JP2789951B2 - Absorption refrigerator - Google Patents
Absorption refrigeratorInfo
- Publication number
- JP2789951B2 JP2789951B2 JP4215306A JP21530692A JP2789951B2 JP 2789951 B2 JP2789951 B2 JP 2789951B2 JP 4215306 A JP4215306 A JP 4215306A JP 21530692 A JP21530692 A JP 21530692A JP 2789951 B2 JP2789951 B2 JP 2789951B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- solution
- evaporator
- pipe
- absorber
- 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 - Fee Related
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、吸収式冷凍機、詳しく
は、発生器と、凝縮器、蒸発器及び吸収器とを備え、前
記蒸発器の底部に冷媒液溜を設け、上部に冷媒液供給部
を設けて、前記冷媒液溜と冷媒液供給部との間に、冷媒
ポンプを備えた冷媒循環路を設けると共に、前記吸収器
と発生器との間に溶液ポンプをもった溶液管を設けて、
冷媒を吸収した稀溶液を前記吸収器から前記発生器に戻
すようにした吸収式冷凍機に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption refrigerator, and more particularly, to an absorption refrigerator comprising a generator, a condenser, an evaporator, and an absorber. A solution pipe provided with a liquid supply unit, a refrigerant circuit provided with a refrigerant pump between the refrigerant liquid reservoir and the refrigerant liquid supply unit, and having a solution pump between the absorber and the generator; With
The present invention relates to an absorption refrigerator in which a dilute solution having absorbed a refrigerant is returned from the absorber to the generator.
【0002】[0002]
【従来の技術】従来、この種吸収式冷凍機としては、冷
凍空調技術VOL.20,NO.230(昭和44年4
月発行)第52乃至第69頁に記載されたものが知られ
ている。この吸収式冷凍機は、図2に示すように、発生
器A、凝縮器B及び熱交換器Cを下部に配設すると共
に、これら各機器の上部に吸収器Dと蒸発器Eとを配設
する一方、前記蒸発器Eの底部に形成する冷媒液溜F
と、上部に設ける冷媒散布装置Gとの間に冷媒循環路H
を接続し、前記蒸発器Eの冷媒液溜Fから前記熱交換器
Cの下方に配置した冷媒ポンプIに流下した冷媒を、該
冷媒ポンプIにより前記冷媒循環路Hを介して前記冷媒
散布装置Gに供給し、該冷媒散布装置Gからの冷媒の冷
水管Jへの散布により冷媒を蒸発させ、このときの冷媒
の蒸発熱により前記冷水管Jを流れる冷水を冷却するよ
うにしている。2. Description of the Related Art Conventionally, this type of absorption chiller includes refrigeration and air conditioning technology VOL. 20, NO. 230 (Showa 44
Monthly publications) are known from pages 52 to 69. In this absorption refrigerator, as shown in FIG. 2, a generator A, a condenser B, and a heat exchanger C are provided at a lower portion, and an absorber D and an evaporator E are provided at an upper portion of each of these devices. On the other hand, a refrigerant reservoir F formed at the bottom of the evaporator E
And a refrigerant distribution device G provided on the upper side, and a refrigerant circulation path H
And the refrigerant flowing from the refrigerant reservoir F of the evaporator E to the refrigerant pump I disposed below the heat exchanger C through the refrigerant circulation path H by the refrigerant pump I to distribute the refrigerant in the refrigerant spraying device. G, and the refrigerant is evaporated by dispersing the refrigerant from the refrigerant dispersing device G to the cold water pipe J, and the cold water flowing through the cold water pipe J is cooled by the heat of evaporation of the refrigerant at this time.
【0003】また、前記吸収器Dの上部に設ける溶液散
布装置Kと前記熱交換器Cとの間に溶液管Lを接続し、
該熱交換器Cの下方に配置した溶液ポンプMにより前記
発生器Aから濃溶液を矢印で示したように前記溶液管L
を介して前記溶液散布装置Kに供給し、該溶液散布装置
Kからの濃溶液の冷却水管Nへの散布により、前記蒸発
器Eで発生した蒸気を溶液に吸収するようにしている。[0003] A solution pipe L is connected between a solution spraying device K provided above the absorber D and the heat exchanger C,
A concentrated solution is supplied from the generator A by the solution pump M disposed below the heat exchanger C as indicated by an arrow in the solution tube L.
Is supplied to the solution spraying device K through the above, and by spraying the concentrated solution from the solution spraying device K to the cooling water pipe N, the vapor generated in the evaporator E is absorbed in the solution.
【0004】ところで、以上のように液冷媒を前記冷媒
循環路Hを介して前記冷媒液溜Fから前記冷媒散布装置
Gに循環供給するようにした構造においては、前記吸収
器Dからミスト状の溶液が蒸発器Eに流れ込むことによ
り、前記冷媒の純度が低下することになる。また、前記
冷媒が溶液により汚染されてその純度が低下すると、前
記蒸発器Eにおける冷媒の蒸発温度が上昇し該蒸発器E
の冷却能力が低下することになる。このため、前記した
従来例では前記冷媒循環路Hにおける前記冷媒ポンプI
と前記冷媒散布装置Gとの間に、電磁弁Oを介装した冷
媒再生管Pを分岐させ、前記電磁弁Oを開くことにより
前記冷媒ポンプIから前記冷媒散布装置Gへ送る冷媒の
ほゞ全量を前記発生器Aに供給して蒸発させるようにし
ている。また、前記電磁弁Oは、タイマーにより定期的
に開くようにして、溶液によって汚染された冷媒を、冷
媒の汚染状態を目視により監視することなく再生し、冷
媒の溶液による汚染により蒸発温度が上昇するのを防止
して蒸発器Eの能力低下を防止するようにしている。By the way, as described above, in the structure in which the liquid refrigerant is circulated and supplied from the refrigerant liquid reservoir F to the refrigerant dispersion device G through the refrigerant circulation path H, a mist-like liquid is supplied from the absorber D. When the solution flows into the evaporator E, the purity of the refrigerant decreases. When the purity of the refrigerant decreases due to the contamination of the refrigerant by the solution, the evaporation temperature of the refrigerant in the evaporator E increases and the evaporator E
The cooling capacity of the device is reduced. For this reason, in the conventional example described above, the refrigerant pump I in the refrigerant circuit H
A refrigerant regeneration pipe P provided with an electromagnetic valve O is branched between the refrigerant spraying device G and the refrigerant spraying device G. When the electromagnetic valve O is opened, the refrigerant pump I sends the refrigerant to the refrigerant spraying device G. The whole amount is supplied to the generator A and evaporated. In addition, the solenoid valve O is opened periodically by a timer to regenerate the refrigerant contaminated by the solution without visually monitoring the state of contamination of the refrigerant, and the evaporation temperature increases due to the contamination of the refrigerant by the solution. And the deterioration of the capacity of the evaporator E is prevented.
【0005】尚、Qは前記凝縮器Bで凝縮した冷媒を前
記冷媒循環路Hを介して前記蒸発器Eに供給する冷媒供
給管である。A refrigerant supply pipe Q supplies the refrigerant condensed in the condenser B to the evaporator E through the refrigerant circulation path H.
【0006】[0006]
【発明が解決しようとする課題】ところが、以上の吸収
式冷凍機では、前記冷媒再生管Pは前記冷媒ポンプIと
冷媒散布装置Gとの間から分岐すると共に、前記冷媒散
布装置Gは、前記再生管Pの分岐位置より上位にあるこ
とから、前記電磁弁Oを開いて前記液冷媒を発生器Aに
戻して再生するとき、前記冷媒循環路Hを循環する大半
の液冷媒が発生器Aに流れてしまい、前記蒸発器Eでの
能力が著しく低下し、正常な運転の継続が行えない問題
があった。また、前記タイマーにより電磁弁Oを定期的
に開き、前記電磁弁Oの開動作により溶液によって汚染
された冷媒を再生するようにしているから、前記タイマ
ーや電磁弁Oの故障により冷媒を再生するできなくなる
のを防止するために、タイマーや電磁弁Oを定期的に保
守点検しなければならない問題もあった。However, in the above absorption refrigerator, the refrigerant regeneration pipe P branches off from between the refrigerant pump I and the refrigerant distribution device G, and the refrigerant distribution device G is Since the liquid refrigerant is higher than the branch position of the regeneration pipe P, when the electromagnetic valve O is opened to return the liquid refrigerant to the generator A for regeneration, most of the liquid refrigerant circulating in the refrigerant circulation path H is generated by the generator A. And the performance in the evaporator E is remarkably reduced, so that normal operation cannot be continued. Further, since the solenoid valve O is periodically opened by the timer and the refrigerant contaminated by the solution is regenerated by the opening operation of the solenoid valve O, the refrigerant is regenerated by failure of the timer and the solenoid valve O. There was also a problem that the timer and the solenoid valve O had to be regularly maintained and inspected in order to prevent it from becoming impossible.
【0007】しかして、本発明の目的は、運転中に蒸発
器の能力を低下させることなく再生ができ、しかも定期
的な保守点検を行うことなく、液冷媒の純度を、蒸発温
度の低下に影響を与えない程度の純度に保つことができ
るようにする点にある。SUMMARY OF THE INVENTION It is an object of the present invention to regenerate an evaporator during operation without deteriorating the capacity of the evaporator and to reduce the purity of the liquid refrigerant to a lower evaporating temperature without performing periodic maintenance. The point is to be able to maintain the purity to such an extent that no influence is exerted.
【0008】[0008]
【課題を解決するための手段】上記目的を得るため、本
発明は、発生器1と、凝縮器2、蒸発器3及び吸収器4
とを備え、前記蒸発器3の底部に冷媒液溜6を設け、上
部に冷媒液供給部7を設けて、前記冷媒液溜6と冷媒液
供給部7との間に、冷媒ポンプ8を備えた冷媒循環路9
を設けると共に、前記吸収器4と発生器1との間に溶液
ポンプ12をもった溶液管14を設けて、冷媒を吸収し
た稀溶液を前記吸収器4から前記発生器1に戻すように
した吸収式冷凍機であって、前記冷媒循環路9における
前記冷媒ポンプ8の出口側に、流量調整機構22を備
え、前記冷媒液溜6の冷媒液の1部を前記吸収器4又は
前記溶液管14にバイパスさせる冷媒再生管21を設け
たものである。To achieve the above object, the present invention provides a generator 1, a condenser 2, an evaporator 3, and an absorber 4.
A refrigerant liquid reservoir 6 is provided at a bottom portion of the evaporator 3, a refrigerant liquid supply portion 7 is provided at an upper portion, and a refrigerant pump 8 is provided between the refrigerant liquid reservoir 6 and the refrigerant liquid supply portion 7. Refrigerant circuit 9
And a solution pipe 14 having a solution pump 12 is provided between the absorber 4 and the generator 1 so that the dilute solution that has absorbed the refrigerant is returned from the absorber 4 to the generator 1. An absorption refrigerator, which is provided with a flow rate adjusting mechanism 22 at an outlet side of the refrigerant pump 8 in the refrigerant circulation path 9, wherein a part of the refrigerant liquid in the refrigerant liquid reservoir 6 is supplied to the absorber 4 or the solution pipe. 14 is provided with a refrigerant regeneration pipe 21 to be bypassed.
【0009】加えて、流量調整機構22の下流側におけ
る冷媒再生管21と、凝縮器2と蒸発器3の冷媒液溜6
とを接続する冷媒供給管10との間で熱交換する熱交換
器23を設けたものである。In addition , the refrigerant regeneration pipe 21 on the downstream side of the flow control mechanism 22 and the refrigerant reservoir 6 of the condenser 2 and the evaporator 3
It is provided with a heat exchanger 23 for exchanging heat between the refrigerant supply pipe 10 for connecting and.
【0010】[0010]
【作用】前記冷媒液溜6から前記冷媒液供給部7へ循環
供給される冷媒液の1部が、前記流量調整機構22をも
った前記冷媒再生管21を介して少しづつ前記吸収器4
又は前記溶液管14にバイパスされるから、バイパスし
た冷媒は前記発生器1へ送られて前記発生器1で蒸発
し、前記蒸発器3を循環する冷媒液を再生することがで
きる。従って、従来例のように冷媒の再生時に蒸発器の
能力を低下さたり、また、定期的にタイマーや電磁弁な
どの保守点検を行うことなく、溶液で汚染された冷媒を
運転中に常時再生することができ、冷媒の溶液汚染によ
る蒸発器3の能力低下を防止できる。A part of the refrigerant liquid circulated and supplied from the refrigerant liquid reservoir to the refrigerant liquid supply section is gradually supplied to the absorber through the refrigerant regeneration pipe having the flow rate adjusting mechanism.
Alternatively, since the refrigerant is bypassed by the solution pipe 14, the bypassed refrigerant is sent to the generator 1 and evaporated by the generator 1, and the refrigerant liquid circulating through the evaporator 3 can be regenerated. Therefore, the refrigerant contaminated with the solution is constantly regenerated during operation without reducing the capacity of the evaporator at the time of regenerating the refrigerant as in the conventional example and without regularly performing maintenance and inspection of the timer and the solenoid valve. Thus, it is possible to prevent the performance of the evaporator 3 from decreasing due to the solution contamination of the refrigerant.
【0011】また、流量調整機構22の下流側における
冷媒再生管21と、凝縮器2と蒸発器3の冷媒液溜6と
を接続する冷媒供給管10との間で熱交換する熱交換器
23を設けたから、前記熱交換器23により前記吸収器
4又は前記溶液管14にバイパスする温度の低い冷媒を
利用して前記凝縮器2から前記冷媒液溜6に流入する温
度の高い冷媒液を冷却することができるから、冷却しな
いで前記冷媒液溜6へ流入するときに発生する冷媒液の
フラッシュによるウオターハンマーの発生を防止するこ
とができる。A heat exchanger 23 for exchanging heat between the refrigerant regeneration pipe 21 downstream of the flow control mechanism 22 and the refrigerant supply pipe 10 connecting the condenser 2 and the refrigerant reservoir 6 of the evaporator 3. Is provided, the high-temperature refrigerant flowing from the condenser 2 into the refrigerant liquid reservoir 6 is cooled by utilizing the low-temperature refrigerant bypassed to the absorber 4 or the solution pipe 14 by the heat exchanger 23. Therefore, it is possible to prevent the occurrence of a water hammer due to the flushing of the refrigerant liquid generated when the refrigerant liquid flows into the refrigerant liquid reservoir 6 without cooling.
【0012】[0012]
【実施例】図1に示した吸収式冷凍機は、加熱蒸気の供
給により溶液を加熱する発生器1と、該発生器1で蒸発
した冷媒蒸気を凝縮する凝縮器2と、蒸発器3及び吸収
器4とを備え、この蒸発器3及び吸収器4を一つの容器
5に内装し、エリミネータ51及び隔壁52により前記
容器5内を前記蒸発器3と吸収器4とに区画している。
また、前記蒸発器3の底部に冷媒液溜6を形成すると共
に、上部には冷媒を冷却管31上に散布するスプレー装
置から成る冷媒液供給部7を設け、前記冷媒液溜6と冷
媒液供給部7との間には、冷媒ポンプ8を備えた冷媒循
環路9を設け、前記冷媒液溜6の液冷媒を前記冷媒液供
給部7へ循環供給するようにしている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The absorption refrigerator shown in FIG. 1 comprises a generator 1 for heating a solution by supplying heated steam, a condenser 2 for condensing refrigerant vapor evaporated by the generator 1, an evaporator 3, The evaporator 3 and the absorber 4 are provided in one container 5, and the inside of the container 5 is divided into the evaporator 3 and the absorber 4 by an eliminator 51 and a partition 52.
Further, a refrigerant liquid reservoir 6 is formed at the bottom of the evaporator 3 and a refrigerant liquid supply unit 7 composed of a spray device for spraying the refrigerant onto the cooling pipe 31 is provided at the upper part. A refrigerant circulation path 9 including a refrigerant pump 8 is provided between the supply part 7 and the refrigerant circulation path 9. The liquid refrigerant in the refrigerant liquid reservoir 6 is circulated and supplied to the refrigerant liquid supply part 7.
【0013】また、前記凝縮器2と前記冷媒液溜6との
間には、前記凝縮器2で凝縮した冷媒を前記冷媒液溜6
に供給する冷媒供給管10を接続する一方、前記吸収器
4の下部に形成する溶液液溜11と前記発生器1との間
には溶液ポンプ12及び熱交換器13をもった溶液管1
4を設けて、冷媒を吸収した稀溶液を前記熱交換器13
で加熱してから前記発生器1に戻すようにすると共に、
前記吸収器4と前記発生器1との間には、該発生器1の
濃溶液を前記熱交換器13を経て前記吸収器4の上部に
設けたスプレー装置から成る溶液供給部15に供給する
濃溶液管16を設け、前記吸収器4において前記蒸発器
3で蒸発した冷媒蒸気を溶液に吸収するようにしてい
る。The refrigerant condensed in the condenser 2 is provided between the condenser 2 and the refrigerant liquid reservoir 6.
A solution supply pipe 10 having a solution pump 12 and a heat exchanger 13 is provided between the generator 1 and a solution liquid reservoir 11 formed below the absorber 4 while a refrigerant supply pipe 10 is connected to the supply pipe 10.
4 is provided, and the diluted solution having absorbed the refrigerant is transferred to the heat exchanger 13.
And then return to the generator 1;
Between the absorber 4 and the generator 1, the concentrated solution of the generator 1 is supplied through the heat exchanger 13 to a solution supply unit 15 composed of a spray device provided above the absorber 4. A concentrated solution pipe 16 is provided to absorb the refrigerant vapor evaporated by the evaporator 3 in the absorber 4 into a solution.
【0014】尚、図1に示した吸収式冷凍機では、臭化
リチュウムなどの溶液を用いて、該溶液に冷媒の蒸気を
吸収することにより冷凍を行うようにしている。また、
図1において、17は前記発生器1内の溶液を蒸気によ
り加熱する加熱装置、18は前記発生器1と凝縮器2と
の間に設けたエリミネータ、19は前記凝縮器2内の冷
媒蒸気を凝縮する冷却水管、20は前記吸収器4に設け
た冷却水管である。In the absorption refrigerator shown in FIG. 1, refrigeration is performed by using a solution of lithium bromide or the like and absorbing the refrigerant vapor into the solution. Also,
In FIG. 1, 17 is a heating device for heating the solution in the generator 1 with steam, 18 is an eliminator provided between the generator 1 and the condenser 2, and 19 is a refrigerant vapor in the condenser 2. A cooling water pipe 20 for condensing is a cooling water pipe provided in the absorber 4.
【0015】しかして、本発明では、以上のように構成
した吸収式冷凍機において、前記冷媒循環路9における
前記冷媒ポンプ8の出口側に、該冷媒循環路9から分岐
して前記吸収器4の前記溶液液溜11に連通する冷媒再
生管21を設け、該冷媒再生管21に所定の流通抵抗を
もった主としてオリフィスから成る流量調整機構22を
介装して、前記冷媒ポンプ8により前記冷媒液供給部7
に供給する冷媒の1部を前記溶液液溜11にバイパスさ
せると共に、前記冷媒再生管21と前記冷媒供給管10
との間に熱交換器23を設け、該熱交換器23により前
記流量調整機構22の下流側を流れる低温の冷媒液によ
り前記冷媒供給管10を前記凝縮器2から前記冷媒液溜
6へ流れる高温の液冷媒を冷却できるようにするのであ
る。尚、24は、開閉弁25を介装した補助再生管であ
る。According to the present invention, in the absorption refrigerating machine configured as described above, the absorber 4 branches off from the refrigerant circuit 9 to the outlet side of the refrigerant pump 8 in the refrigerant circuit 9. A refrigerant regenerating pipe 21 communicating with the solution liquid reservoir 11 is provided, and a flow regulating mechanism 22 mainly composed of an orifice having a predetermined flow resistance is interposed in the refrigerant regenerating pipe 21. Liquid supply unit 7
A part of the refrigerant to be supplied to the refrigerant is bypassed to the solution reservoir 11, and the refrigerant regeneration pipe 21 and the refrigerant supply pipe 10
A heat exchanger 23 is provided between the refrigerant supply pipe 10 and the refrigerant supply pipe 10 flowing from the condenser 2 to the refrigerant liquid reservoir 6 by a low-temperature refrigerant liquid flowing downstream of the flow rate adjusting mechanism 22 by the heat exchanger 23. It is possible to cool the high-temperature liquid refrigerant. Reference numeral 24 denotes an auxiliary regeneration pipe provided with an on-off valve 25.
【0016】次に、以上のように構成した吸収式冷凍機
の作動を説明する。Next, the operation of the absorption refrigerator configured as described above will be described.
【0017】前記冷媒液溜6から前記冷媒循環路9を経
て前記冷媒液供給部7へ供給された冷媒液は、前記冷却
管31上に散布されて蒸発し、前記蒸発器3の冷却管3
1を流れる冷却水を冷却すると共に、蒸発した冷媒蒸気
は前記エリミネータ51を通過してから前記吸収器4の
上部に設けた前記溶液供給部15から流下する溶液に吸
収され、冷媒蒸気を吸収した稀溶液は、前記溶液液溜1
1から前記熱交換器13を経て前記発生器1に戻るので
ある。The refrigerant liquid supplied from the refrigerant liquid reservoir 6 to the refrigerant liquid supply section 7 through the refrigerant circulation path 9 is scattered on the cooling pipe 31 and evaporates.
While cooling the cooling water flowing through 1, the evaporated refrigerant vapor was absorbed by the solution flowing down from the solution supply unit 15 provided above the absorber 4 after passing through the eliminator 51, and absorbed the refrigerant vapor. The diluted solution is the solution reservoir 1
1 returns to the generator 1 via the heat exchanger 13.
【0018】また、前記冷媒液溜6から前記冷媒液供給
部7へ循環供給される冷媒液の1部は、運転中常時前記
冷媒再生管21を介して少しづつ前記吸収器4の溶液液
溜11へ流入し、該溶液液溜11に流入した冷媒液は、
該溶液液溜11から前記発生器1へ送られ該発生器1に
おける蒸発により冷媒を再生することができるのであっ
て、この冷媒液の再生により運転を継続しながら前記循
環路9を循環する冷媒の純度を蒸発温度の低下に影響を
与えない程度の純度(例えば2%以下)に保つことがで
きるのである。しかも、前記吸収器4の溶液液溜11へ
バイパスされる冷媒液量は前記循環路9を循環する冷媒
液の全量でなく、その1部であって、前記冷媒液供給部
7から冷却管31上に散布される冷媒液量を減少させる
ものでないから、蒸発器3の能力低下はないのであり、
その上、前記溶液液溜11への冷媒液バイパスは運転中
常時行うものであって、運転しながら再生し冷媒純度を
保つようにしているから、従来例のように定期的にタイ
マーや電磁弁などの保守点検を行う必要もないのであ
る。尚、前記補助再生管24の前記開閉弁25を開いて
定期的に冷媒の再生を行うこともできる。この場合その
再生間隔を従来例より広げられることはいうまでもない
し、また、特に必要なものでもない。A part of the refrigerant liquid circulated and supplied from the refrigerant liquid reservoir 6 to the refrigerant liquid supply part 7 is gradually supplied to the solution liquid reservoir of the absorber 4 through the refrigerant regeneration pipe 21 during operation. 11 and the refrigerant liquid flowing into the solution reservoir 11
The refrigerant that is sent from the solution reservoir 11 to the generator 1 can be regenerated by evaporation in the generator 1, and the refrigerant that circulates in the circulation path 9 while continuing operation by regenerating the refrigerant liquid Can be maintained at such a level that does not affect the decrease in the evaporation temperature (for example, 2% or less). Moreover, the amount of the refrigerant liquid bypassed to the solution liquid reservoir 11 of the absorber 4 is not the entire amount of the refrigerant liquid circulating in the circulation path 9 but a part thereof, Since it does not reduce the amount of the refrigerant liquid sprayed on the top, there is no decrease in the performance of the evaporator 3.
In addition, the refrigerant liquid bypass to the solution liquid reservoir 11 is always performed during the operation, and is regenerated while the operation is being performed to maintain the refrigerant purity. There is no need to perform maintenance inspections such as these. The on-off valve 25 of the auxiliary regeneration pipe 24 can be opened to periodically regenerate the refrigerant. In this case, it goes without saying that the reproduction interval can be extended as compared with the conventional example, and it is not particularly necessary.
【0019】また、以上のように前記熱交換器23を設
けた場合には、前記凝縮器2から前記冷媒液溜6に流入
する温度の高い冷媒液を前記溶液液溜11にバイパスす
る冷媒液により冷却することができるから、冷却しない
で前記冷媒液溜6へ流入するときに発生する冷媒液のフ
ラッシュによるウオターハンマーの発生を防止すること
ができる。In the case where the heat exchanger 23 is provided as described above, the refrigerant liquid which flows from the condenser 2 into the refrigerant liquid reservoir 6 to bypass the high-temperature refrigerant liquid to the solution liquid reservoir 11 is provided. Therefore, it is possible to prevent the occurrence of a water hammer due to the flushing of the coolant liquid generated when the coolant flows into the coolant reservoir 6 without cooling.
【0020】尚、図1に示した実施例は、前記発生器1
で発生した冷媒蒸気を前記凝縮器2で凝縮する単効用の
吸収式冷凍機について説明したが、高温及び低温発生器
を用いる二重効用の吸収式冷凍機に適用してもよい。ま
た、前記冷媒再生管21を前記溶液液溜11に接続した
が前記溶液管14に接続してもよいし、また、前記オリ
フィスを用いて前記溶液液溜11へバイパスする冷媒流
量を所定の流量に設定したが、キャピラリーや流量調整
弁を用いて所定の流量に設定するようにしてもよい。Incidentally, the embodiment shown in FIG.
Although the single-effect absorption refrigerator which condenses the refrigerant vapor generated in the above in the condenser 2 has been described, the invention may be applied to a double-effect absorption refrigerator using a high-temperature and low-temperature generator. Although the refrigerant regeneration pipe 21 is connected to the solution reservoir 11, the refrigerant regeneration pipe 21 may be connected to the solution pipe 14, or the flow rate of the refrigerant bypassed to the solution reservoir 11 using the orifice may be a predetermined flow rate. However, a predetermined flow rate may be set using a capillary or a flow rate control valve.
【0021】[0021]
【発明の効果】以上説明したように、本発明は、発生器
1と、凝縮器2、蒸発器3及び吸収器4とを備え、前記
蒸発器3の底部に冷媒液溜6を設け、上部に冷媒液供給
部7を設けて、前記冷媒液溜6と冷媒液供給部7との間
に、冷媒ポンプ8を備えた冷媒循環路9を設けると共
に、前記吸収器4と発生器1との間に溶液ポンプ12を
もった溶液管14を設けて、冷媒を吸収した稀溶液を前
記吸収器4から前記発生器1に戻すようにした吸収式冷
凍機であって、前記冷媒循環路9における前記冷媒ポン
プ8の出口側に、流量調整機構22を備え、前記冷媒液
溜6の冷媒液の1部を前記吸収器4又は前記溶液管14
にバイパスさせる冷媒再生管21を設けたから、前記冷
媒液溜6から前記冷媒液供給部7へ循環供給される冷媒
液の1部が、前記冷媒再生管21を介して少しづつ前記
吸収器4又は溶液管14にバイパスされ、バイパスした
冷媒は前記発生器1へ送られて前記発生器1で蒸発する
ことにより、蒸発器3の能力を低下させることなく冷媒
を再生することができる。従って、従来例のように冷媒
の再生時に蒸発器の能力を低下さたり、また、定期的に
タイマーや電磁弁などの保守点検を行うことなく、溶液
で汚染された冷媒を運転中に常時再生することができ、
冷媒の溶液汚染による蒸発器3の能力低下を防止でき
る。As described above, the present invention comprises a generator 1, a condenser 2, an evaporator 3 and an absorber 4, and a refrigerant liquid reservoir 6 is provided at the bottom of the evaporator 3, and And a refrigerant circulation path 9 provided with a refrigerant pump 8 between the refrigerant liquid reservoir 6 and the refrigerant liquid supply section 7, and a connection between the absorber 4 and the generator 1. An absorption refrigerator in which a solution pipe 14 having a solution pump 12 is provided therebetween to return a dilute solution having absorbed a refrigerant from the absorber 4 to the generator 1. On the outlet side of the refrigerant pump 8, a flow rate adjusting mechanism 22 is provided, and a part of the refrigerant liquid in the refrigerant liquid reservoir 6 is supplied to the absorber 4 or the solution pipe 14.
Is provided, a part of the refrigerant liquid circulated and supplied from the refrigerant liquid reservoir 6 to the refrigerant liquid supply unit 7 is gradually passed through the refrigerant regeneration pipe 21 to the absorber 4 or The refrigerant bypassed by the solution pipe 14 is sent to the generator 1 and evaporated by the generator 1, so that the refrigerant can be regenerated without lowering the capacity of the evaporator 3. Therefore, the refrigerant contaminated with the solution is constantly regenerated during operation without reducing the capacity of the evaporator at the time of regenerating the refrigerant as in the conventional example and without regularly performing maintenance and inspection of the timer and the solenoid valve. Can be
It is possible to prevent the performance of the evaporator 3 from lowering due to the solution contamination of the refrigerant.
【0022】また、流量調整機構22の下流側における
冷媒再生管21と、凝縮器2と蒸発器3の冷媒液溜6と
を接続する冷媒供給管10との間で熱交換する熱交換器
23を設けたから、前記熱交換器23において前記凝縮
器2から前記冷媒液溜6に流入する温度の高い冷媒液
を、前記冷媒液溜6から前記吸収器4又は溶液管14に
バイパスする温度の低い冷媒液により冷却することがで
きるから、冷却しないで前記冷媒液溜6へ流入するとき
に発生する冷媒液のフラッシュによるウオターハンマー
の発生を防止することができる。A heat exchanger 23 for exchanging heat between the refrigerant regeneration pipe 21 downstream of the flow rate adjusting mechanism 22 and the refrigerant supply pipe 10 connecting the condenser 2 and the refrigerant reservoir 6 of the evaporator 3. Is provided, the high-temperature refrigerant liquid flowing from the condenser 2 to the refrigerant liquid reservoir 6 in the heat exchanger 23 is bypassed from the refrigerant liquid reservoir 6 to the absorber 4 or the solution pipe 14 at a low temperature. Since cooling can be performed by the refrigerant liquid, it is possible to prevent the occurrence of water hammer due to the flushing of the refrigerant liquid that occurs when the refrigerant liquid flows into the refrigerant liquid reservoir 6 without cooling.
【図1】本発明の吸収式冷凍機の配管系統図である。FIG. 1 is a piping diagram of an absorption refrigerator of the present invention.
【図2】従来例を示す配管系統図である。FIG. 2 is a piping system diagram showing a conventional example.
1 発生器 2 凝縮器 3 蒸発器 4 吸収器 6 冷媒液溜 7 冷媒液供給部 8 冷媒ポンプ 9 冷媒循環路 10 冷媒供給管 12 溶液ポンプ 14 溶液管 21 冷媒再生管 22 流量調整機構 23 熱交換器 DESCRIPTION OF SYMBOLS 1 Generator 2 Condenser 3 Evaporator 4 Absorber 6 Refrigerant liquid reservoir 7 Refrigerant liquid supply part 8 Refrigerant pump 9 Refrigerant circulation path 10 Refrigerant supply pipe 12 Solution pump 14 Solution pipe 21 Refrigerant regeneration pipe 22 Flow rate adjusting mechanism 23 Heat exchanger
Claims (1)
収器4とを備え、前記蒸発器3の底部に冷媒液溜6を設
け、上部に冷媒液供給部7を設けて、前記冷媒液溜6と
冷媒液供給部7との間に、冷媒ポンプ8を備えた冷媒循
環路9を設けると共に、前記吸収器4と発生器1との間
に溶液ポンプ12をもった溶液管14を設けて、冷媒を
吸収した稀溶液を前記吸収器4から前記発生器1に戻す
ようにした吸収式冷凍機であって、前記冷媒循環路9に
おける前記冷媒ポンプ8の出口側に、流量調整機構22
を備え、前記冷媒液溜6の冷媒液の一部を前記吸収器4
又は前記溶液管14にバイパスさせる冷媒再生管21を
設け、かつ、流量調整機構22の下流側における冷媒再
生管21と、凝縮器2と蒸発器3の冷媒液溜6とを接続
する冷媒供給管10との間で熱交換する熱交換器23を
設けたことを特徴とする吸収式冷凍機。An evaporator includes a generator, a condenser, an evaporator, and an absorber. A refrigerant liquid reservoir is provided at a bottom part of the evaporator, and a refrigerant liquid supply part is provided at an upper part of the evaporator. A solution circulation path 9 having a coolant pump 8 is provided between the coolant reservoir 6 and the coolant supply unit 7, and a solution pipe having a solution pump 12 between the absorber 4 and the generator 1. 14. An absorption refrigerator in which a dilute solution having absorbed refrigerant is returned from the absorber 4 to the generator 1 by providing a refrigerant flow path 14 at the outlet side of the refrigerant pump 8 in the refrigerant circulation path 9. Adjustment mechanism 22
And a part of the refrigerant liquid in the refrigerant liquid reservoir 6 is transferred to the absorber 4
Alternatively, a refrigerant regeneration pipe 21 for bypassing the solution pipe 14 is provided , and a refrigerant recycle pipe downstream of the flow control mechanism 22 is provided .
The raw tube 21 is connected to the condenser 2 and the refrigerant reservoir 6 of the evaporator 3.
The heat exchanger 23 that exchanges heat with the refrigerant supply pipe 10
An absorption type refrigerator characterized by being provided .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4215306A JP2789951B2 (en) | 1992-08-12 | 1992-08-12 | Absorption refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4215306A JP2789951B2 (en) | 1992-08-12 | 1992-08-12 | Absorption refrigerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0666454A JPH0666454A (en) | 1994-03-08 |
JP2789951B2 true JP2789951B2 (en) | 1998-08-27 |
Family
ID=16670143
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4215306A Expired - Fee Related JP2789951B2 (en) | 1992-08-12 | 1992-08-12 | Absorption refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2789951B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102654327A (en) * | 2011-03-04 | 2012-09-05 | 中国海洋大学 | Forced convection absorption device |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106482382B (en) * | 2016-11-14 | 2019-06-07 | 双良节能系统股份有限公司 | Direct combustion type first class lithium bromide absorptive heat pump unit with direct heating |
CN106482381B (en) * | 2016-11-14 | 2019-06-07 | 双良节能系统股份有限公司 | The steam type first-class lithium bromide absorption type heat pump unit of carrying vapour direct heating |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5860171A (en) * | 1981-10-02 | 1983-04-09 | 三洋電機株式会社 | Absorption refrigerator |
-
1992
- 1992-08-12 JP JP4215306A patent/JP2789951B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102654327A (en) * | 2011-03-04 | 2012-09-05 | 中国海洋大学 | Forced convection absorption device |
CN102654327B (en) * | 2011-03-04 | 2014-07-16 | 中国海洋大学 | Forced convection absorption device |
Also Published As
Publication number | Publication date |
---|---|
JPH0666454A (en) | 1994-03-08 |
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