JPS58130972A - Absorption type refrigerator - Google Patents

Absorption type refrigerator

Info

Publication number
JPS58130972A
JPS58130972A JP416183A JP416183A JPS58130972A JP S58130972 A JPS58130972 A JP S58130972A JP 416183 A JP416183 A JP 416183A JP 416183 A JP416183 A JP 416183A JP S58130972 A JPS58130972 A JP S58130972A
Authority
JP
Japan
Prior art keywords
refrigerant
solution
absorber
liquid level
bypass
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
JP416183A
Other languages
Japanese (ja)
Inventor
長尾雅司
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP416183A priority Critical patent/JPS58130972A/en
Publication of JPS58130972A publication Critical patent/JPS58130972A/en
Pending legal-status Critical Current

Links

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】 〔発明の利用分野〕 本発明は少くとも1個の再生器、凝縮器、蒸発器、熱交
換器および冷媒と溶液の各循環ポンプを有する吸収冷凍
機に関するものでおる。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to an absorption refrigerator having at least one regenerator, a condenser, an evaporator, a heat exchanger and refrigerant and solution circulation pumps. .

〔従来技術〕[Prior art]

従来のこの種吸収冷凍機において、凝縮器、吸収器の冷
却水温度が基準値よりも低くなった場合の対応として冷
媒液面の検知して冷媒ポンプを運転および停止すること
により冷凍機の運転を継続できるようにしている。
In conventional absorption refrigerators of this type, when the temperature of the cooling water in the condenser or absorber becomes lower than the standard value, the refrigerator is operated by detecting the refrigerant liquid level and starting and stopping the refrigerant pump. We are making it possible to continue.

このように冷媒液面を検知して冷媒散布量を制御する場
合には、冷媒液面の上昇あるいは下降に伴って散布量が
増減する。この散布量の増減は直接に冷凍能力の増減に
影響するため広範囲の制御は望めず、液面下限近傍にお
ける制御にとどめる必要があり、実際には冷媒液面低下
による冷媒ポンプのキャビテーション防止の役目を果す
程度の意義しかない。
When controlling the amount of refrigerant sprayed by detecting the refrigerant liquid level in this way, the amount of sprayed increases or decreases as the refrigerant liquid level rises or falls. Since the increase or decrease in the amount of spraying directly affects the increase or decrease in refrigeration capacity, it is not possible to control over a wide range, and it is necessary to limit the control to near the lower limit of the liquid level.Actually, it serves to prevent cavitation in the refrigerant pump due to a drop in the refrigerant liquid level. It is only meaningful to the extent that it fulfills its purpose.

一方、冷媒液面の検知によシ冷媒ポンプを運転および停
止させる制御では、液面下限近傍の制御の際に冷凍能力
が大幅にハンチングして安定した冷水供給を行うことが
不可能である。そして冷凍機の運転可能領域を広げるた
めには、冷媒保有量を増加させねばならない。
On the other hand, in the control in which the refrigerant pump is operated and stopped based on the detection of the refrigerant liquid level, the refrigerating capacity significantly hunts when the liquid level is near the lower limit, making it impossible to stably supply cold water. In order to expand the operating range of the refrigerator, it is necessary to increase the amount of refrigerant held.

吸収式冷凍機の冷却水入口温度は、通常32r程度であ
るが、需要家の用途および外気温度により広範囲にわた
って変化する。そして、32Cを基準にして設計された
ものの場合には、対応できる冷却水温度の下限tli2
0r程度である。
The cooling water inlet temperature of an absorption chiller is normally about 32r, but it varies over a wide range depending on the customer's usage and the outside air temperature. In the case of a device designed based on 32C, the lower limit of the corresponding cooling water temperature tli2
It is about 0r.

〔発明の目的〕[Purpose of the invention]

本発明の目的運転可能な冷却水温度の下限をlθ〜15
C程度まで広げ、かつ全域にわたって安定した冷水供給
が可能な吸収式冷凍機を提供することにある。
The purpose of the present invention is to set the lower limit of the cooling water temperature that can be operated to lθ~15
It is an object of the present invention to provide an absorption chiller capable of stably supplying cold water over the entire area.

〔発明の概要〕[Summary of the invention]

本発明は、吸収器の液面を検知してその伝熱管への溶液
散布量を増減させることを特徴とする。
The present invention is characterized in that the liquid level in the absorber is detected and the amount of solution sprayed onto the heat transfer tube is increased or decreased.

このようにすれば、冷却水温度および負荷などの変動要
因によるサイクル濃度および循環量の変化幅を一定範囲
内に抑制し、冷却水温度および負荷の許容変動幅を増大
し、かつ限定した冷媒保有量で対処できる。
In this way, changes in cycle concentration and circulation amount due to fluctuation factors such as cooling water temperature and load can be suppressed within a certain range, the permissible fluctuation range of cooling water temperature and load can be increased, and the refrigerant inventory can be limited. It can be handled by quantity.

〔発明の実施例〕[Embodiments of the invention]

以下本発明の実施ガを図面を参照して説明する。 DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.

まず吸収式冷凍機の美形例の構成および冷媒と溶液の循
環サイクルを第1図に示す一重効用吸収式冷凍機につい
て述べる。
First, a single-effect absorption refrigerating machine will be described, the configuration of which is a beautiful example of an absorption refrigerating machine, and the refrigerant and solution circulation cycle shown in FIG.

第1図において、1は蒸発器、2は蒸発器lの3の伝熱
管を流通する冷却水、5は溶液循環ポンプ、6は熱交換
器、7は再生器、8は凝縮器、9は冷媒ポンプである。
In Fig. 1, 1 is an evaporator, 2 is cooling water flowing through 3 heat transfer tubes of the evaporator L, 5 is a solution circulation pump, 6 is a heat exchanger, 7 is a regenerator, 8 is a condenser, and 9 is a It is a refrigerant pump.

低圧に保たれた蒸発器1のシェル側に存在する冷媒(水
)は、その伝熱管を流通する冷水2から熱を奪って蒸発
し冷凍作用を行い、蒸発した冷媒ガスは吸収器3へ流れ
る。この吸収器3のシェル内には、その伝熱管を流通す
る冷却水4により一定温度に保持された臭化リチュウム
水溶液が存在しているから、この水溶液に前記冷媒ガス
は吸収されて希溶液となる。
The refrigerant (water) present on the shell side of the evaporator 1, which is kept at a low pressure, takes heat from the cold water 2 flowing through the heat transfer tube and evaporates to perform a freezing action, and the evaporated refrigerant gas flows to the absorber 3. . Inside the shell of the absorber 3, there is an aqueous lithium bromide solution maintained at a constant temperature by the cooling water 4 flowing through the heat transfer tube, so the refrigerant gas is absorbed into this aqueous solution and turned into a dilute solution. Become.

上記希溶液は溶液循環ボーンプ5により、熱交換器6を
経て再生器7へ給送される。この給送された希溶液は再
生器7中の高温蒸気などの熱源により蒸発して冷媒蒸気
と濃溶液とに分離される。その冷媒蒸気は凝縮器8に至
り、その伝熱管内を流通する冷却水4により冷却されて
液冷媒となる。
The dilute solution is fed to the regenerator 7 via the heat exchanger 6 by the solution circulation bone pump 5. This fed dilute solution is evaporated by a heat source such as high-temperature steam in the regenerator 7 and separated into refrigerant vapor and a concentrated solution. The refrigerant vapor reaches the condenser 8, where it is cooled by the cooling water 4 flowing through the heat transfer tube and becomes a liquid refrigerant.

この液冷媒は蒸発器1に戻されて冷凍サイクルを形成す
る。
This liquid refrigerant is returned to the evaporator 1 to form a refrigeration cycle.

一方、再生器7において冷媒の分離によシ生成された濃
溶液は熱交換器6を経て吸収器3へ戻され、再び蒸発器
lからの冷媒蒸気を吸収して希溶液となシ溶液サイクル
を形成する。
On the other hand, the concentrated solution generated by separation of the refrigerant in the regenerator 7 is returned to the absorber 3 via the heat exchanger 6, and again absorbs refrigerant vapor from the evaporator 1 to become a dilute solution. form.

次に本発明の実施例の要部を第2図について説明するに
、3は伝熱管3mを内蔵する吸収器、10は溶液循環ボ
ンン5(第1図)に接続され、かつ伝熱管3aの上方に
設置された溶液散布管、11は溶液散布管10の途中に
接続されたバイパス管・、12はバイパス管11に設け
られたフロート12aを有するフロートバルブ、15F
i、吸収器3内の溶液の液面でめる。
Next, the main parts of the embodiment of the present invention will be explained with reference to FIG. 2. Reference numeral 3 denotes an absorber incorporating 3 m of heat exchanger tubes, 10 is connected to the solution circulation bong 5 (FIG. 1), and the heat exchanger tube 3a is connected to the absorber 3. A solution dispersion pipe installed above, 11 a bypass pipe connected in the middle of the solution dispersion pipe 10, 12 a float valve having a float 12a provided in the bypass pipe 11, 15F
i. Fill with the liquid level of the solution in the absorber 3.

本実施例は上記のような構造からなるので、液面15が
上昇すると、70−ト12aの作用によpフロートパル
プ12は開かれるので、溶液散布管10内を流通する溶
液の一部はバイパス管11を経て吸収器3内へ流出する
。逆に液面15が低下すると、フロートバルブ12ri
徐々に閉じ量終的には全閉となりバイパス管11からの
吸収器3への流出は停止され、る。
Since this embodiment has the above-described structure, when the liquid level 15 rises, the p-float pulp 12 is opened by the action of the 70-t 12a, so that part of the solution flowing through the solution dispersion pipe 10 is It flows out into the absorber 3 via the bypass pipe 11. Conversely, when the liquid level 15 decreases, the float valve 12ri
The amount of gradual closing eventually becomes fully closed, and the outflow from the bypass pipe 11 to the absorber 3 is stopped.

上記のように吸収器3の液面15が上昇することは、サ
イクル濃度が低下していることを示している。このとき
に溶液散布量を減少させれば、サイクル濃度は上昇する
。このように制御することにより冷却水温度および負荷
の変化、特に負荷の減少に対してサイクル濃度を一定の
変動幅内に抑制することができるので、冷媒保有量を増
大させることなく、冷却温度および負荷の変化に対処で
き、かつ低冷却水温度に対して安定したサイクルを構成
することができる。
The rise in the liquid level 15 in the absorber 3 as described above indicates that the cycle concentration is decreasing. If the amount of solution sprayed is reduced at this time, the cycle concentration will increase. By controlling in this way, it is possible to suppress the cycle concentration within a certain fluctuation range in response to changes in cooling water temperature and load, especially decreases in load, so the cooling temperature and It is possible to configure a cycle that can cope with changes in load and is stable at low cooling water temperatures.

本実施例ではバイパス管11にフロートバルブ12を設
けたが、これに代り第3図に示すようにバイパス管11
に制御弁13を設け、この制御弁13を液面検知器14
に接続しても同様な効果をうろことが可能である。
In this embodiment, the float valve 12 is provided in the bypass pipe 11, but instead of this, as shown in FIG.
A control valve 13 is provided in the liquid level detector 14.
It is possible to obtain the same effect by connecting it to .

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明によれば冷却水温度および
負荷の変動に対して安定した冷水(冷凍能力)を供給す
ることができる。ま九冷却水温度の下限を通常よりも大
幅に低い温度レベルまで拡大できるとともに、冷媒保有
量および保有スペースを減少させると共に、吸収器の液
面を一定高さ以下に保つことができる。
As described above, according to the present invention, it is possible to supply stable cold water (refrigeration capacity) against fluctuations in cooling water temperature and load. The lower limit of the cooling water temperature can be expanded to a much lower temperature level than usual, the amount and space of refrigerant held can be reduced, and the liquid level in the absorber can be kept below a certain level.

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

第1図は吸収式冷凍機の典型例の概略図、第2図および
第3図は本発明の一実施例を示す断面図でるる。 3・・・吸収器、3a・・・伝熱管、1o・・・溶液散
布管、11・・・バイバス!、12・・・フロートバル
ブ、13・・・制’X1ff。
FIG. 1 is a schematic diagram of a typical example of an absorption refrigerator, and FIGS. 2 and 3 are sectional views showing an embodiment of the present invention. 3...Absorber, 3a...Heat transfer tube, 1o...Solution distribution tube, 11...Bypass! , 12...Float valve, 13...Control'X1ff.

Claims (1)

【特許請求の範囲】[Claims] 吸収器の伝熱管の上方に設置した溶液散布管にバイパス
管を接続し、このバイパス管に吸収器の溶液液面の高さ
の変動に応じて動作するバイパス量制御弁を設け、かつ
バイパス量制御弁を前記溶液液面が上昇した場合、バイ
パス量を増加させ、前記溶液液面が低下した場合、バイ
パス量を減少させる方向に動作するように連動させたこ
とを特徴とする吸収式冷凍機。
A bypass pipe is connected to the solution dispersion pipe installed above the heat transfer pipe of the absorber, and a bypass amount control valve is provided in this bypass pipe that operates according to fluctuations in the height of the solution level in the absorber, and the bypass amount is An absorption chiller characterized in that the control valve is operated in such a way as to increase the bypass amount when the solution level rises and to decrease the bypass amount when the solution level falls. .
JP416183A 1983-01-17 1983-01-17 Absorption type refrigerator Pending JPS58130972A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP416183A JPS58130972A (en) 1983-01-17 1983-01-17 Absorption type refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP416183A JPS58130972A (en) 1983-01-17 1983-01-17 Absorption type refrigerator

Publications (1)

Publication Number Publication Date
JPS58130972A true JPS58130972A (en) 1983-08-04

Family

ID=11577013

Family Applications (1)

Application Number Title Priority Date Filing Date
JP416183A Pending JPS58130972A (en) 1983-01-17 1983-01-17 Absorption type refrigerator

Country Status (1)

Country Link
JP (1) JPS58130972A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003130486A (en) * 2001-10-19 2003-05-08 Hitachi Ltd Absorption chilled or hot-water machine and method of controlling the machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003130486A (en) * 2001-10-19 2003-05-08 Hitachi Ltd Absorption chilled or hot-water machine and method of controlling the machine

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