JPS6025708B2 - absorption refrigeration equipment - Google Patents
absorption refrigeration equipmentInfo
- Publication number
- JPS6025708B2 JPS6025708B2 JP7305277A JP7305277A JPS6025708B2 JP S6025708 B2 JPS6025708 B2 JP S6025708B2 JP 7305277 A JP7305277 A JP 7305277A JP 7305277 A JP7305277 A JP 7305277A JP S6025708 B2 JPS6025708 B2 JP S6025708B2
- Authority
- JP
- Japan
- Prior art keywords
- generator
- absorption
- pressurizing device
- heat
- cold
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は、低温熱源による運転ができるようにした吸収
冷凍装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigeration system that can be operated using a low-temperature heat source.
工場廃液等の低温熱源による運転ができるようにした吸
収冷凍装置の従来の技術として、例えば特公昭51−3
425号公報にみられるように、発生器と凝縮器の連絡
管途中に圧縮機を配設した多段型冷凍装置が知られてい
る。しかし、この多段型冷凍装置においては、圧縮機の
駆動エネルギーで加圧昇温された冷煤の熱を吸収液の濃
縮と冷媒蒸気の分離に活用することなく凝縮器から装置
外へ棄てているため、その分、成績係数が低下する点を
有している。かつまた、圧縮機の駆動を制御する手段が
備えられてないため、その冷凍能力を冷凍負荷に見合う
ように調整し得ない欠点も有している。本発明これら問
題点に鑑みてなされたもので、以下、図に従い本発明に
よる吸収冷凍装置の実施例について説明する。図におい
て、1は排ガス等の適当な熱源流体により加熱され、吸
収液から冷煤を気化分離する発生器、2は凝縮器、3は
蒸発器、4は蒸発器3において気化した袷媒を吸収して
器内を低圧に保つ吸収器、5は発生器1から流入する高
温の濃吸収液と吸収器4から発生器1に戻る低温の稀吸
収液とを熱交換する熱交換器である。As a conventional technology for absorption refrigeration equipment that can be operated using a low-temperature heat source such as factory waste liquid, for example,
As seen in Japanese Patent No. 425, a multi-stage refrigeration system is known in which a compressor is disposed in the middle of a connecting pipe between a generator and a condenser. However, in this multi-stage refrigeration system, the heat of the cold soot, which is pressurized and heated by the drive energy of the compressor, is discarded from the condenser outside the system without being utilized for concentrating the absorption liquid and separating the refrigerant vapor. Therefore, the coefficient of performance will decrease accordingly. Furthermore, since there is no means for controlling the drive of the compressor, there is also the drawback that the refrigerating capacity cannot be adjusted to match the refrigerating load. The present invention has been made in view of these problems, and embodiments of the absorption refrigeration apparatus according to the present invention will be described below with reference to the drawings. In the figure, 1 is a generator that is heated by an appropriate heat source fluid such as exhaust gas and vaporizes and separates cold soot from the absorption liquid, 2 is a condenser, 3 is an evaporator, and 4 is the evaporator 3 that absorbs the vaporized slag medium. The absorber 5 is a heat exchanger that exchanges heat between the high temperature concentrated absorption liquid flowing from the generator 1 and the low temperature dilute absorption liquid returning from the absorber 4 to the generator 1.
而して、発生器1において吸収液から加熱分離された気
状の冷煤を凝縮器2に送る本発明の冷煤管路6にはター
ボファンやコンブレッサー等の冷煤加圧装置7及び発生
器中の吸収液を再加熱する熱交換器8が配設されており
、該熱交換器で吸収液を再加熱して凝縮した冷煤液は、
発生器1に戻る稀吸収液と熱交換した後凝縮器2に流入
する。The cold soot pipe 6 of the present invention that sends the gaseous cold soot heated and separated from the absorption liquid in the generator 1 to the condenser 2 is equipped with a cold soot pressurizing device 7 such as a turbo fan or a compressor. A heat exchanger 8 is provided to reheat the absorption liquid in the generator, and the cold soot liquid that is reheated and condensed by the heat exchanger is
After exchanging heat with the dilute absorption liquid that returns to the generator 1, it flows into the condenser 2.
このような作動の一例として、発生圧力60肋Hgで発
生した冷煤ガスを加圧装置7で650脚Hg迄昇圧する
と、冷煤温度は約95ooとなり、これを熱交換器8に
導くと、発生器内の吸収液はこの冷煤の凝縮潜熱によっ
て再熱され、再び袷線を分離することができる。第2図
は、本発明の他の実施例であり、発生器1と凝縮器2と
は冷媒管路6の他の冷水負荷によって開度の調整される
弁9を有した側路管10が付設されている。冷水負荷が
減少したとき、蒸発器3の冷水出口温度を感知する検出
器からの信号を受ける制御器11により、加圧装置7は
その運転動力が抑制されるように制御される。また、冷
水負荷がさらに減少したり、排ガス等の低温熱源の熱エ
ネルギーが増大することによって低温熱源のみで十分に
運転が可能となった場合には、制御器11により、加圧
装置7の運転は停止されると共に弁9の開度が制御され
る。なお、この弁9は、加圧装置7を運転しているとき
、閉じられるようにしても良く、加圧装置7と共に制御
されるようにしても良い。このように、本発明の吸収冷
凍装置は加圧装置で昇圧昇温された冷蝶の熱を発生器に
おける冷媒の発生と吸収液の濃縮に活用し、かつ、発生
器へ供給する低温熱源の冷水負荷に対する熱量不足の大
きさに応じてこの熱量不足分を加圧装置の運転エネルギ
ーで補充調整する機能をもつものであるから、発生器の
加熱熱源は低温のものでも吸収冷濠機の運転には支障は
なく、かつ、負荷に見合う冷水を取出すことができ、又
、成績係数も向上することができ排ガス利用等の吸収冷
凍機として応用範囲が広いものである。As an example of such an operation, when cold soot gas generated at a pressure of 60 Hg is increased in pressure to 650 Hg by the pressurizing device 7, the temperature of the cold soot becomes approximately 95 oo, and when it is led to the heat exchanger 8, The absorption liquid in the generator is reheated by the latent heat of condensation of this cold soot, and the lining can be separated again. FIG. 2 shows another embodiment of the present invention, in which the generator 1 and the condenser 2 are connected to a side pipe 10 having a valve 9 whose opening degree is adjusted depending on the load of other cold water in the refrigerant pipe 6. It is attached. When the chilled water load decreases, the controller 11 receives a signal from a detector that detects the chilled water outlet temperature of the evaporator 3, and controls the pressurizing device 7 so that its operating power is suppressed. In addition, if the chilled water load further decreases or the thermal energy of the low-temperature heat source such as exhaust gas increases, and it becomes possible to operate with just the low-temperature heat source, the controller 11 controls the operation of the pressurizing device 7. is stopped and the opening degree of the valve 9 is controlled. Note that this valve 9 may be closed when the pressurizing device 7 is in operation, or may be controlled together with the pressurizing device 7. As described above, the absorption refrigeration system of the present invention utilizes the heat of the cold butterfly whose temperature has been raised by the pressurizing device to generate refrigerant and concentrate the absorption liquid in the generator, and also uses the heat of the low-temperature heat source to supply the generator to the generator. Since it has the function of replenishing and adjusting the heat shortage with the operating energy of the pressurizing device according to the size of the heat shortage for the chilled water load, even if the heating heat source of the generator is low temperature, the operation of the absorption cold moat machine is not affected. There is no problem with this, and it is possible to take out cold water commensurate with the load, and the coefficient of performance can also be improved, so it has a wide range of applications as an absorption refrigerating machine that uses exhaust gas, etc.
第1図は本発明の一実施例を示す吸収冷凍装置の構成図
、第2図は同じく他の実施例を示す構成図である。
1……発生器、2…・・・凝縮器、6・・・…冷煤管路
、7・・・・・・加圧装置、8・・・・・・熱交換器、
11・・…・制御器。
第1図
第2図FIG. 1 is a block diagram of an absorption refrigerating apparatus showing one embodiment of the present invention, and FIG. 2 is a block diagram showing another embodiment. 1... Generator, 2... Condenser, 6... Cold soot pipe line, 7... Pressurizing device, 8... Heat exchanger,
11...Controller. Figure 1 Figure 2
Claims (1)
冷媒管路に冷媒加圧装置、及び加圧装置によつて昇圧さ
れた冷媒と発生器に流入する吸収液とが熱交換する熱交
換器を配設し、かつ、加圧装置の運転を吸収冷凍機の負
荷に応じて制御する制御器を配設したことを特徴とする
吸収冷凍装置。1. A refrigerant pressurizing device is installed in the refrigerant pipe connecting the generator and condenser that make up the absorption refrigerator, and heat is exchanged between the refrigerant pressurized by the pressurizing device and the absorption liquid flowing into the generator. 1. An absorption refrigerating apparatus, comprising an exchanger and a controller for controlling the operation of a pressurizing apparatus according to the load of an absorption refrigerating machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7305277A JPS6025708B2 (en) | 1977-06-17 | 1977-06-17 | absorption refrigeration equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7305277A JPS6025708B2 (en) | 1977-06-17 | 1977-06-17 | absorption refrigeration equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS547651A JPS547651A (en) | 1979-01-20 |
JPS6025708B2 true JPS6025708B2 (en) | 1985-06-19 |
Family
ID=13507198
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7305277A Expired JPS6025708B2 (en) | 1977-06-17 | 1977-06-17 | absorption refrigeration equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6025708B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5749770A (en) * | 1980-09-10 | 1982-03-23 | Ebara Mfg | Cold fluid producing equipment |
JPS60103276A (en) * | 1983-11-07 | 1985-06-07 | 范姜 増承 | Evaporating method and device thereof |
-
1977
- 1977-06-17 JP JP7305277A patent/JPS6025708B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS547651A (en) | 1979-01-20 |
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