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JPH0413064A - Absorption type water cooler/heater - Google Patents

Absorption type water cooler/heater

Info

Publication number
JPH0413064A
JPH0413064A JP11232690A JP11232690A JPH0413064A JP H0413064 A JPH0413064 A JP H0413064A JP 11232690 A JP11232690 A JP 11232690A JP 11232690 A JP11232690 A JP 11232690A JP H0413064 A JPH0413064 A JP H0413064A
Authority
JP
Japan
Prior art keywords
refrigerant
absorption liquid
heater
cooling
absorption
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.)
Pending
Application number
JP11232690A
Other languages
Japanese (ja)
Inventor
Takashi Kaneyama
兼山 尚
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.)
Fujitsu VLSI Ltd
Fujitsu Ltd
Original Assignee
Fujitsu VLSI Ltd
Fujitsu 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 Fujitsu VLSI Ltd, Fujitsu Ltd filed Critical Fujitsu VLSI Ltd
Priority to JP11232690A priority Critical patent/JPH0413064A/en
Publication of JPH0413064A publication Critical patent/JPH0413064A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔概 要〕 各種の熱利用設備に冷水と温水を供給する冷温水機に関
し、 冷媒の分離に際し加熱設備を必要としない吸収式冷温水
機の捉供を目的とし、 伝熱管および伝熱管に冷媒を散布する冷媒散布管を有し
、冷媒の蒸発によって伝熱管中の水を冷却する蒸発器と
、吸収液を散布する吸収液散布管および冷却水を流す冷
却管を有し、冷媒の蒸気を散布された吸収液に吸収させ
る吸収器と、冷媒が吸収された吸収液を回収し圧力を加
えるポンプ、および吸収液から冷媒を分離する逆浸透膜
ユニットを有する再生器と、前記吸収器の冷却管の出口
に連通ずる冷却管を有し冷媒を冷却する冷却器とで構成
する。
[Detailed Description of the Invention] [Summary] The present invention relates to a water chiller/heater that supplies cold water and hot water to various types of heat utilization equipment, and aims to provide an absorption type water chiller/heater that does not require heating equipment when separating refrigerant. It has a heat exchanger tube and a refrigerant distribution tube that distributes refrigerant to the heat exchanger tube, an evaporator that cools the water in the heat exchanger tube by evaporation of the refrigerant, an absorption liquid distribution tube that distributes an absorption liquid, and a cooling tube that flows cooling water. A regenerator that has an absorber that absorbs refrigerant vapor into the dispersed absorption liquid, a pump that collects and applies pressure to the absorption liquid in which the refrigerant has been absorbed, and a reverse osmosis membrane unit that separates the refrigerant from the absorption liquid. and a cooler having a cooling pipe communicating with the outlet of the cooling pipe of the absorber and cooling the refrigerant.

〔産業上の利用分野〕[Industrial application field]

本発明は各種の熱利用設備に冷水と温水を供給する冷温
水機に係り、特に冷媒の分離に際して加熱設備を必要と
しない吸収式冷温水機に関する。
The present invention relates to a water chiller/heater that supplies cold water and hot water to various types of heat utilization equipment, and particularly relates to an absorption type water chiller/heater that does not require heating equipment when separating a refrigerant.

吸収式の冷温水機は圧縮機や電熱ヒータを用いた冷温水
機に比べて振動や騒音が小さく、騒音や極く僅かな振動
も問題視される半導体製造工場等において、熱利用設備
に冷水と温水を供給する手段として広く利用されている
Absorption-type water cooler/heater has less vibration and noise than water cooler/heater that uses a compressor or electric heater, and is used in heat utilization equipment such as semiconductor manufacturing factories where noise and even the slightest vibration are considered a problem. It is widely used as a means of supplying hot water.

しかし現在利用されている吸収式冷温水機は冷媒の分離
に際して、ボイラーから供給される蒸気等の外部熱源を
必要とするため、熱源を供給する手段の無い場所では使
用できないという問題がある。そこで冷媒の分離に際し
て外部熱源を必要としない吸収式冷温水機の開発が要望
されている。
However, the absorption type water chiller/heater currently in use requires an external heat source such as steam supplied from a boiler when separating the refrigerant, so there is a problem that it cannot be used in places without a means to supply a heat source. Therefore, there is a need for the development of an absorption type water chiller/heater that does not require an external heat source when separating the refrigerant.

〔従来の技術〕[Conventional technology]

第2図は従来の吸収式冷温水機を示す模式図である。 FIG. 2 is a schematic diagram showing a conventional absorption type water chiller/heater.

図において従来の吸収式冷温水機は2個の真空容器1お
よび2を有し、内部圧力の低い(7mmHg程度)真空
容器1には蒸発器3と吸収器4が内蔵されている。蒸発
器3は冷水が内部を流れる伝熱管31と冷媒(水)を散
布する冷媒散布管32からなり、伝熱管31上に散布さ
れた冷媒は極く低温で蒸発し伝熱管31内の冷水を5℃
程度に冷却する。
In the figure, the conventional absorption type water chiller/heater has two vacuum containers 1 and 2, and the vacuum container 1, which has a low internal pressure (about 7 mmHg), has an evaporator 3 and an absorber 4 built therein. The evaporator 3 consists of a heat exchanger tube 31 through which cold water flows and a refrigerant distribution tube 32 that distributes refrigerant (water). 5℃
Cool to a certain degree.

また吸収器4はリチウムブロマイド(LiBr)の水溶
液等の吸収液を散布する吸収液散布管41と、吸収液が
冷媒の蒸気を吸収したときに発生する吸収熱を除去する
冷却管42を具えており、蒸発器3において発生した冷
媒の蒸気を吸収液に吸収させることによって、真空容器
1の内部における蒸発圧力を一定に保ち連続的な蒸発を
可能にしている。
The absorber 4 also includes an absorption liquid distribution pipe 41 for dispersing an absorption liquid such as an aqueous solution of lithium bromide (LiBr), and a cooling pipe 42 for removing absorption heat generated when the absorption liquid absorbs refrigerant vapor. By absorbing the refrigerant vapor generated in the evaporator 3 into the absorption liquid, the evaporation pressure inside the vacuum container 1 is kept constant and continuous evaporation is possible.

一方、内部圧力が高い(75mm1g程度)真空容器2
には再生器5と凝縮器6が内蔵されており、前記吸収器
4において冷媒を吸収し真空容器1の底に溜まった吸収
液は、ポンプ7によって汲み上げられ配管71を介して
再生器5に供給される。
On the other hand, vacuum container 2 with high internal pressure (about 75 mm and 1 g)
has a built-in regenerator 5 and a condenser 6, and the absorbed liquid that has absorbed the refrigerant in the absorber 4 and accumulated at the bottom of the vacuum container 1 is pumped up by a pump 7 and sent to the regenerator 5 via piping 71. Supplied.

再生器5は外部熱源から供給される蒸気が中を流れる伝
熱管5】を有し、再生器5に供給された冷媒を吸収して
なる吸収液は加熱濃縮されて、真空容器2の底部に開口
している吸収液散布管41を介し再び吸収器4に戻され
る。
The regenerator 5 has heat transfer tubes 5 through which steam supplied from an external heat source flows, and the absorption liquid formed by absorbing the refrigerant supplied to the regenerator 5 is heated and concentrated, and is deposited at the bottom of the vacuum container 2. The absorbent is returned to the absorber 4 via the open absorption liquid distribution pipe 41.

また凝縮器6は再生器5で冷媒を吸収してなる吸収液を
加熱濃縮する際に、蒸気となって吸収液から分離された
冷媒を冷却する冷却管61と、冷却管61によって冷却
され液化した冷媒を受ける受皿62を有し、液化した冷
媒は受皿62に開口している冷媒散布管32を介して再
び蒸発器3に戻される。
In addition, the condenser 6 has a cooling pipe 61 that cools the refrigerant that is separated from the absorption liquid as vapor when heating and concentrating the absorption liquid obtained by absorbing the refrigerant in the regenerator 5, and a cooling pipe 61 that cools the refrigerant that is separated from the absorption liquid and is liquefied. The liquefied refrigerant is returned to the evaporator 3 via the refrigerant distribution pipe 32 that is open to the receiver 62.

このように蒸発と吸収と再生と凝縮を繰り返し冷媒と吸
収液を循環させることによって、蒸発器3の伝熱管31
から冷水を連続的に取り出すことができる。また凝縮器
6の冷却管61は吸収器4の冷却管42に連通しており
、冷却管42に供給された冷却水は吸収器4において吸
収液から吸収熱を奪い、更に凝縮器6において蒸気化し
た冷媒から凝縮潜熱を奪って温水になる。即ち、凝縮器
の冷却管から温水を連続的に取り出すことができる。
By repeating evaporation, absorption, regeneration, and condensation in this way and circulating the refrigerant and absorption liquid, the heat exchanger tubes 31 of the evaporator 3
Cold water can be extracted continuously. Further, the cooling pipe 61 of the condenser 6 is connected to the cooling pipe 42 of the absorber 4, and the cooling water supplied to the cooling pipe 42 absorbs absorbed heat from the absorption liquid in the absorber 4, and further vaporizes in the condenser 6. It takes away the latent heat of condensation from the refrigerant and turns it into hot water. That is, hot water can be continuously taken out from the cooling pipe of the condenser.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

吸収式の冷温水機は圧縮機等の可動部がないため振動や
騒音が小さく、騒音や掻く僅かな振動も問題視される半
導体製造工場等において、熱利用設備に冷水と温水を供
給する手段として広(利用されている。しかし、従来の
吸収式冷温水機は蒸気の如く冷媒の分離に際して、ボイ
ラーから供給される蒸気等の外部熱源を必要とするため
、熱源を供給する手段の無い場所では使用できないとい
う問題があった。
Absorption-type water chillers and hot water machines have low vibration and noise because they do not have moving parts such as compressors, and are a means of supplying cold and hot water to heat utilization equipment in semiconductor manufacturing factories and other places where noise and slight vibrations are considered a problem. However, conventional absorption type water chillers and hot water machines require an external heat source such as steam supplied from a boiler to separate the refrigerant, so they are used in places where there is no means to supply a heat source. There was a problem that it could not be used.

本発明の目的は冷媒の分離に際し加熱設備を必要としな
い吸収式冷温水機を提供することにある。
An object of the present invention is to provide an absorption type water chiller/heater that does not require heating equipment when separating the refrigerant.

〔課題を解決するための手段〕[Means to solve the problem]

第1図は本発明になる吸収式冷温水機を示す模式図であ
る。なお全図を通し同し対象物は同一記号で表している
FIG. 1 is a schematic diagram showing an absorption type water chiller/heater according to the present invention. The same objects are represented by the same symbols throughout the figures.

上記課題は伝熱管31および伝熱管31に冷媒を散布す
る冷媒散布管32を有し、冷媒の蒸発によって伝熱管3
1中の水を冷却する蒸発器3と、吸収液を散布する吸収
液散布管41および冷却水を流す冷却管42を有し、冷
媒の蒸気を散布された吸収液に吸収させる吸収器4と、
冷媒が吸収された吸収液を回収し圧力を加えるポンプ8
1、および吸収液から冷媒を分離する逆浸透膜ユニット
82を有する再生器8と、前記吸収器4の冷却管42の
出口に連通ずる冷却管91を有し、冷媒を冷却する冷却
器9とを具えてなる本発明の吸収式冷温水機によって達
成される。
The above-mentioned problem has a heat exchanger tube 31 and a refrigerant distribution tube 32 that distributes refrigerant to the heat exchanger tube 31, and the heat exchanger tube
1, an absorber 4 having an evaporator 3 for cooling the water in the 1, an absorption liquid distribution pipe 41 for dispersing an absorption liquid, and a cooling pipe 42 for flowing cooling water, and for absorbing refrigerant vapor into the sprayed absorption liquid. ,
A pump 8 that collects the absorption liquid in which the refrigerant has been absorbed and applies pressure.
1, a regenerator 8 having a reverse osmosis membrane unit 82 that separates the refrigerant from the absorption liquid, and a cooler 9 having a cooling pipe 91 communicating with the outlet of the cooling pipe 42 of the absorber 4 and cooling the refrigerant. This is achieved by the absorption type water chiller/heater of the present invention comprising:

〔作 用〕[For production]

第1図において冷媒が吸収された吸収液を回収し圧力を
加えるポンプ、および吸収液から冷媒を分離する逆浸透
膜ユニットを有する再生器と、前記吸収器の冷却管の出
口に連通ずる冷却管を有し、冷媒を冷却する冷却器とを
具えてなる本発明の吸収式冷温水機は、冷媒が吸収され
てなる吸収液から冷媒を分離する際に加熱する必要がな
い。即ち、冷媒の分離に際し加熱設備を必要としない吸
収式冷温水機を実現することができる。
In FIG. 1, there is shown a regenerator having a pump that collects and applies pressure to the absorption liquid in which refrigerant has been absorbed, a reverse osmosis membrane unit that separates the refrigerant from the absorption liquid, and a cooling pipe that communicates with the outlet of the cooling pipe of the absorber. The absorption type water chiller/heater of the present invention, which includes a cooler for cooling a refrigerant, does not need to be heated when separating the refrigerant from the absorption liquid in which the refrigerant is absorbed. That is, it is possible to realize an absorption type water chiller/heater that does not require heating equipment when separating the refrigerant.

〔実施例〕〔Example〕

以下第1図により本発明の実施例について詳細に説明す
る。
Embodiments of the present invention will be described in detail below with reference to FIG.

図において本発明になる吸収式冷温水機は真空容器1を
有し、内部圧力の低い(7II1mog程度)真空容器
1には蒸発器3と吸収器4が内蔵されている。蒸発器3
は冷水が内部を流れる伝熱管31と冷媒(水)を散布す
る冷媒散布管32からなり、伝熱管31上に散布された
冷媒は極く低温で蒸発し伝熱管31内の冷水を5°C程
度に冷却する。
In the figure, the absorption type water chiller/heater according to the present invention has a vacuum container 1, and an evaporator 3 and an absorber 4 are built into the vacuum container 1, which has a low internal pressure (about 7II1 mog). Evaporator 3
consists of a heat exchanger tube 31 through which cold water flows and a refrigerant distribution tube 32 that distributes refrigerant (water).The refrigerant sprinkled onto the heat exchanger tube 31 evaporates at an extremely low temperature and cools the cold water inside the heat exchanger tube 31 to 5°C. Cool to a certain degree.

また吸収器4はLiBrの水溶液等の吸収液を散布する
吸収液散布管41と、吸収液が冷媒の蒸気を吸収したと
きに発生する吸収熱を除去する冷却管42を具えており
、蒸発器3において発生した冷媒の蒸気を吸収液に吸収
させることによって、真空容器1の内部における蒸発圧
力を一定に保ち連続的な蒸発を可能にしている。
The absorber 4 also includes an absorption liquid dispersion pipe 41 for dispersing an absorption liquid such as an aqueous solution of LiBr, a cooling pipe 42 for removing absorption heat generated when the absorption liquid absorbs refrigerant vapor, and an evaporator. By absorbing the refrigerant vapor generated in step 3 into the absorption liquid, the evaporation pressure inside the vacuum container 1 is kept constant and continuous evaporation is possible.

一方、真空容器1の外部には再生器8と冷却器9とが配
設されており、再生器8は真空容器1から冷媒が吸収さ
れた吸収液を回収し圧力を加えるポンプ81と、吸収液
から冷媒を分離する逆浸透膜ユニット82とで構成され
、冷却器9は前記吸収器4が有する冷却管42の出口に
連通ずる冷却管91を具えている。
On the other hand, a regenerator 8 and a cooler 9 are disposed outside the vacuum vessel 1, and the regenerator 8 includes a pump 81 that collects and applies pressure to the absorption liquid in which the refrigerant has been absorbed from the vacuum vessel 1, and a pump 81 that applies pressure. The cooler 9 includes a reverse osmosis membrane unit 82 that separates refrigerant from liquid, and a cooling pipe 91 that communicates with the outlet of the cooling pipe 42 of the absorber 4.

逆浸透膜ユニット82は内部に逆浸透膜83が組み込ま
れており、冷媒が吸収された吸収液をポンプ81で冷媒
の浸透圧より高く加圧することによって、吸収液に吸収
されている冷媒だけが逆浸透膜83の反対側に抽出され
る。また冷媒を分離することによって濃縮された吸収液
は減圧され、逆浸透膜ユニット82に開口している吸収
液散布管41を介し再び吸収器4に戻される。
The reverse osmosis membrane unit 82 has a reverse osmosis membrane 83 incorporated therein, and by pressurizing the absorption liquid in which refrigerant has been absorbed to a level higher than the osmotic pressure of the refrigerant using the pump 81, only the refrigerant absorbed in the absorption liquid is removed. It is extracted to the opposite side of the reverse osmosis membrane 83. Further, the absorbent liquid concentrated by separating the refrigerant is depressurized and returned to the absorber 4 via the absorbent liquid distribution pipe 41 that is open to the reverse osmosis membrane unit 82.

逆浸透膜83の反対側に抽出された冷媒を冷媒散布管3
2を介して蒸発器3に戻しても良い。しかしかかる冷媒
はポンプ81による加圧で温度が上昇しており、これを
冷却管91によって冷却し冷媒散布管32を介して蒸発
器3に戻している。
The extracted refrigerant is transferred to the opposite side of the reverse osmosis membrane 83 through the refrigerant distribution pipe 3
2 may be returned to the evaporator 3. However, the temperature of the refrigerant has increased due to pressurization by the pump 81, and the refrigerant is cooled by the cooling pipe 91 and returned to the evaporator 3 via the refrigerant distribution pipe 32.

上記の蒸発と吸収と再生と冷却を繰り返し冷媒と吸収液
を循環させることによって、蒸発器3の伝熱管31から
冷水を連続的に取り出すことができる。また冷却器9の
冷却管91は吸収器4が有する冷却管42の出口に連通
しており、冷却管42に供給された冷却水は吸収器4に
おいて吸収液から吸収熱を奪い、更に冷却器9において
加圧された冷媒から潜熱を奪って温水になる。即ち、冷
却器の冷却管から温水を連続的に取り出すことができる
By repeating the above evaporation, absorption, regeneration, and cooling and circulating the refrigerant and absorption liquid, cold water can be continuously taken out from the heat transfer tube 31 of the evaporator 3. The cooling pipe 91 of the cooler 9 is connected to the outlet of the cooling pipe 42 of the absorber 4, and the cooling water supplied to the cooling pipe 42 absorbs absorbed heat from the absorption liquid in the absorber 4, and further At step 9, latent heat is removed from the pressurized refrigerant and it becomes hot water. That is, hot water can be continuously taken out from the cooling pipe of the cooler.

このように冷媒が吸収された吸収液を回収し圧力を加え
るポンプ、および吸収液から冷媒を分離する逆浸透膜ユ
ニットを有する再生器と、前記吸収器の冷却管の出口に
連通ずる冷却管を有し、冷媒を冷却する冷却器とを具え
てなる本発明の吸収式冷温水機は、冷媒が吸収されてな
る吸収液から冷媒を分離する際に加熱する必要がない。
A regenerator having a pump that collects and applies pressure to the absorption liquid in which the refrigerant has been absorbed, a reverse osmosis membrane unit that separates the refrigerant from the absorption liquid, and a cooling pipe that communicates with the outlet of the cooling pipe of the absorber. The absorption type water chiller/heater of the present invention, which includes a cooler for cooling a refrigerant, does not require heating when separating the refrigerant from the absorption liquid in which the refrigerant is absorbed.

〔発明の効果〕〔Effect of the invention〕

上述の如く本発明によれば冷媒の分離に際し加熱設備を
必要としない吸収式冷温水機を提供することができる。
As described above, according to the present invention, it is possible to provide an absorption type water chiller/heater that does not require heating equipment when separating the refrigerant.

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

第1図は本発明になる吸収式冷温水機を示す模式図、 第2図は従来の吸収式冷温水機を示す模式図、である。 図において 1は真空容器、 4は吸収器、 9は冷却器、 32は冷媒散布管、 42は冷却管、 82は逆浸透膜ユニット、 91は冷却管、 をそれぞれ表す。 3は蒸発器、 8は再生器、 31は伝熱管、 41は吸収液散布管、 81はポンプ、 83は逆浸透膜1 FIG. 1 is a schematic diagram showing an absorption type water chiller/heater according to the present invention, FIG. 2 is a schematic diagram showing a conventional absorption type water chiller/heater. In the figure 1 is a vacuum container, 4 is an absorber, 9 is a cooler; 32 is a refrigerant distribution pipe; 42 is a cooling pipe; 82 is a reverse osmosis membrane unit, 91 is a cooling pipe, respectively. 3 is the evaporator, 8 is a regenerator, 31 is a heat exchanger tube, 41 is an absorption liquid distribution pipe; 81 is a pump, 83 is reverse osmosis membrane 1

Claims (1)

【特許請求の範囲】[Claims] 伝熱管(31)および該伝熱管(31)に冷媒を散布す
る冷媒散布管(32)を有し、該冷媒の蒸発によって該
伝熱管(31)中の水を冷却する蒸発器(3)と、吸収
液を散布する吸収液散布管(41)および冷却水を流す
冷却管(42)を有し、該冷媒の蒸気を散布された該吸
収液に吸収させる吸収器(4)と、冷媒が吸収された吸
収液を回収し圧力を加えるポンプ(81)、および該吸
収液から冷媒を分離する逆浸透膜ユニット(82)を有
する再生器(8)と、前記吸収器(4)の冷却管(42
)の出口に連通する冷却管(91)を有し、冷媒を冷却
する冷却器(9)とを具えてなることを特徴とする吸収
式冷温水機。
an evaporator (3) having a heat exchanger tube (31) and a refrigerant distribution tube (32) for distributing a refrigerant to the heat exchanger tube (31), and cooling the water in the heat exchanger tube (31) by evaporating the refrigerant; , an absorber (4) having an absorption liquid dispersion pipe (41) for dispersing an absorption liquid and a cooling pipe (42) for flowing cooling water, and for absorbing the vapor of the refrigerant into the sprayed absorption liquid; A regenerator (8) having a pump (81) that collects and applies pressure to the absorbed absorption liquid, and a reverse osmosis membrane unit (82) that separates a refrigerant from the absorption liquid, and a cooling pipe of the absorber (4). (42
), and a cooler (9) for cooling a refrigerant.
JP11232690A 1990-04-28 1990-04-28 Absorption type water cooler/heater Pending JPH0413064A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11232690A JPH0413064A (en) 1990-04-28 1990-04-28 Absorption type water cooler/heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11232690A JPH0413064A (en) 1990-04-28 1990-04-28 Absorption type water cooler/heater

Publications (1)

Publication Number Publication Date
JPH0413064A true JPH0413064A (en) 1992-01-17

Family

ID=14583879

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11232690A Pending JPH0413064A (en) 1990-04-28 1990-04-28 Absorption type water cooler/heater

Country Status (1)

Country Link
JP (1) JPH0413064A (en)

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