JPS6148067B2 - - Google Patents
Info
- Publication number
- JPS6148067B2 JPS6148067B2 JP56151943A JP15194381A JPS6148067B2 JP S6148067 B2 JPS6148067 B2 JP S6148067B2 JP 56151943 A JP56151943 A JP 56151943A JP 15194381 A JP15194381 A JP 15194381A JP S6148067 B2 JPS6148067 B2 JP S6148067B2
- Authority
- JP
- Japan
- Prior art keywords
- absorber
- solution
- bleed
- evaporator
- pipe
- 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、冷媒及び吸収溶液を用いて吸収冷凍
サイクルを行う吸収冷凍機の抽気装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an air extraction device for an absorption refrigerator that performs an absorption refrigeration cycle using a refrigerant and an absorption solution.
吸収冷凍機にあつては、機外から漏入する空気
あるいは内部で発生するガス等の不凝縮ガスが存
在すると、冷凍機の能力低下を引起し、甚しい場
合には作動不能に陥るためこの不凝縮ガスを排除
する必要がある。 In the case of an absorption chiller, the presence of non-condensable gas such as air leaking from outside the machine or gas generated inside the machine will cause the capacity of the chiller to decrease, and in severe cases, it will become inoperable. It is necessary to exclude non-condensable gases.
不凝縮ガスを捕集、排除する方法としては真空
ポンプにより吸収器等から直接不凝縮ガスを吸引
排出する方式、溶液ポンプからの吐出液をエゼク
タに導き吸引捕集する方式又は吸収器に流入する
濃溶液の一部を冷却し、低圧部を形成して吸引捕
集する方式などがある。 Methods for collecting and eliminating non-condensable gas include a method in which a vacuum pump directly sucks and discharges the non-condensable gas from an absorber, etc., a method in which the discharged liquid from a solution pump is guided to an ejector and collected by suction, or a method in which it flows into an absorber. There is a method in which a part of the concentrated solution is cooled, a low-pressure part is formed, and the solution is collected by suction.
しかしながら、濃溶液の一部を利用する抽気装
置にあつては機外からの空気漏入、又は冷水、冷
却水温の変動等により溶液の濃度が異常に上昇し
た際、結晶を引起し、抽気装置が、満足に作動し
なくなる欠点がある。 However, in the case of an air bleed system that uses a portion of a concentrated solution, if the concentration of the solution rises abnormally due to air leakage from outside the machine or changes in cold water or cooling water temperature, crystals may form and the bleed system However, there is a drawback that it does not work satisfactorily.
本発明の目的は、この欠点を除去すると共に、
不凝縮ガスの排除を有効に行うことができる装置
を提供することにある。 The aim of the invention is to eliminate this drawback and
The object of the present invention is to provide a device that can effectively eliminate non-condensable gas.
すなわち本発明を概説すれば、本発明は吸収
器、蒸発器、発生器、凝縮器及び熱交換器とこれ
らを接続する冷媒径路及び溶液径路から構成され
る吸収冷凍機において、内部に冷却管を配置した
抽気タンクに吸収器へ流入する濃溶液の一部を分
岐すると共に、該抽気タンクと吸収器とを接続す
る管路を設け、更に該抽気タンクと蒸発器とを濃
度調整用管路で接続したことを特徴とする吸収冷
凍機の抽気装置に関する。 That is, to summarize the present invention, the present invention provides an absorption refrigerator that includes an absorber, an evaporator, a generator, a condenser, a heat exchanger, and a refrigerant path and a solution path that connect these. A part of the concentrated solution flowing into the absorber is branched into the arranged bleed tank, and a pipe is provided to connect the bleed tank and the absorber, and a concentration adjustment pipe is connected between the bleed tank and the evaporator. The present invention relates to a bleed device for an absorption refrigerator, which is characterized in that it is connected to the bleed device.
以下、本発明を添付図面に基づいて詳細に説明
する。 Hereinafter, the present invention will be explained in detail based on the accompanying drawings.
第1図は、本発明の一実施の態様を示す単効用
吸収冷凍機の装置の系統図である。 FIG. 1 is a system diagram of a single-effect absorption refrigerator device showing an embodiment of the present invention.
第1図に示した吸収冷凍機には、吸収器1、蒸
発器2、発生器3、凝縮器4、熱交換器5、抽気
タンク11、気液分離器12、不凝縮ガス溜め1
3、それらを駆動させる、溶液ポンプ6、冷媒ポ
ンプ7、冷却水通路8、冷水通路9、加熱源1
0、そして各配管14〜22が配置されている。 The absorption refrigerating machine shown in FIG.
3. Solution pump 6, refrigerant pump 7, cooling water passage 8, cold water passage 9, heating source 1 to drive them.
0, and each piping 14 to 22 are arranged.
第1図において、冷却水通路8の吸収器1入口
側から分岐した冷却管16が、抽気タンク11内
を通り、吸収器出口側に接続されている。抽気タ
ンク11には発生器3において加熱源10により
加熱濃縮され、熱交換器5、配管14を通り吸収
器1に流入する濃溶液の一部が分岐管15により
導びかれる。 In FIG. 1, a cooling pipe 16 branched from the absorber 1 inlet side of the cooling water passage 8 passes through the bleed tank 11 and is connected to the absorber outlet side. A part of the concentrated solution that is heated and concentrated by the heat source 10 in the generator 3 and flows into the absorber 1 through the heat exchanger 5 and piping 14 is guided to the bleed tank 11 through a branch pipe 15 .
抽気タンク11では、分岐管15により流入し
た濃溶液の一部が冷却水管16により冷却され、
吸収器1の圧力より若干低い低圧部を形成するの
で吸収器内の冷媒蒸気の一部と不凝縮ガスは、不
凝縮ガス捕集管17で抽気タンク11内に吸引さ
れ冷媒蒸気は濃溶液に吸収される。 In the bleed tank 11, a part of the concentrated solution flowing through the branch pipe 15 is cooled by the cooling water pipe 16.
Since a low-pressure part is formed that is slightly lower than the pressure of the absorber 1, a part of the refrigerant vapor and non-condensable gas in the absorber are sucked into the extraction tank 11 through the non-condensable gas collection pipe 17, and the refrigerant vapor becomes a concentrated solution. Absorbed.
冷却管16で冷却され冷媒蒸気の一部を吸収し
た溶液は、抽気タンク11内に吸引された不凝縮
ガスを巻込みながらサイホン管18を通り気液分
離器12に導かれ、不凝縮ガスと溶液とは分離さ
れ不凝縮ガスは、ガス通路22を上昇し、不凝縮
ガス溜め13に蓄えられる。他方溶液は、溶液戻
し管20で溶液ポンプ6の吸込側に戻される。 The solution, which has been cooled by the cooling pipe 16 and has absorbed a portion of the refrigerant vapor, passes through the siphon pipe 18 and is guided to the gas-liquid separator 12 while entraining the non-condensable gas sucked into the bleed tank 11, where it is separated from the non-condensable gas. The non-condensable gas separated from the solution ascends through the gas passage 22 and is stored in the non-condensable gas reservoir 13. On the other hand, the solution is returned to the suction side of the solution pump 6 through a solution return pipe 20.
更に、本発明の抽気装置では、蒸発器2と抽気
タンク11を連通する濃度調整管19が設けられ
ている。 Further, in the air extraction device of the present invention, a concentration adjustment pipe 19 that communicates the evaporator 2 and the air extraction tank 11 is provided.
吸収冷凍機では溶液サイクル中の溶液の平均濃
度が上昇すると蒸発器2内に保有される冷媒量は
増加する。 In an absorption refrigerator, as the average concentration of the solution during the solution cycle increases, the amount of refrigerant held in the evaporator 2 increases.
したがつて溶液が所定の濃度以上に上昇した場
合、すなわち蒸発器内の冷媒液面が所定の高さ以
上に上昇した際、冷媒がオーバーフローする位置
に冷媒配管19の取出し口を設置しておけば機外
からの空気漏入、冷水、冷却水温度の変動等に伴
い溶液濃度が異常に上昇した場合にも、抽気タン
ク内には蒸発器2内の冷媒がオーバーフローして
流入するため、結晶析出を防止し、正常な抽気動
作を維持することができる。 Therefore, the outlet of the refrigerant pipe 19 should be installed at a position where the refrigerant will overflow when the solution rises to a predetermined concentration or higher, that is, when the refrigerant liquid level in the evaporator rises to a predetermined height or higher. For example, even if the solution concentration abnormally increases due to air leakage from outside the machine, chilled water, or fluctuations in cooling water temperature, the refrigerant in the evaporator 2 will overflow and flow into the bleed tank, causing crystallization. Precipitation can be prevented and normal extraction operation can be maintained.
本発明の実施の態様において、別の例では、上
記の場合に、冷却管16が冷水通路9から分岐し
たものでもよい。 In another example of the embodiment of the present invention, the cooling pipe 16 may be branched from the cold water passage 9 in the above case.
次に第2図は、本発明の一実施の態様である二
重効用吸収冷凍機の装置の系統図である。 Next, FIG. 2 is a system diagram of a dual-effect absorption refrigerating machine which is an embodiment of the present invention.
第2図において、符号1,2,4,6〜9,1
1〜22は第1図と同義である。そして25は第
1発生器、26は第2発生器、27は第2熱交換
器、28は第1熱交換器である。 In Figure 2, symbols 1, 2, 4, 6 to 9, 1
1 to 22 have the same meanings as in FIG. 25 is a first generator, 26 is a second generator, 27 is a second heat exchanger, and 28 is a first heat exchanger.
第2図に示した本発明による二重効用吸収冷凍
機においても、抽気タンク11、管路17及び1
9の作用効果が第1図に示した装置と同じであ
る。 Also in the double effect absorption refrigerator according to the present invention shown in FIG.
The operation and effect of No. 9 are the same as those of the device shown in FIG.
以上、詳細に説明したとおり、本発明によれ
ば、内部に冷却管を配置した抽気タンクに吸収器
へ流入する濃溶液の一部を分岐すると共に、該抽
気タンクと吸収器とを接続する管路を設け、更に
該抽気タンクと蒸発器とを濃度調節用管路で接続
したことにより、不凝縮ガスの排除を有効に行う
ことができると共に、溶液濃度の異常上昇時に、
抽気装置内での結晶析出を防止することができる
という、実用上、従来の吸収冷凍機に勝る効果を
奏する。 As described in detail above, according to the present invention, a part of the concentrated solution flowing into the absorber is branched to the bleed tank having a cooling pipe arranged inside, and a pipe connecting the bleed tank and the absorber is provided. By connecting the bleed tank and the evaporator with a concentration adjustment pipe, it is possible to effectively eliminate non-condensable gases, and also to prevent the concentration of the solution from increasing abnormally.
In practical terms, it is more effective than conventional absorption refrigerators in that crystal precipitation within the bleed device can be prevented.
第1図は、本発明の一実施の態様を示す単効用
吸収冷凍機の装置の系統図である。第2図は、本
発明の一実施の態様を示す二重効用吸収冷凍機の
装置の系統図である。
1:吸収器、2:蒸発器、3:発生器、4:凝
縮器、5:熱交換器、6:溶液ポンプ、7:冷媒
ポンプ、8:冷却水通路、9:冷水通路、10:
加熱源、11:抽気タンク、12:気液分離器、
13:不凝縮ガス溜め、19:濃度調整管、2
5:第1発生器、26:第2発生器、27:第2
熱交換器、28:第1熱交換器。
FIG. 1 is a system diagram of a single-effect absorption refrigerator device showing an embodiment of the present invention. FIG. 2 is a system diagram of a dual-effect absorption refrigerator device showing an embodiment of the present invention. 1: Absorber, 2: Evaporator, 3: Generator, 4: Condenser, 5: Heat exchanger, 6: Solution pump, 7: Refrigerant pump, 8: Cooling water passage, 9: Cold water passage, 10:
heating source, 11: extraction tank, 12: gas-liquid separator,
13: Non-condensable gas reservoir, 19: Concentration adjustment tube, 2
5: first generator, 26: second generator, 27: second
Heat exchanger, 28: first heat exchanger.
Claims (1)
器と、それらを接続する冷媒径路及び溶液径路か
ら構成される吸収冷凍機において、内部に冷却管
を配置した抽気タンクに吸収器へ流入する濃溶液
の一部を分岐すると共に、該抽気タンクと吸収器
とを接続する管路を設け、更に該抽気タンクと蒸
発器とを濃度調整用管路で接続したことを特徴と
する吸収冷凍機の抽気装置。1. In an absorption refrigerator consisting of an absorber, evaporator, generator, condenser, and heat exchanger, and a refrigerant path and a solution path that connect them, air flows into the absorber into a bleed tank with a cooling pipe inside. Absorption refrigeration characterized in that a part of the concentrated solution to be extracted is branched, a pipe line is provided to connect the bleed tank and the absorber, and the bleed tank and the evaporator are further connected by a concentration adjustment pipe line. Air extraction device of the machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15194381A JPS5855665A (en) | 1981-09-28 | 1981-09-28 | Bleed device for absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15194381A JPS5855665A (en) | 1981-09-28 | 1981-09-28 | Bleed device for absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5855665A JPS5855665A (en) | 1983-04-02 |
| JPS6148067B2 true JPS6148067B2 (en) | 1986-10-22 |
Family
ID=15529595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15194381A Granted JPS5855665A (en) | 1981-09-28 | 1981-09-28 | Bleed device for absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5855665A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56156932U (en) * | 1980-04-22 | 1981-11-24 | ||
| JPS59160843U (en) * | 1983-04-13 | 1984-10-27 | 愛三工業株式会社 | Pressure regulation mechanism of fuel supply system of LPG engine |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55102869A (en) * | 1979-01-31 | 1980-08-06 | Hitachi Ltd | Automatic bleeder for absorption type water cooling and heating machine |
-
1981
- 1981-09-28 JP JP15194381A patent/JPS5855665A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5855665A (en) | 1983-04-02 |
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