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JPH0353542B2 - - Google Patents
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JPH0353542B2 - - Google Patents

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Publication number
JPH0353542B2
JPH0353542B2 JP21515382A JP21515382A JPH0353542B2 JP H0353542 B2 JPH0353542 B2 JP H0353542B2 JP 21515382 A JP21515382 A JP 21515382A JP 21515382 A JP21515382 A JP 21515382A JP H0353542 B2 JPH0353542 B2 JP H0353542B2
Authority
JP
Japan
Prior art keywords
refrigerant
pipe
hot water
temperature generator
evaporator
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
Application number
JP21515382A
Other languages
Japanese (ja)
Other versions
JPS59107161A (en
Inventor
Toshitaka Takei
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP21515382A priority Critical patent/JPS59107161A/en
Publication of JPS59107161A publication Critical patent/JPS59107161A/en
Publication of JPH0353542B2 publication Critical patent/JPH0353542B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は吸収式冷凍機、詳しくは高温発生器
と、この高温発生器から延びる冷媒蒸気管に接続
する伝熱管を設けた低温発生器と、この低温発生
器から延びる冷媒蒸気管に接続する凝縮器と、こ
の凝縮器と接続する蒸発器及びこの蒸発器に並接
され、前記蒸発器とともに胴体に内装する吸収器
とを備え、前記胴体に冷温水管と接続する伝熱管
を設け、冷水を形成する冷水運転時、冷媒タンク
に冷媒液を貯留し、温水を形成する温水運転時前
記冷媒タンクの冷媒液を溶液中に放出して温水運
転時の溶液濃度を低下させる如くした吸収式冷凍
機に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigerating machine, specifically, a high temperature generator, a low temperature generator provided with a heat transfer tube connected to a refrigerant vapor pipe extending from the high temperature generator, and a low temperature generator extending from the low temperature generator. A transmission system comprising a condenser connected to a refrigerant vapor pipe, an evaporator connected to the condenser, and an absorber installed in a body together with the evaporator in parallel with the evaporator, and connected to a hot and cold water pipe in the body. A heat pipe is installed to form cold water. During cold water operation, refrigerant liquid is stored in a refrigerant tank to form hot water. During hot water operation, the refrigerant liquid in the refrigerant tank is released into solution to reduce the solution concentration during hot water operation. This invention relates to an absorption refrigerator.

従来、此種吸収式冷凍機として特公昭55−
32982号公報に記載され、第4図に示すものが知
られている。第4図に示すものは、二重効用吸収
式冷凍機の一部で高温発生器Aと低温発生器(図
示せず)と凝縮器(図示せず)と蒸発器(図示せ
ず)とを順次接続し、冷水運転時に前記高温発生
器Aから蒸発器(図示せず)に冷媒を送る冷媒管
Bとは別に蒸発器(図示せず)の冷媒受(図示せ
ず)と前記高温発生器Aとを接続する冷媒配管C
を設け、前記冷媒配管Cに冷媒タンクDを介装
し、そして前記冷媒タンクD内の冷媒の貯留・放
出を行うために一対の開閉弁E,Fを前記冷媒タ
ンクDの前後に設けているのである。
Conventionally, this type of absorption refrigerator was developed in 1983.
The one described in Japanese Patent No. 32982 and shown in FIG. 4 is known. The one shown in Fig. 4 is part of a dual-effect absorption refrigerator, which includes a high temperature generator A, a low temperature generator (not shown), a condenser (not shown), and an evaporator (not shown). A refrigerant receiver (not shown) of the evaporator (not shown) and a refrigerant pipe (not shown) of the evaporator (not shown) and a refrigerant pipe (not shown) of the evaporator (not shown) and a refrigerant pipe B that are sequentially connected and send refrigerant from the high temperature generator A to the evaporator (not shown) during cold water operation Refrigerant pipe C connecting with A
A refrigerant tank D is interposed in the refrigerant pipe C, and a pair of on-off valves E and F are provided before and after the refrigerant tank D in order to store and release the refrigerant in the refrigerant tank D. It is.

そして更に、各前記開閉弁E,Fとは別に、
冷・温水運転で冷媒流れをそれぞれ変更し、即
ち、温水運転時には前記した冷水運転時とは相違
して、冷媒を高温発生器Aから温水器Gを通つて
再び前記高温発生器Aに返送するようにするため
の冷温水切換弁Hを前記冷媒管Bに介装し、さら
に中間濃度溶液管Iと稀溶液管Jとに冷水運転時
に開き温水運転時に閉じる開閉弁K,Lをそれぞ
れ介装しているのである。
Furthermore, apart from each of the on-off valves E and F,
The refrigerant flow is changed in cold and hot water operation, that is, in hot water operation, unlike in the above-mentioned cold water operation, the refrigerant is returned from high temperature generator A to high temperature generator A through water heater G. A cold/hot water switching valve H is installed in the refrigerant pipe B, and open/close valves K and L are installed in the intermediate concentration solution pipe I and the dilute solution pipe J, respectively, to open during cold water operation and close during hot water operation. That's what I'm doing.

上記したように従来においては、冷水と温水運
転とで冷媒の流れを変更するための前記冷温水切
換弁Hの他に、前記冷媒タンクDの冷媒を貯留ま
たは放出するための開閉弁E,Fや溶液管I,J
用の開閉弁K,Lを必要とするので、使用される
弁の個数が多く、そのため冷凍機全体の気密性が
低下し、かつ、冷・温水運転の切換の操作性が悪
く、又、製造コストが上昇する問題があつた。
As described above, conventionally, in addition to the cold/hot water switching valve H for changing the flow of refrigerant between cold water and hot water operation, on-off valves E and F for storing or releasing the refrigerant in the refrigerant tank D and solution tubes I, J
Since the on-off valves K and L are required, the number of valves used is large, which reduces the airtightness of the entire refrigerator, and makes it difficult to switch between cold and hot water operation. There was a problem of rising costs.

本発明の目的は、一個の冷・温水切換用の開閉
弁を設けるだけで、冷・温水運転の切換時の冷媒
流れの変更と冷媒タンクの冷媒の貯留または放出
とが同時にできるようにして、従来の前記した問
題点を解決する点にある。
An object of the present invention is to enable simultaneous change in refrigerant flow when switching between cold and hot water operation and storage or release of refrigerant in a refrigerant tank by simply providing one on-off valve for switching between cold and hot water. The purpose is to solve the above-mentioned conventional problems.

そのために本発明は、高温発生器1と、この高
温発生器1から延びる冷媒蒸気管8に接続する伝
熱管2bを設けた低温発生器2と、この低温発生
器2から延びる冷媒蒸気管22に接続する凝縮器
6と、この凝縮器6と接続する蒸発器3及びこの
蒸発器3に並接され、前記蒸発器3とともに胴体
5に内装する吸収器4とを備え、前記胴体5に冷
温水管と接続する伝熱管を設け、冷水を形成する
冷水運転と温水を形成する温水運転とを可能にし
た吸収式冷凍機において、前記伝熱管2bの出口
側に冷媒液を受取る冷媒タンク19を連通させ
て、該タンク19の上部に、前記蒸発器3に連通
する第1冷媒管9を開口させると共に、前記タン
ク19の下部に、前記胴体5と連通する第2冷媒
管21を開口させる一方、前記第2冷媒管21
に、温水を形成する温水運転時に開く開閉弁20
を介装したのであつて、一個の前記開閉弁20の
開閉操作によつて、冷水運転時には前記冷媒タン
ク19に冷媒液を貯留して前記第1冷媒管9に冷
媒を流通させる一方、温水運転時には前記第2冷
媒管21に冷媒を流通さると同時に、前記冷媒タ
ンク19に貯留されていた冷媒液を前記胴体5へ
放出できる如く成したことを特徴とするものであ
る。
To this end, the present invention provides a high temperature generator 1, a low temperature generator 2 provided with a heat transfer tube 2b connected to a refrigerant vapor pipe 8 extending from the high temperature generator 1, and a refrigerant vapor pipe 22 extending from the low temperature generator 2. A condenser 6 is connected to the condenser 6, an evaporator 3 is connected to the condenser 6, and an absorber 4 is arranged in parallel with the evaporator 3 and is housed in the body 5 together with the evaporator 3. In an absorption refrigerating machine, a refrigerant tank 19 for receiving a refrigerant liquid is connected to the outlet side of the heat exchanger tube 2b in an absorption refrigerator which enables a cold water operation for forming cold water and a hot water operation for forming hot water. Then, the first refrigerant pipe 9 communicating with the evaporator 3 is opened in the upper part of the tank 19, and the second refrigerant pipe 21 communicating with the body 5 is opened in the lower part of the tank 19. Second refrigerant pipe 21
, an on-off valve 20 that opens during hot water operation to form hot water.
By opening and closing the one on-off valve 20, refrigerant liquid is stored in the refrigerant tank 19 during cold water operation and refrigerant is distributed through the first refrigerant pipe 9, while during hot water operation It is characterized in that the refrigerant liquid stored in the refrigerant tank 19 can be discharged to the body 5 at the same time as the refrigerant is passed through the second refrigerant pipe 21.

以下、本発明の実施例を図面に基づいて説明す
る。
Embodiments of the present invention will be described below based on the drawings.

第1図に示したものは、二重効用吸収式冷凍機
であつて、都市ガスのバーナー1aをもち、該バ
ーナー1aの燃焼により溶液を加熱するごとくし
た直焚式高温発生器1と後記する冷媒蒸発管8に
接続する伝熱管2bを設けた低温発生器2とを備
え、蒸発器3及び吸収器4とを一つの胴体5に内
装すると共に、この胴体5の上部に凝縮器6を構
成する胴体7を一体的に結合している。
The one shown in FIG. 1 is a dual-effect absorption refrigerating machine, which has a city gas burner 1a, and is referred to later as a direct-fired high-temperature generator 1 that heats a solution by combustion of the burner 1a. It is equipped with a low temperature generator 2 provided with a heat transfer tube 2b connected to a refrigerant evaporation tube 8, an evaporator 3 and an absorber 4 are housed in one body 5, and a condenser 6 is configured in the upper part of this body 5. The body 7 is integrally connected.

そして、前記高温発生器1と低温発生器2と凝
縮器6と蒸発器3とをそれぞれ接続する前記冷媒
蒸気管8、第1冷媒管9、冷媒液管10を設け、
前記高温発生器1で発生する冷媒蒸気を凝縮して
蒸発器3に送る如くしている。また、前記低温発
生器2から延びる冷媒蒸気管22に前記凝縮器6
を接続している。
The refrigerant vapor pipe 8, the first refrigerant pipe 9, and the refrigerant liquid pipe 10 are provided to connect the high temperature generator 1, the low temperature generator 2, the condenser 6, and the evaporator 3, respectively,
The refrigerant vapor generated in the high temperature generator 1 is condensed and sent to the evaporator 3. Further, the condenser 6 is connected to the refrigerant vapor pipe 22 extending from the low temperature generator 2.
are connected.

更に高温発生器1から低温発生器2に中間濃度
溶液を送る中間濃度溶液管11、前記低温発生器
2から吸収器4に濃溶液を送る濃溶液管12およ
び前記吸収器4から高温発生器1に稀溶液を返送
する稀溶液管13をそれぞれ設けている。そし
て、前記稀溶液管13には、途中に溶液ポンプ1
4を介装すると共に、この溶液ポンプ14の吐出
側には、前記稀溶液管13を流れる稀溶液と前記
中間濃度溶液管11を流れる中間濃度溶液との間
で熱交換するための高温側熱交換器15および前
記稀溶液と第1冷媒管9を流れる冷媒液および濃
溶液管12を流れる濃溶液との間で熱交換するた
めの低温側熱交換器16とを介装している。
Furthermore, an intermediate concentration solution pipe 11 for conveying an intermediate concentration solution from the high temperature generator 1 to the low temperature generator 2, a concentrated solution tube 12 for conveying a concentrated solution from the low temperature generator 2 to the absorber 4, and a high temperature generator 1 from the absorber 4. A dilute solution tube 13 for returning the dilute solution is provided in each. The dilute solution pipe 13 is provided with a solution pump 1 on the way.
4 is interposed, and a high temperature side heat is provided on the discharge side of the solution pump 14 for heat exchange between the dilute solution flowing through the dilute solution tube 13 and the intermediate concentration solution flowing through the intermediate concentration solution tube 11. An exchanger 15 and a low-temperature side heat exchanger 16 for exchanging heat between the dilute solution and the refrigerant liquid flowing through the first refrigerant pipe 9 and the concentrated solution flowing through the concentrated solution pipe 12 are interposed.

また、前記蒸発器3の伝熱管3aには冷温水管
17を接続すると共に、前記吸収器4の伝熱管4
a及び凝縮器6の伝熱管6aには冷却水管18を
接続し、冷水を形成する冷水運転時冷水を、ま
た、温水を形成する温水運転時温水をそれぞれ取
出すことができるようにしている。
Further, a cold/hot water pipe 17 is connected to the heat transfer tube 3a of the evaporator 3, and a heat transfer tube 4 of the absorber 4 is connected to the heat transfer tube 3a of the evaporator 3.
A and the heat transfer tube 6a of the condenser 6 are connected to a cooling water pipe 18, so that cold water can be taken out during cold water operation to form cold water, and hot water can be taken out during hot water operation to form hot water.

第1図に示したものは、以上の如く接続する吸
収式冷凍機において、前記冷媒タンク19を第2
図に拡大したごとく前記低温発生器2の下部に一
体に設けて、前記低温発生器2に設けた前記伝熱
管2bの一端をヘツダー2aを介して前記冷媒蒸
気管8に連通させ、また前記伝熱管2bの他端を
ヘツダー2cを介して低温発生器2で凝縮する冷
媒液を受取る冷媒タンク19に連通させると共
に、該冷媒タンク19の上部に第1冷媒管9を開
口させる一方、前記冷媒タンク19の底部に、前
記胴体5と連通する第2冷媒管21を開口させ、
該第2冷媒管21の途中に冷・温水切換用であつ
て、温水を形成する温水運転時に開く開閉弁20
を介装するのである。
In the absorption refrigerating machine shown in FIG. 1, the refrigerant tank 19 is connected to the second
As enlarged in the figure, the heat transfer tube 2b is provided integrally with the lower part of the low temperature generator 2, and one end of the heat transfer tube 2b provided in the low temperature generator 2 is communicated with the refrigerant vapor pipe 8 via the header 2a. The other end of the heat pipe 2b is communicated via the header 2c with a refrigerant tank 19 that receives the refrigerant liquid condensed in the low temperature generator 2, and the first refrigerant pipe 9 is opened at the upper part of the refrigerant tank 19, while the refrigerant tank 19, a second refrigerant pipe 21 communicating with the body 5 is opened,
In the middle of the second refrigerant pipe 21, there is an on-off valve 20 for switching between cold and hot water, which opens during hot water operation to form hot water.
It is to intervene.

しかして、前記開閉弁20を閉にすることによ
つて該タンク19の前記第1冷媒管9の入口より
下方の部分に前記低温発生器2で凝縮した冷媒液
を貯留できるように成しているのである。
By closing the on-off valve 20, the refrigerant liquid condensed in the low temperature generator 2 can be stored in a portion of the tank 19 below the inlet of the first refrigerant pipe 9. There is.

次に、以上の如く構成する吸収式冷凍機の作用
を説明する。
Next, the operation of the absorption refrigerating machine constructed as above will be explained.

最初に冷・温水切換用の開閉弁20を閉にして
冷水運転を行う場合を説明する。
First, a case will be described in which cold water operation is performed by closing the on-off valve 20 for switching between cold and hot water.

先ず、前記バーナー1aを燃焼して高温発生器
1を加熱すると、器内の稀溶液が加熱沸騰するの
であつて、冷媒蒸気は、前記低温発生器2で、前
記高温発生器1から高温側熱交換器15を経て導
入される中間濃度溶液に放熱し、一部が凝縮して
気液混合の冷媒となつて前記ヘツダー2cから冷
媒タンク19に流入する。
First, when the burner 1a is burned to heat the high-temperature generator 1, the dilute solution in the vessel is heated to boiling, and the refrigerant vapor is transferred from the high-temperature generator 1 to the high-temperature side heat in the low-temperature generator 2. Heat is radiated to the intermediate concentration solution introduced through the exchanger 15, and a portion of the solution condenses to become a gas-liquid mixture that flows into the refrigerant tank 19 from the header 2c.

このとき前記開閉弁20は閉鎖されているた
め、前記冷媒タンク19に流入した気液混合の前
記冷媒中の冷媒液は、前記冷媒タンク19の液面
が前記第1冷媒管9の入口の位置に達するまで前
記冷媒タンク19内に貯留されるのである。そし
て前記液面が前記入口の位置と同じになると前記
冷媒タンク19に流入する全ての冷媒が第1冷媒
管9に流出されるのである。更に、前記第1冷媒
管9に流出された冷媒液は低温側熱交換器16で
冷却され、更に凝縮器6に送られるのである。
At this time, since the on-off valve 20 is closed, the refrigerant liquid in the gas-liquid mixture that has flowed into the refrigerant tank 19 is such that the liquid level of the refrigerant tank 19 is at the position of the inlet of the first refrigerant pipe 9. The refrigerant is stored in the refrigerant tank 19 until the refrigerant reaches . When the liquid level becomes the same as the inlet position, all the refrigerant flowing into the refrigerant tank 19 is discharged into the first refrigerant pipe 9. Further, the refrigerant liquid discharged into the first refrigerant pipe 9 is cooled by the low temperature side heat exchanger 16 and further sent to the condenser 6.

一方、低温発生器2で中間溶液から発生する冷
媒蒸気は、前記冷媒蒸気管22を介して前記凝縮
器6に流入するのである。
On the other hand, refrigerant vapor generated from the intermediate solution in the low temperature generator 2 flows into the condenser 6 via the refrigerant vapor pipe 22.

前記凝縮器6に流入する冷媒は伝熱管6aを流
れる冷却水に放熱して全て凝縮するのである。そ
して、前記凝縮器6からの液冷媒は冷媒液管10
を介して前記蒸発器3に入り、前記伝熱管3aに
分散装置3bを介して分散され、前記伝熱管3a
を流れる水から熱を奪つて蒸発し、冷水を形成す
るのである。
The refrigerant flowing into the condenser 6 radiates heat to the cooling water flowing through the heat transfer tubes 6a and is completely condensed. The liquid refrigerant from the condenser 6 is then transferred to a refrigerant liquid pipe 10.
enters the evaporator 3 through the heat exchanger tube 3a, is dispersed into the heat exchanger tube 3a through the dispersion device 3b, and is dispersed into the heat exchanger tube 3a through the dispersion device 3b.
It takes heat from the flowing water and evaporates it, forming cold water.

尚、蒸発器3で蒸発した冷媒蒸気は、エリミネ
ータ(図示せず)を介して前記吸収器4に流入し
て、前記低温発生器2から前記低温側熱交換器1
6を経て吸収器4に入る濃溶液に吸収されるので
あり、また、前記冷媒蒸気を吸収した稀溶液は、
前記溶液ポンプ14により、前記稀溶液管13を
介して前記低温側熱交換器16及び高温側熱交換
器15を経て高温発生器1に戻るのである。
The refrigerant vapor evaporated in the evaporator 3 flows into the absorber 4 via an eliminator (not shown), and is transferred from the low temperature generator 2 to the low temperature side heat exchanger 1.
The refrigerant vapor is absorbed into the concentrated solution that enters the absorber 4 through the refrigerant vapor.
The solution pump 14 returns the solution to the high temperature generator 1 via the dilute solution pipe 13, the low temperature side heat exchanger 16 and the high temperature side heat exchanger 15.

上記した如く、冷水運転時には、冷・温水切換
用の開閉弁20を閉にすることによつて、冷媒を
第1冷媒管9に流通させられると同時に、低温発
生器2で凝縮した冷媒液を前記冷媒タンク19に
貯留でき、従つて溶液濃度を冷水運転に適する所
定の値に高くすることができるのである。
As mentioned above, during cold water operation, by closing the cold/hot water switching valve 20, the refrigerant is allowed to flow through the first refrigerant pipe 9, and at the same time, the refrigerant liquid condensed in the low temperature generator 2 is The solution can be stored in the refrigerant tank 19, and the concentration of the solution can therefore be increased to a predetermined value suitable for cold water operation.

次に、冷・温水切換用の前記開閉弁20を開に
して温水運転を行う場合を説明する。
Next, a case will be described in which hot water operation is performed by opening the on-off valve 20 for switching between cold and hot water.

尚、この場合には、冷却水管18の通水は停止
している。
Note that in this case, water flow through the cooling water pipe 18 is stopped.

先ず、前記開閉弁20を開にすることによつ
て、前記冷媒タンク19に貯留されていた冷媒が
第2冷媒管21を介してすべて蒸発器3に、従つ
て稀溶液中に放出されるのである。
First, by opening the on-off valve 20, all of the refrigerant stored in the refrigerant tank 19 is released into the evaporator 3 and into the dilute solution via the second refrigerant pipe 21. be.

そして、冷水運転と同様に高温発生器1で発生
する高温冷媒蒸気は低温発生器2で気液混合の状
態になつて冷媒タンク19に流入する。
Similarly to the cold water operation, the high temperature refrigerant vapor generated in the high temperature generator 1 becomes a gas-liquid mixture in the low temperature generator 2 and flows into the refrigerant tank 19.

そして、今度は前記開閉弁20が開になつてい
るので、前記冷媒タンク19に流入する前記冷媒
は全く前記冷媒タンク19に貯留されることなく
前記タンク19の底部から前記第2冷媒管21を
介して蒸発器3に送られるのである。
This time, since the on-off valve 20 is open, the refrigerant flowing into the refrigerant tank 19 is not stored in the refrigerant tank 19 at all, and is passed through the second refrigerant pipe 21 from the bottom of the tank 19. It is sent to the evaporator 3 via the evaporator 3.

尚、第1冷媒管9の流路抵抗は、低温側熱交換
器16を経由するために第2冷媒管21の流路抵
抗よりもかなり大きいので、冷媒タンク19から
前記第1冷媒管9にはほとんど冷媒が流出しない
のである。
Note that the flow resistance of the first refrigerant pipe 9 is considerably larger than the flow resistance of the second refrigerant pipe 21 because it passes through the low-temperature side heat exchanger 16. Almost no refrigerant flows out.

又、前記低温発生器2で生じる冷媒蒸気は凝縮
器6を通り、しかも凝縮されることなく蒸発器3
に送られるのである。
Further, the refrigerant vapor generated in the low temperature generator 2 passes through the condenser 6 and is not condensed until it reaches the evaporator 3.
It is sent to.

そして、蒸発器3に流入した冷媒蒸気は伝熱管
3aを流れる水に凝縮熱を放出して水を加熱する
と共に凝縮し、然る後前記低温発生器2から吸収
器4に流入する濃溶液と混合され、稀溶液となつ
て前記吸収器4の下部から稀溶液管13を介して
高温発生器1に返送されるのである。
The refrigerant vapor that has flowed into the evaporator 3 releases heat of condensation to the water flowing through the heat transfer tube 3a, heats the water and condenses, and then forms a concentrated solution that flows from the low temperature generator 2 into the absorber 4. The dilute solution is mixed and returned to the high temperature generator 1 from the lower part of the absorber 4 via the dilute solution pipe 13.

以上の如く、冷・温水切換用の開閉弁20を開
にすることによつて、冷媒を第2冷媒管21に流
通させられると同時に冷媒タンク19に貯留して
いた冷媒液を全て溶液中に放出して、前記溶液の
濃度を所定の値に下げて運転することができるの
である。
As described above, by opening the on-off valve 20 for cold/hot water switching, the refrigerant is allowed to flow through the second refrigerant pipe 21, and at the same time, all the refrigerant liquid stored in the refrigerant tank 19 is turned into solution. The concentration of the solution can be lowered to a predetermined value for operation.

従つて、本実施例によれば、冷媒の流れを変え
るための冷・温水切換用の開閉弁20を一個用い
るだけで冷媒タンク19への冷媒液の貯留・放出
の操作も行えるので、冷凍機に用いる開閉弁の数
を従来に比して少なくできるのである。従つて、
開閉弁の数が少ないから、それだけ冷凍機の気密
性が向上し、かつ冷・温水切換時の操作も容易に
なり、更に製造コストも低下させることができる
のである。
Therefore, according to this embodiment, operations for storing and discharging refrigerant liquid in the refrigerant tank 19 can be carried out by using only one on-off valve 20 for switching between cold and hot water to change the flow of the refrigerant. The number of on-off valves used can be reduced compared to the conventional method. Therefore,
Since the number of on-off valves is small, the airtightness of the refrigerator is improved accordingly, the operation when switching between cold and hot water is facilitated, and manufacturing costs can also be reduced.

更に、本実施例においては、冷媒タンク19を
低温発生器2の下部に一体に設けたから、前記冷
媒タンク19の上面も前記低温発生器2の溶液へ
の伝熱面として利用できるので、冷水運転時によ
り効率的な運転が行えるのである。
Furthermore, in this embodiment, since the refrigerant tank 19 is integrally provided at the lower part of the low temperature generator 2, the upper surface of the refrigerant tank 19 can also be used as a heat transfer surface to the solution in the low temperature generator 2, so that cold water operation is possible. This allows for more efficient operation at times.

尚、上記実施例においては、冷媒タンク19を
低温発生器2と凝縮器6とを結ぶ冷媒管に介装し
たが、第3図に示すように前記冷媒タンク19を
凝縮器6と蒸発器3とを結ぶ冷媒管に介装しても
よい。その場合は、前記冷媒タンク19の上部に
蒸発器3に接続される第1冷媒管9を開口させる
一方、底部に冷・温水切換用の開閉弁20を介装
し、同じく蒸発器3に接続される第2冷媒管21
を開口させるのである。
In the above embodiment, the refrigerant tank 19 was installed in the refrigerant pipe connecting the low temperature generator 2 and the condenser 6, but as shown in FIG. It may also be installed in a refrigerant pipe that connects the In that case, the first refrigerant pipe 9 connected to the evaporator 3 is opened at the top of the refrigerant tank 19, and an on-off valve 20 for switching between cold and hot water is installed at the bottom, which is also connected to the evaporator 3. The second refrigerant pipe 21
It opens the door.

尚、第3図において25は低温発生器2と凝縮
器6とを結ぶ冷媒管で、その他の番号を示すもの
は前記実施例と同じである。
In FIG. 3, 25 is a refrigerant pipe connecting the low temperature generator 2 and the condenser 6, and the other numbers are the same as in the previous embodiment.

又、以上の実施例では、冷媒タンク19の下部
に一端を開口させた第2冷媒管21の他端を、胴
体5の蒸発器3側に開口させたが、吸収器4側に
開口させてもよい。この場合、吸収器4の伝熱管
4aに流通させる水を吸収熱によつて加熱するこ
とにより温水を形成するのである。
Further, in the above embodiment, the second refrigerant pipe 21, one end of which was opened at the bottom of the refrigerant tank 19, was opened at the evaporator 3 side of the body 5, but the other end was opened at the absorber 4 side. Good too. In this case, hot water is formed by heating the water flowing through the heat transfer tubes 4a of the absorber 4 by absorbed heat.

以上の如く本発明は、高温発生器1と、この高
温発生器1から延びる冷媒蒸気管8に接続する伝
熱管2bを設けた低温発生器2と、この低温発生
器2から延びる冷媒蒸気管22に接続する凝縮器
6と、この凝縮器6と接続する蒸発器3及びこの
蒸発器3に並設され、前記蒸発器3とともに胴体
5に内装する吸収器4とを備え、前記胴体5に冷
温水管と接続する伝熱管を設け、冷水を形成する
冷水運転と温水を形成する温水運転とを可能にし
た吸収式冷凍機において、前記伝熱管2bの出口
側に冷媒液を受取る冷媒タンク19を連通させ
て、該タンク19の上部に、前記蒸発器3に連通
する第1冷媒管9を開口させると共に、前記タン
ク19の下部に、前記胴体5と連通する第2冷媒
管21を開口させる一方、前記第2冷媒管21
に、温水を形成する温水運転時に開く開閉弁20
を介装したから、冷・温水切換用の開閉弁20を
一個用いるだけで該開閉弁1の開閉操作により
冷・温水運転時の冷媒流れを変えることができる
と共に、前記冷媒タンク19の冷媒の貯留・放出
の切換も行えるのである。従つて、前記冷媒タン
ク19の冷媒の貯留・放出のためだけの開閉弁を
別途に設ける必要がないので、従来に比して使用
する開閉弁の使用個数を減少できるのである。
As described above, the present invention includes a high temperature generator 1, a low temperature generator 2 provided with a heat transfer tube 2b connected to a refrigerant vapor pipe 8 extending from the high temperature generator 1, and a refrigerant vapor pipe 22 extending from the low temperature generator 2. A condenser 6 connected to the body 5, an evaporator 3 connected to the condenser 6, and an absorber 4 installed in parallel with the evaporator 3 and housed in the body 5 together with the evaporator 3. In an absorption refrigerator that is provided with a heat transfer tube connected to a water tube and enables a cold water operation for forming cold water and a hot water operation for forming hot water, a refrigerant tank 19 for receiving refrigerant liquid is communicated with the outlet side of the heat transfer tube 2b. Then, a first refrigerant pipe 9 communicating with the evaporator 3 is opened in the upper part of the tank 19, and a second refrigerant pipe 21 communicating with the body 5 is opened in the lower part of the tank 19, Said second refrigerant pipe 21
, an on-off valve 20 that opens during hot water operation to form hot water.
, the refrigerant flow during cold/hot water operation can be changed by opening/closing the on-off valve 1 by simply using one on-off valve 20 for switching between cold and hot water, and the flow of refrigerant in the refrigerant tank 19 can be changed by opening and closing the on-off valve 1. It is also possible to switch between storage and release. Therefore, there is no need to separately provide an on-off valve just for storing and discharging the refrigerant in the refrigerant tank 19, so the number of on-off valves used can be reduced compared to the conventional art.

その結果開閉弁の数を少なくできる分だけ吸収
式冷凍機の気密性を向上させることができ、又、
冷・温水運転の切換操作を容易にでき、更に製造
コストも低下させることができるのである。
As a result, the airtightness of the absorption refrigerator can be improved by reducing the number of on-off valves, and
It is possible to easily switch between cold and hot water operation, and furthermore, it is possible to reduce manufacturing costs.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例を示す配管系統図、第
2図は前記実施例の要部の側面断面図、第3図は
他の実施例の部分図、第4図は従来例の一部を示
す配管系統図である。 1……高温発生器、2……低温発生器、2b…
…伝熱管、3……蒸発器、4……吸収器、5……
胴体、6……凝縮器、8……冷媒蒸気管、9……
第1冷媒管、19……冷媒タンク、20……開閉
弁、21……第2冷媒管。
Fig. 1 is a piping system diagram showing an embodiment of the present invention, Fig. 2 is a side sectional view of the main part of the above embodiment, Fig. 3 is a partial view of another embodiment, and Fig. 4 is a diagram of a conventional example. FIG. 1...High temperature generator, 2...Low temperature generator, 2b...
...heat exchanger tube, 3...evaporator, 4...absorber, 5...
Body, 6... Condenser, 8... Refrigerant vapor pipe, 9...
1st refrigerant pipe, 19... Refrigerant tank, 20... Open/close valve, 21... Second refrigerant pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 高温発生器1と、この高温発生器1から延び
る冷媒蒸気管8に接続する伝熱管2bを設けた低
温発生器2と、この低温発生器2から延びる冷媒
蒸気管22に接続する凝縮器6と、この凝縮器6
と接続する蒸発器3及びこの蒸発器3に並接さ
れ、前記蒸発器3とともに胴体5に内装する吸収
器4とを備え、前記胴体5に冷温水管と接続する
伝熱管を設け、冷水を形成する冷水運転と温水を
形成する温水運転とを可能にした吸収式冷凍機で
あつて、前記伝熱管2bの出口側に冷媒液を受取
る冷媒タンク19を連通させて、該タンク19の
上部に、前記蒸発器3に連通する第1冷媒管9を
開口させると共に、前記タンク19の下部に、前
記胴体5と連通する第2冷媒管21を開口させる
一方、前記第2冷媒管21に、温水を形成する温
水運転時に開く開閉弁20を介装したことを特徴
とする吸収式冷凍機。
1 A high temperature generator 1, a low temperature generator 2 provided with a heat transfer tube 2b connected to a refrigerant vapor pipe 8 extending from this high temperature generator 1, and a condenser 6 connected to a refrigerant vapor pipe 22 extending from this low temperature generator 2. And this condenser 6
an evaporator 3 connected to the evaporator 3; and an absorber 4 which is connected to the evaporator 3 and is housed in the body 5 together with the evaporator 3; This is an absorption refrigerator that enables a cold water operation to generate hot water and a hot water operation to generate hot water, in which a refrigerant tank 19 for receiving refrigerant liquid is communicated with the outlet side of the heat transfer tube 2b, and an upper part of the tank 19 is provided with: A first refrigerant pipe 9 communicating with the evaporator 3 is opened, and a second refrigerant pipe 21 communicating with the body 5 is opened at the lower part of the tank 19, while hot water is supplied to the second refrigerant pipe 21. An absorption refrigerating machine characterized by being equipped with an on-off valve 20 that opens during hot water operation.
JP21515382A 1982-12-07 1982-12-07 Absorption type refrigerator Granted JPS59107161A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21515382A JPS59107161A (en) 1982-12-07 1982-12-07 Absorption type refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21515382A JPS59107161A (en) 1982-12-07 1982-12-07 Absorption type refrigerator

Publications (2)

Publication Number Publication Date
JPS59107161A JPS59107161A (en) 1984-06-21
JPH0353542B2 true JPH0353542B2 (en) 1991-08-15

Family

ID=16667541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21515382A Granted JPS59107161A (en) 1982-12-07 1982-12-07 Absorption type refrigerator

Country Status (1)

Country Link
JP (1) JPS59107161A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4566919B2 (en) * 2006-01-24 2010-10-20 株式会社日本製鋼所 Double-effect absorption chill generation / output device

Also Published As

Publication number Publication date
JPS59107161A (en) 1984-06-21

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