JPS6113144B2 - - Google Patents

Info

Publication number
JPS6113144B2
JPS6113144B2 JP13960177A JP13960177A JPS6113144B2 JP S6113144 B2 JPS6113144 B2 JP S6113144B2 JP 13960177 A JP13960177 A JP 13960177A JP 13960177 A JP13960177 A JP 13960177A JP S6113144 B2 JPS6113144 B2 JP S6113144B2
Authority
JP
Japan
Prior art keywords
refrigerant
liquid
refrigerant tank
evaporator
condenser
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
JP13960177A
Other languages
Japanese (ja)
Other versions
JPS5472549A (en
Inventor
Tomoyuki Murayama
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Denki 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 Tokyo Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP13960177A priority Critical patent/JPS5472549A/en
Publication of JPS5472549A publication Critical patent/JPS5472549A/en
Publication of JPS6113144B2 publication Critical patent/JPS6113144B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は吸収冷凍機の液面制御装置に関するも
ので、特に吸収冷凍機の運転状況によつて変化す
る器内圧力の変化を利用して吸収冷凍機に付設し
た冷媒タンクの貯液量を変え、冷却水温度や冷房
負荷の変動に対応した吸収液の濃度の自動調整と
共に、ポンプ運転中は連続した冷媒循環量を確保
することにより冷媒ポンプの頻繁な発停を防止す
ることを目的としたものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a liquid level control device for an absorption refrigerating machine, and in particular, the present invention relates to a liquid level control device for an absorption refrigerating machine. By changing the amount of liquid stored in the tank and automatically adjusting the concentration of the absorption liquid in response to fluctuations in cooling water temperature and cooling load, this system also prevents frequent starting and stopping of the refrigerant pump by ensuring continuous refrigerant circulation during pump operation. The purpose is to prevent

一般に吸収冷凍機に冷媒タンクを付設し、該冷
凍機の運転状況、例えば冷房負荷の変動、冷却水
温度の変化等に応じて冷凍サイクルを循環する吸
収液の濃度を自動調整する方式は各種のものが提
案され実用化されているが、従来の冷媒タンクに
は、冷媒ポンプ吸込側に位置する冷媒溜の液面を
一定量以上に確保する機能は無く、このために、
冷媒液面が低下した場合に冷媒ポンプがキヤビテ
イシヨンを生じ、ポンプ故障の誘因となつたり、
或いは、冷媒液面が一定量以下になつた場合に冷
媒ポンプを停止させるときは、ポンプの発停頻度
が増すためにポンプの故障を生じ易いという欠点
を有していた。
In general, various methods are available in which a refrigerant tank is attached to an absorption chiller and the concentration of the absorption liquid circulating in the refrigeration cycle is automatically adjusted according to the operating conditions of the chiller, such as fluctuations in cooling load and changes in cooling water temperature. However, conventional refrigerant tanks do not have a function to ensure that the liquid level in the refrigerant reservoir located on the suction side of the refrigerant pump exceeds a certain level.
If the refrigerant liquid level drops, the refrigerant pump may cavitate, causing pump failure.
Alternatively, when the refrigerant pump is stopped when the refrigerant liquid level falls below a certain level, the frequency of starting and stopping of the pump increases, making the pump more likely to malfunction.

斯る点に鑑みなされた本発明を以下に図面に従
い説明すると、1は冷媒を吸収した稀吸収液を加
熱器2で加熱して再度冷媒と吸収液とに分離する
発生器、3は該発生器から流入する冷媒を冷却器
4によつて凝縮して液化する凝縮器、5は該凝縮
器からの液冷媒を散布し気化させる際の潜熱を利
用して冷房用の冷水を得るようにした蒸発器、6
は蒸発器内の冷水器7に冷媒を散布するための散
布器8に冷媒を供給する冷媒ポンプ、9は凝縮器
4からの液冷媒および蒸発器5で散布された未気
化冷媒を集めて冷媒ポンプ6に補給する冷媒溜、
10は発生器において冷媒が分離された後の吸収
液を散布し蒸発器で気化した冷媒蒸気を吸収する
ことにより蒸発器5の内部を低圧に保ち、連続し
た冷水の供給を可能にする吸収器、11は発生器
1から吸収器10に流入する濃吸収液と、吸収液
ポンプ12により吸収器10から発生器1に還流
される稀吸収液とを熱交換する熱交換器であり、
これらの機器は、冷媒管13、稀液管14、濃液
管15等をもつて気密に配管接続され、吸収冷凍
機を構成している。
The present invention, which was made in view of this point, will be explained below with reference to the drawings. 1 is a generator that heats a dilute absorption liquid that has absorbed a refrigerant with a heater 2 and separates it into the refrigerant and absorption liquid again; 3 is a generator that generates the A condenser 4 condenses and liquefies the refrigerant flowing from the condenser, and a condenser 5 distributes the liquid refrigerant from the condenser and uses latent heat when vaporizing it to obtain cold water for air conditioning. Evaporator, 6
9 is a refrigerant pump that supplies refrigerant to a sprayer 8 for spraying refrigerant to a water cooler 7 in the evaporator; 9 is a refrigerant pump that collects liquid refrigerant from the condenser 4 and unvaporized refrigerant sprayed in the evaporator 5; a refrigerant reservoir for replenishing the pump 6;
Reference numeral 10 denotes an absorber that keeps the inside of the evaporator 5 at a low pressure by dispersing the absorption liquid after the refrigerant is separated in the generator and absorbs the refrigerant vapor vaporized in the evaporator, thereby making it possible to continuously supply cold water. , 11 is a heat exchanger that exchanges heat between the concentrated absorption liquid flowing into the absorber 10 from the generator 1 and the dilute absorption liquid returned from the absorber 10 to the generator 1 by the absorption liquid pump 12,
These devices are airtightly connected through a refrigerant pipe 13, a dilute liquid pipe 14, a concentrated liquid pipe 15, etc., and constitute an absorption refrigerator.

而して、この吸収冷凍機には、気相部16を凝
縮器4と連通され、内部を溢流堰17によつて液
溜18と通液路19とに区分された第1冷媒タン
ク20と、該冷媒タンク20より高い位置に取付
けられ、気相部21を蒸発器5に連通された第2
冷媒タンク22とが付設されており、第1冷媒タ
ンク20の液溜18と第2冷媒タンク22の底部
とはU字管23で接続すると共に、液溜18と冷
媒ポンプ6の吐出側24とはオリフイス等の減圧
装置25を介して、また、第1冷媒タンクの通液
路19と蒸発器冷媒溜9とは液冷媒管26で接続
したものである。
This absorption refrigerator includes a first refrigerant tank 20 whose gas phase portion 16 is communicated with the condenser 4 and whose interior is divided into a liquid reservoir 18 and a liquid passage 19 by an overflow weir 17. and a second tank installed at a higher position than the refrigerant tank 20 and having the gas phase section 21 communicated with the evaporator 5.
A refrigerant tank 22 is attached, and the liquid reservoir 18 of the first refrigerant tank 20 and the bottom of the second refrigerant tank 22 are connected by a U-shaped pipe 23, and the liquid reservoir 18 and the discharge side 24 of the refrigerant pump 6 are connected. The liquid refrigerant passage 19 of the first refrigerant tank and the evaporator refrigerant reservoir 9 are connected via a pressure reducing device 25 such as an orifice, and a liquid refrigerant pipe 26.

また、27は第1冷媒タンクの液溜から液冷媒
が流下するのを防止する逆止弁であり、減圧装置
25の抵抗Rおよび堰の高さhは、この吸収冷凍
機の100%負荷運転時における蒸発器内圧力E
と、凝縮器の圧力Cと、ポンプ吐出圧力Pとの関
係が、h+H+R=E+P−Cの関係式を満足す
る値を標準にして決定される。
Further, 27 is a check valve that prevents the liquid refrigerant from flowing down from the liquid reservoir of the first refrigerant tank, and the resistance R of the pressure reducing device 25 and the height h of the weir are determined when the absorption refrigerator is operated at 100% load. The pressure inside the evaporator at E
The relationship between the condenser pressure C and the pump discharge pressure P is determined based on a value that satisfies the relational expression h+H+R=E+P−C.

但し、Hは第1冷媒タンク20の底と冷媒溜9
の液面とのヘツド差であり、式は逆止弁27や管
路抵抗を加味しない基本式として示す。
However, H refers to the bottom of the first refrigerant tank 20 and the refrigerant reservoir 9.
The equation is shown as a basic equation that does not take into account the check valve 27 or pipe resistance.

このような構成を有する本発明の吸収冷媒機に
おいて、運転停止状態においては、第1図に示す
ように、第1冷媒タンクの液溜18の液面と、第
2冷媒タンク21の液面、および、蒸発器の冷媒
溜9の液面と液冷媒管26の液面とは夫々、同一
水準にある。
In the absorption refrigerant machine of the present invention having such a configuration, when the operation is stopped, the liquid level of the liquid reservoir 18 of the first refrigerant tank, the liquid level of the second refrigerant tank 21, The liquid level in the refrigerant reservoir 9 of the evaporator and the liquid level in the liquid refrigerant pipe 26 are at the same level.

次に、発生器1で加熱を開始し、凝縮器および
吸収器の冷却器4,4′に、冷却水を流し、ポン
プ6,12の始動をして冷房運転を開始すると、
発生器1では多量の気状冷媒が発生して凝縮器3
に流入するため、凝縮器3の圧力は上昇し、か
つ、液冷媒量も増大して次第に第2図のような冷
媒液面状態に移行する。
Next, heating is started in the generator 1, cooling water is flowed into the condenser and absorber coolers 4 and 4', and the pumps 6 and 12 are started to start cooling operation.
A large amount of gaseous refrigerant is generated in the generator 1 and sent to the condenser 3.
As a result, the pressure in the condenser 3 increases, and the amount of liquid refrigerant also increases, gradually shifting to the refrigerant liquid level state as shown in FIG.

すなわち、第2図は高冷房負荷時、或いは、冷
却水温度が設計時の温度より高く、冷凍機に対す
るみかけの負荷が大きい場合の状態を示してお
り、凝縮器3で液化された冷媒は、凝縮器3と蒸
発器5との圧力差によつて、液冷媒管26を経て
蒸発器の液溜9に流入し、この液冷媒は冷媒ポン
プ6によつて散布器8に送られて気化し、冷水器
7を冷却する一方、一部の液冷媒は蒸発器5と凝
縮器3との圧力差を均衡するヘツド差h′に至る迄
第2冷媒タンク21に溜められるため、吸冷冷凍
機中を循環する冷媒量が減り、吸収液の濃度を上
げて高負荷に対応した冷房出力を得られる。
That is, FIG. 2 shows a state under a high cooling load, or when the cooling water temperature is higher than the designed temperature and the apparent load on the refrigerator is large, and the refrigerant liquefied in the condenser 3 is Due to the pressure difference between the condenser 3 and the evaporator 5, the liquid refrigerant flows through the liquid refrigerant pipe 26 into the liquid reservoir 9 of the evaporator, and this liquid refrigerant is sent to the spargeer 8 by the refrigerant pump 6 and vaporized. , while cooling the water cooler 7, some of the liquid refrigerant is stored in the second refrigerant tank 21 until it reaches the head difference h' that balances the pressure difference between the evaporator 5 and the condenser 3. The amount of refrigerant circulating inside is reduced, and the concentration of the absorption liquid is increased to provide cooling output that corresponds to high loads.

次いで、冷房負荷が減少してきたり、冷却水の
温度が低下して見掛の冷房負荷が減少した場合、
加熱器における加熱量が減じられるため、運転開
始時と同じ吸収液濃度のときは凝縮器3に流入す
る冷媒量、従つて蒸発器の冷媒溜9の液量が枯渇
するおそれもあるが、本発明においては、凝縮器
3の圧力の低下(吸収器および蒸発器でも圧力は
下るが、凝縮器程に大きな圧力の低下はない)に
伴つて、ヘツド差h′が減少し、第2冷媒タンク2
1に溜められていた冷媒がU字管23を経て第1
冷媒タンクの液溜18に放出されるため、冷媒液
は溢流堰17を越え、液冷媒管26を経て蒸発器
5に流入し、一部は吸収液に混入して吸収冷凍サ
イクル、残部は冷媒ポンプ6、第1冷媒タンクの
液溜18を経て再び冷媒管26へと循環する。従
つて、従来のように蒸発器の液溜の液量が枯渇し
て冷媒ポンプ6でキヤビテーシヨンを生じる弊害
を防止することができ、また余剰の液冷媒が第1
冷媒タンクを経て再循環されるため、冷媒液面を
検知して冷媒ポンプのキヤビテーシヨン防止を図
る特別な装置は必要なく、何らかの異常が発生し
て保護装置が働らく迄は冷媒ポンプは連続した運
転が続けられ、頻繁な冷媒ポンプの発停によつて
生じる制御機器の故障、ポンプの損耗を大巾に減
少させることもできるものである。
Next, when the cooling load decreases or the cooling water temperature decreases and the apparent cooling load decreases,
Since the amount of heating in the heater is reduced, when the absorption liquid concentration is the same as at the start of operation, there is a risk that the amount of refrigerant flowing into the condenser 3, and therefore the amount of liquid in the refrigerant reservoir 9 of the evaporator, will be depleted. In the invention, as the pressure in the condenser 3 decreases (the pressure also decreases in the absorber and evaporator, but the pressure decrease is not as large as in the condenser), the head difference h' decreases, and the pressure in the second refrigerant tank decreases. 2
The refrigerant stored in No. 1 passes through U-shaped pipe 23 to No. 1.
Since the refrigerant liquid is discharged into the liquid reservoir 18 of the refrigerant tank, the refrigerant liquid crosses the overflow weir 17 and flows into the evaporator 5 through the liquid refrigerant pipe 26. A part of the refrigerant liquid is mixed with the absorption liquid and is used in the absorption refrigeration cycle. The refrigerant is circulated through the refrigerant pump 6 and the liquid reservoir 18 of the first refrigerant tank to the refrigerant pipe 26 again. Therefore, it is possible to prevent the problem of cavitation in the refrigerant pump 6 due to depletion of the liquid amount in the liquid reservoir of the evaporator, as in the conventional case, and also to prevent excess liquid refrigerant from flowing into the first refrigerant.
Since the refrigerant is recirculated through the refrigerant tank, there is no need for a special device to detect the refrigerant liquid level and prevent cavitation of the refrigerant pump, and the refrigerant pump will continue to operate until some abnormality occurs and the protection device is activated. This can greatly reduce control equipment failure and pump wear and tear caused by frequent turning on and off of the refrigerant pump.

更にまた、本発明の装置を有する吸収冷凍機
は、運転停止時に徐々に、第1図の状態になり、
この間に、各管路から蒸発器の流入した冷媒はそ
のまま溢流して吸収器側に落下して吸収液を稀釈
するため、吸収液の稀釈時間が短縮され、連転停
止時における吸収液管路での結晶生成の問題解決
できるものであり、かつ、逆止弁により液溜内の
液冷媒の流下も防止されて第1冷媒タンク内に一
定量の液冷媒を保有するので、運転再開時におけ
る冷凍性能の立上りが早くなる効果も発揮する。
かつまた、本発明の装置を有する吸収冷凍機は、
凝縮器と吸収器間の圧力差に直接応じて吸収液濃
度を調整するので、負荷の変化や冷却水の温度変
化などに対して濃度調整の追従性に秀れるという
効果も発揮する。
Furthermore, the absorption refrigerator having the device of the present invention gradually enters the state shown in FIG. 1 when the operation is stopped,
During this time, the refrigerant flowing into the evaporator from each pipe overflows and falls to the absorber side to dilute the absorption liquid, so the dilution time of the absorption liquid is shortened, and the absorption liquid pipe when continuous operation is stopped. In addition, since the check valve prevents the liquid refrigerant in the liquid reservoir from flowing down and a certain amount of liquid refrigerant is retained in the first refrigerant tank, it is possible to solve the problem of crystal formation when restarting operation. It also has the effect of accelerating the start-up of refrigeration performance.
Moreover, an absorption refrigerator having the device of the present invention is
Since the absorption liquid concentration is adjusted directly according to the pressure difference between the condenser and the absorber, it also exhibits the effect of excellent ability to follow concentration adjustment to changes in load and temperature of cooling water.

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

第1図は本発明による液面制御装置を有した吸
収冷凍機の回路図、第2図は同じく別の作動状態
を示す要部回路図である。 1……発生器、3……凝縮器、5……蒸発器、
6……冷媒ポンプ、9……冷媒溜、10……吸収
器、17……溢流堰、18……液溜、19……通
液路、20……第1冷媒タンク、22……第2冷
媒タンク、23……U字管、25……減圧装置、
26……液冷媒管。
FIG. 1 is a circuit diagram of an absorption refrigerator having a liquid level control device according to the present invention, and FIG. 2 is a circuit diagram of the main parts similarly showing another operating state. 1... Generator, 3... Condenser, 5... Evaporator,
6...Refrigerant pump, 9...Refrigerant reservoir, 10...Absorber, 17...Overflow weir, 18...Liquid reservoir, 19...Liquid passage, 20...First refrigerant tank, 22...No. 2 refrigerant tank, 23... U-shaped pipe, 25... pressure reducing device,
26...Liquid refrigerant pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 発生器、凝縮器、蒸気器、吸収器、熱交換器
等を順次配管接続して冷凍サイクルを構成すると
共に蒸発器から機外に冷房用冷水を供給できるよ
うにした吸収冷凍機において、前記冷凍サイクル
に気相部を凝縮器と連通され内部を溢流堰によつ
て液溜と通液路とに区分された第1冷媒タンク
と、該第1冷媒タンクより高い位置に取り付けら
れ、気相部を蒸発器に連通された第2冷媒タンク
とを付設し、第1冷媒タンクの液溜と第2冷媒タ
ンクの底部とはU字管で接続すると共に、第1冷
媒タンクの液溜と冷媒ポンプの吐出側とはオリフ
イス等の減圧装置および逆止弁を介して、また第
1冷媒タンクの通液路と蒸発器の冷媒溜とは液冷
媒管を介して、夫々、接続したことを特徴とする
吸収冷凍機の液面制御装置。
1. In an absorption refrigerator in which a generator, a condenser, a steamer, an absorber, a heat exchanger, etc. are sequentially connected via piping to form a refrigeration cycle, and chilled water for cooling can be supplied from the evaporator to the outside of the machine, the above-mentioned The refrigeration cycle includes a first refrigerant tank whose gas phase is communicated with the condenser and whose interior is divided into a liquid reservoir and a liquid passage by an overflow weir; A second refrigerant tank whose phase part is communicated with the evaporator is attached, and the liquid reservoir of the first refrigerant tank and the bottom of the second refrigerant tank are connected by a U-shaped pipe, and the liquid reservoir of the first refrigerant tank and the bottom part of the second refrigerant tank are connected. The discharge side of the refrigerant pump is connected through a pressure reducing device such as an orifice and a check valve, and the liquid passage of the first refrigerant tank and the refrigerant reservoir of the evaporator are connected through a liquid refrigerant pipe. Features: Liquid level control device for absorption refrigerators.
JP13960177A 1977-11-18 1977-11-18 Liquid level controlling apparatus of absorption refrigerator Granted JPS5472549A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13960177A JPS5472549A (en) 1977-11-18 1977-11-18 Liquid level controlling apparatus of absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13960177A JPS5472549A (en) 1977-11-18 1977-11-18 Liquid level controlling apparatus of absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS5472549A JPS5472549A (en) 1979-06-11
JPS6113144B2 true JPS6113144B2 (en) 1986-04-11

Family

ID=15249061

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13960177A Granted JPS5472549A (en) 1977-11-18 1977-11-18 Liquid level controlling apparatus of absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS5472549A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0743182B2 (en) * 1986-06-16 1995-05-15 三洋電機株式会社 Absorption refrigerator

Also Published As

Publication number Publication date
JPS5472549A (en) 1979-06-11

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