JP3167491B2 - Absorption refrigerator - Google Patents

Absorption refrigerator

Info

Publication number
JP3167491B2
JP3167491B2 JP06269193A JP6269193A JP3167491B2 JP 3167491 B2 JP3167491 B2 JP 3167491B2 JP 06269193 A JP06269193 A JP 06269193A JP 6269193 A JP6269193 A JP 6269193A JP 3167491 B2 JP3167491 B2 JP 3167491B2
Authority
JP
Japan
Prior art keywords
temperature
liquid
refrigerant
pipe
low
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
JP06269193A
Other languages
Japanese (ja)
Other versions
JPH06249538A (en
Inventor
直樹 坂本
英一 榎本
朗 畑山
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
Original Assignee
Sanyo Electric 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 filed Critical Sanyo Electric Co Ltd
Priority to JP06269193A priority Critical patent/JP3167491B2/en
Publication of JPH06249538A publication Critical patent/JPH06249538A/en
Application granted granted Critical
Publication of JP3167491B2 publication Critical patent/JP3167491B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は吸収冷凍機に係わり、特
に詳しくは室内側機器の起動/停止によって熱源側機器
の起動/停止を制御するタイプの吸収冷凍機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption chiller, and more particularly to an absorption chiller of a type in which the start / stop of a heat source side device is controlled by the start / stop of an indoor device.

【0002】[0002]

【従来の技術】従来の吸収冷凍機においては、運転を停
止するに際し、熱源側機器をファンコイルなどの二次側
機器に先行して停止している。この操作により、蒸発器
には二次側機器で熱交換して温度上昇した冷水が最後ま
で供給されるので、蒸発器における冷媒の蒸発が最後ま
で妨げられることがない。このため、吸収器においては
吸収液による冷媒の吸収が進み、吸収液循環による稀釈
が行われて、停止後の吸収液の結晶防止が図られる。
2. Description of the Related Art In a conventional absorption refrigerator, when the operation is stopped, a heat source side device is stopped prior to a secondary side device such as a fan coil. By this operation, the evaporator is supplied with the cold water whose temperature has risen due to heat exchange in the secondary device to the end, so that the evaporation of the refrigerant in the evaporator is not hindered to the end. For this reason, in the absorber, absorption of the refrigerant by the absorbing liquid proceeds, and dilution is performed by circulating the absorbing liquid, thereby preventing crystallization of the absorbing liquid after stopping.

【0003】しかし、近年は空調性を高める目的で、熱
源側機器を主体とした起動/停止制御ではなく、室内
側、すなわち空調機端末側からの起動/停止によって熱
源側機器の起動/停止を制御するタイプの吸収冷凍機を
求める声が、市場で高まって来ている。
However, in recent years, for the purpose of improving air conditioning, the start / stop of the heat source side device is not started / stopped mainly by the heat source side device but is started / stopped from the indoor side, that is, the air conditioner terminal side. There is an increasing demand in the market for controlled absorption chillers.

【0004】ところが、二次側機器を熱源側機器より先
に停止すると、蒸発器には冷水が低温度のままで還流す
るため、冷媒の蒸発量が減少しても冷水系はさらに冷却
されることになり、この状態が進むと冷水が過冷却状態
となるばかりか、蒸発器内の冷媒が凍結すると云った問
題も生じるので、この状態を回避しようとして冷却水ポ
ンプを止めると、今度は吸収器と凝縮器の圧力上昇を招
いて、吸収液の流れが阻害され吸収液が稀釈されなくな
ると云った問題を生じる。
However, when the secondary device is stopped before the heat source device, the cold water flows back to the evaporator at a low temperature while maintaining a low temperature, so that the chilled water system is further cooled even if the evaporation amount of the refrigerant decreases. As a result, not only does the cooling water become supercooled when this state progresses, but also there is a problem that the refrigerant in the evaporator freezes.If the cooling water pump is stopped to avoid this state, it will be absorbed this time. This causes a problem that the flow of the absorbing solution is obstructed and the absorbing solution cannot be diluted because the pressure of the vessel and the condenser increases.

【0005】このように、二次側機器の起動/停止に熱
源側機器を追随させる場合は、冷凍負荷が急減した時の
冷水が過冷却状態にならないように、また冷媒が凍結し
ないようにする必要がある。このためには、二次側機器
を停止した後の冷凍能力を速やかに低下させる必要があ
り、また吸収液の濃縮により得られた濃度差エネルギー
についても速やかに低下させる必要があった。これを解
決すれば、従来必要とされていた稀釈運転時間を大幅に
短縮することが可能になる。
As described above, when the heat-source-side device follows the start / stop of the secondary-side device, the chilled water is not supercooled when the refrigeration load is rapidly reduced, and the refrigerant is not frozen. There is a need. For this purpose, it is necessary to quickly reduce the refrigerating capacity after stopping the secondary device, and it is also necessary to rapidly reduce the concentration difference energy obtained by concentrating the absorbing solution. If this is solved, it is possible to greatly reduce the conventionally required dilution operation time.

【0006】冷水の過冷却と冷媒の凍結を防止するた
め、冷水や冷媒について対処する温度を予め設定してお
き、この温度にまで冷水や冷媒の温度が低下すると、熱
源側機器(高温再生器)や吸収液ポンプを停止したり、
冷却水ポンプの運転を停止する対策を講じていた。しか
し、この対策だけではそれまで冷凍能力を保持するため
に作っていた濃度の高い吸収液はそのまま残っているの
で、再び冷却水ポンプを起動させると、冷水が再度過冷
却となる、冷媒が凍結する、あるいは吸収液が結晶する
と云った問題点があった。
[0006] In order to prevent the supercooling of the cold water and the freezing of the refrigerant, a temperature corresponding to the cold water or the refrigerant is set in advance, and when the temperature of the cold water or the refrigerant decreases to this temperature, the heat source side device (high temperature regenerator). ) Or stop the absorption liquid pump,
Measures were taken to stop the operation of the cooling water pump. However, with this measure alone, the high-concentration absorbing liquid that had been created to maintain the refrigeration capacity remains as it is, so when the cooling water pump is started again, the cold water will be supercooled again, and the refrigerant will freeze. Or the absorption liquid crystallized.

【0007】一方、吸収液を短時間で稀釈する技術とし
ては、冷媒貯蔵室と低温熱交換器入口側の濃液配管とを
開閉弁を介して配管接続しておき、停止時の稀釈運転中
あるいは冷却水温度がある設定温度以下になった時に、
高温再生器の圧力を利用して冷媒を濃液配管に圧入して
稀釈するものがある。しかし、この方法は濃度差の著し
く大きい冷媒と吸収液とが濃液配管内で激しく混合する
ため、大きな混合音が発生するだけでなく、混合する際
に発生する振動によって配管系統が損傷する懸念がある
と云った問題点があった。
On the other hand, as a technique for diluting the absorbing liquid in a short time, the refrigerant storage chamber and the concentrated liquid pipe on the inlet side of the low-temperature heat exchanger are connected to each other via an on-off valve, and the dilution operation during stoppage is performed. Or, when the cooling water temperature falls below a certain set temperature,
There is a type in which a refrigerant is press-fitted into a concentrated liquid pipe using a pressure of a high-temperature regenerator to be diluted. However, in this method, since the refrigerant and the absorbing liquid having a remarkably large concentration difference are mixed violently in the concentrated liquid pipe, not only a large mixing noise is generated, but also the piping system may be damaged due to vibration generated during mixing. There was a problem that there was.

【0008】[0008]

【発明が解決しようとする課題】すなわち、室内側、す
なわち空調機端末側からの起動/停止によって熱源側機
器の起動/停止が制御できる方式で、しかも二次側機器
が急停止するなどして冷凍負荷が急減することがあって
も、冷水が過冷却されたり、冷媒が凍結することがな
く、冷水温度の低下時でも吸収液を稀釈することのでき
る吸収冷凍機の開発が課題となっていた。
That is, a method in which the start / stop of the heat source side device can be controlled by the start / stop from the indoor side, that is, the air conditioner terminal side, and the secondary side device suddenly stops. Even if the refrigeration load suddenly decreases, the development of an absorption refrigerator that can dilute the absorption liquid even when the temperature of the chilled water is low without supercooling the chilled water or freezing the refrigerant has been an issue. Was.

【0009】[0009]

【課題を解決するための手段】本発明は上記した従来技
術の課題を解決するためになされたもので、吸収器、蒸
発器、凝縮器、高温再生器、低温再生器、低温熱交換
器、高温熱交換器および吸収液ポンプを配管接続して冷
媒と吸収液の循環サイクルを形成する二重効用吸収冷凍
機において、吸収液ポンプの吐出側配管と、低温再生器
から低温熱交換器に至る濃液配管および高温再生器から
高温熱交換器に至る中間液配管の少なくとも何れかと
を、通常閉の開閉弁が介在し、稀液吐出口が被流入側配
管の液流れ方向に開口している分岐管を介して連通可能
に接続すると共に、吸収冷凍機の運転停止時に前記開閉
弁を開にする制御器を設けたことを特徴とする吸収冷凍
機と、
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems of the prior art, and includes an absorber, an evaporator, a condenser, a high-temperature regenerator, a low-temperature regenerator, a low-temperature heat exchanger, In a double-effect absorption refrigerator that connects a high-temperature heat exchanger and an absorption liquid pump to form a circulation cycle of refrigerant and absorption liquid, the discharge-side piping of the absorption liquid pump and the low-temperature regenerator to the low-temperature heat exchanger At least one of the concentrated liquid pipe and the intermediate liquid pipe from the high-temperature regenerator to the high-temperature heat exchanger is provided with a normally closed on-off valve, and the diluted liquid discharge port is opened in the liquid flow direction of the inflow-side pipe. An absorption refrigerator, which is connected so as to be able to communicate via a branch pipe and is provided with a controller that opens the on-off valve when the operation of the absorption refrigerator is stopped,

【0010】吸収器、蒸発器、凝縮器、高温再生器、低
温再生器、低温熱交換器、高温熱交換器および吸収液ポ
ンプを配管接続して冷媒と吸収液の循環サイクルを形成
する二重効用吸収冷凍機において、吸収液ポンプの吐出
側配管と、低温再生器から低温熱交換器に至る濃液配管
とを、通常閉の開閉弁が介在し、稀液吐出口が被流入側
配管の液流れ方向に開口している分岐管を介して連通可
能に接続すると共に、少なくとも冷水温度か冷却水温度
か蒸発器における冷媒温度の何れかが所定温度に低下し
た時に、前記開閉弁を開にする制御器を設けたことを特
徴とする吸収冷凍機と、を提供することにより、前記従
来技術の課題を解決するものである。
[0010] A double connection in which an absorber, an evaporator, a condenser, a high-temperature regenerator, a low-temperature regenerator, a low-temperature heat exchanger, a high-temperature heat exchanger and an absorbent pump are connected by piping to form a circulation cycle of the refrigerant and the absorbent. In a utility absorption refrigerator, a normally closed on-off valve is interposed between the discharge pipe of the absorption pump and the concentrated pipe from the low-temperature regenerator to the low-temperature heat exchanger, and the diluted liquid discharge port is connected to the inflow pipe. Connected communicably via a branch pipe that opens in the liquid flow direction, and when at least one of the chilled water temperature, the chilled water temperature, or the refrigerant temperature in the evaporator drops to a predetermined temperature, the on-off valve is opened. An object of the present invention is to solve the above-mentioned problem of the related art by providing an absorption refrigerator having a controller provided.

【0011】[0011]

【作用】吸収冷凍機本体の運転が停止するか、冷水温度
が所定温度に低下するか、冷却水温度が所定温度に低下
するか、蒸発器における冷媒温度が所定温度に低下した
時などに、稀液吐出口が被流入側配管の液流れ方向に開
口している分岐管の開閉弁が開いて稀液が吸収液ポンプ
により、低温再生器から低温熱交換器に至る濃液配管お
よび/または高温再生器から高温熱交換器に至る中間液
配管に供給されるので、濃液管内の濃液や中間液管内の
中間液が短時間で稀釈される。このため、冷凍能力が速
やかに低下し、蒸発器の圧力が上昇するので、冷水が過
冷却となったり、冷媒が凍結すると云ったことがなくな
る。
When the operation of the absorption refrigerator is stopped, when the temperature of the cold water drops to a predetermined temperature, when the temperature of the cooling water drops to a predetermined temperature, or when the temperature of the refrigerant in the evaporator drops to a predetermined temperature, The on-off valve of the branch pipe whose diluent discharge port opens in the liquid flow direction of the inflow side pipe is opened, and the dilute liquid is pumped by the absorbent pump to the concentrated liquid pipe from the low-temperature regenerator to the low-temperature heat exchanger and / or. Since the liquid is supplied to the intermediate liquid pipe from the high temperature regenerator to the high temperature heat exchanger, the concentrated liquid in the concentrated liquid pipe and the intermediate liquid in the intermediate liquid pipe are diluted in a short time. For this reason, the refrigerating capacity is quickly reduced and the pressure of the evaporator is increased, so that the cooling water is not overcooled or the refrigerant is not frozen.

【0012】[0012]

【実施例】(実施例1) 図1に基づいて第1の実施例を説明すると、1はガス・
灯油などの燃焼装置2を備え、稀液を加熱することによ
って冷媒蒸気を発生させて中間液に濃縮する高温再生
器、3はこの再生器から揚液された冷媒蒸気と中間液と
を分ける分離器、4はこの分離器からの冷媒蒸気で中間
液を加熱して濃液にする低温再生器、5は前記両再生器
1・4からの冷媒蒸気を冷却して凝縮する凝縮器、6は
冷媒分配器30から冷媒液を散布・滴下などして蒸発さ
せる蒸発器、7はこの蒸発器からの冷媒蒸気を前記低温
再生器4からの濃液に吸収させて器内を低圧に維持する
吸収器、8は前記低温再生器4において中間液を加熱し
た後の冷媒の余熱で蒸発器6における未蒸発冷媒を揚液
する気泡ポンプ、9および10は低温および高温熱交換
器で、これらは揚液管11、中間液管12、濃液管1
3、吸収液ポンプ14を有する稀液管15、冷媒導管1
6、冷媒液管17および冷媒還流管18により接続され
て、冷媒と吸収液の循環サイクルを形成しており、
(Embodiment 1) A first embodiment will be described with reference to FIG.
A high-temperature regenerator that includes a combustion device 2 such as kerosene and generates a refrigerant vapor by heating a dilute liquid and concentrates the intermediate liquid into an intermediate liquid. A high-temperature regenerator 3 separates the refrigerant vapor pumped from the regenerator and the intermediate liquid. , A low-temperature regenerator that heats the intermediate liquid with the refrigerant vapor from the separator to make it a concentrated liquid, 5 a condenser that cools and condenses the refrigerant vapor from both the regenerators 1 and 4, and 6 a condenser An evaporator 7 for spraying and dropping the refrigerant liquid from the refrigerant distributor 30 to evaporate the refrigerant. An absorption unit 7 absorbs the refrigerant vapor from the evaporator into the concentrated liquid from the low-temperature regenerator 4 to maintain the inside of the container at a low pressure. 8 is a bubble pump for pumping the unevaporated refrigerant in the evaporator 6 with the residual heat of the refrigerant after heating the intermediate liquid in the low-temperature regenerator 4; 9 and 10 are low- and high-temperature heat exchangers; Liquid pipe 11, intermediate liquid pipe 12, concentrated liquid pipe 1
3, diluent pipe 15 having absorbent pump 14, refrigerant pipe 1
6, connected by a refrigerant liquid pipe 17 and a refrigerant return pipe 18 to form a circulation cycle of the refrigerant and the absorbing liquid,

【0013】さらに通常閉の開閉弁19を有する分岐管
22によって、稀液管15の低温熱交換器9への流入側
と濃液管13の低温熱交換器9への流入側とが連通可能
に接続され、また通常閉の開閉弁20を有する分岐管2
3によって、稀液管15の低温熱交換器9への流入側と
中間液管12の高温熱交換器10への流入側とが連通可
能に接続されると共に、蒸発器6の冷媒液溜め24と吸
収器7とが、通常閉の開閉弁21を有する冷媒ブロー管
25を介して連通可能に接続されている。
Further, a branch pipe 22 having a normally closed on-off valve 19 allows communication between the inflow side of the dilute tube 15 into the low-temperature heat exchanger 9 and the inflow side of the concentrated tube 13 into the low-temperature heat exchanger 9. And a branch pipe 2 having a normally closed on-off valve 20
3 connects the inflow side of the diluent tube 15 to the low-temperature heat exchanger 9 and the inflow side of the intermediate liquid tube 12 to the high-temperature heat exchanger 10 while allowing the refrigerant reservoir 24 of the evaporator 6 to communicate. And the absorber 7 are communicably connected via a refrigerant blow pipe 25 having a normally closed on-off valve 21.

【0014】なお、分岐管22と濃液管13、あるいは
分岐管23と中間液管12とは図5に示したように、分
岐管の開口端を濃液管13または中間液管12の内部に
延設し、しかも開口部を濃液管13または中間液管12
を流れる吸収液の流れ方向に一致して設置されている。
As shown in FIG. 5, the branch pipe 22 and the concentrated liquid pipe 13 or the branch pipe 23 and the intermediate liquid pipe 12 are connected to the open end of the branched pipe inside the concentrated liquid pipe 13 or the intermediate liquid pipe 12. And the opening is formed in the concentrated liquid pipe 13 or the intermediate liquid pipe 12.
It is installed in accordance with the flow direction of the absorbing liquid flowing through.

【0015】特に、(b)のように開口端部を絞って形
成することにより、一段と大きい圧力を付与することが
できるので、吸収液の循環が順調に行われるようにな
り、中間液あるいは濃液を稀釈する作用効果が一層大き
く発現される。
In particular, by forming the opening end portion to be narrowed as shown in (b), a still higher pressure can be applied, so that the absorption liquid can be circulated smoothly, and the intermediate liquid or the concentrated liquid can be concentrated. The effect of diluting the liquid is further enhanced.

【0016】また、26は蒸発器6の内部を経由して配
管した冷水管、27は冷却水ポンプ28を有し、吸収器
7・凝縮器5の内部を経由して配管した冷却水管、29
は吸収冷凍機本体が運転停止信号を受信した時に、冷却
水ポンプ28の運転を停止すると共に、開閉弁19・2
0・21を開き、且つ吸収液ポンプ14の運転を所定時
間だけ遅延して停止するように設けた制御器である。
Reference numeral 26 denotes a cooling water pipe connected through the interior of the evaporator 6, 27 denotes a cooling water pump, and a cooling water pipe connected via the interior of the absorber 7 and the condenser 5;
When the main body of the absorption chiller receives the operation stop signal, the operation of the cooling water pump 28 is stopped, and
The controller is provided so as to open 0.21 and stop the operation of the absorbent pump 14 with a delay of a predetermined time.

【0017】なお、開閉弁19・20・21を開にする
順序とタイミング、吸収液ポンプ14の運転を停止タイ
ミングなどについては、制御器29により適宜設定する
ことができる。
The order and timing of opening the on-off valves 19, 20 and 21 and the timing of stopping the operation of the absorbent pump 14 can be appropriately set by the controller 29.

【0018】上記構成の吸収冷凍機においては、二次側
(図示せず)機器の運転が停止されるなどして冷凍負荷
が急減すると、冷水管26を通って蒸発器6に還流して
くる冷水の温度は下がり続けて蒸発温度に近い温度にま
で低下する。このため、吸収冷凍機本体の運転停止が指
示されるので、制御器29が送信する制御信号によっ
て、冷却水ポンプ28が運転を停止して冷却動作を停止
すると共に、開閉弁19・20・21が例えば同時に開
き、冷媒液溜め24の冷媒が冷媒ブロー管25・開閉弁
21を介して吸収器7に流入してここの吸収液を速やか
に稀釈し、この稀釈された吸収液が吸収液ポンプ14の
ポンプ圧により、分岐管22・開閉弁19を介して濃液
管13の低温熱交換器9入口側に圧入されてこの部分の
濃液を稀釈し、分岐管23・開閉弁20を介して中間液
管12の高温熱交換器10入口側に圧入されてこの部分
の中間液を速やかに稀釈する。したがって、機器全体の
吸収液濃度が速やかに低下し、稀釈時間を短縮すること
ができ、吸収液の結晶化を回避でき、さらに吸収器7で
は吸収液の濃度が大幅に低下して冷媒を吸収する能力が
低下し、蒸発器6における冷媒の蒸発が抑制されること
から、冷水管26の冷水が過冷却となったり冷媒が凍結
すると云ったことが回避される。
In the absorption refrigerator having the above-mentioned structure, when the operation of the secondary side (not shown) is stopped and the refrigerating load is suddenly reduced, the refrigerant is returned to the evaporator 6 through the cold water pipe 26. The temperature of the chilled water continues to drop and drops to a temperature close to the evaporation temperature. For this reason, the operation stop of the absorption chiller body is instructed, and the control signal transmitted by the controller 29 stops the operation of the cooling water pump 28 to stop the cooling operation, and the on-off valves 19, 20, and 21. Are simultaneously opened, for example, and the refrigerant in the refrigerant reservoir 24 flows into the absorber 7 via the refrigerant blow pipe 25 and the on-off valve 21 to quickly dilute the absorbed liquid, and the diluted absorbed liquid is supplied to the absorbent pump. By the pump pressure 14, the concentrated liquid 13 is press-fitted into the low-temperature heat exchanger 9 on the inlet side through the branch pipe 22 and the on-off valve 19 to dilute the concentrated liquid in this part. Then, the intermediate liquid is press-fitted into the intermediate liquid pipe 12 at the inlet side of the high-temperature heat exchanger 10 to quickly dilute the intermediate liquid in this portion. Therefore, the concentration of the absorbing solution in the entire apparatus is rapidly reduced, the dilution time can be shortened, the crystallization of the absorbing solution can be avoided, and the absorber 7 significantly reduces the concentration of the absorbing solution to absorb the refrigerant. The cooling capacity of the evaporator 6 is suppressed, and the evaporation of the refrigerant in the evaporator 6 is suppressed, so that the cooling water in the chilled water pipe 26 is overcooled or the refrigerant is frozen.

【0019】(実施例2) 図2に基づいて第2の実施例を説明する。この実施例
は、前記第1の実施例の吸収冷凍機に、温度検出器31
を設置して蒸発器6における冷媒の温度が検出可能であ
り、また、燃焼装置2の動作を制御器29により制御可
能としている。なお、実施例1と同様の機能を有する機
器には同一の符号を付し、その説明は実施例の理解を妨
げない範囲で省略した。
(Embodiment 2) A second embodiment will be described with reference to FIG. This embodiment is different from the absorption refrigerator of the first embodiment in that a temperature detector 31 is provided.
Is installed so that the temperature of the refrigerant in the evaporator 6 can be detected, and the operation of the combustion device 2 can be controlled by the controller 29. The devices having the same functions as those of the first embodiment are denoted by the same reference numerals, and the description thereof is omitted to the extent that the understanding of the first embodiment is not hindered.

【0020】この実施例における前記制御器29は、前
記した温度検出器31が検出する冷媒分配器30を流れ
る冷媒の温度が所定温度(例えば、2℃)に低下した時
に、冷却水ポンプ28と燃焼装置2の運転を停止させる
と共に、開閉弁19・20・21を例えば同時に開くよ
うに設けてあるので、運転中に冷媒温度が所定温度に低
下すると、前記実施例1の場合と同様に冷媒液溜め24
の冷媒が吸収器7に流入してここの吸収液を速やかに稀
釈し、この稀釈された吸収液が吸収液ポンプ14のポン
プ圧により、分岐管22・開閉弁19を介して濃液管1
3の低温熱交換器9入口側に圧入されてこの部分の濃液
を稀釈し、分岐管23・開閉弁20を介して中間液管1
2の高温熱交換器10入口側に圧入されてこの部分の中
間液を速やかに稀釈する。このため、吸収器7では吸収
液濃度が大幅に低下して冷媒を吸収する能力が低下し、
蒸発器6における冷媒の蒸発が抑制されることから、冷
水管26の冷水が過冷却となったり冷媒が凍結すると云
ったことが回避される。
When the temperature of the refrigerant flowing through the refrigerant distributor 30 detected by the temperature detector 31 decreases to a predetermined temperature (for example, 2 ° C.), the controller 29 in this embodiment controls the cooling water pump 28 Since the operation of the combustion device 2 is stopped and the on-off valves 19, 20, and 21 are provided to be simultaneously opened, for example, when the refrigerant temperature decreases to a predetermined temperature during the operation, the refrigerant is discharged in the same manner as in the first embodiment. Reservoir 24
Flows into the absorber 7 to quickly dilute the absorbing liquid, and the diluted absorbing liquid is pumped by the absorbing liquid pump 14 through the branch pipe 22 and the on-off valve 19 to form the concentrated liquid pipe 1.
3 is press-fitted into the inlet side of the low-temperature heat exchanger 9 to dilute the concentrated liquid in this portion.
The intermediate liquid in this portion is rapidly diluted by being press-fitted into the inlet side of the high-temperature heat exchanger 10 of No. 2. Therefore, in the absorber 7, the absorption liquid concentration is significantly reduced, and the ability to absorb the refrigerant is reduced,
Since the evaporation of the refrigerant in the evaporator 6 is suppressed, it is possible to prevent the chilled water in the chilled water pipe 26 from being supercooled or the refrigerant from being frozen.

【0021】なお、温度検出器31によって蒸発器6に
おける冷媒温度の低下が検出された時に、冷却水ポンプ
28の運転を停止しても、冷水管26を介して供給する
冷水の循環は止める必要がないので、冷房運転などに支
障を来すことはない。
When the temperature detector 31 detects a decrease in the refrigerant temperature in the evaporator 6, even if the operation of the cooling water pump 28 is stopped, the circulation of the cooling water supplied through the cooling water pipe 26 must be stopped. Because there is no, there is no hindrance to cooling operation.

【0022】(実施例3) 図3に基づいて第3の実施例を説明する。ここに例示し
た吸収冷凍機は、図2に示した吸収冷凍機における温度
検出器31に代えて、温度検出器32を蒸発器6で熱交
換した後の冷水温度が検出可能に、冷水管26の蒸発器
6からの出口部に設置したものである。この場合も、実
施例1・2と同様の機能を有する機器には同一の符号を
付し、その説明は実施例の理解を妨げない範囲で省略し
た。
(Embodiment 3) A third embodiment will be described with reference to FIG. The absorption chiller exemplified here is capable of detecting the chilled water temperature after heat exchange of the temperature detector 32 with the evaporator 6 instead of the temperature detector 31 in the absorption chiller shown in FIG. This is installed at the outlet from the evaporator 6. Also in this case, the devices having the same functions as those of the first and second embodiments are denoted by the same reference numerals, and the description thereof is omitted to the extent that the understanding of the embodiments is not hindered.

【0023】上記構成の吸収冷凍機においては、温度検
出器32が検出する冷水の温度が所定温度(例えば、3
℃)に低下した時に、制御器29が前記第2の実施例に
おいて前記温度検出器31が所定温度を検出した時に前
記制御器29が発信したのと同様の制御信号を発信する
よう設けてあるので、冷水温度が所定温度に低下する
と、冷却水ポンプ28と燃焼装置2の運転を停止すると
共に開閉弁19・20・21が開いて吸収器7の吸収液
が稀釈され、この稀釈された吸収液が濃液管13の低温
熱交換器9入口側および中間液管12の高温熱交換器1
0入口側に圧入されてこの部分の濃液および中間液を稀
釈する。このため、前記実施例1・2の場合と同様に、
吸収器7では吸収液濃度が大幅に低下して冷媒を吸収す
る能力が低下し、蒸発器6における冷媒の蒸発が抑制さ
れることから、冷水管26の冷水が過冷却となったり冷
媒が凍結すると云ったことが回避される。
In the absorption refrigerator having the above structure, the temperature of the chilled water detected by the temperature detector 32 is set to a predetermined temperature (for example, 3
° C), the controller 29 transmits a control signal similar to that transmitted by the controller 29 when the temperature detector 31 detects a predetermined temperature in the second embodiment. Therefore, when the temperature of the chilled water drops to a predetermined temperature, the operation of the cooling water pump 28 and the combustion device 2 is stopped, and the on-off valves 19, 20, and 21 are opened to dilute the absorbent in the absorber 7, and the diluted absorption The liquid is the inlet of the low temperature heat exchanger 9 of the concentrated liquid tube 13 and the high temperature heat exchanger 1 of the intermediate liquid tube 12.
It is press-fitted to the inlet side of 0 to dilute the concentrated liquid and intermediate liquid in this part. Therefore, as in the case of the first and second embodiments,
In the absorber 7, the absorption liquid concentration is greatly reduced and the ability to absorb the refrigerant is reduced, and the evaporation of the refrigerant in the evaporator 6 is suppressed. Therefore, the chilled water in the chilled water pipe 26 becomes supercooled or the refrigerant is frozen. That is avoided.

【0024】(実施例4) 図4に基づいて第4の実施例を説明する。ここに例示し
た吸収冷凍機は、図2に示した吸収冷凍機における温度
検出器31に代えて、温度検出器33を吸収器7に流入
する冷却水の温度が検出可能に、冷却水管27の吸収器
7入口部に設けたものである。この場合も、実施例1な
どと同様の機能を有する機器には同一の符号を付し、そ
の説明は実施例の理解を妨げない範囲で省略した。
(Embodiment 4) A fourth embodiment will be described with reference to FIG. The absorption chiller exemplified here uses a temperature detector 33 instead of the temperature detector 31 in the absorption chiller shown in FIG. 2 so that the temperature of the cooling water flowing into the absorber 7 can be detected. It is provided at the inlet of the absorber 7. Also in this case, the same reference numerals are given to the devices having the same functions as those in the first embodiment and the like, and the description thereof is omitted without impairing the understanding of the embodiments.

【0025】上記構成の吸収冷凍機においては、温度検
出器33が検出する冷却水温度が所定温度(例えば、2
6℃)に低下した時に、制御器29が前記第1の実施例
において吸収冷凍機本体停止時に前記制御器29が発信
したのと同様の制御信号を発信するよう設けてあるの
で、冷却水温度が所定温度に低下すると、冷却水ポンプ
28の運転が停止すると共に開閉弁19・20・21が
開いて吸収器7の吸収液が稀釈され、この稀釈された吸
収液が濃液管13の低温熱交換器9入口側および中間液
管12の高温熱交換器10入口側に圧入されてこの部分
の濃液および中間液を稀釈する。このため、前記実施例
1・2・3の場合と同様に、吸収器7では吸収液濃度が
大幅に低下して冷媒を吸収する能力が低下し、蒸発器6
における冷媒の蒸発が抑制されることから、冷水管26
の冷水が過冷却となったり冷媒が凍結すると云ったこと
が回避される。
In the absorption refrigerator having the above configuration, the cooling water temperature detected by the temperature detector 33 is equal to a predetermined temperature (for example, 2
When the temperature is lowered to 6 ° C.), the controller 29 is provided so as to transmit a control signal similar to that transmitted by the controller 29 when the absorption refrigerator is stopped in the first embodiment. Is lowered to a predetermined temperature, the operation of the cooling water pump 28 is stopped, and the on-off valves 19, 20, and 21 are opened to dilute the absorbent in the absorber 7, and the diluted absorbent is cooled to a low temperature in the concentrated pipe 13. It is press-fitted into the heat exchanger 9 inlet side and the high temperature heat exchanger 10 inlet side of the intermediate liquid pipe 12 to dilute the concentrated liquid and the intermediate liquid in this portion. Therefore, as in the case of the first, second and third embodiments, in the absorber 7, the absorption liquid concentration is greatly reduced, and the ability to absorb the refrigerant is reduced.
The evaporation of the refrigerant in the cooling water pipe 26 is suppressed.
It is avoided that the cold water becomes supercooled or the refrigerant freezes.

【0026】なお、本発明は上記実施例に限定されるも
のではないので、特許請求の範囲に記載の趣旨から逸脱
しない範囲で各種の変形実施が可能である。
Since the present invention is not limited to the above embodiment, various modifications can be made without departing from the spirit of the appended claims.

【0027】例えば、吸収液ポンプ14と分岐管22・
23との間の稀液管15に逆止弁34を設置して、吸収
液ポンプの運転停止時に濃液が吸収器7側に流入しない
ようにしたり、分岐管23に逆止弁35を設置して、濃
液が中間液側に流入しないようにすることも可能であ
る。
For example, the absorbent pump 14 and the branch pipe 22.
A check valve 34 is installed in the diluent pipe 15 between the suction pipe 23 and the suction pipe to prevent the concentrated liquid from flowing into the absorber 7 when the operation of the absorbent pump is stopped, or a check valve 35 is installed in the branch pipe 23. Thus, it is possible to prevent the concentrated liquid from flowing into the intermediate liquid.

【0028】また、温度検出器31は冷媒液溜め24に
ある冷媒の温度を検出するように設置しても良いし、温
度検出器32は蒸発器6に流入する冷水の温度あるいは
蒸発器6で冷却されている冷水の温度を検出するよう
に、蒸発器6の入口部や内部に設置することなども可能
である。
Further, the temperature detector 31 may be installed so as to detect the temperature of the refrigerant in the refrigerant reservoir 24, and the temperature detector 32 may be the temperature of the cold water flowing into the evaporator 6 or the temperature of the evaporator 6. It is also possible to install it at the inlet or inside the evaporator 6 so as to detect the temperature of the cooled cold water.

【0029】また、冷媒の温度を検出する温度検出器3
1と、冷水の温度を検出する温度検出器32と、冷却水
の温度を検出する温度検出器33とを、同時に2個ある
いは3個設置しておき、これらが同時に所定の温度を計
測した時に、制御器29が冷却水ポンプ28を停止する
と共に、開閉弁19・20・21を開く構成とすること
も可能である。
A temperature detector 3 for detecting the temperature of the refrigerant
1, two or three temperature detectors 32 for detecting the temperature of the cooling water, and two or three temperature detectors 33 for detecting the temperature of the cooling water are installed at the same time. It is also possible that the controller 29 stops the cooling water pump 28 and opens the on-off valves 19, 20, and 21.

【0030】また、分岐管22・23の何れか一方のみ
を設置する構成の吸収冷凍機とすることもできる。
An absorption refrigerator having only one of the branch pipes 22 and 23 may be provided.

【0031】また、気泡ポンプ8の代わりに通常の冷媒
ポンプとしたり、分離器3を有しない構造の吸収冷凍機
とすることなども可能である。
It is also possible to use a normal refrigerant pump instead of the bubble pump 8 or an absorption refrigerator having no separator 3.

【0032】[0032]

【発明の効果】以上説明したように本発明になる吸収冷
凍機は、吸収器、蒸発器、凝縮器、高温再生器、低温再
生器、低温熱交換器、高温熱交換器および吸収液ポンプ
を配管接続して冷媒と吸収液の循環サイクルを形成する
二重効用吸収冷凍機において、吸収液ポンプの吐出側配
管と、低温再生器から低温熱交換器に至る濃液配管およ
び高温再生器から高温熱交換器に至る中間液配管の少な
くとも何れかとを、通常閉の開閉弁が介在し、稀液吐出
口が被流入側配管の液流れ方向に開口している分岐管を
介して連通可能に接続すると共に、吸収冷凍機の運転停
止時に前記開閉弁を開にする制御器を設けたことを特徴
とする吸収冷凍機であり、
As described above, the absorption refrigerator according to the present invention comprises an absorber, an evaporator, a condenser, a high-temperature regenerator, a low-temperature regenerator, a low-temperature heat exchanger, a high-temperature heat exchanger and an absorbent pump. In a double-effect absorption refrigerator that connects the pipes to form a circulation cycle of the refrigerant and the absorption liquid, the piping on the discharge side of the absorption pump, the concentrated liquid piping from the low-temperature regenerator to the low-temperature heat exchanger, and the high-temperature regenerator At least one of the intermediate liquid pipes leading to the heat exchanger is connected to be able to communicate via a branch pipe with a normally closed on-off valve and a dilute liquid discharge port opened in the liquid flow direction of the inflow side pipe. And an absorption refrigerator characterized by having a controller that opens the on-off valve when the operation of the absorption refrigerator is stopped,

【0033】吸収器、蒸発器、凝縮器、高温再生器、低
温再生器、低温熱交換器、高温熱交換器および吸収液ポ
ンプを配管接続して冷媒と吸収液の循環サイクルを形成
する二重効用吸収冷凍機において、吸収液ポンプの吐出
側配管と、低温再生器から低温熱交換器に至る濃液配管
とを、通常閉の開閉弁が介在し、稀液吐出口が被流入側
配管の液流れ方向に開口している分岐管を介して連通可
能に接続すると共に、少なくとも冷水温度か冷却水温度
か蒸発器における冷媒温度の何れかが所定温度に低下し
た時に、前記開閉弁を開にする制御器を設けたことを特
徴とする吸収冷凍機であるので、
[0033] Duplexing which connects the absorber, evaporator, condenser, high-temperature regenerator, low-temperature regenerator, low-temperature heat exchanger, high-temperature heat exchanger and absorbent pump to form a circulation cycle of refrigerant and absorbent. In a utility absorption refrigerator, a normally closed on-off valve is interposed between the discharge pipe of the absorption pump and the concentrated pipe from the low-temperature regenerator to the low-temperature heat exchanger, and the diluted liquid discharge port is connected to the inflow pipe. Connected communicably via a branch pipe that opens in the liquid flow direction, and when at least one of the chilled water temperature, the chilled water temperature, or the refrigerant temperature in the evaporator drops to a predetermined temperature, the on-off valve is opened. Since it is an absorption refrigerator characterized by having a controller that performs

【0034】吸収冷凍機本体の運転が停止するか、冷水
温度が所定温度に低下するか、冷却水温度が所定温度に
低下するか、蒸発器における冷媒温度が所定温度に低下
した時などに、分岐管の開閉弁が開いて稀液が吸収液ポ
ンプにより、低温再生器から低温熱交換器に至る濃液配
管および/または高温再生器から高温熱交換器に至る中
間液配管に供給されて、濃液管内の濃液や中間液管内の
中間液が短時間で稀釈される。このため、冷凍能力が速
やかに低下し、蒸発器の圧力が上昇するので、冷水が過
冷却となったり、冷媒が凍結すると云ったことがなくな
る。また、濃度差の著しく大きい冷媒と吸収液とを混合
することがないので、大きな音や振動を発生する懸念が
ない。さらに、冷水温度が低下した時にも、機器全体の
吸収液濃度を速やかに低下させることができ、この結果
として冷水温度が低下した時にも確実に吸収液を稀釈す
ることができるなど、顕著な効果を奏するものである。
When the operation of the absorption refrigerator is stopped, when the temperature of the cooling water drops to a predetermined temperature, when the temperature of the cooling water drops to a predetermined temperature, or when the temperature of the refrigerant in the evaporator drops to a predetermined temperature, The on / off valve of the branch pipe is opened and the diluted liquid is supplied to the concentrated liquid pipe from the low-temperature regenerator to the low-temperature heat exchanger and / or the intermediate liquid pipe from the high-temperature regenerator to the high-temperature heat exchanger by the absorbing liquid pump. The concentrated liquid in the concentrated liquid tube and the intermediate liquid in the intermediate liquid tube are diluted in a short time. For this reason, the refrigerating capacity is quickly reduced and the pressure of the evaporator is increased, so that the cooling water is not overcooled or the refrigerant is not frozen. Further, since there is no mixing of the refrigerant and the absorbing liquid having a remarkably large concentration difference, there is no fear of generating a loud noise or vibration. Furthermore, even when the temperature of the chilled water is reduced, the concentration of the absorbing solution in the entire apparatus can be rapidly reduced, and as a result, the absorbing solution can be reliably diluted even when the temperature of the chilled water is reduced. Is played.

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

【図1】実施例1の説明図である。FIG. 1 is an explanatory diagram of a first embodiment.

【図2】実施例2の説明図である。FIG. 2 is an explanatory diagram of a second embodiment.

【図3】実施例3の説明図である。FIG. 3 is an explanatory diagram of a third embodiment.

【図4】実施例4の説明図である。FIG. 4 is an explanatory diagram of a fourth embodiment.

【図5】分岐管の配管説明図である。FIG. 5 is an explanatory diagram of piping of a branch pipe.

【符号の説明】[Explanation of symbols]

1 高温再生器 2 燃焼装置 3 分離器 4 低温再生器 5 凝縮器 6 蒸発器 7 吸収器 8 気泡ポンプ 9 低温熱交換器 10 高温熱交換器 11 揚液管 12 中間液管 13 濃液管 14 吸収液ポンプ 15 稀液管 16 冷媒導管 17 冷媒液管 18 冷媒還流管 19・20・21 開閉弁 22・23 分岐管 24 冷媒液溜め 25 冷媒ブロー管 26 冷水管 27 冷却水管 28 冷却水ポンプ 29 制御器 30 冷媒分配器 31・32・33 温度検出器 34・35 逆止弁 DESCRIPTION OF SYMBOLS 1 High temperature regenerator 2 Combustion apparatus 3 Separator 4 Low temperature regenerator 5 Condenser 6 Evaporator 7 Absorber 8 Bubble pump 9 Low temperature heat exchanger 10 High temperature heat exchanger 11 Pumping pipe 12 Intermediate liquid pipe 13 Concentrated liquid pipe 14 Absorption Liquid pump 15 Dilute liquid pipe 16 Refrigerant conduit 17 Refrigerant liquid pipe 18 Refrigerant recirculation pipe 19, 20, 21 Open / close valve 22, 23 Branch pipe 24 Refrigerant liquid reservoir 25 Refrigerant blow pipe 26 Cold water pipe 27 Cooling water pipe 28 Cooling water pump 29 Controller 30 Refrigerant distributor 31 ・ 32 ・ 33 Temperature detector 34 ・ 35 Check valve

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平4−363562(JP,A) 特開 昭55−17065(JP,A) 特開 平4−340066(JP,A) 実開 昭54−155656(JP,U) (58)調査した分野(Int.Cl.7,DB名) F25B 15/00 306 F25B 41/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-4-363562 (JP, A) JP-A-55-17065 (JP, A) JP-A-4-340066 (JP, A) 155656 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) F25B 15/00 306 F25B 41/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 吸収器、蒸発器、凝縮器、高温再生器、
低温再生器、低温熱交換器、高温熱交換器および吸収液
ポンプを配管接続して冷媒と吸収液の循環サイクルを形
成する二重効用吸収冷凍機において、吸収液ポンプの吐
出側配管と、低温再生器から低温熱交換器に至る濃液配
管および高温再生器から高温熱交換器に至る中間液配管
の少なくとも何れかとを、通常閉の開閉弁が介在し、稀
液吐出口が被流入側配管の液流れ方向に開口している分
岐管を介して連通可能に接続すると共に、吸収冷凍機の
運転停止時に前記開閉弁を開にする制御器を設けたこと
を特徴とする吸収冷凍機。
1. An absorber, an evaporator, a condenser, a high-temperature regenerator,
In a double-effect absorption refrigerator in which a low-temperature regenerator, a low-temperature heat exchanger, a high-temperature heat exchanger and an absorption liquid pump are connected by piping to form a circulation cycle of the refrigerant and the absorption liquid, the discharge-side piping of the absorption liquid pump and the low-temperature At least one of the concentrated liquid pipe from the regenerator to the low-temperature heat exchanger and the intermediate liquid pipe from the high-temperature regenerator to the high-temperature heat exchanger is provided with a normally closed on-off valve, and the diluted liquid discharge port is connected to the inflow side pipe. And a controller that opens and closes the on-off valve when the operation of the absorption chiller is stopped, the controller being connected to be communicable via a branch pipe that opens in the liquid flow direction.
【請求項2】 吸収器、蒸発器、凝縮器、高温再生器、
低温再生器、低温熱交換器、高温熱交換器および吸収液
ポンプを配管接続して冷媒と吸収液の循環サイクルを形
成する二重効用吸収冷凍機において、吸収液ポンプの吐
出側配管と、低温再生器から低温熱交換器に至る濃液配
管とを、通常閉の開閉弁が介在し、稀液吐出口が被流入
側配管の液流れ方向に開口している分岐管を介して連通
可能に接続すると共に、少なくとも冷水温度か冷却水温
度か蒸発器における冷媒温度の何れかが所定温度に低下
した時に、前記開閉弁を開にする制御器を設けたことを
特徴とする吸収冷凍機。
2. An absorber, an evaporator, a condenser, a high-temperature regenerator,
In a double-effect absorption refrigerator in which a low-temperature regenerator, a low-temperature heat exchanger, a high-temperature heat exchanger and an absorption liquid pump are connected by piping to form a circulation cycle of the refrigerant and the absorption liquid, the discharge-side piping of the absorption liquid pump and the low-temperature The concentrated liquid pipe from the regenerator to the low-temperature heat exchanger can communicate with the concentrated liquid pipe through a branch pipe with a normally closed on-off valve and a diluted liquid discharge port opened in the liquid flow direction of the inflow side pipe. An absorption refrigerator connected with a controller that opens the on-off valve when at least one of the chilled water temperature, the chilled water temperature, and the refrigerant temperature in the evaporator drops to a predetermined temperature.
JP06269193A 1993-02-26 1993-02-26 Absorption refrigerator Expired - Fee Related JP3167491B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06269193A JP3167491B2 (en) 1993-02-26 1993-02-26 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06269193A JP3167491B2 (en) 1993-02-26 1993-02-26 Absorption refrigerator

Publications (2)

Publication Number Publication Date
JPH06249538A JPH06249538A (en) 1994-09-06
JP3167491B2 true JP3167491B2 (en) 2001-05-21

Family

ID=13207572

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06269193A Expired - Fee Related JP3167491B2 (en) 1993-02-26 1993-02-26 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JP3167491B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5457163B2 (en) * 2009-12-21 2014-04-02 川重冷熱工業株式会社 Control method and apparatus for absorption chiller / heater using exhaust gas of distributed power generation system

Also Published As

Publication number Publication date
JPH06249538A (en) 1994-09-06

Similar Documents

Publication Publication Date Title
JP2008116173A (en) Absorption type refrigerating machine
KR100337209B1 (en) Method of stopping an absorption refrigerator
JP3167491B2 (en) Absorption refrigerator
JPS62186178A (en) Absorption refrigerator
JP2003194427A (en) Cooling device
JP3081472B2 (en) Control method of absorption refrigerator
JP4279917B2 (en) Absorption refrigerator
KR20180085363A (en) Low load control system for 2-stage low temperature hot water absorption chiller
JP3143227B2 (en) Refrigerant freezing prevention device for absorption refrigerator
JP3133538B2 (en) Absorption refrigerator
KR200308240Y1 (en) Absorption refrigerator with preventing the crystallization of a solution
JPH05312430A (en) Absorption refrigerator
JP2011220675A (en) Absorption refrigerating machine
JP3142997B2 (en) Air conditioner using absorption refrigerator
KR100214171B1 (en) Absorption type cooler
JP2940787B2 (en) Double effect absorption refrigerator
JPH04295558A (en) Absorption refrigerator
JP3188111B2 (en) Absorption chiller / heater and control method thereof
JP3429904B2 (en) Absorption refrigerator
JP2001317835A (en) Absorption refrigeration machine
JP3174674B2 (en) Air conditioner using absorption refrigerator
KR950008337B1 (en) By-pass line in absorption refregerator
JPS6135893Y2 (en)
JP3313486B2 (en) Air conditioner using absorption refrigerator
JPS58124177A (en) Water-lithium salt absorption type refrigerator

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090309

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100309

Year of fee payment: 9

LAPS Cancellation because of no payment of annual fees