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JPH0215788B2 - - Google Patents
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JPH0215788B2 - - Google Patents

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Publication number
JPH0215788B2
JPH0215788B2 JP56050336A JP5033681A JPH0215788B2 JP H0215788 B2 JPH0215788 B2 JP H0215788B2 JP 56050336 A JP56050336 A JP 56050336A JP 5033681 A JP5033681 A JP 5033681A JP H0215788 B2 JPH0215788 B2 JP H0215788B2
Authority
JP
Japan
Prior art keywords
absorption
liquid
pump
absorption liquid
generator
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 - Lifetime
Application number
JP56050336A
Other languages
Japanese (ja)
Other versions
JPS57164262A (en
Inventor
Hidetoshi Arima
Naoki Sakamoto
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 JP56050336A priority Critical patent/JPS57164262A/en
Publication of JPS57164262A publication Critical patent/JPS57164262A/en
Publication of JPH0215788B2 publication Critical patent/JPH0215788B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は負荷に応じた冷凍機の能力の制御を簡
易化した吸収冷凍機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigerator in which the capacity of the refrigerator can be easily controlled according to the load.

従来より、小型の吸収冷凍機における部分負荷
時の制御方式としては、発生器において稀吸収液
を加熱する燃焼系統の制御が行なわれるだけで、
液の循環量の制御は行なわれていなかつた。
Conventionally, the control method for small absorption refrigerators during partial load has simply been to control the combustion system that heats the dilute absorption liquid in the generator.
The amount of liquid circulated was not controlled.

これは、吸収冷凍機を構成する冷媒と吸収液と
の循環サイクルがいずれも真空部で形成されてい
るため、このような液の循環量の調整に制御弁や
可動ダンパを用いるときには気密度の高い部品を
用いる必要があり、小型、小容量の吸収冷凍機で
はコスト的に使用が困難視される上に、耐真空の
問題或いは保守サービスの面からも、液の循環量
の制御はON−OFF制御とし、非真空部となる発
生器の燃焼系統のみに強、弱、切の3位置制御を
採用してきたわけである。
This is because the circulation cycle of the refrigerant and absorption liquid that make up the absorption refrigerator are both formed in a vacuum section, so when using a control valve or movable damper to adjust the amount of circulation of such liquid, the airtightness must be adjusted. It requires the use of expensive parts, making it difficult to use in small, small-capacity absorption refrigerators due to cost considerations. Furthermore, controlling the amount of liquid circulated is not possible due to vacuum-proof issues and maintenance services. OFF control has been adopted, and three-position control (strong, weak, and off) has been adopted only for the combustion system of the generator, which is a non-vacuum part.

本発明は斯る点に鑑み、部品の気密度、耐真空
度或いは大掛かりな制御装置を増設することなし
に、小型の吸収冷凍機にも随時採用して循環液量
を制御できるようにした吸収冷凍機を提供するも
のである。
In view of these points, the present invention provides an absorption system that can be applied to small-sized absorption refrigerators at any time to control the amount of circulating fluid without changing the airtightness of parts, vacuum resistance, or adding large-scale control equipment. It provides refrigerators.

以下に本発明の一実施例を示す図面に従つて説
明すると、第1図において、1はガスや油などの
燃焼ガスを用いて稀吸収液を加熱する高温発生
器、2は該高温発生器1で加熱され揚液管3を上
昇してきた稀吸収液から気状冷媒と吸収液とを分
離する分離器、4は該分離器2で分離された冷媒
蒸気を熱源として中間吸収液を更に加熱分離する
低温発生器、5は発生器1,4から流入する冷媒
を冷却器6で冷却し、凝縮させる凝縮器、7は該
凝縮器5からの液冷媒を散布し気化させる際の潜
熱を利用して熱交換器8から冷房用の冷水を得る
ようにした蒸発器、9は該蒸発器7で気化しなか
つた液冷媒を再び蒸発器7に還流させる気泡ポン
プ、10は発生器1,4において冷媒が分離され
た濃吸収液を散布して器内の冷媒蒸気を吸収する
ことにより前記蒸発器7の内部を低圧に維持し、
連続して冷水の供給を行なえるようにした吸収
器、11は開閉弁12を有し、暖房時に該開閉弁
12を開くことにより分離器2の高温の冷媒を吸
収液と共に蒸発吸収胴13に導くことにより、暖
房時には熱交換器8から温水の取り出しができる
ようにしたバイパス管、14はこのような冷暖房
時において吸収器10に散布される稀吸収液を発
生器1に還流する吸収液ポンプ(キヤンドポン
プ)、15,16は吸収器10から発生器1に戻
る低温の吸収液と発生器1から吸収器13に流下
する濃吸収液とを熱交換する熱交換器であり、こ
れらは冷媒管17,18、吸収液管19,20,
21、揚液管3、バイパス管11で接続されて冷
媒と吸収液との気密な循環サイクルを構成してい
る。
An embodiment of the present invention will be described below with reference to the drawings. In FIG. 1, 1 is a high-temperature generator that heats a dilute absorption liquid using combustion gas such as gas or oil; 2 is the high-temperature generator; 1 is a separator that separates the gaseous refrigerant and absorption liquid from the dilute absorption liquid that has been heated and ascended through the pumping pipe 3; 4 is a separator that further heats the intermediate absorption liquid using the refrigerant vapor separated in the separator 2 as a heat source; A low-temperature generator to be separated; 5 is a condenser that cools and condenses the refrigerant flowing from the generators 1 and 4 in a cooler 6; 7 uses latent heat when dispersing and vaporizing the liquid refrigerant from the condenser 5; 9 is a bubble pump that returns the liquid refrigerant that has not been vaporized in the evaporator 7 to the evaporator 7; 10 is a generator 1, 4; The inside of the evaporator 7 is maintained at a low pressure by scattering a concentrated absorption liquid from which the refrigerant has been separated and absorbing the refrigerant vapor inside the vessel;
The absorber 11 that can continuously supply cold water has an on-off valve 12, and by opening the on-off valve 12 during heating, the high temperature refrigerant from the separator 2 is transferred to the evaporation absorption shell 13 together with the absorption liquid. 14 is an absorption liquid pump that returns the diluted absorption liquid sprayed in the absorber 10 to the generator 1 during heating and cooling. (canned pump), 15 and 16 are heat exchangers that exchange heat between the low temperature absorption liquid returning from the absorber 10 to the generator 1 and the concentrated absorption liquid flowing down from the generator 1 to the absorber 13. 17, 18, absorption liquid pipe 19, 20,
21, liquid lift pipe 3, and bypass pipe 11 to form an airtight circulation cycle of refrigerant and absorption liquid.

而して、本発明の吸収冷凍機に用いられる吸収
液ポンプ14には例えば第2図にその性能曲線を
もつて示すように、ポンプを正回転させる場合と
逆回転させる場合とで液吐出量および揚程が変化
する可逆転ポンプを用いてあり、例えば、正回転
で100%の液循環量に対し、逆回転では60乃至40
%の液循環量となるようにしている。
As shown in the performance curve of the absorption liquid pump 14 used in the absorption refrigerator of the present invention, for example, as shown in FIG. A reversible pump with variable pump head is used. For example, while the liquid circulation rate is 100% in forward rotation, it is 60 to 40% in reverse rotation.
% liquid circulation amount.

このように構成された本発明の吸収冷凍機にお
いては、熱交換器8に取り付けられた温度検出器
22,22′によつて冷暖房等の調温負荷の減少
が感知された場合に、この感知温度を入力とする
制御器23が弁24の開度を狭めて高温発生器1
での加熱量を減じると共に吸収液ポンプ14の接
点25を図の状態から反対の位置に切替えてポン
プ14の回転を正転から逆転方向に回転させて吸
収液の循環量を減少させ、これにより、従来の小
型の吸収冷凍機では難かしかつた制御特性の向
上、例えば、吸収冷凍機としての冷媒および吸収
液の循環の液濃度と圧力バランスを保ちつつ冷暖
房の能力のみを減小させるような運転制御が、単
に、非真空部の電気的な操作のみで可能となるも
のであり、小型の吸収冷凍機の制御特性の向上と
制御の簡便化に実用的効果の大きいものである。
In the absorption refrigerator of the present invention configured as described above, when a decrease in temperature control load such as air conditioning is detected by the temperature detectors 22 and 22' attached to the heat exchanger 8, this detection A controller 23 that receives the temperature as an input narrows the opening degree of the valve 24 to close the high temperature generator 1.
At the same time, the contact point 25 of the absorption liquid pump 14 is switched from the state shown in the figure to the opposite position, and the rotation of the pump 14 is rotated from the normal rotation to the reverse direction, thereby reducing the circulation amount of the absorption liquid. , improved control characteristics that were difficult to achieve with conventional small-sized absorption chillers, for example, reducing only the heating and cooling capacity while maintaining the liquid concentration and pressure balance in the circulation of refrigerant and absorption liquid as an absorption chiller. Operational control is possible simply by electrically operating the non-vacuum section, and this has a great practical effect in improving the control characteristics and simplifying the control of small-sized absorption refrigerators.

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

第1図は本発明による吸収冷凍機の一実施例を
示す構造図、第2図は同じく吸収液ポンプの性能
曲線図である。 1,4……発生器、7……蒸発器、10……吸
収器、14……吸収液ポンプ、23……制御器、
25……接点。
FIG. 1 is a structural diagram showing an embodiment of an absorption refrigerator according to the present invention, and FIG. 2 is a performance curve diagram of an absorption liquid pump. 1, 4... Generator, 7... Evaporator, 10... Absorber, 14... Absorption liquid pump, 23... Controller,
25...Contact.

Claims (1)

【特許請求の範囲】[Claims] 1 蒸発器で気化した冷媒を吸収して稀釈された
吸収液をポンプにより発生器に還流すると共に前
記ポンプを正転時と逆転時とで吐出液量が異なる
可逆転ポンプとし、この可逆転ポンプの回転方向
を冷暖房等の調温負荷の変化時に切替える機構を
備えたことを特徴とする吸収冷凍機。
1. Absorbing refrigerant vaporized in the evaporator and diluting the absorption liquid is returned to the generator by a pump, and the pump is a reversible pump that discharges a different amount of liquid during forward rotation and reverse rotation, and this reversible pump What is claimed is: 1. An absorption refrigerating machine characterized by having a mechanism for switching the direction of rotation of the refrigerating machine when a temperature control load such as air conditioning or heating changes.
JP56050336A 1981-04-02 1981-04-02 Absorption refrigerating machine Granted JPS57164262A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56050336A JPS57164262A (en) 1981-04-02 1981-04-02 Absorption refrigerating machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56050336A JPS57164262A (en) 1981-04-02 1981-04-02 Absorption refrigerating machine

Publications (2)

Publication Number Publication Date
JPS57164262A JPS57164262A (en) 1982-10-08
JPH0215788B2 true JPH0215788B2 (en) 1990-04-13

Family

ID=12856069

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56050336A Granted JPS57164262A (en) 1981-04-02 1981-04-02 Absorption refrigerating machine

Country Status (1)

Country Link
JP (1) JPS57164262A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06100400B2 (en) * 1984-12-12 1994-12-12 三洋電機株式会社 Absorption heat pump device

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4863306U (en) * 1971-11-17 1973-08-11
JPS5043903U (en) * 1973-08-17 1975-05-02
JPS51150505U (en) * 1975-05-28 1976-12-01
JPS5666666A (en) * 1979-11-02 1981-06-05 Ebara Mfg Absorption refrigerating machine

Also Published As

Publication number Publication date
JPS57164262A (en) 1982-10-08

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