JPH025990B2 - - Google Patents
Info
- Publication number
- JPH025990B2 JPH025990B2 JP12586782A JP12586782A JPH025990B2 JP H025990 B2 JPH025990 B2 JP H025990B2 JP 12586782 A JP12586782 A JP 12586782A JP 12586782 A JP12586782 A JP 12586782A JP H025990 B2 JPH025990 B2 JP H025990B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- evaporator
- cooling
- absorption liquid
- heating
- 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
- 239000003507 refrigerant Substances 0.000 claims description 84
- 239000007788 liquid Substances 0.000 claims description 72
- 238000010521 absorption reaction Methods 0.000 claims description 63
- 238000010438 heat treatment Methods 0.000 claims description 36
- 238000001816 cooling Methods 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 238000005086 pumping Methods 0.000 claims description 12
- 239000006096 absorbing agent Substances 0.000 claims description 9
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000007710 freezing Methods 0.000 description 4
- 230000008014 freezing Effects 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は、吸収冷凍機の冷暖切替装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heating/cooling switching device for an absorption refrigerator.
特に冷房及び暖房の運転の切替を1個の冷暖切
替弁の操作により簡単にできるようにし、外気温
の低い暖房時における冷媒の凍結と吸収液の結晶
の防止を図つたものである。 In particular, it is possible to easily switch between cooling and heating operations by operating a single cooling/heating switching valve, and is intended to prevent freezing of the refrigerant and crystallization of the absorption liquid during heating when the outside temperature is low.
従来、吸収冷凍機においては、暖房運転時には
温水が冷房運転時の吸収器及び凝縮器の冷却水系
統より取り出されるため、機械の附帯設備側でも
関連する多数の冷暖切替弁を操作する必要があり
甚だ煩雑であつた。そこで、このような煩雑な冷
暖切替弁を全廃し、温水を冷却水系統に代えて冷
房運転時の蒸発器の冷水系統から取り出す方法を
講じている。 Conventionally, in absorption chillers, during heating operation, hot water is taken out from the cooling water system of the absorber and condenser during cooling operation, so it is necessary to operate a large number of related cooling/heating switching valves on the machine's auxiliary equipment side. It was extremely complicated. Therefore, such a complicated cooling/heating switching valve is completely abolished and hot water is taken out from the evaporator's cold water system during cooling operation instead of the cooling water system.
すなわち、第1図に示すように、高度に真空に
保たれた筒状体の胴部1内は仕切壁2によつて上
下に仕切られ、その上部高圧側には低温再生器5
と凝縮器6が、また下部低圧側には吸収器3と蒸
発器4がそれぞれ収納されており、これらは全べ
て伝熱管群で構成されている。 That is, as shown in FIG. 1, the inside of the body 1 of the cylindrical body kept in a highly vacuum state is divided into upper and lower parts by a partition wall 2, and a low-temperature regenerator 5 is installed on the high-pressure side of the upper part.
and a condenser 6, and an absorber 3 and an evaporator 4 are housed on the lower low-pressure side, all of which are composed of a group of heat transfer tubes.
冷房運転時には、冷媒液散布装置8によつて蒸
発器4の管群の管表面に散布された冷媒は蒸発器
4の管内を流通している水より熱を奪い気化して
蒸発する。 During cooling operation, the refrigerant sprayed onto the tube surface of the tube group of the evaporator 4 by the refrigerant liquid dispersion device 8 absorbs heat from the water flowing through the tubes of the evaporator 4 and evaporates.
この蒸発した冷媒蒸気は、吸収液散布装置9よ
り吸収器3の管群の管表面に散布される濃吸収液
に吸収される。この吸収作用によつて蒸発器4で
の冷媒の蒸発が連続的に行なわれ、蒸発器4の管
内の水が管壁を通じ連続的に冷却される。従つ
て、この冷水を各種の冷却用に使用することがで
きる。 This evaporated refrigerant vapor is absorbed by the concentrated absorption liquid that is sprayed onto the tube surface of the tube group of the absorber 3 by the absorption liquid distribution device 9. Due to this absorption action, the refrigerant in the evaporator 4 is continuously evaporated, and the water in the tube of the evaporator 4 is continuously cooled through the tube wall. Therefore, this cold water can be used for various cooling purposes.
冷媒蒸気を吸収した吸収液は稀吸収液として液
溜11に溜る。この稀吸収液は吸収液ポンプ14
によつて管路を通らせて低温熱交換器12を経て
高温熱交換器13によつて昇温した後、管路を通
り高温再生器7に導かれる。この高温再生器7に
は吸収液が所定の液面を保つまで充填されてお
り、その吸収液中にこの例では加熱源として外部
より管路17で供給する燃料を燃焼させる燃焼室
16で生じる燃焼ガスの通路を形成する伝熱管群
が配置され、これにより燃焼の熱により吸収液を
加熱沸騰させると、吸収器3で吸収した水分の一
部を蒸発させ濃縮され中間濃度吸収液となる。こ
の中間濃度吸収液は高温再生器7より管路に流出
し高温熱交換器13に流入し、ここで稀吸収液と
熱交換した後、低温再生器5に導かれ、この低温
再生器5での管群内を流れる冷媒蒸気により再び
加熱され冷媒が蒸発し濃縮され高濃度の吸収液と
なる。この高濃度吸収液は低温再生器5より流出
し管路を経て低温熱交換器12に入り稀吸収液と
熱交換した後、吸収液散布装置9によつて吸収器
3の管群の管表面に散布され、蒸発器4からの冷
媒蒸気を吸収し、再び稀吸収液として液溜11に
流下して溜り循環を繰り返えす。 The absorption liquid that has absorbed the refrigerant vapor is collected in the liquid reservoir 11 as a dilute absorption liquid. This diluted absorption liquid is absorbed by the absorption liquid pump 14.
The heat is passed through a pipe, passed through a low-temperature heat exchanger 12, heated by a high-temperature heat exchanger 13, and then guided to a high-temperature regenerator 7 through a pipe. This high-temperature regenerator 7 is filled with an absorption liquid until a predetermined liquid level is maintained. A group of heat transfer tubes is arranged to form a path for combustion gas, and when the absorption liquid is heated and boiled by the heat of combustion, a part of the water absorbed in the absorber 3 is evaporated and concentrated to become an intermediate concentration absorption liquid. This intermediate concentration absorption liquid flows out from the high temperature regenerator 7 into the pipe line, flows into the high temperature heat exchanger 13, where it exchanges heat with the dilute absorption liquid, and then is led to the low temperature regenerator 5, where it is The refrigerant is heated again by the refrigerant vapor flowing through the tube group, and the refrigerant evaporates and concentrates to become a highly concentrated absorption liquid. This high-concentration absorbent flows out from the low-temperature regenerator 5 and enters the low-temperature heat exchanger 12 through a pipe, where it exchanges heat with the dilute absorbent. It absorbs the refrigerant vapor from the evaporator 4, flows down to the liquid reservoir 11 again as a dilute absorption liquid, and repeats the reservoir circulation.
一方、高温再生器7で蒸発した冷媒蒸気は、管
路を通り低温再生器5の管群の管内に流入し、高
温再生器7からの中間濃度吸収液を加熱濃縮した
後、凝縮器6に導かれて凝縮し冷媒液となる。こ
の冷媒液は、冷媒溜10に溜つた冷媒液と混合
し、冷媒散布装置8から散布され、蒸発器4の管
群の管表面を流下しつつ蒸発した冷媒蒸気は吸収
器3で吸収液に吸収されるが、未蒸発の冷媒は冷
媒溜10に溜る。 On the other hand, the refrigerant vapor evaporated in the high-temperature regenerator 7 flows through the pipe line into the tube group of the low-temperature regenerator 5, heats and concentrates the intermediate concentration absorption liquid from the high-temperature regenerator 7, and then flows into the condenser 6. It condenses and becomes a refrigerant liquid. This refrigerant liquid mixes with the refrigerant liquid accumulated in the refrigerant reservoir 10 and is dispersed from the refrigerant distribution device 8, and the refrigerant vapor that evaporates while flowing down the tube surface of the tube group of the evaporator 4 becomes an absorption liquid in the absorber 3. The absorbed but unevaporated refrigerant accumulates in the refrigerant reservoir 10.
次いで管路を通り冷媒ポンプ15によつて冷媒
液は、冷媒散布装置8に戻り循環を繰り返えす。 The refrigerant liquid then passes through the pipe and is returned to the refrigerant distribution device 8 by the refrigerant pump 15 to repeat the circulation.
以上が吸収冷凍機の冷房時の冷媒及び吸収液の
動きであるが、暖房時には温水を取出すのに、こ
の例では、低温再生器5から凝縮器6の冷媒液溜
に導く高温の冷媒蒸気をバイパスして蒸発器4に
供給し、蒸発器の管内を流通する水を加熱昇温し
て温水を発生させるようにしている。暖房運転時
は冷房運転時に比べ外気温が低いため、運転停止
時には吸収液の結晶及び蒸発器4の下部の冷媒溜
10に溜つた冷媒液の凍結のおそれがある。 The above is the movement of refrigerant and absorption liquid during cooling in an absorption refrigerator.In order to extract hot water during heating, in this example, high-temperature refrigerant vapor is guided from the low-temperature regenerator 5 to the refrigerant reservoir in the condenser 6. The water is bypassed and supplied to the evaporator 4, and the water flowing through the pipes of the evaporator is heated and heated to generate hot water. Since the outside temperature is lower during heating operation than during cooling operation, there is a risk of crystallization of the absorption liquid and freezing of the refrigerant liquid accumulated in the refrigerant reservoir 10 at the bottom of the evaporator 4 when the operation is stopped.
前記要求から暖房時運転用の冷媒蒸気として、
低温再生器5の出口から凝縮器6の冷媒液溜に導
く管路から分岐して分岐管18を設け、この分岐
管すなわち冷媒蒸気導管によつて高温の冷媒蒸気
を再生器から蒸発器4に直接供給するようにして
いる。一方、吸収液の結晶防止及び冷媒の凍結防
止のため、吸収液ポンプ14の吐出側の管路から
分岐管20を分岐させ、吸収器3の下部の液溜1
1の稀吸収液の一部を蒸発器4の下部の冷媒溜1
0に導くことにより冷媒溜10内の冷媒の一部を
オーバーフローさせて稀吸収液の液溜11に流入
させ、稀吸収液の濃度を上げないようにしてい
る。そして暖房運転時には、各分岐管18,20
に設けた冷暖切替弁19,21の操作によつて弁
を開放していた。 Based on the above requirements, as refrigerant vapor for heating operation,
A branch pipe 18 is provided branching from the pipe leading from the outlet of the low-temperature regenerator 5 to the refrigerant reservoir of the condenser 6, and the high-temperature refrigerant vapor is transferred from the regenerator to the evaporator 4 through this branch pipe, that is, the refrigerant vapor conduit. We are trying to supply it directly. On the other hand, in order to prevent crystallization of the absorption liquid and prevention of freezing of the refrigerant, a branch pipe 20 is branched from the discharge side pipe of the absorption liquid pump 14, and a liquid reservoir 1 at the lower part of the absorber 3 is provided.
A part of the dilute absorption liquid of 1 is transferred to the refrigerant reservoir 1 at the bottom of the evaporator 4.
By guiding the refrigerant to zero, a part of the refrigerant in the refrigerant reservoir 10 overflows and flows into the dilute absorption liquid reservoir 11, thereby preventing the concentration of the dilute absorption liquid from increasing. During heating operation, each branch pipe 18, 20
The valves were opened by operating the cooling/heating switching valves 19 and 21 provided in the air conditioner.
このように従来の冷暖切替装置では、冷暖切替
弁を2個必要とするため、切替時の操作が煩雑で
あるばかりでなく、誤操作に基く機械故障の原因
ともなつていた。 As described above, the conventional heating/cooling switching device requires two heating/cooling switching valves, which not only complicates switching operations but also causes mechanical failures due to erroneous operations.
本発明は前記従来の欠点をすべて除去したもの
であつて、冷暖切替装置に新規な工夫を施し、操
作がワンタツチ(一動作)でよく、誤操作の無い
吸収冷凍機の冷暖切替装置を提供しようとするも
のである。 The present invention eliminates all of the above-mentioned conventional drawbacks, and aims to provide a heating/cooling switching device for an absorption chiller that requires only one touch (one action) to operate and is free from erroneous operation by applying new innovations to the heating/cooling switching device. It is something to do.
その要旨は、冷房時に冷水の流通する蒸発器か
ら暖房時に温水を取出す吸収冷凍機において、高
温の冷媒蒸気を再生器から蒸発器に供給する冷媒
蒸気導管に、稀吸収液を吸収液の液溜より蒸発器
の冷媒溜に供給する稀吸収液導管を揚液装置を介
して連結し、前記冷媒蒸気導管に冷暖切替弁を設
けることにより、冷房運転及び暖房運転相互の切
替えを容易にできるようにしたことを特徴とする
吸収冷凍機の冷暖切替装置にある。 The gist of this is that in an absorption refrigerator that extracts hot water during heating from an evaporator through which cold water flows during cooling, a dilute absorption liquid is placed in a liquid reservoir of absorption liquid in a refrigerant vapor conduit that supplies high-temperature refrigerant vapor from a regenerator to an evaporator. By connecting the dilute absorption liquid conduit that supplies the refrigerant reservoir of the evaporator to the refrigerant reservoir of the evaporator via a liquid pumping device, and by providing a cooling/heating switching valve in the refrigerant vapor conduit, it is possible to easily switch between cooling operation and heating operation. A heating/cooling switching device for an absorption refrigerator is characterized by the following.
以下第2図及び第3図に示す実施例により本発
明を説明する。第2図は二重効用吸収冷凍機に、
又第3図は一重効用吸収冷凍機にそれぞれ適用し
た場合の構造系統図を示す。従来の第1図と同一
部分には同一符号を付し説明は省略する。 The present invention will be explained below with reference to embodiments shown in FIGS. 2 and 3. Figure 2 shows a dual-effect absorption refrigerator.
Moreover, FIG. 3 shows a structural system diagram when each of these is applied to a single-effect absorption refrigerator. Components that are the same as those in the conventional FIG.
先ず、第2図において、高温再生器7で蒸発し
た冷媒蒸気は、管路を通り低温再生器5に導か
れ、凝縮器6に管路で導かれるが、その管路より
分岐した冷媒蒸気導管28を設け、高温の冷媒蒸
気を蒸発器4に供給するようにしている。この冷
媒蒸気導管28の所要の位置に揚液装置23を介
装し、これに稀吸収液の液溜11よりの稀吸収液
導管22を連結する。これにより揚液装置23に
おける気泡ポンプや冷媒蒸気導管28を流れる冷
媒蒸気のインジエクタ効果などを利用する揚液手
段によつて稀吸収液導管22を流れる稀吸収液を
円滑に液溜11から冷媒溜10に流動できるよう
にしている。 First, in FIG. 2, the refrigerant vapor evaporated in the high-temperature regenerator 7 is guided through a pipe to the low-temperature regenerator 5, and then to the condenser 6 via a pipe, but a refrigerant vapor pipe branches from the pipe. 28 is provided to supply high temperature refrigerant vapor to the evaporator 4. A liquid pumping device 23 is interposed at a required position of the refrigerant vapor conduit 28, and a dilute absorption liquid conduit 22 from the dilute absorption liquid reservoir 11 is connected to this. As a result, the dilute absorption liquid flowing through the dilute absorption liquid conduit 22 is smoothly transferred from the liquid reservoir 11 to the refrigerant reservoir by the liquid pumping means that utilizes the bubble pump in the liquid pumping device 23 or the injector effect of the refrigerant vapor flowing through the refrigerant vapor conduit 28. It is possible to flow to 10.
第3図に示す他の実施例の場合は、高温再生器
7で蒸発した冷媒蒸気を凝縮器6に流入前に冷媒
蒸気導管38によつて蒸発器4に供給するように
した点が前記第2図の実施例と異るほか他の部分
は同様である。第2図の冷媒蒸気導管28及び第
3図の冷媒蒸気導管38における19は冷暖切替
弁である。 In the case of another embodiment shown in FIG. 3, the refrigerant vapor evaporated in the high temperature regenerator 7 is supplied to the evaporator 4 through the refrigerant vapor conduit 38 before flowing into the condenser 6. Other than being different from the embodiment shown in FIG. 2, other parts are the same. Reference numeral 19 in the refrigerant vapor conduit 28 in FIG. 2 and the refrigerant vapor conduit 38 in FIG. 3 is a cooling/heating switching valve.
次に作用について説明する。 Next, the effect will be explained.
第2図に示す実施例の場合は先ず、冷房運転時
においては、冷暖切替弁19は閉の状態に保たれ
ている。この時の冷媒と吸収液の循環は第1図に
示す従来の吸収式冷凍機と変りなく、管路24よ
り蒸発器4に流入してきた水を冷却して冷水とし
て管路25より取り出し冷房に供される。 In the case of the embodiment shown in FIG. 2, first, during cooling operation, the cooling/heating switching valve 19 is kept in a closed state. The circulation of the refrigerant and absorption liquid at this time is the same as in the conventional absorption refrigerator shown in Fig. 1, and the water flowing into the evaporator 4 from the pipe 24 is cooled and taken out as cold water from the pipe 25 for cooling. Served.
次に暖房運転時には冷暖切替弁19は開の状態
に保持されている。 Next, during heating operation, the cooling/heating switching valve 19 is kept open.
高温再生器7で蒸発分離した冷媒蒸気は管路を
経て低温再生器5の管群の管内を通り冷媒蒸気導
管28に導かれて凝縮器6をバイパスして蒸発器
4の下部の冷媒溜10近傍に供給される。一方、
この冷媒蒸気導管28に介装した揚液装置23に
連結した吸収器3の下部の液溜11よりの稀吸収
液導管22に流れる稀吸収液は揚液手段によつて
冷媒蒸気に同伴させて好適に冷媒溜10に供給さ
れる。この冷媒蒸気は蒸発器4で凝縮し、その凝
縮潜熱によつて蒸発器4の管内を流れる水に熱を
与えて温水を取り出せるようにして暖房を行なう
ものである。 The refrigerant vapor evaporated and separated in the high-temperature regenerator 7 passes through the pipe line and inside the pipe group of the low-temperature regenerator 5, is guided to the refrigerant vapor pipe 28, bypasses the condenser 6, and enters the refrigerant reservoir 10 in the lower part of the evaporator 4. Supplied nearby. on the other hand,
The dilute absorption liquid flowing into the dilute absorption liquid conduit 22 from the liquid reservoir 11 at the lower part of the absorber 3 connected to the liquid pumping device 23 installed in the refrigerant vapor conduit 28 is entrained with the refrigerant vapor by the liquid pumping means. It is preferably supplied to the refrigerant reservoir 10. This refrigerant vapor is condensed in the evaporator 4, and the latent heat of condensation gives heat to the water flowing in the pipes of the evaporator 4, allowing hot water to be taken out for heating.
又、冷媒の一部は冷媒溜10からオーバーフロ
ーして稀吸収液の液溜11に流入し、稀吸収液を
稀釈する。この稀吸収液は高温再生器7に送ら
れ、ここで濃縮され、冷媒蒸気を蒸発させ、この
冷媒蒸気は前記冷媒蒸気導管28によつて蒸発器
4の加熱媒体とし繰り返えし利用される。 Further, a portion of the refrigerant overflows from the refrigerant reservoir 10 and flows into the dilute absorption liquid reservoir 11 to dilute the dilute absorption liquid. This dilute absorption liquid is sent to the high-temperature regenerator 7, where it is concentrated and evaporated into refrigerant vapor, which is repeatedly used as a heating medium for the evaporator 4 through the refrigerant vapor conduit 28. .
又、第3図に示す実施例の場合は、冷暖切替弁
19を開く暖房時においては、高温再生器7から
の冷媒蒸気は凝縮器6をバイパスさせて冷媒蒸気
導管38によつて蒸発器4の下部の冷媒溜10近
傍に送られるが、その途中に介装した揚液装置2
3に連結した稀吸収液の液溜11よりの稀吸収液
導管22を流れる稀吸収液を気泡ポンプを形成せ
しめるなどの揚液手段によつて同伴して供給され
る冷媒蒸気は、蒸発器4で凝縮し、その凝縮熱に
よつて蒸発器の管内を流れる水に熱を与え凝縮し
た冷媒は冷媒溜10に溜る。この場合の冷媒と吸
収液の循環は前記実施例と同様に行なわれるもの
である。 In the case of the embodiment shown in FIG. 3, during heating when the cooling/heating switching valve 19 is opened, the refrigerant vapor from the high-temperature regenerator 7 bypasses the condenser 6 and is transferred to the evaporator 4 via the refrigerant vapor conduit 38. The refrigerant is sent to the vicinity of the refrigerant reservoir 10 at the bottom of the
The refrigerant vapor is supplied along with the dilute absorption liquid flowing through the dilute absorption liquid conduit 22 from the dilute absorption liquid reservoir 11 connected to the evaporator 3 by a pumping means such as forming a bubble pump. The condensed refrigerant gives heat to the water flowing in the evaporator tube by the heat of condensation, and the condensed refrigerant accumulates in the refrigerant reservoir 10. In this case, the refrigerant and absorption liquid are circulated in the same manner as in the previous embodiment.
以上詳述した通り構成された本発明によれば、
凝縮器をバイパスさせて冷媒蒸気を蒸発器に導く
冷媒蒸気導管を設け、その導管と稀吸収液の液溜
よりの稀吸収液導管とを揚液装置を介して連結
し、前記冷媒蒸気導管に冷暖切替弁を設けたか
ら、冷房及び暖房の切換が一動作で操作をするこ
とができるので簡単化され、しかも誤操作のおそ
れも無く、従つて誤操作による機械の故障のおそ
れもない。又稀吸収液を揚液手段によつて冷媒溜
に導き、オーバーフローさせるので、特に外気温
の低い暖房運転時における冷媒の凍結や吸収液の
結晶を防止するのに役立ち有意義な発明である。 According to the present invention configured as detailed above,
A refrigerant vapor conduit is provided that bypasses the condenser and leads the refrigerant vapor to the evaporator, and the conduit is connected to a dilute absorption liquid conduit from a dilute absorption liquid reservoir via a liquid pumping device, and the refrigerant vapor conduit is connected to the diluted absorption liquid conduit through a liquid pumping device. Since the cooling/heating switching valve is provided, switching between cooling and heating can be performed in one operation, which simplifies the operation, and there is no risk of erroneous operation, and therefore, there is no risk of machine failure due to erroneous operation. Furthermore, since the diluted absorption liquid is guided to the refrigerant reservoir by the pumping means and caused to overflow, this invention is useful in preventing freezing of the refrigerant and crystallization of the absorption liquid, especially during heating operations at low outside temperatures.
第1図は従来の吸収冷凍機の冷暖切替装置の構
造系統図、第2図は本発明を二重効用吸収冷凍機
に適用した一実施例を示す構造系統図、第3図は
一重効用吸収冷凍機に適用した他の実施例を示す
構造系統図である。
3……吸収器、4……蒸発器、5……低温再生
器、6……凝縮器、7……高温再生器、10……
冷媒溜、11……液溜、22……稀吸収液導管、
23……揚液装置、28,38……冷媒蒸気導
管。
Figure 1 is a structural diagram of a conventional cooling/heating switching device for an absorption refrigerator, Figure 2 is a structural diagram showing an embodiment of the present invention applied to a dual-effect absorption refrigerator, and Figure 3 is a single-effect absorption refrigerator. It is a structural system diagram showing another example applied to a refrigerator. 3...Absorber, 4...Evaporator, 5...Low temperature regenerator, 6...Condenser, 7...High temperature regenerator, 10...
Refrigerant reservoir, 11...liquid reservoir, 22...dilute absorption liquid conduit,
23... Liquid pumping device, 28, 38... Refrigerant vapor conduit.
Claims (1)
又は温水を取出す吸収冷凍機において、高温の冷
媒を再生器から蒸発器に供給する冷媒蒸気導管
に、稀吸収液を吸収器の液溜より蒸発器の冷媒溜
に供給する稀吸収液導管を揚液装置を介して連結
し、前記冷媒蒸気導管に冷暖切替弁を設けること
により、冷房運転及び暖房運転相互の切替えを容
易にできるようにしたことを特徴とする吸収冷凍
機の冷暖切替装置。1. In an absorption refrigerator that switches between cooling and heating to extract cold water or hot water from the evaporator, dilute absorption liquid is transferred from the absorber's liquid reservoir to the evaporator in the refrigerant vapor conduit that supplies high-temperature refrigerant from the regenerator to the evaporator. The dilute absorption liquid conduit that supplies the refrigerant reservoir is connected via a pumping device, and the refrigerant vapor conduit is provided with a cooling/heating switching valve, thereby making it possible to easily switch between cooling operation and heating operation. Features a heating/cooling switching device for absorption refrigerators.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12586782A JPS5918353A (en) | 1982-07-21 | 1982-07-21 | Air-conditioning changeover device for absorption refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12586782A JPS5918353A (en) | 1982-07-21 | 1982-07-21 | Air-conditioning changeover device for absorption refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5918353A JPS5918353A (en) | 1984-01-30 |
| JPH025990B2 true JPH025990B2 (en) | 1990-02-06 |
Family
ID=14920893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12586782A Granted JPS5918353A (en) | 1982-07-21 | 1982-07-21 | Air-conditioning changeover device for absorption refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5918353A (en) |
-
1982
- 1982-07-21 JP JP12586782A patent/JPS5918353A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5918353A (en) | 1984-01-30 |
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