弁の弁開度検出器である特許請求の範囲第1項記載
の冷凍機。 5、前記負荷検出器が、前記高温発生器内の圧力を検出
する圧力検出器である特許請求の範囲第1項記載の冷凍
機。
[Claims] 1. An evaporator, an absorber, a high-temperature generator, a low-temperature generator, a condenser, a solution path connecting these devices, a refrigerant path, a solution pump provided in these paths, a refrigerant pump, A cooling water path communicating with the absorber and the condenser, a cooling water pump provided in the cooling water path, a cold water path communicating with the evaporator, and a cold water pump provided in the cold water path. In a heavy-effect absorption chiller, the load detector detects the load state before the operation is stopped, a timer mechanism that issues a signal to stop the operation of the cooling water pump after a predetermined set time after the operation is stopped, and the load detector. A dual-effect absorption refrigerating machine comprising: a control mechanism that selects the predetermined set time according to a detected load state before stopping operation. 2. The refrigerator according to claim 1, wherein the load detector is a temperature detector that detects a solution temperature in a high temperature section. 3. The refrigerator according to claim 1, wherein the load detector is a flow rate detector of the heating source fluid in the generator. 4. The refrigerator according to claim 1, wherein the load detector is a valve opening degree detector of a flow rate control valve for the heating source fluid of the generator. 5. The refrigerator according to claim 1, wherein the load detector is a pressure detector that detects the pressure within the high temperature generator.
JP61006254A 1986-01-17 1986-01-17 Double-effect absorption refrigerator Granted JPS62166272A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP61006254A JPS62166272A (en) 1986-01-17 1986-01-17 Double-effect absorption refrigerator
KR1019870000317A KR960002565B1 (en) 1986-01-17 1987-01-16 Double effective absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61006254A JPS62166272A (en) 1986-01-17 1986-01-17 Double-effect absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS62166272A true JPS62166272A (en) 1987-07-22
JPH0478903B2 JPH0478903B2 (en) 1992-12-14

Family

ID=11633347

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61006254A Granted JPS62166272A (en) 1986-01-17 1986-01-17 Double-effect absorption refrigerator

Country Status (2)

Country Link
JP (1) JPS62166272A (en)
KR (1) KR960002565B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02213659A (en) * 1989-02-14 1990-08-24 Sanyo Electric Co Ltd Absorption type freezer
JPH1183229A (en) * 1997-09-09 1999-03-26 Mitsubishi Heavy Ind Ltd Device for stopping operation of absorption refrigerating machine

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10325636A (en) * 1997-05-22 1998-12-08 Rinnai Corp Absorption type air-conditioning device
KR100337395B1 (en) * 1999-07-20 2002-05-21 이동수 Apparatus for sterilizing vacuum pack

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5222142A (en) * 1975-08-13 1977-02-19 Sanenerugii Kk Water heater by solar heat
JPS6021719U (en) * 1983-07-21 1985-02-14 石渡 裕子 glasses

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5222142A (en) * 1975-08-13 1977-02-19 Sanenerugii Kk Water heater by solar heat
JPS6021719U (en) * 1983-07-21 1985-02-14 石渡 裕子 glasses

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02213659A (en) * 1989-02-14 1990-08-24 Sanyo Electric Co Ltd Absorption type freezer
JPH1183229A (en) * 1997-09-09 1999-03-26 Mitsubishi Heavy Ind Ltd Device for stopping operation of absorption refrigerating machine

Also Published As

Publication number Publication date
JPH0478903B2 (en) 1992-12-14
KR960002565B1 (en) 1996-02-22
KR870007409A (en) 1987-08-19

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