JPH0439589B2 - - Google Patents

Info

Publication number
JPH0439589B2
JPH0439589B2 JP18129883A JP18129883A JPH0439589B2 JP H0439589 B2 JPH0439589 B2 JP H0439589B2 JP 18129883 A JP18129883 A JP 18129883A JP 18129883 A JP18129883 A JP 18129883A JP H0439589 B2 JPH0439589 B2 JP H0439589B2
Authority
JP
Japan
Prior art keywords
absorption
refrigerant
pump
absorption liquid
stopped
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
JP18129883A
Other languages
Japanese (ja)
Other versions
JPS6071867A (en
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 filed Critical
Priority to JP18129883A priority Critical patent/JPS6071867A/en
Publication of JPS6071867A publication Critical patent/JPS6071867A/en
Publication of JPH0439589B2 publication Critical patent/JPH0439589B2/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
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/006Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、水−臭化リチウムやアルコール−塩
化リチウムなど塩類溶液を吸収液に用いるように
した吸収冷凍機の冷凍運転を停止する際に、吸収
液の吸収剤濃度を低くするために吸収冷凍機を運
転する装置すなわち吸収冷凍機の稀釈運転装置の
改良に関する。
[Detailed description of the invention] (a) Industrial application field The present invention is applicable to stopping the refrigeration operation of an absorption refrigerator using a salt solution such as water-lithium bromide or alcohol-lithium chloride as an absorption liquid. The present invention relates to an apparatus for operating an absorption refrigerating machine to lower the absorbent concentration of an absorption liquid, that is, an improvement of a dilution operating apparatus for an absorption refrigerating machine.

(ロ) 従来技術 吸収冷凍機においては、効率の良い冷凍運転を
行うために、例えば臭化リチウム水溶液の臭化リ
チウム濃度を62%程度に高めている。そのため、
冷凍運転の停止時、外気温が低いと吸収液(臭化
リチウム水溶液)が結晶して次の冷凍運転の再開
に支障を来す。それ故、塩類溶液を用いる吸収冷
凍機(以下、この種の吸収冷凍機という)におい
ては、冷凍運転の停止時に吸収液の濃度を低くす
るための運転すなわち稀釈運転を行う必要があ
る。そして、従来、この稀釈運転は、発生器の加
熱を停止した後も、吸収液の濃度が十分に低下す
るまで吸収液用のポンプ、冷媒用のポンプ、冷却
水用のポンプおよび冷水用のポンプを作動し続け
ることによつて、行われている。
(b) Prior art In absorption refrigerators, the concentration of lithium bromide in an aqueous lithium bromide solution is increased to about 62%, for example, in order to perform efficient refrigeration operation. Therefore,
When the refrigeration operation is stopped, if the outside temperature is low, the absorption liquid (lithium bromide aqueous solution) will crystallize, which will hinder the resumption of the next refrigeration operation. Therefore, in an absorption refrigerator using a salt solution (hereinafter referred to as this type of absorption refrigerator), it is necessary to perform an operation to lower the concentration of the absorption liquid, that is, a dilution operation, when stopping the refrigeration operation. Conventionally, this dilution operation is continued even after the heating of the generator is stopped, until the concentration of the absorption liquid is sufficiently reduced. This is done by keeping the .

このような従来の稀釈運転方法は、稀釈運転の
初期には冷凍能力を発揮できる利点すなわち低温
の冷水が暫くは得られる利点を有するものの、稀
釈運転の完了までに時間がかかり過ぎる欠点を有
している。
Although such conventional dilution operation methods have the advantage of being able to utilize the refrigerating capacity at the beginning of the dilution operation, that is, the advantage of being able to obtain low-temperature cold water for a while, they have the disadvantage that it takes too much time to complete the dilution operation. ing.

(ハ) 発明の目的 本発明は、この種の吸収冷凍機において、稀釈
運転の時間を短かくすることのできる装置の提供
を目的としたものである。
(c) Purpose of the Invention The purpose of the present invention is to provide an apparatus that can shorten the dilution operation time in this type of absorption refrigerator.

(ニ) 発明の構成 本発明は、この種の吸収冷凍機において、冷凍
運転を停止する際、発生器の加熱、冷却水用のポ
ンプ、および吸収液用のポンプを停止し、かつ、
この吸収液用のポンプをタイマーにより所定時間
経過後に再び作動させて吸収液を一定時間稀釈す
るように構成したものである。
(d) Structure of the Invention The present invention provides that in this type of absorption refrigerator, when stopping the refrigeration operation, the generator heating, the cooling water pump, and the absorption liquid pump are stopped, and
The absorbent pump is configured to be activated again after a predetermined time has elapsed using a timer to dilute the absorbent for a predetermined period of time.

本発明によれば、冷凍運転の停止後、短時間で
凝縮器内に残留している冷媒液の殆んどが吸収器
内の吸収液に混入するので、冷媒能力を徐々に低
下させつつ吸収液を稀釈する従来の装置にくら
べ、稀釈運転の時間を短かくすることができる。
According to the present invention, most of the refrigerant liquid remaining in the condenser is mixed into the absorption liquid in the absorber in a short time after the refrigeration operation is stopped, so that the refrigerant capacity is gradually reduced and absorbed. Compared to conventional devices for diluting liquid, the dilution operation time can be shortened.

(ホ) 実施例 図面は本発明装置の一実施例を示す概略構成説
明図であり、1は高温発生器、2は低温発生器、
3は凝縮器、4は蒸発器、5は吸収器、6は低温
溶液熱交換器、7は高温溶液熱交換器、8は吸収
液用のポンプ(以下、溶液ポンプという)、9は
冷媒用のポンプ(以下、冷媒ポンプという)で、
これら機器は冷媒の流れる管10,10′、冷媒
液の流下する管11、冷媒液の還流する管12,
12′、吸収液の流れる管13,13′,14,1
4′,15,15′で接続されて冷媒と吸収液の循
環路を構成している。
(E) Embodiment The drawing is a schematic configuration explanatory diagram showing an embodiment of the device of the present invention, in which 1 is a high temperature generator, 2 is a low temperature generator,
3 is a condenser, 4 is an evaporator, 5 is an absorber, 6 is a low temperature solution heat exchanger, 7 is a high temperature solution heat exchanger, 8 is a pump for absorption liquid (hereinafter referred to as solution pump), 9 is for refrigerant pump (hereinafter referred to as refrigerant pump),
These devices include pipes 10 and 10' through which the refrigerant flows, a pipe 11 through which the refrigerant liquid flows, a pipe 12 through which the refrigerant liquid flows back,
12', pipes 13, 13', 14, 1 through which absorption liquid flows
4', 15, and 15' to form a circulation path for refrigerant and absorption liquid.

16は蒸発器4に内蔵した冷水器、17,18
は吸収器5、凝縮器3にそれぞれ内蔵した冷却
器、19は低温発生器2に内蔵した給熱器、20
は高温発生器1に内蔵した加熱器である。21,
21′は冷水の流れる管、22,22′,22″は
冷却水の流れる管、23,23′は熱源蒸気の流
れる管で、24は管21に備えた冷水用のポンプ
(以下、冷水ポンプという)、25は管22″に備
えた冷却水用のポンプ(以下、冷却水ポンプとい
う)、26は管23′に備えた弁である。27,2
8は凝縮器3、蒸発器4の冷媒液溜め、29,3
0,31は低温発生器2、高温発生器1、吸収器
5の溶液溜めである。
16 is a water cooler built into the evaporator 4, 17, 18
are coolers built into the absorber 5 and condenser 3, 19 is a heat feeder built into the low temperature generator 2, and 20
is a heater built into the high temperature generator 1. 21,
21' is a pipe through which cold water flows, 22, 22', 22'' are pipes through which cooling water flows, 23, 23' are pipes through which heat source steam flows, and 24 is a cold water pump provided in the pipe 21 (hereinafter referred to as cold water pump). ), 25 is a cooling water pump (hereinafter referred to as cooling water pump) provided in the pipe 22'', and 26 is a valve provided in the pipe 23'. 27,2
8 is a refrigerant liquid reservoir for the condenser 3 and evaporator 4, 29,3
0 and 31 are solution reservoirs for the low temperature generator 2, high temperature generator 1, and absorber 5.

32は運転の発停を行う制御器で、この制御器
にはタイマーと発停スイツチが内蔵されており、
停止スイツチにより溶液ポンプ8、冷媒ポンプ
9、冷水ポンプ24および冷却水ポンプ25の作
動が停止されると共に弁26が閉じられるように
なつている。そして、制御器32のタイマーによ
り、溶液ポンプ8が停止してから所定の時間(お
よそ20分)経過した後、再び溶液ポンプ8が一定
時間(およそ5分)作動するようになつている。
32 is a controller for starting and stopping the operation, and this controller has a built-in timer and a start/stop switch.
The stop switch stops the operation of the solution pump 8, refrigerant pump 9, cold water pump 24, and cooling water pump 25, and closes the valve 26. The timer of the controller 32 causes the solution pump 8 to operate again for a predetermined period of time (approximately 5 minutes) after a predetermined period of time (approximately 20 minutes) has elapsed since the solution pump 8 was stopped.

なお、33は管15′の低温溶液熱交換器6近
傍の位置に備えたサーモスタツトで、このサーモ
スタツトはその感知温度が設定温度以下になると
停止された溶液ポンプ8を作動させる機能を有し
ている。すなわち、冷凍運転が停止されてから所
定の時間(およそ20分)が経過するまでに、管1
5′および低温溶液熱交換器6内の濃度の高い吸
収液(濃液)が外気の影響で結晶温度に近ずいた
場合、この濃液を溶液ポンプ8によつて送られる
吸収液(稀釈)で昇温かつ稀釈して濃液の結晶化
を防止するようにしているのである。
In addition, 33 is a thermostat provided in the vicinity of the low-temperature solution heat exchanger 6 in the pipe 15', and this thermostat has a function of operating the solution pump 8 which has been stopped when the detected temperature falls below the set temperature. ing. In other words, by the time a predetermined period of time (approximately 20 minutes) has elapsed after the refrigeration operation was stopped, the pipe 1
5' and the high-concentration absorption liquid (concentrated liquid) in the low-temperature solution heat exchanger 6 approaches the crystallization temperature due to the influence of outside air, this concentrated liquid is transferred to the absorption liquid (diluted) sent by the solution pump 8. This is to prevent the concentrated liquid from crystallizing by raising the temperature and diluting it.

次に、このように構成された吸収冷凍機の稀釈
運転装置(以下、本装置という)の動作例を、冷
凍能力を徐々に低下させつつ吸収液を稀釈する従
来の装置の動作と比較して、説明する。
Next, we will compare an example of the operation of the absorption chiller dilution operation device (hereinafter referred to as this device) configured in this way with the operation of a conventional device that dilutes the absorption liquid while gradually decreasing the refrigerating capacity. ,explain.

本装置において、冷凍運転の停止時、制御器3
2の停止スイツチにより弁26が全閉されると共
にポンプ8,9,24,25の作動が停止され
る。弁26が全閉されて高温発生器1の加熱が停
止されると、この発生器の冷媒を分離する機能が
停止し、かつ、低温発生器2の冷媒を分離する機
能も殆んど停止する。冷却水ポンプ8が停止され
て冷却器17,18に冷却水が通水されなくなる
と、冷却器17に散布された濃液が降温しなくな
つて吸収器5の冷媒を吸収する機能が停止し、か
つ凝縮器3の冷媒を凝縮する機能も停止する。ま
た、冷媒ポンプ9および冷水ポンプ24が停止す
ると、蒸発器4の冷媒を蒸発させる機能も停止す
る。その結果、冷媒と吸収液の循環による吸収冷
凍サイクルが短時間で形成されなくなる一方、残
留している冷媒と吸収液の余熱によつて凝縮器3
側の圧力が蒸発器4側の圧力よりも暫くの時間
(およそ60分)高く保たれるため、その間に凝縮
器3の冷媒液溜め27に残留している冷媒液の殆
んどが圧力差と落差とにより管11、蒸発器4の
冷媒液溜め28を経て吸収器5の溶液溜め31へ
流下し、この溶液溜めの吸収液が稀釈される。そ
して、制御器32に内蔵されているタイマーによ
り溶液ポンプ8が停止してから所定の時間(およ
そ20分)経過後に一定時間(およそ5分)再作動
され、溶液溜め31の稀釈された吸収液が吸収液
の循環路を循環しつつこの循環路内に残留してい
た吸収液の濃度を低下させる。このようにして本
装置の稀釈運転は完了する。
In this device, when the refrigeration operation is stopped, the controller 3
The stop switch No. 2 completely closes the valve 26 and stops the operation of the pumps 8, 9, 24, and 25. When the valve 26 is fully closed and the heating of the high temperature generator 1 is stopped, the function of separating the refrigerant of this generator is stopped, and the function of separating the refrigerant of the low temperature generator 2 is also almost completely stopped. . When the cooling water pump 8 is stopped and cooling water is no longer passed through the coolers 17 and 18, the temperature of the concentrated liquid sprayed in the cooler 17 no longer decreases, and the function of the absorber 5 to absorb refrigerant stops. , and the function of condensing the refrigerant of the condenser 3 also stops. Moreover, when the refrigerant pump 9 and the cold water pump 24 stop, the function of evaporating the refrigerant of the evaporator 4 also stops. As a result, an absorption refrigeration cycle due to the circulation of the refrigerant and absorption liquid is no longer formed in a short time, and the residual heat of the remaining refrigerant and absorption liquid causes the condenser 3
Since the pressure on the side of the evaporator 4 is maintained higher than the pressure on the side of the evaporator 4 for a while (approximately 60 minutes), most of the refrigerant liquid remaining in the refrigerant reservoir 27 of the condenser 3 is absorbed by the pressure difference. The refrigerant liquid flows down to the solution reservoir 31 of the absorber 5 through the pipe 11 and the refrigerant reservoir 28 of the evaporator 4 due to the head difference, and the absorbed liquid in this solution reservoir is diluted. Then, after a predetermined time (approximately 20 minutes) has elapsed since the solution pump 8 was stopped by a timer built in the controller 32, it is restarted for a certain period of time (approximately 5 minutes), and the diluted absorption liquid in the solution reservoir 31 is While circulating through the absorption liquid circulation path, the concentration of the absorption liquid remaining in this circulation path is reduced. In this way, the dilution operation of this device is completed.

これに対して、従来の装置においては、冷凍運
転の停止時に、弁26のみを全閉にしてポンプ
8,9,24,25を作動しているために、高温
発生器1の機能は停止するものの、吸収器5、凝
縮器3、蒸発器4および低温発生器2の機能は完
全に停止しない。その結果、冷凍運転がかなりの
時間継続されている状態となり、その分稀釈運転
時間(およそ30分)が長くなる。
On the other hand, in the conventional device, when the refrigeration operation is stopped, only the valve 26 is fully closed and the pumps 8, 9, 24, and 25 are operated, so the function of the high temperature generator 1 is stopped. However, the functions of the absorber 5, condenser 3, evaporator 4, and low temperature generator 2 do not completely stop. As a result, the refrigeration operation continues for a considerable period of time, and the dilution operation time (approximately 30 minutes) increases accordingly.

このように、従来の装置においては稀釈運転時
間がおよそ30分であるのに対して本装置において
はおよそ5分であり、本装置は従来の装置よりも
稀釈運転時間を約1/6に短縮できる。
In this way, the dilution operation time for the conventional device is approximately 30 minutes, whereas for this device it is approximately 5 minutes, and this device reduces the dilution operation time to approximately 1/6 of that of the conventional device. can.

なお、実施例においては、弁26を全閉すると
同時に冷媒ポンプ9および冷水ポンプ24を停止
しているが、これらポンプ9,24を作動させて
いても本発明装置の稀釈運転時間はこれらポンプ
を停止した場合と大差ない。その理由は、冷却水
ポンプ25の停止によつて吸収器5の冷媒を吸収
する機能が停止する結果、蒸発器4において冷媒
が蒸発できなくなり、すぐに吸収冷凍サイクルが
形成されなくなるからである。尤も、これらポン
プ9,24を停止する方が、これらポンプの動力
費を節約できるので、好ましい。
In the embodiment, the refrigerant pump 9 and the cold water pump 24 are stopped at the same time as the valve 26 is fully closed, but even if these pumps 9 and 24 are operated, the dilution operation time of the present invention apparatus is limited to the time when these pumps are operated. It's not much different than if it stopped. This is because the refrigerant absorption function of the absorber 5 is stopped due to the stoppage of the cooling water pump 25, and as a result, the refrigerant cannot be evaporated in the evaporator 4, and an absorption refrigeration cycle is not formed immediately. Of course, it is preferable to stop these pumps 9 and 24 because the power costs for these pumps can be saved.

なおまた、実施例においては、溶液ポンプ8の
停止から再び作動させるまでの時間がおよそ20
分、溶液ポンプ8の再作動の時間がおよそ5分と
なるようにタイマーを設定したが、このタイマー
の設定は吸収冷凍機の型式〔一重効用型、多重効
用型〕、塩類溶液の種類、吸収冷凍機の容量など
の仕様に応じて適宜選定される。
Furthermore, in the embodiment, the time from stopping the solution pump 8 to starting it again is about 20 minutes.
The timer was set so that the reactivation time of the solution pump 8 would be approximately 5 minutes, but the settings of this timer depend on the type of absorption refrigerator (single effect type, multiple effect type), type of saline solution, absorption It is selected as appropriate depending on the specifications such as the capacity of the refrigerator.

また、管21に低温の熱源水を流して管22″
から温水を取出す場合、すなわち、吸収冷凍機を
ヒートポンプとして用いる場合にも、本発明装置
を適用できることは勿論である。
In addition, by flowing low-temperature heat source water into the pipe 21, the pipe 22''
It goes without saying that the device of the present invention can also be applied when hot water is extracted from a refrigerator, that is, when an absorption refrigerator is used as a heat pump.

(ヘ) 発明の効果 以上のように、本発明装置は、この種の吸収冷
凍機において、冷凍運転の停止後凝縮器に残留し
ている冷媒液の殆んどが短時間で吸収器内の吸収
液中に流入するように冷却水の通水と吸収液の循
環を止め、さらに、冷媒液が流入して濃度の低く
なつた吸収液を再循環させているので、従来の装
置にくらべて稀釈運転を大巾に短縮できる。
(f) Effects of the Invention As described above, the device of the present invention, in this type of absorption refrigerator, can quickly remove most of the refrigerant liquid remaining in the condenser after stopping the refrigeration operation. The flow of cooling water and the circulation of the absorption liquid are stopped so that the cooling water flows into the absorption liquid, and the absorption liquid whose concentration has become low due to the flow of refrigerant liquid is recirculated, so this system is more effective than conventional equipment. Dilution operation can be greatly shortened.

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

図面は本発明装置の一実施例を示す概略構成説
明図である。 1……高温発生器、2……低温発生器、3……
凝縮器、4……蒸発器、5……吸収器、8……溶
液ポンプ、9……冷媒ポンプ、24……冷水ポン
プ、25……冷却水ポンプ、26……弁、32…
…制御器。
The drawing is a schematic structural explanatory diagram showing an embodiment of the device of the present invention. 1... High temperature generator, 2... Low temperature generator, 3...
Condenser, 4... Evaporator, 5... Absorber, 8... Solution pump, 9... Refrigerant pump, 24... Chilled water pump, 25... Cooling water pump, 26... Valve, 32...
...Controller.

Claims (1)

【特許請求の範囲】[Claims] 1 臭化リチウム水溶液その他の塩類溶液を吸収
液に用いるようにした吸収冷凍機において、運転
を停止する際に、発生器の加熱、冷却水用のポン
プ、および吸収液用のポンプを停止し、かつ、こ
の吸収液用のポンプをタイマーにより所定時間経
過後に再び作動させて吸収液を一定時間稀釈する
ようにしたことを特徴とする吸収冷凍機の稀釈運
転装置。
1. In an absorption refrigerator that uses an aqueous lithium bromide solution or other salt solution as the absorption liquid, when stopping operation, stop the generator heating, the cooling water pump, and the absorption liquid pump, A dilution operation device for an absorption refrigerator, characterized in that the absorption liquid pump is operated again after a predetermined time has elapsed using a timer to dilute the absorption liquid for a certain period of time.
JP18129883A 1983-09-28 1983-09-28 Diluting operating device for absorption refrigerator Granted JPS6071867A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18129883A JPS6071867A (en) 1983-09-28 1983-09-28 Diluting operating device for absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18129883A JPS6071867A (en) 1983-09-28 1983-09-28 Diluting operating device for absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS6071867A JPS6071867A (en) 1985-04-23
JPH0439589B2 true JPH0439589B2 (en) 1992-06-30

Family

ID=16098231

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18129883A Granted JPS6071867A (en) 1983-09-28 1983-09-28 Diluting operating device for absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS6071867A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3283780B2 (en) * 1997-03-03 2002-05-20 リンナイ株式会社 Absorption cooling device
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
JPS6071867A (en) 1985-04-23

Similar Documents

Publication Publication Date Title
JP2560550B2 (en) Absorption cooling / heating device and control method thereof
US3296814A (en) Absorption refrigeration systems, methods, and absorbent compositions
JP3223122B2 (en) Method of stopping operation of absorption refrigeration system
US4445340A (en) Dilution cycle control for an absorption refrigeration system
JPH0439589B2 (en)
JP2009243705A (en) Absorption heat pump
KR102010832B1 (en) Low load control system for 2-stage low temperature hot water absorption chiller
JP3280169B2 (en) Double effect absorption refrigerator and chiller / heater
JPS6086353A (en) Preventive device for crystal of absorption refrigerator
JPS62106268A (en) Absorption refrigerator
JP2757858B2 (en) Absorption chiller / heater and absorption chiller / heater using the same
KR100330542B1 (en) Absorption refrigerator
JPS6118368Y2 (en)
JP2000018759A (en) Absorption refrigerating machine
JPS62778A (en) Single-double effect absorption refrigerator
KR910008683Y1 (en) Absorption type refrigerator
JPH05113266A (en) Controller of absorption refrigerating machine
KR0124786B1 (en) Diluting operation apparatus for air-cooling absorptive type refrigerator and heater
JP4115020B2 (en) Control method of absorption refrigerator
JPS61143664A (en) Antifreezing device for refrigerant of absorption refrigerator
JPH02140564A (en) Controlling method for absorption refrigerator
JP2657701B2 (en) Operating method of absorption refrigeration system
JPS5813967A (en) Controller for absorption refrigerator
JPH0820141B2 (en) Absorption refrigerator
JPH02213659A (en) Absorption type freezer