JPH079002Y2 - Absorption refrigerator - Google Patents
Absorption refrigeratorInfo
- Publication number
- JPH079002Y2 JPH079002Y2 JP8822088U JP8822088U JPH079002Y2 JP H079002 Y2 JPH079002 Y2 JP H079002Y2 JP 8822088 U JP8822088 U JP 8822088U JP 8822088 U JP8822088 U JP 8822088U JP H079002 Y2 JPH079002 Y2 JP H079002Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat medium
- transfer pipe
- absorber
- regenerator
- absorbent
- 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
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【考案の詳細な説明】 産業上の利用分野 本考案は吸収式冷凍機に関するものである。TECHNICAL FIELD The present invention relates to an absorption chiller.
従来の技術 最近、たとえば室内の空調装置に吸収式冷凍機を用いた
ものがあり、この吸収式冷凍機には、吸収液(たとえば
臭化リチウム水溶液)が使用されている。ところで、こ
の吸収液の濃度は濃い状態で運転されており、この状態
で運転が停止して吸収液の温度が低下すると、結晶が析
出して、運転再開時に解晶作業などを必要とするため、
従来、運転停止前に吸収液の濃度を薄めるための稀釈運
転が行なわれていた。2. Description of the Related Art Recently, for example, there is an air conditioner for indoor use that uses an absorption refrigerator, and an absorption liquid (for example, an aqueous solution of lithium bromide) is used for this absorption refrigerator. By the way, the concentration of this absorbing solution is high, and if the operation is stopped in this state and the temperature of the absorbing solution decreases, crystals will precipitate, and crystallization work etc. will be required when restarting the operation. ,
Conventionally, a dilution operation was performed to dilute the concentration of the absorbing solution before the operation was stopped.
考案が解決しようとする課題 上記従来の構成によると、稀釈運転を行なえる場合はよ
いが、停電時などの非常停止時には、稀釈運転が行なえ
ないという問題があった。Problems to be Solved by the Invention According to the above-described conventional configuration, it is preferable that the dilution operation can be performed, but there is a problem that the dilution operation cannot be performed during an emergency stop such as a power failure.
そこで、本考案は上記問題点を解消し得る吸収式冷凍機
を提供することを目的とする。Then, this invention aims at providing the absorption type refrigerator which can eliminate the said problem.
課題を解決するための手段 上記問題点を解決するため、本考案の吸収式冷凍機は、
熱媒体を蒸発させる蒸発器と、この蒸発器で発生した熱
媒蒸気を吸収液に吸収させる吸収器と、熱媒蒸気を吸収
して濃度が薄くなった稀吸収液を加熱する再生器と、こ
の再生器で得られた熱媒蒸気を凝縮させる凝縮器と、上
記吸収器内の稀吸収液を再生器に移送する稀吸収液移送
管と、上記再生器で再生された濃吸収液を吸収器に移送
する濃吸収液移送管と、上記凝縮器で凝縮された熱媒体
を蒸発器に移送する熱媒体移送管と、途中に第1自動開
閉弁が介装されるとともに上記濃吸収液移送管途中の濃
吸収液を重力により吸収器内または液溜めタンク内に排
出する濃吸収液排出管と、途中に第2自動開閉弁が介装
されるとともに上記蒸発器内の熱媒体を重力により上記
稀吸収液移送管内に導く熱媒体導入管とから構成し、か
つ運転非常停止時に上記第1および第2自動開閉弁が開
状態となるように構成したものである。Means for Solving the Problems In order to solve the above problems, the absorption refrigerator of the present invention is
An evaporator that evaporates the heat medium, an absorber that absorbs the heat medium vapor generated in this evaporator into an absorption liquid, and a regenerator that absorbs the heat medium vapor and heats the rare absorption liquid that has become thin, A condenser for condensing the heat medium vapor obtained in this regenerator, a rare absorbent transfer pipe for transferring the rare absorbent in the absorber to the regenerator, and a concentrated absorbent regenerated in the regenerator. Transfer pipe for transferring the concentrated absorbent to the evaporator, transfer pipe for transferring the heat medium condensed in the condenser to the evaporator, and a first automatic opening / closing valve in the middle, and transfer of the concentrated absorbent A concentrated absorbent discharge pipe that discharges the concentrated absorbent in the middle of the pipe into the absorber or the liquid storage tank by gravity, and a second automatic opening / closing valve in the middle, and the heat medium in the evaporator is gravity driven. Consists of a heat medium introduction pipe that leads into the rare absorption liquid transfer pipe, and during an emergency stop In which said first and second automatic opening and closing valve is configured to be opened.
作用 上記構成において、運転が非常停止すると、各自動開閉
弁が開いて濃吸収液移送管内の濃吸収液は吸収器内また
は液溜めタンク内に排出されるとともに、稀吸収液移送
管内には熱媒体が導入されて吸収液の濃度が薄められる
ため、吸収液の温度が低下しても配管内で結晶が析出す
ることはない。Action In the above configuration, when the operation is stopped, each automatic opening / closing valve is opened, the concentrated absorbent in the concentrated absorbent transfer pipe is discharged into the absorber or the reservoir tank, and the rare absorbent transfer pipe receives heat. Since the medium is introduced to dilute the concentration of the absorbing liquid, crystals do not precipitate in the pipe even if the temperature of the absorbing liquid decreases.
実施例 以下、本考案の一実施例を吸収式冷凍機の概略構成を示
す模式図に基づき説明する。Embodiment An embodiment of the present invention will be described below with reference to a schematic diagram showing a schematic configuration of an absorption refrigerator.
本実施例における吸収式冷凍機は、熱媒体の一例である
水を蒸発させる蒸発器1と、この蒸発器1で発生した水
蒸気を連通部2を介して導くとともにこの水蒸気を吸収
する臭化リチウム(LiBr)水溶液(以下、吸収液とい
う)を有する吸収器3と、水蒸気を吸収して濃度が薄く
なった稀吸収液を加熱する再生器4と、この再生器4で
加熱されることにより発生した水蒸気を連通部5を介し
て導くとともにこの水蒸気を凝縮させる凝縮器6と、途
中に溶液ポンプ7を有して上記吸収器3内の稀吸収液を
再生器4に移送する稀吸収液移送管8と、上記凝縮器6
で凝縮された凝縮水を蒸発器1に移送する凝縮水移送管
9と、途中に熱媒ポンプ10を有するとともに凝縮器6の
底部に溜まった熱媒体である凝縮水を上記凝縮水移送管
9の一部を介して凝縮器6内に循環させる凝縮水循環管
11と、上記再生器4で水蒸気が分離されて濃くなった濃
吸収液を吸収器3に移送する濃吸収液移送管12と、蒸発
器1内に配置された被冷却用流体たとえば水を冷却する
ための第1熱交換器13と、上記吸収器3内に配置された
内部冷却用の第2熱交換器14と、第1熱交換器13に被冷
却用流体である水を導くための被冷却用流体配管15と、
第2熱交換器14に冷却用流体である冷却水を導くための
冷却用流体配管(この冷却用流体配管の出口側部分は凝
縮器6内に導かれて凝縮熱を奪うようにしている。)16
と、再生器4内に配置された吸収液加熱用の加熱管17
と、上記濃吸収液移送管12と稀吸収液移送管8とに亘っ
て設けられて濃吸収液の持つ熱を稀吸収液側に回収する
ための熱回収器18と、一端部が濃吸収液移送管12の途中
に接続されるとともに他端部が吸収器3内の底部に開口
されかつ途中に第1自動開閉弁19が介装された濃吸収液
排出管20と、一端部が凝縮水循環管11途中に接続される
とともに他端部が上記稀吸収液移送管8途中に接続され
かつ途中に第2自動開閉弁21が介装された凝縮水導入管
(熱媒体導入管)22とから構成されている。また、上記
濃吸収液排出管20および凝縮水導入管22においては、そ
れぞれの液体が重力によりすなわち自然落下により流れ
るようにされている。すなわち、濃吸収液排出管20は、
その最下部位置が吸収器3内の液面より必ず上方に位置
するように設けられ、また蒸発器1は吸収器3内の液面
より必ず上方に位置するように設けられている。そし
て、さらに上記第1および第2自動開閉弁19,21は運転
非常停止時に、たとえば停電時に開状態となるように電
気回路とが組まれている。The absorption refrigerating machine in the present embodiment is an example of a heat medium, an evaporator 1 that evaporates water, and a lithium bromide that guides water vapor generated in the evaporator 1 through a communication part 2 and absorbs the water vapor. Absorber 3 having (LiBr) aqueous solution (hereinafter referred to as "absorption liquid"), regenerator 4 that absorbs water vapor and heats the dilute absorption liquid that has become thin, and generated by being heated by this regenerator 4 Transferring the rare absorbed liquid in the absorber 3 to the regenerator 4 having a condenser 6 for guiding the generated water vapor through the communication part 5 and condensing the water vapor, and a solution pump 7 on the way. Tube 8 and the condenser 6
The condensed water transfer pipe 9 for transferring the condensed water condensed in 1 to the evaporator 1 and the heat transfer medium pump 10 in the middle, and the condensed water which is the heat medium accumulated at the bottom of the condenser 6 is transferred to the condensed water transfer pipe 9 Condensed water circulation pipe that circulates in the condenser 6 through a part of
11, a concentrated absorption liquid transfer pipe 12 for transferring the concentrated absorption liquid, which has become thick due to the separation of water vapor in the regenerator 4, to the absorber 3, and a fluid to be cooled, such as water, arranged in the evaporator 1 A first heat exchanger 13 for cooling, a second heat exchanger 14 for internal cooling arranged in the absorber 3, and a first heat exchanger 13 for introducing water as a fluid to be cooled. Fluid pipe 15 for cooling,
A cooling fluid pipe for introducing cooling water, which is a cooling fluid, to the second heat exchanger 14 (the outlet side portion of this cooling fluid pipe is introduced into the condenser 6 so as to remove the heat of condensation. ) 16
And a heating pipe 17 arranged in the regenerator 4 for heating the absorbing liquid.
And a heat recovery device 18 provided between the concentrated absorbent transfer pipe 12 and the rare absorbent transfer pipe 8 for recovering the heat of the concentrated absorbent to the rare absorbent side, and one end of the concentrated heat absorber 18. A concentrated absorbent discharge pipe 20 connected to the middle of the liquid transfer pipe 12, the other end of which is opened to the bottom of the absorber 3 and the first automatic opening / closing valve 19 is interposed, and one end of which is condensed. A condensed water introduction pipe (heat medium introduction pipe) 22 connected to the water circulation pipe 11 and having the other end connected to the rare absorbent transfer pipe 8 and a second automatic opening / closing valve 21 interposed therebetween. It consists of Further, in the concentrated absorbent discharge pipe 20 and the condensed water introduction pipe 22, the respective liquids are caused to flow by gravity, that is, by spontaneous fall. That is, the concentrated absorbent discharge pipe 20 is
The lowermost position is provided so as to always be located above the liquid level in the absorber 3, and the evaporator 1 is provided so as to be always located above the liquid level in the absorber 3. Further, the first and second automatic open / close valves 19 and 21 are assembled with an electric circuit so that they are opened during an emergency stop of operation, for example, during a power failure.
上記構成において、通常運転時には、蒸発→吸収→再生
→凝縮作用が繰返されて冷却機能が発揮される。たとえ
ば、空調装置の室内熱交換器に循環される被冷却用流体
である水が蒸発器1に設けられた第1熱交換器13にて冷
却される。上記通常運転時においては、濃吸収液の濃度
は61%程度であり、稀吸収液の濃度は57%程度である。In the above configuration, during normal operation, the cooling function is exerted by repeating the evaporation, absorption, regeneration, and condensation actions. For example, water that is a fluid to be cooled circulated in the indoor heat exchanger of the air conditioner is cooled by the first heat exchanger 13 provided in the evaporator 1. During the above normal operation, the concentration of the concentrated absorbing liquid is about 61%, and the concentration of the rare absorbing liquid is about 57%.
そして、運転中、たとえば停電により運転が非常停止す
ると、第1および第2自動開閉弁19,21が自動的に開
き、濃吸収液移送管12内の濃吸収液は吸収器3内に排出
されるとともに稀吸収液移送管8には熱媒体である水が
流入してその濃度は25%〜35%程度に薄められる。この
濃度は吸収液の温度が低下した場合でも、結晶しない濃
度である。このように、運転非常停止時に、濃吸収液移
送管12内の濃吸収液はほとんど吸収器3内に排出される
とともに、稀吸収液移送管8内の稀吸収液を所定の濃度
に薄めるようにしたので、各移送管内に結晶が析出せ
ず、したがって非常停止の場合の運転再開時に解晶作業
を行う必要がない。なお、通常の終了時には、従来通り
の稀釈運転が行われる。Then, during operation, for example, when the operation is stopped due to a power failure, the first and second automatic opening / closing valves 19 and 21 are automatically opened, and the concentrated absorbent in the concentrated absorbent transfer pipe 12 is discharged into the absorber 3. At the same time, water, which is a heat medium, flows into the dilute absorption liquid transfer pipe 8 and its concentration is diluted to about 25% to 35%. This concentration is a concentration that does not crystallize even when the temperature of the absorbing liquid decreases. Thus, during an emergency stop of operation, most of the concentrated absorbent in the concentrated absorbent transfer pipe 12 is discharged into the absorber 3, and the diluted absorbent in the rare absorbent transfer pipe 8 is diluted to a predetermined concentration. Therefore, crystals do not precipitate in each transfer pipe, and therefore, it is not necessary to perform the crystallization process when the operation is restarted in the case of an emergency stop. At the normal end, the conventional dilution operation is performed.
ところで、図面においては、蒸発器1、吸収器3、再生
器4および凝縮器6を一体的に図示したが、勿論、これ
は模式図であるため、実際には、各機器は場合に応じて
別体構成とされる。また、吸収器3、凝縮器6などにお
ける熱交換用流体として水を使用したが、勿論、空気な
どの気体を使用してもよい。By the way, in the drawings, the evaporator 1, the absorber 3, the regenerator 4 and the condenser 6 are shown in an integrated manner, but of course, this is a schematic diagram, and therefore, in practice, each device may be different depending on the case. It is configured separately. Further, although water is used as the heat exchange fluid in the absorber 3, the condenser 6, etc., of course, a gas such as air may be used.
また、上記実施例においては、再生器4内の溶液は特別
に稀釈していないが、結晶した場合でも再加熱時に溶解
するので問題はないが、たとえば上記濃吸収液排出管20
などと同様に自動開閉弁を有する配管を別に設けて吸収
器内の底部に排出するようにしてもよい。Further, in the above embodiment, the solution in the regenerator 4 is not particularly diluted, but even if it crystallizes, there is no problem because it dissolves when reheated. For example, the concentrated absorbent discharge pipe 20
Similarly to the above, a pipe having an automatic opening / closing valve may be separately provided to discharge to the bottom of the absorber.
ところで、上記実施例においては、濃吸収液移送管内の
濃吸収液を、吸収器内に排出するようにしたが、別途液
溜めタンクを設けてこの液溜めタンク内に濃吸収液を排
出するようにしてもよい。By the way, in the above-described embodiment, the concentrated absorbent in the concentrated absorbent transfer pipe is discharged into the absorber, but a separate reservoir tank is provided so that the concentrated absorbent is discharged into the reservoir tank. You may
考案の効果 上記本考案の構成によると、運転非常停止時に、各自動
開閉弁が開いて濃吸収液移送管内の濃吸収液は吸収器内
または液溜めタンク内に排出されるとともに、稀吸収液
移送管内には熱媒体が導入されて吸収液の濃度が薄めら
れるため、吸収液の温度が低下しても配管内で結晶が析
出せず、したがって運転再開時に解晶作業を必要としな
い。Effect of the Invention According to the configuration of the present invention described above, at the time of an emergency stop of operation, each automatic opening / closing valve is opened so that the concentrated absorbent in the concentrated absorbent transfer pipe is discharged into the absorber or the reservoir tank, and the rare absorbent is also absorbed. Since the heat medium is introduced into the transfer pipe to dilute the concentration of the absorbing liquid, crystals do not precipitate in the pipe even if the temperature of the absorbing liquid is lowered, and therefore, no crystallization work is required when restarting the operation.
図面は本考案の一実施例における吸収式冷凍機の概略構
成を示す模式図である。 1……蒸発器、3……吸収器、4……再生器、6……凝
縮器、8……稀吸収液移送管、9……凝縮水移送管、11
……凝縮水循環管、12………濃吸収液移送管、19……第
1自動開閉弁、20……濃吸収液排出管、21……第2自動
開閉弁、22……凝縮水導入管。The drawings are schematic views showing a schematic configuration of an absorption refrigerator according to an embodiment of the present invention. 1 ... Evaporator, 3 ... Absorber, 4 ... Regenerator, 6 ... Condenser, 8 ... Rare absorbent transfer pipe, 9 ... Condensate transfer pipe, 11
...... Condensed water circulation pipe, 12 ...... Concentrated absorbent transfer pipe, 19 ...... First automatic opening / closing valve, 20 ...... Dense absorbent discharging pipe, 21 ...... Second automatic opening / closing valve, 22 ...... Condensed water introduction pipe .
───────────────────────────────────────────────────── フロントページの続き (72)考案者 坂端 伸治 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (72)考案者 河内 襄介 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (72)考案者 梅田 辰彦 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (72)考案者 古寺 雅晴 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (72)考案者 松田 光史 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (72)考案者 矢野 猛 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (72)考案者 岡本 英明 大阪府大阪市西区江戸堀1丁目6番14号 日立造船株式会社内 (56)参考文献 特開 昭57−74562(JP,A) 特開 昭51−52545(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Shinji Sakabata 1-6-14 Edobori, Nishi-ku, Osaka City, Osaka Prefecture Hitachi Shipbuilding Co., Ltd. (72) Yosuke Kawauchi 1-6, Edobori, Nishi-ku, Osaka City, Osaka Prefecture 14 Hitachi Shipbuilding Co., Ltd. (72) Inventor Tatsuhiko Umeda 1-6-14 Edobori, Nishi-ku, Osaka-shi, Osaka Prefecture Hitachi Shipbuilding Co., Ltd. (72) Masaharu Furuji 1-6-14 Edobori, Nishi-ku, Osaka City, Osaka Prefecture Inside Hitachi Shipbuilding Co., Ltd. (72) Mitsufumi Matsuda 1-6-14 Edobori, Nishi-ku, Osaka City, Osaka Prefecture Hitachi Shipbuilding Co., Ltd. (72) Takeshi Yano 1-6-14 Edobori, Nishi-ku, Osaka City, Osaka Prefecture Hitachi Shipbuilding Incorporated (72) Inventor Hideaki Okamoto 1-6-14 Edobori, Nishi-ku, Osaka City, Osaka Prefecture Hitachi Shipbuilding Co., Ltd. (56) Reference JP-A-57-74562 ( P, A) JP Akira 51-52545 (JP, A)
Claims (1)
で発生した熱媒蒸気を吸収液に吸収させる吸収器と、熱
媒蒸気を吸収して濃度が薄くなった稀吸収液を加熱する
再生器と、この再生器で得られた熱媒蒸気を凝縮させる
凝縮器と、上記吸収器内の稀吸収液を再生器に移送する
稀吸収液移送管と、上記再生器で再生された濃吸収液を
吸収器に移送する濃吸収液移送管と、上記凝縮器で凝縮
された熱媒体を蒸発器に移送する熱媒体移送管と、途中
に第1自動開閉弁が介装されるとともに上記濃吸収液移
送管途中の濃吸収液を重力により吸収器内または液溜め
タンク内に排出する濃吸収液排出管と、途中に第2自動
開閉弁が介装されるとともに上記蒸発器内の熱媒体を重
力により上記稀吸収液移送管内に導く熱媒体導入管とか
ら構成し、かつ運転非常停止時に上記第1および第2自
動開閉弁が開状態となるように構成したことを特徴とす
る吸収式冷凍機。1. An evaporator for evaporating a heat medium, an absorber for absorbing a heat medium vapor generated in the evaporator into an absorbing liquid, and a rare absorbing liquid whose concentration is thinned by absorbing the heat medium vapor. Regenerator, a condenser for condensing the heat medium vapor obtained in the regenerator, a rare absorbent transfer pipe for transferring the rare absorbent in the absorber to the regenerator, and a regenerator regenerated in the regenerator. A rich absorption liquid transfer pipe for transferring the concentrated absorption liquid to the absorber, a heat medium transfer pipe for transferring the heat medium condensed in the condenser to the evaporator, and a first automatic opening / closing valve provided in the middle A concentrated absorbent discharge pipe for discharging the concentrated absorbent in the middle of the concentrated absorbent transfer pipe into the absorber or the reservoir tank by gravity, and a second automatic opening / closing valve provided in the middle of the concentrated absorbent transfer pipe It is composed of a heat medium introducing pipe that guides the heat medium into the rare absorbent transfer pipe by gravity, and Emergency stop absorption refrigerating machine, characterized in that said first and second automatic opening and closing valve is configured so as to be opened at the time.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8822088U JPH079002Y2 (en) | 1988-07-02 | 1988-07-02 | Absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8822088U JPH079002Y2 (en) | 1988-07-02 | 1988-07-02 | Absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH029765U JPH029765U (en) | 1990-01-22 |
| JPH079002Y2 true JPH079002Y2 (en) | 1995-03-06 |
Family
ID=31312795
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8822088U Expired - Lifetime JPH079002Y2 (en) | 1988-07-02 | 1988-07-02 | Absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH079002Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5457163B2 (en) * | 2009-12-21 | 2014-04-02 | 川重冷熱工業株式会社 | Control method and apparatus for absorption chiller / heater using exhaust gas of distributed power generation system |
-
1988
- 1988-07-02 JP JP8822088U patent/JPH079002Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH029765U (en) | 1990-01-22 |
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