JPS6018764Y2 - Absorption chiller control device - Google Patents
Absorption chiller control deviceInfo
- Publication number
- JPS6018764Y2 JPS6018764Y2 JP17700979U JP17700979U JPS6018764Y2 JP S6018764 Y2 JPS6018764 Y2 JP S6018764Y2 JP 17700979 U JP17700979 U JP 17700979U JP 17700979 U JP17700979 U JP 17700979U JP S6018764 Y2 JPS6018764 Y2 JP S6018764Y2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- separator
- absorption liquid
- absorption
- liquid
- 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
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 38
- 239000007788 liquid Substances 0.000 claims description 41
- 239000003507 refrigerant Substances 0.000 claims description 19
- 238000005057 refrigeration Methods 0.000 claims description 3
- 239000006096 absorbing agent Substances 0.000 claims description 2
- 230000008016 vaporization Effects 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 238000009834 vaporization Methods 0.000 claims 1
- 238000010790 dilution Methods 0.000 description 4
- 239000012895 dilution Substances 0.000 description 4
- 230000009977 dual effect Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【考案の詳細な説明】
本案は比較的小型の二重効用吸収冷凍機の吸収液の流動
制御に関するものである。[Detailed Description of the Invention] The present invention relates to flow control of an absorption liquid in a relatively small-sized dual-effect absorption refrigerator.
吸収冷凍機における吸収液および冷媒の循環は液体ポン
プを利用して行なわれる部分もあるが、構成機器の各部
の圧力差、ヘッド差を利用して液体の流水を確保してい
る部分も少なくない。The circulation of absorption liquid and refrigerant in absorption refrigerators is carried out in some parts using liquid pumps, but in many parts the flow of liquid is ensured by utilizing pressure differences and head differences between various parts of the component equipment. .
特に小型の吸収冷凍機においては圧力差やヘッド差を利
用して液循環をしている部分が多く、ポンプを用いず圧
力差やヘッド差のみによって液循環の確保がなされる自
然循環式吸収冷凍機もある。Particularly in small absorption refrigerators, there are many parts that use pressure differences and head differences to circulate liquid, and natural circulation absorption refrigeration uses only pressure differences and head differences to ensure liquid circulation without using a pump. There is also a machine.
しかし、このような圧力差やヘッド差による液循環は吸
収冷凍機を構成する機器の温度条件、圧力条件が定常の
運転状態になったときにはじめて安定して流れるような
構造であり、このために、吸収冷凍機の起動後、これが
定常運転状態になる迄の時間(起動特性)、或いは、吸
収冷凍機の運転を停止する前に各部の吸収液濃度を低下
させる稀釈時間(稀釈特性)は犠性にされ易いものであ
った。However, liquid circulation due to such pressure differences and head differences is structured so that it can only flow stably when the temperature and pressure conditions of the equipment that make up the absorption refrigerator reach steady operating conditions. In addition, the time required for the absorption chiller to reach a steady operating state after it is started (startup characteristics), or the dilution time (dilution characteristics) required to reduce the absorption liquid concentration in each part before stopping the operation of the absorption chiller. It was easy to be victimized.
本案は斯る点に鑑み、特に二重効用吸収冷凍機の起動特
性及び稀釈特性を向上させるようにしたものであり、以
下に図面に従い説明する。In view of these points, the present invention is designed to particularly improve the startup characteristics and dilution characteristics of a dual-effect absorption refrigerator, and will be described below with reference to the drawings.
1は燃焼バーナ2によって加熱され、稀吸収液(以下補
液という)から冷媒を加熱分離する高温発生器、3は該
発生器1で発生した気状冷媒によって吸収液を送出する
揚液管、4は揚液管3を経て流入する吸収液と冷媒とを
分離する分離器、5は分離器4から送出された冷媒蒸気
を熱源として中間濃度の吸収液(以下中間液という)か
ら冷媒を更に加熱分離する低温発生器、6は冷却器7に
よって発生器1,5から流入する気状冷媒を液化し冷却
する凝縮器、8は該凝縮器6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却機能を得る蒸発器、9は
低温発生器5で冷媒が分離された濃吸収液(以下濃液と
いう)を散布して蒸発器8の内部を低圧に維持し連続し
た冷水の供給を行なえるようにした吸収器、10は低温
熱交換器、11は高温熱交換器であり、これらは冷媒蒸
気管12、冷媒液管13、吸収液ポンプ14を有する稀
液管15、中間液管16、濃液管17で配管接続されて
冷凍サイクルを構成している。1 is a high-temperature generator that is heated by a combustion burner 2 and heats and separates a refrigerant from a dilute absorption liquid (hereinafter referred to as replacement liquid); 3 is a liquid lift pipe that sends out an absorption liquid using the gaseous refrigerant generated in the generator 1; 4; 5 is a separator that separates the absorption liquid and refrigerant that flow in through the liquid pumping pipe 3, and 5 further heats the refrigerant from the intermediate concentration absorption liquid (hereinafter referred to as intermediate liquid) using the refrigerant vapor sent out from the separator 4 as a heat source. 6 is a condenser that liquefies and cools the gaseous refrigerant flowing in from the generators 1 and 5 using a cooler 7; 8 is a condenser that uses latent heat when dispersing and vaporizing the liquid refrigerant from the condenser 6; The evaporator 9 uses a low-temperature generator 5 to maintain a low pressure inside the evaporator 8 by spraying concentrated absorption liquid (hereinafter referred to as concentrated liquid) from which the refrigerant has been separated, thereby continuously supplying cold water. 10 is a low-temperature heat exchanger, 11 is a high-temperature heat exchanger, and these are a refrigerant vapor pipe 12, a refrigerant liquid pipe 13, a dilute liquid pipe 15 having an absorption liquid pump 14, and an intermediate liquid A refrigeration cycle is configured by being connected by a pipe 16 and a concentrated liquid pipe 17.
而して、18は分離器4と低温発生器5との間を、高温
熱交換器11を側路して接続する吸収液管、19は該吸
収液管18に取り付けられた自動弁、20は分離器4に
設置された温度(又は圧力)検知器21からの入力に応
じて自動弁19の開度を調節する制御器である。18 is an absorption liquid pipe that connects the separator 4 and the low temperature generator 5 by bypassing the high temperature heat exchanger 11; 19 is an automatic valve attached to the absorption liquid pipe 18; and 20 is a controller that adjusts the opening degree of the automatic valve 19 according to the input from the temperature (or pressure) detector 21 installed in the separator 4.
斯る構成を有する本案の吸収冷凍機においては吸収冷凍
機の起動時、分離器の温度(又は圧力)が低いあいだは
自動弁19の開度を大として、分離器4の中間液が吸収
液管18を介して低温発生器5に流れるようにすること
ができ、起動時に、分離器と低温発生器との圧力差が小
さいために中間液が殆ど流れず、多量の吸収液が分離器
に滞溜して吸収液の循環が止ってしまうという従来の此
の種の吸収冷凍機の欠点を解消できる。In the absorption refrigerating machine of the present invention having such a configuration, when the absorption refrigerating machine is started, the automatic valve 19 is opened to a large degree while the temperature (or pressure) of the separator is low, so that the intermediate liquid in the separator 4 becomes the absorption liquid. It can be made to flow to the low temperature generator 5 through the pipe 18, and at startup, because the pressure difference between the separator and the low temperature generator is small, very little intermediate liquid flows, and a large amount of absorption liquid flows into the separator. This eliminates the drawback of this type of conventional absorption refrigerator, in which the circulation of the absorption liquid stops due to stagnation.
尚、自動弁19の開度は分離器4の温度(又は圧力)が
高くなるにつれて閉じるようにすれば、必要量以上の吸
収液が分離器4に溜らないようにすることができる。In addition, if the opening degree of the automatic valve 19 is set so that it closes as the temperature (or pressure) of the separator 4 increases, it is possible to prevent an amount of absorption liquid exceeding the required amount from accumulating in the separator 4.
又、吸収冷凍機の停止時は、逆に、分離器4の温度の高
い間に自動弁19を開放すれば、低温発生器5、濃液管
17側にすみやかに中間液を流入させることができ吸収
冷凍機停止時の稀釈特性も向上するものである。Furthermore, when the absorption refrigerator is stopped, if the automatic valve 19 is opened while the temperature of the separator 4 is high, the intermediate liquid can quickly flow into the low temperature generator 5 and concentrated liquid pipe 17 side. This also improves dilution characteristics when the absorption refrigerator is stopped.
図は本案による吸収冷凍機の構造を示す回路構成図であ
る。
1・・・・・・高温発生器、4・・・・・・分離器、5
・・・・・・低温発生器、6・・・・・・凝縮器、8・
・・・・・蒸発器、9・・・・・・吸収器、18・・・
・・・吸収液管、19・・・・・・自動弁、21・・・
・・・検知器。The figure is a circuit configuration diagram showing the structure of an absorption refrigerator according to the present invention. 1... High temperature generator, 4... Separator, 5
... Low temperature generator, 6 ... Condenser, 8.
...Evaporator, 9...Absorber, 18...
... Absorption liquid pipe, 19 ... Automatic valve, 21 ...
...Detector.
Claims (1)
吸収液とを分離する分離器、該分離器から流出する冷媒
蒸気の熱を用いて吸収液から冷媒を分離する低温発生器
、気状冷媒を液化し冷却する凝縮器、冷媒の気化潜熱を
利用して冷却機能を得る蒸発器、気化した冷媒を吸収し
て蒸発器内を低圧に保つ吸収器等を冷媒管及び吸収液管
で接続して冷凍サイクルを形成すると共に、分離器と低
温発生器との間を自動弁材の吸収液管で接続し、分離器
内の温度又は圧力に応じ前記自動弁を開いて分離器から
低温発生器へ吸収液を側路して流すようにした吸収冷凍
機の制御装置。A high-temperature generator that vaporizes and separates the refrigerant from the absorption liquid, a separator that separates the gaseous refrigerant and the absorption liquid, a low-temperature generator that separates the refrigerant from the absorption liquid using the heat of the refrigerant vapor flowing out from the separator, and a A condenser that liquefies and cools a refrigerant, an evaporator that uses the latent heat of vaporization of the refrigerant to obtain a cooling function, an absorber that absorbs vaporized refrigerant and maintains a low pressure inside the evaporator, etc. are installed using refrigerant pipes and absorption liquid pipes. The separator and low temperature generator are connected to form a refrigeration cycle, and the separator and low temperature generator are connected by an absorption liquid pipe made of automatic valve material, and the automatic valve is opened depending on the temperature or pressure inside the separator to release low temperature from the separator. A control device for an absorption refrigerator that bypasses the absorption liquid to the generator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17700979U JPS6018764Y2 (en) | 1979-12-19 | 1979-12-19 | Absorption chiller control device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17700979U JPS6018764Y2 (en) | 1979-12-19 | 1979-12-19 | Absorption chiller control device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5694451U JPS5694451U (en) | 1981-07-27 |
JPS6018764Y2 true JPS6018764Y2 (en) | 1985-06-06 |
Family
ID=29687617
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17700979U Expired JPS6018764Y2 (en) | 1979-12-19 | 1979-12-19 | Absorption chiller control device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6018764Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60156369U (en) * | 1984-03-28 | 1985-10-18 | 矢崎総業株式会社 | Dual effect absorption chiller |
-
1979
- 1979-12-19 JP JP17700979U patent/JPS6018764Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5694451U (en) | 1981-07-27 |
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