JPS6225947B2 - - Google Patents

Info

Publication number
JPS6225947B2
JPS6225947B2 JP18600383A JP18600383A JPS6225947B2 JP S6225947 B2 JPS6225947 B2 JP S6225947B2 JP 18600383 A JP18600383 A JP 18600383A JP 18600383 A JP18600383 A JP 18600383A JP S6225947 B2 JPS6225947 B2 JP S6225947B2
Authority
JP
Japan
Prior art keywords
concentration
heat source
time
room temperature
supply
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
Application number
JP18600383A
Other languages
Japanese (ja)
Other versions
JPS6078262A (en
Inventor
Yozo Okamoto
Mokichi Kurosawa
Shozo Saito
Osayuki Inoe
Yoshiharu Tanaka
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
Tokyo Gas Co Ltd
Original Assignee
Ebara Corp
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 Ebara Corp, Tokyo Gas Co Ltd filed Critical Ebara Corp
Priority to JP18600383A priority Critical patent/JPS6078262A/en
Publication of JPS6078262A publication Critical patent/JPS6078262A/en
Publication of JPS6225947B2 publication Critical patent/JPS6225947B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、吸収冷凍機の停止時期を制御する方
法、特に停止前の吸収冷凍機内の吸収溶液の濃度
を測定し、この濃度との関連において吸収冷凍機
の適正な停止時期を決定する方法に関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention provides a method for controlling the timing of stopping an absorption refrigerator, in particular, measuring the concentration of an absorption solution in the absorption refrigerator before stopping, and determining the relationship with this concentration. This invention relates to a method for determining an appropriate time to stop an absorption refrigerator.

〔従来技術〕[Prior art]

従来、吸収冷凍機の運転を停止する(発生器へ
の熱源の供給を停止する)場合、建物の所定の空
調時間完了時刻(終業時刻)に合わせて運転を停
止するか、又は気温、室内温度等を考慮して所定
の空調時間完了時刻の数分前に経験的に停止して
おり、数分前に停止する場合も何分前にするかは
全く運転員の感にたよるもので、科学的数値に基
いて停止時刻を決定することは行われていなかつ
た。
Conventionally, when stopping the operation of an absorption chiller (stopping the supply of heat source to the generator), the operation was stopped according to the completion time of the building's predetermined air conditioning time (end time), or when the air temperature Based on our experience, the air conditioning system stops several minutes before the end of the specified air conditioning time, and even if it stops several minutes before, the exact number of minutes before it stops depends entirely on the operator's intuition. There was no determination of stop times based on scientific numbers.

〔発明の目的〕[Purpose of the invention]

本発明は、発生器への熱源の供給を停止した後
室温が空調時の室温許容範囲の上限へ達する時間
は、外気温度にもよるが、外気温度が一定の場
合、前記停止時の室温の外、吸収溶液の濃度に大
きく依存していることに鑑み、吸収溶液の濃度を
測定し、該濃度との関連においてできるだけ早い
時刻に発生器への熱源の供給を停止し、エネルギ
ーの無駄な消費をさけることを目的とするもので
ある。
In the present invention, the time required for the room temperature to reach the upper limit of the allowable room temperature range during air conditioning after the supply of heat source to the generator is stopped depends on the outside air temperature, but if the outside air temperature is constant, the room temperature at the time of the stop is In addition, considering that the concentration of the absorption solution is highly dependent on the concentration of the absorption solution, the concentration of the absorption solution should be measured and the supply of heat source to the generator should be stopped as early as possible in relation to the concentration to avoid wasteful energy consumption. The purpose is to avoid

〔発明の構成〕[Structure of the invention]

従来、吸収冷凍機の運転を停止する場合、停止
中に吸収溶液の温度が常温まで低下しても溶液中
で結晶が生成するのを防止する為、蒸発器側の冷
媒液を吸収溶液側に移動させ、吸収溶液全体の濃
度を低下させている。発生器でガスなどのエネル
ギーにより加熱されて再生された蒸発器側の冷媒
液は、本来ならば蒸発して冷凍効果を発揮しなが
ら蒸気の形で吸収溶液側に移動するはずのもので
あるが、吸収冷凍機の運転停止時には、冷凍効果
を発揮しないまゝ上述のように冷媒液の形で吸収
溶液側に移動させ、高濃度吸収溶液を希釈してし
まう為、高濃度吸収溶液は末だ冷却能力即ち濃度
エネルギーを有しているにもかゝわらず、これは
全く利用されない結果となつている。
Conventionally, when stopping operation of an absorption chiller, the refrigerant liquid from the evaporator side is transferred to the absorption solution side to prevent crystals from forming in the solution even if the temperature of the absorption solution drops to room temperature during the stoppage. and lowering the overall concentration of the absorption solution. Normally, the refrigerant liquid on the evaporator side that is heated and regenerated by energy such as gas in the generator would evaporate and move to the absorption solution side in the form of vapor while exerting a refrigeration effect. When the absorption chiller stops operating, the high-concentration absorbent solution is destroyed because it moves to the absorption solution side in the form of a refrigerant and dilutes the high-concentration absorbent solution as described above without exerting its freezing effect. Although it has cooling capacity, i.e., concentration energy, it ends up being completely unused.

本発明は、吸収冷凍機を停止する場合、この高
濃度吸収溶液の持つている濃度エネルギーを有効
に利用しつゝ結晶の折出をも防止しようとするも
のであつて、 熱源供給停止前における吸収溶液の濃度又は該
濃度と負荷条件を検知し、該検知された吸収溶液
の濃度又は該濃度及び負荷条件と、予め設定され
ている吸収溶液の濃度又は該濃度及び負荷条件と
熱源供給停止時刻から室温が室温許容範囲の上限
に達するまでの時間との関係から、熱源の供給を
停止した後室温が室温許容範囲の上限に達するま
での時間を求め、この求めた時間に基いて吸収冷
凍機の熱源の供給停止時刻を制御する方法であ
る。
The present invention aims to effectively utilize the concentration energy possessed by this high concentration absorption solution when stopping the absorption refrigerator and also to prevent precipitation of crystals before the heat source supply is stopped. The concentration of the absorbing solution or the concentration and the load condition are detected, the detected concentration of the absorbing solution or the concentration and the load condition, the preset concentration of the absorbing solution or the concentration and the load condition, and the heat source supply stop time. From the relationship between the time from This is a method of controlling the supply stop time of the heat source.

吸収溶液の濃度と発生器への熱源の供給停止時
刻の関係を第1図に基いて説明する。
The relationship between the concentration of the absorption solution and the time when the supply of heat source to the generator is stopped will be explained based on FIG. 1.

室温がTになるような条件で運転されている吸
収冷凍機の発生器への熱源の供給を停止した場
合、室温は次第に上昇して遂に室温許容範囲の上
限であるT1に達するが、このT1に達するまでの
時間は建物の熱容量や冷(温)水配管容量その他
の要因によつて異なる。しかし建物の熱容量は一
定であるから、結局T1に達するまでの時間に影
響を及ぼす因子としては、吸収冷凍機の発生器へ
の熱源の供給を停止する際の室温、外気温並びに
吸収溶液の濃度がある。尚該吸収溶液の温度の影
響も考えられるが、運転状況による該温度の差異
は殆んどないので、吸収溶液の温度の差は無視し
てよい。即ち熱源の供給停止直前における室温が
Tで、外気温が同一であるとすれば、発生機への
熱源の供給を停止する時刻TS直前の吸収溶液の
濃度がC1のときの室温の変化が線l1で示されると
すれば、該溶液の濃度がC1より濃くC2である場
合には室温の変化は線l2で示されることとなる。
即ち発生器への熱源の供給を停止する前の吸収溶
液の濃度が濃い場合には、発生器への熱源の供給
を停止してから室温許容範囲の上限の温度である
T1に達するまでの時間は吸収溶液の濃度が薄い
場合に比し長いこととなる。即ち、吸収溶液の濃
度が濃い程濃度エネルギーは大である。例えば吸
収冷凍機の運転停止前の室温がTで外気温が同一
であるとすれば、吸収溶液の濃度がC1のとき発
生器への熱源の供給停止後△T分で室内温度T1
となるが、吸収溶液の濃度がC2のときには(△
T+△T1)分後に室内温度はT1となるので、吸収
溶液の濃度がC1のときには終業時刻前△T分
に、吸収溶液の濃度がC2のときには、濃度がC1
のときに比し△T1分だけ早く即ち終業時刻前
(△T+△T1)分に発生器への熱源の供給を停止
すれば、終業時に室温は室温許容範囲の上限値
T1となり、無駄なエネルギーの消費を防止する
ことができる。
When the supply of heat to the generator of an absorption chiller that is operated under conditions such that the room temperature is The time it takes to reach T 1 depends on the building's thermal capacity, cold (hot) water piping capacity, and other factors. However, since the heat capacity of the building is constant, the factors that affect the time it takes to reach T 1 are the room temperature at the time of stopping the supply of heat source to the generator of the absorption chiller, the outside temperature, and the temperature of the absorption solution. There is concentration. Although the influence of the temperature of the absorption solution may be considered, there is almost no difference in temperature depending on the operating conditions, so the difference in temperature of the absorption solution can be ignored. In other words, if the room temperature immediately before the supply of heat source is stopped is T and the outside temperature is the same, then the change in room temperature when the concentration of the absorbing solution is C 1 immediately before the time T S when supply of the heat source to the generator is stopped is If the concentration of the solution is C2 , which is higher than C1 , then the change in room temperature will be shown by line l2 .
That is, if the concentration of the absorption solution is high before the supply of heat source to the generator is stopped, the temperature is at the upper limit of the room temperature tolerance range after the supply of heat source to the generator is stopped.
The time required to reach T 1 is longer than when the concentration of the absorption solution is low. That is, the higher the concentration of the absorption solution, the higher the concentration energy. For example, if the room temperature before stopping the operation of the absorption refrigerator is T and the outside temperature is the same, when the concentration of the absorption solution is C 1 , the indoor temperature will be T 1 in △T minutes after the supply of heat source to the generator is stopped.
However, when the concentration of the absorption solution is C 2 (△
T + △T 1 ) minutes later, the room temperature becomes T 1. Therefore, when the concentration of the absorption solution is C 1 , the concentration of the absorption solution is C 1 at △T minutes before the end of the workday, and when the concentration of the absorption solution is C 2 , the temperature becomes T 1.
If the heat source supply to the generator is stopped △T 1 minute earlier than when the work day ends, that is, △T + △T 1 minutes before the end of the work day, the room temperature will be the upper limit of the allowable room temperature range at the end of the work day.
T 1 , and wasteful energy consumption can be prevented.

尚△T或いは△T+△T1の値は、停止前にお
いて吸収溶液中に貯えられている濃度エネルギー
から放出可能な冷房容量を算出し、その時点にお
ける空調負荷を基にして熱源停止後何分程度空調
可能かを算出することが可能であるが、この時間
は、吸収冷凍機を或る部屋を空調する為設置した
際、予め種々の負荷条件下における吸収溶液の濃
度との関係を試験することにより求めておくこと
も出来る。そしてこれらの結果から、特定の吸収
溶液濃度に対し求められた時間の中、最も短い時
間をその濃度に対する△Tであるとしておけば、
濃度を測定するのみで、所定の空調終了前何分前
に熱源の供給を停止すればよいかゞわかり、従来
の感にたよつていた場合に比し熱源停止時刻を早
めることが可能となるのでエネルギーの節約がで
きる。又吸収溶液の濃度の外、負荷条件(例えば
外気温及び室温等)をも考慮してこれら両者を基
に停止時刻を制御するようにすればより細かな即
ち効果的な制御が可能となる。即ち、種々の負荷
条件下における吸収溶液の濃度と熱源停止後の空
調可能時間△Tを求めた場合、吸収溶液の濃度が
同一の場合外気温T2のとき△TがX2分であり、
それより高い外気温T3のときの△TがX3分であ
つたとする。この場合X3の方が短いが、吸収溶
液の濃度のみを指標として熱源停止時刻を制御す
るとすればどのような負荷の場合にも所定の空調
終了前に室温が室温許容範囲以上に上昇しないよ
うに制御する必要があるため、外気温が高い場合
の時間であるX3分前に熱源の供給を停止するこ
とになるが、吸収溶液の濃度以外の負荷条件、例
えば外気温をも考慮して該停止時刻を制御する場
合、外気温がT3の場合には所定の空調終了前X3
分前に熱源の供給を停止でき、また外気温がT2
の場合にはX2分前に熱源の供給を停止すればよ
いこととなるので、より細めな制御が可能とな
る。
The value of △T or △T + △T 1 is determined by calculating the cooling capacity that can be released from the concentrated energy stored in the absorption solution before stopping, and calculating the number of minutes after the heat source stops based on the air conditioning load at that time. It is possible to calculate the degree to which air conditioning is possible, but when an absorption refrigerator is installed to air condition a certain room, the relationship between this time and the concentration of absorption solution under various load conditions must be tested in advance. You can also ask for it. From these results, if we assume that the shortest time among the times determined for a specific absorption solution concentration is ΔT for that concentration, then
By simply measuring the concentration, it is possible to know how many minutes before the end of the specified air conditioning the heat source supply should be stopped, making it possible to stop the heat source earlier than when relying on conventional methods. Therefore, energy can be saved. Furthermore, if the stop time is controlled based on both of the load conditions (for example, outside temperature and room temperature) in addition to the concentration of the absorbing solution, more detailed or effective control becomes possible. That is, when determining the concentration of the absorption solution under various load conditions and the air conditioning available time △T after the heat source is stopped, when the concentration of the absorption solution is the same, when the outside temperature is T 2 , △T is X 2 minutes,
Suppose that ΔT is X 3 minutes when the outside temperature is higher than that, T 3 . In this case, X 3 is shorter, but if the heat source stop time is controlled using only the concentration of the absorbing solution as an index, it will be possible to prevent the room temperature from rising above the room temperature allowable range before the end of the specified air conditioning under any load. Therefore, the heat source supply must be stopped before X 3 minutes, which is the time when the outside temperature is high. When controlling the stop time, if the outside temperature is T 3 , the stop time is X 3 before the end of the specified air conditioning.
The heat source supply can be stopped before the outside temperature reaches T 2
In this case, it is only necessary to stop the heat source supply before X 2 minutes, which allows for more precise control.

第2図は、本発明における吸収溶液の濃度を測
定する場所或いは測定方法を説明するためのもの
でGHは高温発生器、GLは低温発生器、Cは凝縮
器、Aは吸収器、Eは蒸発器、L1は吸収器液レ
ベル検出器、L2は蒸発器液レベル検出器、1は
吸収器からの吸収溶液引出し管、2は吸収器への
濃吸収溶液供給管を示す。
Figure 2 is for explaining the location and method of measuring the concentration of the absorption solution in the present invention, where GH is a high temperature generator, GL is a low temperature generator, C is a condenser, A is an absorber, and E is a In the evaporator, L 1 is an absorber liquid level detector, L 2 is an evaporator liquid level detector, 1 is an absorption solution withdrawal pipe from the absorber, and 2 is a concentrated absorption solution supply pipe to the absorber.

吸収溶液の濃度の検出は、第2図に示した装置
においては、吸収器Aの出口部1又は吸収溶液熱
交換器濃溶液出口部2の何れの部分で検出しても
よい。吸収溶液の濃度は、吸収溶液の温度と比重
から常法により容易に求めることができる。温度
は、熱電対又は測温抵抗体等通常の温度センサー
で、比重は、浮力測定器、α線密度計或いは振動
式比重測定器により夫々求めることが可能であ
る。又、吸収溶液の濃度は蒸発器の液レベル検出
器L2により分離冷媒液の量を測定し、この量に
基いて吸収溶液の平均濃度を推定することもでき
る。又、吸収器液レベル検出器L1により吸収器
内の吸収溶液量を測定することにより求めること
ができる。又、発生器出口溶液温度や凝縮温度か
ら吸収溶液濃度を推定することも可能である。
In the apparatus shown in FIG. 2, the concentration of the absorption solution may be detected at either the outlet section 1 of the absorber A or the concentrated solution outlet section 2 of the absorption solution heat exchanger. The concentration of the absorption solution can be easily determined by a conventional method from the temperature and specific gravity of the absorption solution. The temperature can be determined using a normal temperature sensor such as a thermocouple or a resistance temperature detector, and the specific gravity can be determined using a buoyancy meter, an α-ray densitometer, or a vibrating specific gravity meter. Alternatively, the concentration of the absorption solution can be determined by measuring the amount of separated refrigerant liquid using the liquid level detector L2 of the evaporator, and estimating the average concentration of the absorption solution based on this amount. It can also be determined by measuring the amount of absorption solution in the absorber using the absorber liquid level detector L1 . It is also possible to estimate the absorption solution concentration from the generator outlet solution temperature and condensation temperature.

つぎに第3図に基いて本発明の実施例を説明す
る。
Next, an embodiment of the present invention will be described based on FIG.

第3図において符号GH,GL,C,A,E,1
及び2は第2図で示したものと同じ意味を有し、
3は冷水ポンプ、4は空調機、5はフアン、6は
建物、7はコントローラ、8は室温センサー、9
は外気温センサー、10は濃度検出センサー、1
1は冷凍機制御盤、12は停止信号、13はダク
ト(往)及び14はダクト(還)を夫々示す。
In Figure 3, the symbols GH, GL, C, A, E, 1
and 2 have the same meaning as shown in FIG.
3 is a cold water pump, 4 is an air conditioner, 5 is a fan, 6 is a building, 7 is a controller, 8 is a room temperature sensor, 9
is an outside temperature sensor, 10 is a concentration detection sensor, 1
1 is a refrigerator control panel, 12 is a stop signal, 13 is a duct (outward), and 14 is a duct (return).

コントローラー7は、各センサー8,9,10
からの信号を取り込み、演算を行ない、冷凍機を
停止すべき時間を決定する。そして停止時刻にな
つたら、コントローラー7から冷凍機制御盤11
に停止信号12を送り冷凍機を停止させるか、又
は停止時間になつた場合ブザーその他で運転員に
停止時刻になつたことを知らせる。コントローラ
ー7は制御盤に内蔵されていてもいいし、別に設
置されていてもよい。室温は1ケ所で測定しても
よいが、複数の個所で測定するのが好ましい。こ
の場合各部屋の平均値を採用してもいゝし、又、
最高値を採用してもよい。
The controller 7 has each sensor 8, 9, 10
The system receives signals from the refrigerator, performs calculations, and determines the time at which the refrigerator should be stopped. Then, when the stop time comes, the controller 7 sends a message to the refrigerator control panel 11.
A stop signal 12 is sent to stop the refrigerator, or when the stop time is reached, a buzzer or other device is used to notify the operator that the stop time has arrived. The controller 7 may be built into the control panel or may be installed separately. Room temperature may be measured at one location, but preferably at multiple locations. In this case, the average value for each room may be used, or
The highest value may be used.

冷凍機は1台設置されている場合のみでなく、
複数台設置されている場合でもよい。
Not only when one refrigerator is installed,
It is also possible to have multiple units installed.

〔発明の効果〕〔Effect of the invention〕

本発明においては、吸収溶液の濃度を測定する
ことにより、吸収冷凍機への熱源供給停止時刻
を、前記濃度に応じて或いは該濃度と負荷の関係
から従来行われていたよりも早い時刻に行うこと
ができ、吸収溶液の保有する濃度エネルギーを有
効に利用できるので、熱源の熱量及び動力費の節
約を図ることができる。
In the present invention, by measuring the concentration of the absorption solution, the heat source supply to the absorption refrigerator can be stopped in accordance with the concentration or earlier than conventionally due to the relationship between the concentration and the load. Since the concentration energy possessed by the absorbing solution can be effectively used, it is possible to save the heat amount of the heat source and the power cost.

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

第1図は吸収溶液の濃度と、吸収冷凍機への熱
源の供給を停止した後室温が室温許容範囲の上限
に到るまでの時間との関係を示す図であり、第2
図及び第3図は本発明の一実施態様を示す図であ
る。 T……室温、Tp……室温許容範囲の下限、T1
……室温許容範囲の上限、TS……熱源供給停止
時刻、TL,TH……室温が室温許容範囲の上限に
達した時刻、GH……高温発生器、GL……低温発
生器、C……凝縮器、A……吸収器、E……蒸発
器、L1……吸収器溶液レベル検出器、L2……蒸
発器冷媒レベル検出器、1……吸収溶液引出し
管、2……吸収溶液供給管、3……冷水ポンプ、
4……空調機、5……フアン、6……建物、7…
…コントローラー、8……室温センサー、9……
外気温センサー、10……溶液濃度センサー、1
1……冷凍機制御盤、12……停止信号、13…
…ダクト(往)、14……ダクト(還)。
Figure 1 is a diagram showing the relationship between the concentration of the absorption solution and the time it takes for the room temperature to reach the upper limit of the allowable room temperature range after the supply of heat source to the absorption refrigerator is stopped.
3 and 3 are diagrams showing one embodiment of the present invention. T...Room temperature, T p ...Lower limit of room temperature tolerance, T 1
... Upper limit of room temperature allowable range, T S ... Heat source supply stop time, T L , T H ... Time when room temperature reaches the upper limit of room temperature allowable range, GH... High temperature generator, GL... Low temperature generator, C...Condenser, A...Absorber, E...Evaporator, L1 ...Absorber solution level detector, L2 ...Evaporator refrigerant level detector, 1...Absorption solution draw-out pipe, 2... ...Absorption solution supply pipe, 3...Cold water pump,
4... Air conditioner, 5... Fan, 6... Building, 7...
...Controller, 8...Room temperature sensor, 9...
Outside temperature sensor, 10...Solution concentration sensor, 1
1... Refrigerator control panel, 12... Stop signal, 13...
...Duct (outward), 14...Duct (return).

Claims (1)

【特許請求の範囲】 1 使用時間に応じて運転の開始及び停止を行う
吸収冷凍機において、熱源供給停止前における吸
収溶液の濃度を検知し、該検知された吸収溶液の
濃度と、予め設定されている吸収溶液の濃度と熱
源供給停止時刻から室温が室温許容範囲の上限に
達するまでの時間との関係から、熱源の供給を停
止した後室温が室温許容範囲の上限に達するまで
の時間を求め、この求めた時間に基いて吸収冷凍
機の熱源の供給停止時刻を制御する方法。 2 熱源の供給停止前における吸収溶液の濃度と
負荷条件を検知し該検知された濃度及び負荷条件
に基いて、予め設定されている吸収溶液の濃度及
び負荷条件と熱源供給停止時刻から室温が室温許
容範囲の上限に達するまでの時間との関係から、
熱源の供給を停止した後室温が室温許容範囲の上
限に達するまでの時間を求める特許請求の範囲1
記載の吸収冷凍機の熱源の供給停止時刻を制御す
る方法。
[Claims] 1. In an absorption refrigerator whose operation is started and stopped according to the usage time, the concentration of an absorption solution before the heat source supply is stopped is detected, and the detected concentration of the absorption solution is combined with a preset value. From the relationship between the concentration of the absorbing solution and the time from the time the heat source supply is stopped until the room temperature reaches the upper limit of the room temperature tolerance range, find the time until the room temperature reaches the upper limit of the room temperature tolerance range after the heat source supply is stopped. , a method of controlling the supply stop time of the heat source of the absorption chiller based on this determined time. 2. Detect the concentration and load conditions of the absorption solution before the supply of the heat source is stopped, and based on the detected concentration and load conditions, set the concentration and load conditions of the absorption solution in advance and the room temperature from the time when the supply of the heat source is stopped. In relation to the time it takes to reach the upper limit of the tolerance range,
Claim 1 requires the time required for the room temperature to reach the upper limit of the room temperature tolerance range after the supply of the heat source is stopped.
A method for controlling the supply stop time of a heat source of an absorption refrigerator as described above.
JP18600383A 1983-10-06 1983-10-06 Method of controlling shut-down time in absorption refrigerator Granted JPS6078262A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18600383A JPS6078262A (en) 1983-10-06 1983-10-06 Method of controlling shut-down time in absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18600383A JPS6078262A (en) 1983-10-06 1983-10-06 Method of controlling shut-down time in absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS6078262A JPS6078262A (en) 1985-05-02
JPS6225947B2 true JPS6225947B2 (en) 1987-06-05

Family

ID=16180663

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18600383A Granted JPS6078262A (en) 1983-10-06 1983-10-06 Method of controlling shut-down time in absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS6078262A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2562643B2 (en) * 1988-01-29 1996-12-11 三洋電機株式会社 Absorption refrigerator

Also Published As

Publication number Publication date
JPS6078262A (en) 1985-05-02

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