JPS60144574A - Diluting device for absorption cold and hot water machine - Google Patents

Diluting device for absorption cold and hot water machine

Info

Publication number
JPS60144574A
JPS60144574A JP40684A JP40684A JPS60144574A JP S60144574 A JPS60144574 A JP S60144574A JP 40684 A JP40684 A JP 40684A JP 40684 A JP40684 A JP 40684A JP S60144574 A JPS60144574 A JP S60144574A
Authority
JP
Japan
Prior art keywords
refrigerant
absorption liquid
temperature regenerator
low
absorption
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP40684A
Other languages
Japanese (ja)
Inventor
片山 章文
木谷 紘一
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP40684A priority Critical patent/JPS60144574A/en
Publication of JPS60144574A publication Critical patent/JPS60144574A/en
Pending legal-status Critical Current

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  • 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、低温再生器を有する二重効用吸収冷温水機の
稀釈装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a dilution device for a dual-effect absorption chiller/heater with a low temperature regenerator.

従来例の構成とその問題点 第1図は従来の吸収冷温水機の稀釈装置を示すものであ
る。1は低温再生器で、内部には高温再生器で発生した
冷媒と熱交換する熱交換部2bを吸収液4中に有する冷
媒蒸気管2を備えている。
Structure of a conventional example and its problems FIG. 1 shows a dilution device for a conventional absorption chiller/heater. Reference numeral 1 designates a low-temperature regenerator, which includes a refrigerant vapor pipe 2 having a heat exchange section 2b in an absorption liquid 4 for exchanging heat with the refrigerant generated in the high-temperature regenerator.

冷媒蒸気3によって加熱された吸収液4は冷媒蒸気6を
発生し、凝縮器e内で凝縮冷媒7となる。
Absorbing liquid 4 heated by refrigerant vapor 3 generates refrigerant vapor 6, which becomes condensed refrigerant 7 in condenser e.

26−ツ 一方冷媒蒸気3は低温再生器1内で冷却され、凝縮冷媒
となって凝縮器6に入る。凝縮冷媒7は冷媒配管8,9
.10を通って蒸発器13に入り、冷媒ポンプ14によ
って冷水管15に散布される。
26-T On the other hand, the refrigerant vapor 3 is cooled in the low temperature regenerator 1 and enters the condenser 6 as a condensed refrigerant. The condensed refrigerant 7 is connected to refrigerant pipes 8 and 9
.. The refrigerant enters the evaporator 13 through the refrigerant pump 14 and is distributed to the cold water pipes 15 by the refrigerant pump 14 .

この際、冷房負荷に応じて、冷媒配管9,1oに設けた
制御弁11.12を開閉することによって冷媒循環量を
変化させる。すなわち、制御弁11あるいは12を開く
ことによって凝縮器θ内の凝縮冷媒7を蒸発器13へ多
く流すことによりて凝縮冷媒7は蒸発器13内のオーバ
ーフロ一部16から吸収器17に流入し、吸収液濃度を
変化させる。また低温再生器1で冷媒蒸気6を発生し濃
縮された吸収液4は低温再生器1を出て熱交換器を経た
後、吸収器17に導かれて散水管171Lより散布され
る。吸収器17内で蒸気を吸収した吸収液4は吸収液ポ
ンプ18によって機内に循環される。蒸発器13と吸収
器17のバイパス管19に設けられた制御弁2oは運転
停止時に開となり、蒸発器13内の凝縮冷媒液を吸収器
17へ送って吸収液濃度を低くする働きがある。
At this time, the amount of refrigerant circulation is changed by opening and closing control valves 11 and 12 provided in the refrigerant pipes 9 and 1o, depending on the cooling load. That is, by opening the control valve 11 or 12, a large amount of the condensed refrigerant 7 in the condenser θ is allowed to flow into the evaporator 13, so that the condensed refrigerant 7 flows from the overflow portion 16 in the evaporator 13 into the absorber 17. , change the absorbent concentration. Further, the absorbent liquid 4 which has been concentrated by generating refrigerant vapor 6 in the low temperature regenerator 1 exits the low temperature regenerator 1, passes through a heat exchanger, is led to the absorber 17, and is sprayed from the water sprinkler pipe 171L. The absorption liquid 4 that has absorbed vapor in the absorber 17 is circulated into the machine by an absorption liquid pump 18. The control valve 2o provided in the bypass pipe 19 of the evaporator 13 and the absorber 17 is opened when the operation is stopped, and has the function of sending the condensed refrigerant liquid in the evaporator 13 to the absorber 17 to lower the absorption liquid concentration.

3 、。3.

以上の従来例では、運転停止時の稀釈をするためには、
運転中に凝縮器6に貯えられた冷媒を蒸発器13に流す
ことにより、蒸発器13のオーバー7o一部16よりオ
ーバーフローさせて吸収器17に導くか、あるいは、蒸
発器13内に貯えられた冷媒をバイパス管19を通して
吸収器17内−に導き、吸収液ポンプ1Bで機内を循環
させることによって機内の吸収液を稀釈するものであっ
た。
In the conventional example above, in order to dilute when the operation is stopped,
By flowing the refrigerant stored in the condenser 6 into the evaporator 13 during operation, the refrigerant can overflow from the overflow part 16 of the evaporator 13 and be guided to the absorber 17, or the refrigerant stored in the evaporator 13 can be The refrigerant was introduced into the absorber 17 through the bypass pipe 19 and circulated within the machine by the absorption liquid pump 1B, thereby diluting the absorption liquid inside the machine.

このため、運転停止した際には吸収液ポンプ18による
一定時間の稀釈が必要であり運転中の停電の際には吸収
液ポンプ18が停止するため、吸収器17内の吸収液の
濃度が下げられたままで機内の吸収液の稀釈ができず、
特に吸収器の吸収能力を高めるため、濃度が高く結晶し
やすい吸収器散布溶液は、特に結晶しやすいという欠点
を有していた。
Therefore, when the operation is stopped, it is necessary to dilute the absorption liquid for a certain period of time using the absorption liquid pump 18, and if there is a power outage during operation, the absorption liquid pump 18 is stopped, so the concentration of the absorption liquid in the absorber 17 decreases. It was not possible to dilute the absorption liquid inside the aircraft as it remained
In particular, an absorber dispersion solution that is highly concentrated and tends to crystallize in order to increase the absorption capacity of the absorber has the disadvantage of being particularly prone to crystallization.

発明の目的 本発明は、上記欠点に鑑み、稀釈運転の時間を短縮する
とともに停電などにより吸収液ポンプが運転しない時で
も、運転中の吸収冷温水機の構成機器の圧力差を利用し
て稀釈することを目的とする。
Purpose of the Invention In view of the above-mentioned drawbacks, the present invention shortens the dilution operation time, and even when the absorption liquid pump is not operating due to a power outage, etc., the dilution can be carried out by utilizing the pressure difference between the components of the absorption water cooler/heater in operation. The purpose is to

発明の構成 この目的を達成するため、本発明は高温再生器で発生し
た冷媒蒸気が低温再生器で吸収液と熱交換した後の凝縮
冷媒を通す管と低温再生器の吸収液部との間に設け、か
つ開閉弁を有するバイパス管とから構成されており、こ
れによって運転を停止した時あるいは停電時など、高圧
・高温の凝縮冷媒を低圧再生器内の低圧の吸収液に、圧
力差を利用して導入し、最も結晶しやすい吸収液部を稀
釈するものである。
Structure of the Invention In order to achieve this object, the present invention provides a system between a pipe through which condensed refrigerant is passed after the refrigerant vapor generated in the high-temperature regenerator has exchanged heat with the absorption liquid in the low-temperature regenerator, and the absorption liquid part of the low-temperature regenerator. It consists of a bypass pipe with an on-off valve and a bypass pipe with an on-off valve.This allows the high-pressure, high-temperature condensed refrigerant to be transferred to the low-pressure absorption liquid in the low-pressure regenerator by creating a pressure difference when the operation is stopped or during a power outage. It is used to dilute the part of the absorption liquid that is most likely to crystallize.

実施例の説明 以下添付図面に基づいて本発明の一実施例について説明
する。同、従来例と同一部材については同一記号を用い
て説明する。第2図においては、高温再生器で発生した
冷媒蒸気を吸収液4と熱交換させる熱交換器2bの出口
2aと低温再生器1との間を接続したバイパス管、22
はバイパス管21に設けた制御弁、23は凝縮器6の底
部とバ5−...。
DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings. The same members as in the conventional example will be described using the same symbols. In FIG. 2, a bypass pipe 22 is connected between the outlet 2a of the heat exchanger 2b, which exchanges heat between the refrigerant vapor generated in the high-temperature regenerator and the absorption liquid 4, and the low-temperature regenerator 1.
23 is a control valve provided in the bypass pipe 21, and 23 is a control valve provided at the bottom of the condenser 6 and the bar 5-. .. .. .

イパス管210制御弁22とヲ季続したパイプである。This is a pipe connected to the path pipe 210 and the control valve 22.

上記構成において動作を説明すると、吸収冷温水機の運
転中は、冷媒蒸気管2の出口2aの凝縮冷媒は圧力は約
700mmHg(絶対圧・以下同じ)で、温度は96°
Cであり、低温再生器1内の吸収液4は圧力がeomi
Hg、温度96°Cであるため、運転停止時あるいは運
転中の停電時に、制御弁22を開けることによって高圧
の凝縮冷媒が圧力差によってバイパス管21を通って低
温再生器1に流入し、低温再生器1内の吸収液4を稀釈
する。
To explain the operation in the above configuration, during operation of the absorption chiller/heater, the pressure of the condensed refrigerant at the outlet 2a of the refrigerant vapor pipe 2 is approximately 700 mmHg (absolute pressure, the same applies hereinafter), and the temperature is 96°.
C, and the pressure of the absorption liquid 4 in the low-temperature regenerator 1 is eomi
Hg and the temperature is 96°C, when the operation is stopped or a power outage occurs during operation, by opening the control valve 22, the high pressure condensed refrigerant flows into the low temperature regenerator 1 through the bypass pipe 21 due to the pressure difference, and the low temperature The absorbent liquid 4 in the regenerator 1 is diluted.

稀釈された吸収液4は圧力差および落差によって吸収器
17に流入するが、冷媒蒸気管3の低温再生器1の出口
1aの凝縮冷媒の圧力が低くなると、凝縮器6内の凝縮
冷媒7もバイパス管21を通って低温再生器1へ、さら
に吸収器17内に流れ込んで稀釈を継続するという効果
がある。これ以外の動作は上記した従来例と同じなので
省略する。
The diluted absorption liquid 4 flows into the absorber 17 due to the pressure difference and head difference, but when the pressure of the condensed refrigerant at the outlet 1a of the low temperature regenerator 1 of the refrigerant vapor pipe 3 becomes low, the condensed refrigerant 7 in the condenser 6 also flows into the absorber 17. It has the effect of flowing through the bypass pipe 21 to the low temperature regenerator 1 and further into the absorber 17 to continue dilution. The other operations are the same as those of the conventional example described above, and will therefore be omitted.

発明の効果 このように本発明の稲沢装置では、運転停止時6ベー=
ジ あるいは運転中の停電時には運転中に機内の圧力差を利
用して、最も結晶しやすい吸収液散布液部を稀釈するも
のであり、吸収液ポンプによる稀釈運転によらずに稀釈
できるという効果がある。
Effects of the Invention As described above, in the Inazawa equipment of the present invention, when the operation is stopped, 6 bases =
In the event of a power outage or a power outage during operation, the pressure difference inside the machine is used to dilute the absorption liquid sprayed part that is most likely to crystallize. be.

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

第1図は従来の吸収冷温水機の配管回路図、第2図は本
発明の一実施例を示す吸収冷温水機の配管回路図である
。 1・・・・・・低温再生器、2°°°°°°冷媒蒸気管
・6°゛°°°゛凝縮器、17・・・・・・吸収器、2
1・・・・・・バイパス管、22・・・・・・制御弁。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 第2図
FIG. 1 is a piping circuit diagram of a conventional absorption chiller/heater, and FIG. 2 is a piping circuit diagram of an absorption chiller/heater showing an embodiment of the present invention. 1... Low temperature regenerator, 2°°°°°° refrigerant vapor pipe/6°゛°°°゛ condenser, 17... Absorber, 2
1... Bypass pipe, 22... Control valve. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 2

Claims (1)

【特許請求の範囲】[Claims] 高温再生器で発生した冷媒蒸気が吸収液と熱交−換する
熱交換器を設けた低電再生器と、この低温再生器内の熱
交換器の出口と低温再生器の吸収液部との間に接続し、
かつ開閉弁を有するバイパス管とを設けた吸収冷温水機
の稀釈装置。
A low-power regenerator equipped with a heat exchanger in which refrigerant vapor generated in the high-temperature regenerator exchanges heat with an absorption liquid, and a connection between the outlet of the heat exchanger in the low-temperature regenerator and the absorption liquid part of the low-temperature regenerator. connect between
A dilution device for an absorption chiller/heater, which is equipped with a bypass pipe having an on-off valve.
JP40684A 1984-01-05 1984-01-05 Diluting device for absorption cold and hot water machine Pending JPS60144574A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP40684A JPS60144574A (en) 1984-01-05 1984-01-05 Diluting device for absorption cold and hot water machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP40684A JPS60144574A (en) 1984-01-05 1984-01-05 Diluting device for absorption cold and hot water machine

Publications (1)

Publication Number Publication Date
JPS60144574A true JPS60144574A (en) 1985-07-30

Family

ID=11472915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP40684A Pending JPS60144574A (en) 1984-01-05 1984-01-05 Diluting device for absorption cold and hot water machine

Country Status (1)

Country Link
JP (1) JPS60144574A (en)

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