JPH1038408A - Evaporation type cooling liquid generator - Google Patents

Evaporation type cooling liquid generator

Info

Publication number
JPH1038408A
JPH1038408A JP19083696A JP19083696A JPH1038408A JP H1038408 A JPH1038408 A JP H1038408A JP 19083696 A JP19083696 A JP 19083696A JP 19083696 A JP19083696 A JP 19083696A JP H1038408 A JPH1038408 A JP H1038408A
Authority
JP
Japan
Prior art keywords
liquid
internal space
cooling
cooling medium
evaporation
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
JP19083696A
Other languages
Japanese (ja)
Inventor
Masaaki Toyama
正昭 外山
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.)
Mitsubishi Electric Building Solutions Corp
Original Assignee
Mitsubishi Electric Building Techno Service Co 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 Mitsubishi Electric Building Techno Service Co Ltd filed Critical Mitsubishi Electric Building Techno Service Co Ltd
Priority to JP19083696A priority Critical patent/JPH1038408A/en
Publication of JPH1038408A publication Critical patent/JPH1038408A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an evaporation type cooling liquid generator that does not cause air pollution and is suitable for reducing its size. SOLUTION: An evaporation type cooling liquid generator 50 includes an evaporation vessel 51, a liquid sprayer, a vapor discharge device, a cooling medium circulating device and a liquid supply device. The evaporation vessel 51 has a closed space inside. Liquid 61 to be cooled is sprayed in the closed inner space of the evaporation vessel 51 through spray nozzles 52 of the liquid sprayer. The vapor discharge device reduces the vapor pressure in the closed inner space to evaporate the liquid 61 sprayed and discharge the vapor of the liquid 61 outside the evaporation vessel 51. The cooling medium circulation device circulates cooling medium through the closed inner space of the evaporation vessel 51. The liquid 61 to be cooled is supplied from outside the evaporation vessel 51 by the liquid supply device.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、蒸発式冷却液体発
生装置に関し、特に大気汚染がなく、かつ装置の小型化
に最適な蒸発式冷却液体発生装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an evaporative cooling liquid generator, and more particularly to an evaporative cooling liquid generator which is free from air pollution and is most suitable for miniaturization of the apparatus.

【0002】[0002]

【従来の技術】図2は従来技術に係る吸収式冷凍機の原
理図である。図2に示すように、吸収式冷凍機は蒸発器
10、吸収器20、高温再生器(高温分離器)30及び
凝縮器40を備える。蒸発器10は水1を蒸発させて冷
却水を生成しさらにこの冷却水を冷却する。吸収器20
は蒸発器10で蒸発させた水蒸気を臭化リチウムブロマ
イドに吸収させ混合液を生成する。高温再生器30は吸
収器20において生成した混合液から水蒸気と臭化リチ
ウムブロマイドとを分離する。凝縮器40は高温再生器
30において分離された水蒸気を凝縮し水1を生成す
る。
2. Description of the Related Art FIG. 2 is a principle diagram of an absorption refrigerator according to the prior art. As shown in FIG. 2, the absorption refrigerator includes an evaporator 10, an absorber 20, a high-temperature regenerator (high-temperature separator) 30, and a condenser 40. The evaporator 10 evaporates the water 1 to generate cooling water, and further cools the cooling water. Absorber 20
Absorbs water vapor evaporated by the evaporator 10 into lithium bromide to form a mixed solution. The high temperature regenerator 30 separates water vapor and lithium bromide from the liquid mixture generated in the absorber 20. The condenser 40 condenses the water vapor separated in the high-temperature regenerator 30 to produce water 1.

【0003】前記蒸発器10においては内部空間の上部
に散布ノズル11が配設され、この散布ノズル11は凝
縮器40から供給される水1を蒸発器10の内部空間に
散布する。散布された水1は蒸発器10の内部空間に配
設された冷却水管12を冷却する。冷却水管12は蒸発
器10の外部に配設され冷却水を循環する冷却水循環ポ
ンプ13、冷却水により冷却する負荷14にそれぞれ直
列的に接続される。蒸発器10には排気装置15例えば
真空ポンプが連接され、この排気装置15は蒸発器10
の内部空間を真空に保持し散布ノズル11から散布され
る水1を蒸発させる。
[0003] In the evaporator 10, a spray nozzle 11 is disposed above the internal space, and the spray nozzle 11 sprays the water 1 supplied from the condenser 40 into the internal space of the evaporator 10. The sprayed water 1 cools a cooling water pipe 12 provided in the internal space of the evaporator 10. The cooling water pipe 12 is disposed outside the evaporator 10 and is connected in series to a cooling water circulation pump 13 for circulating cooling water and a load 14 for cooling with cooling water. An evacuation device 15 such as a vacuum pump is connected to the evaporator 10.
Is maintained in a vacuum, and the water 1 sprayed from the spray nozzle 11 is evaporated.

【0004】吸収器20は蒸発器10に連接される。こ
の吸収器20においては内部空間の上部に散布ノズル2
1が配設され、この散布ノズル21は高温再生器30か
ら供給される臭化リチウムブロマイド2を吸収器20の
内部空間に散布する。吸収器20の内部空間の底部には
水蒸気と臭化リチウムブロマイドとの混合液3が貯溜さ
れる。吸収器20、高温再生器30はそれぞれ供給管2
2を介して相互に連結され、この供給管22の中間部に
配設された循環ポンプ23により吸収器20で生成され
た混合液3が高温再生器30に供給される。
[0004] The absorber 20 is connected to the evaporator 10. In this absorber 20, the spray nozzle 2 is located above the internal space.
The spray nozzle 21 sprays lithium bromide 2 supplied from the high-temperature regenerator 30 into the interior space of the absorber 20. A mixed solution 3 of water vapor and lithium bromide is stored at the bottom of the internal space of the absorber 20. The absorber 20 and the high-temperature regenerator 30 are respectively connected to the supply pipe 2
The mixed liquid 3 generated by the absorber 20 is supplied to the high-temperature regenerator 30 by the circulation pump 23 which is connected to each other through the supply pipe 22 and disposed at an intermediate portion of the supply pipe 22.

【0005】高温再生器30には過熱ボイラー31が連
接され、この過熱ボイラー31は混合液3の水蒸気と臭
化リチウムブロマイドとを過熱により分離する。混合液
3から分離された臭化リチウムブロマイドは高温再生器
30の底部に貯溜され吸収器20の散布ノズル21に循
環される。混合液3から分離された水蒸気は供給管32
を通して凝縮器40に供給される。
[0005] A superheated boiler 31 is connected to the high temperature regenerator 30, and the superheated boiler 31 separates the water vapor of the mixed solution 3 and lithium bromide by superheating. The lithium bromide separated from the mixture 3 is stored at the bottom of the high-temperature regenerator 30 and circulated to the spray nozzle 21 of the absorber 20. The water vapor separated from the mixture 3 is supplied to the supply pipe 32
To the condenser 40.

【0006】凝縮器40においては内部空間に冷却水管
41が配設され、この冷却水管41は高温再生器30か
ら供給される水蒸気を熱交換により凝縮し水1を生成す
る。生成された水1は凝縮器40の底部に貯溜され、蒸
発器10の散布ノズル11に循環される。前記冷却水管
41は凝縮器40の外部に配設され冷却水を循環させる
循環ポンプ42、熱交換により温度が上昇した冷却水を
冷却するクーリングタワー43にそれぞれ直列的に接続
される。
[0006] In the condenser 40, a cooling water pipe 41 is provided in the internal space. The cooling water pipe 41 condenses steam supplied from the high temperature regenerator 30 by heat exchange to produce water 1. The generated water 1 is stored at the bottom of the condenser 40 and circulated to the spray nozzle 11 of the evaporator 10. The cooling water pipe 41 is disposed outside the condenser 40 and connected in series to a circulation pump 42 for circulating the cooling water and a cooling tower 43 for cooling the cooling water whose temperature has increased due to heat exchange.

【0007】このように構成される吸収式冷凍機におい
ては以下の動作が行われる。まず、蒸発器10の内部空
間が排気装置15により真空に保持され、この状態にお
いて散布ノズル11から水1が蒸発器10の内部空間に
散布される(滴下される)。散布された水1は冷却水管
12に接触し蒸発する。蒸発器10の内部空間は真空に
保持されているので、水1は約5℃において蒸発し、さ
らに水1は冷却水管12の内部に流れる冷却水の潜熱を
奪って蒸発するために、冷却水は一層冷却され、負荷1
4を冷却する。
The following operation is performed in the absorption refrigerator configured as described above. First, the internal space of the evaporator 10 is maintained in a vacuum by the exhaust device 15, and in this state, the water 1 is sprayed (dropped) from the spray nozzle 11 into the internal space of the evaporator 10. The sprayed water 1 comes into contact with the cooling water pipe 12 and evaporates. Since the internal space of the evaporator 10 is kept in a vacuum, the water 1 evaporates at about 5 ° C., and the water 1 evaporates by taking away the latent heat of the cooling water flowing inside the cooling water pipe 12. Is cooled further and load 1
4 is cooled.

【0008】蒸発器10において生成された水蒸気は吸
収器20に供給される。吸収器20においては散布ノズ
ル21から内部空間に臭化リチウムブロマイドが散布さ
れ(滴下され)、水蒸気と臭化リチウムブロマイドとが
混合された混合液3が生成される。この混合液3は吸収
器20の底部に貯溜される。貯溜された混合液3は循環
ポンプ23により供給管22を通して高温再生器30に
供給される。
[0008] The water vapor generated in the evaporator 10 is supplied to an absorber 20. In the absorber 20, lithium bromide is sprayed (dropped) from the spray nozzle 21 into the internal space, and a mixed solution 3 in which steam and lithium bromide are mixed is generated. This liquid mixture 3 is stored at the bottom of the absorber 20. The stored mixed liquid 3 is supplied to the high-temperature regenerator 30 through the supply pipe 22 by the circulation pump 23.

【0009】高温再生器30に供給された混合液3は過
熱ボイラー31により過熱され水蒸気と臭化リチウムブ
ロマイドとに分離される。過熱ボイラー31において
は、水蒸気の沸点と臭化リチウムブロマイドの沸点とが
異なることを利用し、混合液3中から水分のみが蒸発で
きるとともに、臭化リチウムブロマイドのみが凝縮で
き、双方が完全に分離できる。高温再生器30において
混合液3から分離された水蒸気は凝縮器40に供給管3
2を通して供給される。
The mixed solution 3 supplied to the high-temperature regenerator 30 is superheated by the superheater boiler 31 and separated into steam and lithium bromide. In the superheated boiler 31, by utilizing the fact that the boiling point of water vapor and the boiling point of lithium bromide are different, only water can be evaporated from the mixed solution 3 and only lithium bromide can be condensed and both are completely separated. it can. The steam separated from the mixture 3 in the high-temperature regenerator 30 is supplied to the condenser 40 through the supply pipe 3.
2 is supplied.

【0010】凝縮器40に供給された水蒸気は冷却水管
41に接触し、この水蒸気は冷却され凝縮し水1となっ
て凝縮器40の底部に貯溜される。貯溜された水1は蒸
発器10の散布ノズル11に循環される。前記冷却水管
41の内部には冷却水が循環ポンプ42により循環され
ており、水蒸気の凝縮により温度が上昇した冷却水はク
ーリングタワー43により冷却される。
The water vapor supplied to the condenser 40 comes into contact with the cooling water pipe 41, and the water vapor is cooled and condensed to become water 1 and stored at the bottom of the condenser 40. The stored water 1 is circulated to the spray nozzle 11 of the evaporator 10. Cooling water is circulated inside the cooling water pipe 41 by a circulation pump 42, and the cooling water whose temperature has risen due to condensation of steam is cooled by a cooling tower 43.

【0011】[0011]

【発明が解決しようとする課題】前述の従来技術に係る
吸収式冷凍機においては、以下の点の配慮がなされてい
ない。すなわち、吸収式冷凍機は蒸発器10、吸収器2
0、高温再生器30、凝縮器40の複数の処理ユニット
を備え、しかもそれぞれの処理ユニットには循環ポンプ
13、23、42、負荷14、排気装置15、過熱ボイ
ラー31及びクーリングタワー43等の付属装置が配設
される。このため、吸収式冷凍機の装置自体が大型でか
つ複雑な構成を有し、小規模の施設に配備できないとい
う問題があった。さらに、吸収式冷凍機の高温再生器3
0には過熱ボイラー31が配設されており、この過熱ボ
イラー31は燃焼によって排気ガスを発生させ、大気汚
染を誘発するので、排気ガス規制に適合することが難し
いという問題があった。
The following points are not taken into consideration in the above-mentioned absorption refrigerator according to the prior art. That is, the absorption refrigerator has the evaporator 10 and the absorber 2
0, a plurality of processing units including a high-temperature regenerator 30 and a condenser 40, and each of the processing units includes an auxiliary device such as a circulating pump 13, 23, 42, a load 14, an exhaust device 15, a superheated boiler 31, and a cooling tower 43. Is arranged. For this reason, there has been a problem that the absorption chiller device itself has a large and complicated configuration and cannot be deployed in a small-scale facility. Furthermore, the high temperature regenerator 3 of the absorption refrigerator
0 is provided with a superheated boiler 31. This superheated boiler 31 generates exhaust gas by combustion and induces air pollution, so that there is a problem that it is difficult to comply with exhaust gas regulations.

【0012】本発明は上記課題を解決するためになされ
たものであり、本発明の目的は大気汚染がなく、かつ装
置の小型化に最適な蒸発式冷却液体発生装置を提供する
ことにある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide an evaporative cooling liquid generating apparatus which is free from air pollution and is most suitable for downsizing the apparatus.

【0013】[0013]

【課題を解決するための手段】上記課題を解決するため
に、請求項1に記載された発明は、蒸発式冷却液体発生
装置において、密閉内部空間を有する蒸発容器と、前記
蒸発容器の密閉内部空間に冷却される液体を散布する液
体散布手段と、前記蒸発容器の密閉内部空間の蒸気圧を
減少し前記散布された液体を蒸発させるとともに、蒸発
させた液体を蒸発容器の外部に排出する蒸気排出手段
と、前記蒸発容器の密閉内部空間に冷却媒体を循環させ
る冷却媒体循環手段と、前記蒸発容器の外部から液体を
補給する液体補給手段と、を備えたことを特徴とする。
請求項1に記載された発明においては、前記蒸発容器の
密閉内部空間に散布される液体の循環に代えて、前記蒸
発容器の外部から液体を補給し、散布され蒸発させた液
体は蒸発容器の外部に排気するので、液体の循環利用に
必要な吸収器、高温再生器、凝縮器及びこれらの処理ユ
ニットに必要な付属装置が無くなり、装置自体が小型化
できる。さらに、液体の蒸発、冷却等の状態変化により
液体を冷却し、蒸発した液体を外部に排気するので、液
体に無害な水等を使用すれば、大気汚染がなくなる。
Means for Solving the Problems To solve the above-mentioned problems, the invention described in claim 1 is directed to an evaporative cooling liquid generating apparatus, comprising: an evaporating container having a closed internal space; A liquid spraying means for spraying a liquid to be cooled in a space, and a vapor for reducing the vapor pressure in the closed internal space of the evaporation container to evaporate the sprayed liquid and discharging the evaporated liquid to the outside of the evaporation container It is characterized by comprising discharge means, cooling medium circulating means for circulating a cooling medium in the closed internal space of the evaporation container, and liquid replenishing means for replenishing liquid from outside the evaporation container.
In the invention described in claim 1, instead of circulating the liquid sprayed in the closed internal space of the evaporation container, liquid is supplied from the outside of the evaporation container, and the sprayed and evaporated liquid is discharged from the evaporation container. Since the gas is exhausted to the outside, an absorber, a high-temperature regenerator, and a condenser necessary for circulating and using the liquid, and an auxiliary device required for these processing units are eliminated, and the device itself can be reduced in size. Further, the liquid is cooled by a state change such as evaporation and cooling of the liquid, and the evaporated liquid is exhausted to the outside. Therefore, if water or the like harmless to the liquid is used, air pollution is eliminated.

【0014】請求項2に記載された発明は、前記請求項
1に記載される蒸発式冷却液体発生装置において、前記
液体散布手段は、前記蒸発容器の密閉内部空間に液体を
散布する液体散布ノズルと、前記蒸発容器の密閉内部空
間の底部に散布された液体を貯溜する貯溜部と、前記貯
溜部に貯溜された液体を前記液体散布ノズルに循環する
循環ポンプと、を備えたことを特徴とする。
According to a second aspect of the present invention, in the evaporative cooling liquid generator according to the first aspect, the liquid spraying means sprays the liquid in a closed internal space of the evaporation container. And a storage unit for storing the liquid sprayed on the bottom of the closed internal space of the evaporation container, and a circulation pump for circulating the liquid stored in the storage unit to the liquid spray nozzle. I do.

【0015】請求項3に記載された発明は、前記請求項
2に記載された蒸発式冷却液体発生装置において、前記
液体補給手段は、前記蒸発容器の貯溜部に貯溜された液
体を一定量に制御するボールタップを備えたことを特徴
とする。
According to a third aspect of the present invention, in the evaporative cooling liquid generator according to the second aspect, the liquid replenishing means reduces the amount of the liquid stored in the storage section of the evaporation container to a predetermined amount. A ball tap for control is provided.

【0016】[0016]

【発明の実施の形態】以下、本発明の実施の形態である
蒸発式冷却液体発生装置について図面を参照し説明す
る。図1は本発明の実施形態に係る蒸発式冷却液体発生
装置の原理図である。同図に示すように、蒸発式冷却液
体発生装置50は蒸発容器51、液体散布ユニット、冷
却媒体循環ユニット、蒸気排出ユニット及び液体補給ユ
ニットを備える。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An evaporative cooling liquid generator according to an embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a principle diagram of an evaporative cooling liquid generator according to an embodiment of the present invention. As shown in the figure, the evaporative cooling liquid generator 50 includes an evaporating container 51, a liquid spraying unit, a cooling medium circulation unit, a vapor discharging unit, and a liquid replenishing unit.

【0017】前記蒸発容器51は密閉内部空間において
液体61を蒸発させ冷却することにより冷却媒体を生成
する。本実施形態において液体61には蒸発し大気に放
出した際にも無害な水が使用される。
The evaporating container 51 generates a cooling medium by evaporating and cooling the liquid 61 in the closed internal space. In the present embodiment, harmless water is used as the liquid 61 even when it evaporates and is released to the atmosphere.

【0018】前記液体散布ユニットは液体散布ノズル5
2、貯溜部51A、液体供給管58及び液体供給ポンプ
59を備える。液体散布ノズル52は蒸発容器51の密
閉内部空間の上部に配設され、この液体散布ノズル52
は密閉内部空間に液体61を散布する(滴下する)。貯
溜部51Aは蒸発容器51の密閉内部空間の底部に配設
されこの蒸発容器51の内壁を利用して形成される。貯
溜部51Aには貯溜される液量が一定量に制御された液
体61が貯溜される。貯溜部51Aは液体供給管58及
び液体供給ポンプ59を介在して液体散布ノズル52に
連結され、この液体供給管58及び液体供給ポンプ59
は貯溜部51Aに貯溜された液体61を液体散布ノズル
52に供給(循環)する。
The liquid spraying unit comprises a liquid spraying nozzle 5
2, a storage section 51A, a liquid supply pipe 58 and a liquid supply pump 59 are provided. The liquid spray nozzle 52 is disposed above the closed internal space of the evaporation container 51, and the liquid spray nozzle 52
Sprays (drops) the liquid 61 on the closed internal space. The storage part 51 </ b> A is provided at the bottom of the closed internal space of the evaporation container 51, and is formed using the inner wall of the evaporation container 51. A liquid 61 in which the amount of liquid stored is controlled to a constant amount is stored in the storage part 51A. The reservoir 51A is connected to the liquid spray nozzle 52 via a liquid supply pipe 58 and a liquid supply pump 59, and the liquid supply pipe 58 and the liquid supply pump 59
Supplies (circulates) the liquid 61 stored in the storage section 51A to the liquid spray nozzle 52.

【0019】冷却媒体循環ユニットは冷却媒体循環管5
3、冷却媒体循環ポンプ54及び負荷55を備える。冷
却媒体循環管53は蒸発容器51の密閉内部空間の中央
部分に配設され、この冷却媒体循環管53は前記散布ノ
ズル52から散布される液体(蒸発状態の液体)61に
より冷却される。冷却媒体循環ポンプ54、負荷55は
それぞれ冷却媒体循環管53に直列的に接続されるとと
もに蒸発容器51の外部に配設され、冷却媒体循環ポン
プ54は冷却媒体循環管53に流れる冷却媒体を循環さ
せる。本実施形態において冷却媒体には水が使用され
る。
The cooling medium circulation unit includes a cooling medium circulation pipe 5.
3. The cooling medium circulation pump 54 and the load 55 are provided. The cooling medium circulation pipe 53 is disposed at the center of the closed internal space of the evaporation container 51, and the cooling medium circulation pipe 53 is cooled by the liquid (evaporated liquid) 61 sprayed from the spray nozzle 52. The cooling medium circulating pump 54 and the load 55 are respectively connected in series to the cooling medium circulating pipe 53 and disposed outside the evaporating vessel 51, and the cooling medium circulating pump 54 circulates the cooling medium flowing through the cooling medium circulating pipe 53. Let it. In this embodiment, water is used as the cooling medium.

【0020】蒸気排出ユニットは蒸気排気管56及び排
気装置57を備える。蒸気排気管56は排気装置57を
介して蒸発容器51の密閉内部空間と外部大気との間を
連接する。排気装置57は例えば真空ポンプで構成さ
れ、蒸発容器51の内部密閉空間を真空状態にし保持し
散布ノズル52から散布される液体61の蒸発を促進し
つつ、蒸発した蒸気を蒸発容器51の外部に排出する。
The steam discharge unit has a steam exhaust pipe 56 and an exhaust device 57. The steam exhaust pipe 56 connects the closed internal space of the evaporation container 51 and the outside atmosphere via an exhaust device 57. The evacuation device 57 is configured by, for example, a vacuum pump, and keeps the internal sealed space of the evaporating container 51 in a vacuum state to promote the evaporation of the liquid 61 sprayed from the spray nozzle 52 and to transfer the evaporated vapor to the outside of the evaporating container 51. Discharge.

【0021】液体補給ユニットは蒸発容器51の外部か
ら液体61を補給する液体補給管60A及び液体補給管
60Aから補給される液体量を一定量に制御するボール
タップ60Bを備える。このボールタップ60Bは貯溜
部51Aに貯溜される液体61の液面高さが予め設定さ
れた高さよりも低い場合に液体61を補給し、高い場合
には液体61の補給を停止する。
The liquid replenishing unit includes a liquid replenishing pipe 60A for replenishing the liquid 61 from the outside of the evaporation container 51 and a ball tap 60B for controlling the amount of liquid supplied from the liquid replenishing pipe 60A to a constant amount. The ball tap 60B replenishes the liquid 61 when the liquid level of the liquid 61 stored in the storage part 51A is lower than a preset height, and stops the replenishment when the liquid level is higher.

【0022】このように構成される蒸発式冷却液体発生
装置の液体冷却動作は次の通りである。まず、蒸発式冷
却液体発生装置の蒸発容器51の密閉内部空間が蒸気排
出ユニットの排気装置57により真空状態に保持され
る。次に、液体散布ユニットの液体供給ポンプ59を起
動し、貯溜部51Aに貯溜されている液体61を液体供
給管58を通して液体散布ノズル52から蒸発容器51
の密閉内部空間に散布する(滴下する)。散布された液
体61は密閉内部空間において冷却媒体循環管53に接
触し蒸発する。この時、密閉内部空間は排気装置57に
より真空状態に保持されているので、水が使用される場
合、液体61は約5℃で蒸発し、冷却媒体循環管53の
内部に流れる冷却媒体から蒸発潜熱を奪うので、冷却媒
体が冷却される。さらに、密閉内部空間において散布さ
れた液体61は、蒸発容器51自体の熱も奪うので、蒸
発容器51の密閉内部空間の温度も低下させる。この結
果、貯溜部51Aに貯溜されている液体61が冷却さ
れ、液体供給管58、液体供給ポンプ59のそれぞれを
通して液体散布ノズル52から散布される液体61の温
度が下がるので、液体散布ノズル52から散布される液
体61は蒸発し易くなり、冷却効果が高まる。一方、冷
却媒体循環管53に流れる冷却された冷却水は冷却媒体
循環ポンプ54により循環し負荷55に冷却媒体を供給
し、負荷55が冷却される。
The liquid cooling operation of the evaporative cooling liquid generator constructed as described above is as follows. First, the closed internal space of the evaporation container 51 of the evaporative cooling liquid generator is kept in a vacuum state by the exhaust device 57 of the vapor discharge unit. Next, the liquid supply pump 59 of the liquid spraying unit is started, and the liquid 61 stored in the storage section 51A is passed through the liquid supply pipe 58 from the liquid spray nozzle 52 to the evaporation vessel 51.
(Drops) in the closed internal space of The sprayed liquid 61 contacts the cooling medium circulation pipe 53 in the closed internal space and evaporates. At this time, since the sealed internal space is kept in a vacuum state by the exhaust device 57, when water is used, the liquid 61 evaporates at about 5 ° C. and evaporates from the cooling medium flowing inside the cooling medium circulation pipe 53. Since the latent heat is removed, the cooling medium is cooled. Further, the liquid 61 sprayed in the closed internal space also removes the heat of the evaporation container 51 itself, so that the temperature of the closed internal space of the evaporation container 51 is also reduced. As a result, the liquid 61 stored in the storage unit 51A is cooled, and the temperature of the liquid 61 sprayed from the liquid spray nozzle 52 through each of the liquid supply pipe 58 and the liquid supply pump 59 decreases. The liquid 61 to be sprayed evaporates easily, and the cooling effect is enhanced. On the other hand, the cooled cooling water flowing through the cooling medium circulation pipe 53 is circulated by the cooling medium circulation pump 54 to supply the cooling medium to the load 55, and the load 55 is cooled.

【0023】前記蒸発容器51の密閉内部空間において
発生した蒸気は排気装置57により蒸気排気管56を通
して大気中に放出される。前記液体61には水が使用さ
れるので、蒸気は単なる水蒸気であり、大気汚染を生じ
ることはない。蒸気の放出により、貯溜部51Aに貯溜
される液体61の液体量が減少するが、この液体61の
液面はボールタップ60Bにより常時検知されており、
液体61の液面高さが予め設定された液面高さよりも低
くなった場合には液体補給管60Aを通して蒸発容器5
1の外部から密閉内部空間の貯溜部51Aに液体61の
補給が行われる。
The steam generated in the closed internal space of the evaporation vessel 51 is discharged to the atmosphere through a steam exhaust pipe 56 by an exhaust device 57. Since water is used for the liquid 61, the vapor is merely water vapor and does not cause air pollution. Due to the release of the vapor, the liquid amount of the liquid 61 stored in the storage part 51A decreases, but the liquid level of the liquid 61 is constantly detected by the ball tap 60B.
When the liquid level of the liquid 61 becomes lower than the preset liquid level, the evaporating vessel 5 is supplied through the liquid supply pipe 60A.
The liquid 61 is supplied to the storage section 51A in the closed internal space from outside of the storage device 1.

【0024】[0024]

【発明の効果】本発明においては、大気汚染がなく、か
つ装置の小型化に最適な蒸発式冷却液体発生装置が提供
できる。
According to the present invention, it is possible to provide an evaporative cooling liquid generating apparatus which is free from air pollution and is most suitable for downsizing the apparatus.

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

【図1】 本発明の実施形態に係る蒸発式冷却液体発生
装置の原理図である。
FIG. 1 is a principle diagram of an evaporative cooling liquid generator according to an embodiment of the present invention.

【図2】 従来技術に係る吸収式冷凍機の原理図であ
る。
FIG. 2 is a principle diagram of an absorption refrigerator according to the related art.

【符号の説明】[Explanation of symbols]

50 蒸発式冷却液体発生装置、51 蒸発容器、51
A 貯溜部、52 液体散布ノズル、53 冷却媒体循
環管、54 冷却媒体循環ポンプ、55 負荷、56
蒸気排気管、57 排気装置、58 液体供給管、59
液体供給ポンプ、60A 液体補給管、60B ボー
ルタップ、61 液体。
50 Evaporative cooling liquid generator, 51 Evaporation container, 51
A storage unit, 52 liquid spray nozzle, 53 cooling medium circulation pipe, 54 cooling medium circulation pump, 55 load, 56
Steam exhaust pipe, 57 exhaust device, 58 liquid supply pipe, 59
Liquid supply pump, 60A liquid supply tube, 60B ball tap, 61 liquid.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 密閉内部空間を有する蒸発容器と、 前記蒸発容器の密閉内部空間に冷却される液体を散布す
る液体散布手段と、 前記蒸発容器の密閉内部空間の蒸気圧を減少し前記散布
された液体を蒸発させるとともに、蒸発させた液体を蒸
発容器の外部に排出する蒸気排出手段と、 前記蒸発容器の密閉内部空間に冷却媒体を循環させる冷
却媒体循環手段と、 前記蒸発容器の外部から液体を補給する液体補給手段
と、 を備えたことを特徴とする蒸発式冷却液体発生装置。
An evaporating container having a closed internal space; a liquid spraying means for spraying a liquid to be cooled into the closed internal space of the evaporating container; Vapor evacuation means for evaporating the evaporating liquid and discharging the evaporated liquid to the outside of the evaporating container, cooling medium circulating means for circulating a cooling medium in the closed internal space of the evaporating container, and liquid from outside the evaporating container. A liquid replenishing means for replenishing the evaporative cooling liquid generator.
【請求項2】 前記請求項1に記載される蒸発式冷却液
体発生装置において、 前記液体散布手段は、 前記蒸発容器の密閉内部空間に液体を散布する液体散布
ノズルと、 前記蒸発容器の密閉内部空間の底部に散布された液体を
貯溜する貯溜部と、 前記貯溜部に貯溜された液体を前記液体散布ノズルに循
環する循環ポンプと、 を備えたことを特徴とする蒸発式冷却液体発生装置。
2. The evaporative cooling liquid generating apparatus according to claim 1, wherein the liquid spraying means includes: a liquid spray nozzle for spraying a liquid into a closed internal space of the evaporation container; An evaporative cooling liquid generator, comprising: a storage unit that stores liquid sprayed at the bottom of a space; and a circulation pump that circulates the liquid stored in the storage unit to the liquid spray nozzle.
【請求項3】 前記請求項2に記載される蒸発式冷却液
体発生装置において、 前記液体補給手段は、 前記蒸発容器の貯溜部に貯溜された液体を一定量に制御
するボールタップを備えたことを特徴とする蒸発式冷却
液体発生装置。
3. The evaporative cooling liquid generating device according to claim 2, wherein the liquid replenishing means includes a ball tap for controlling a liquid stored in a storage part of the evaporation container to a constant amount. Characteristic evaporative cooling liquid generator.
JP19083696A 1996-07-19 1996-07-19 Evaporation type cooling liquid generator Pending JPH1038408A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19083696A JPH1038408A (en) 1996-07-19 1996-07-19 Evaporation type cooling liquid generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19083696A JPH1038408A (en) 1996-07-19 1996-07-19 Evaporation type cooling liquid generator

Publications (1)

Publication Number Publication Date
JPH1038408A true JPH1038408A (en) 1998-02-13

Family

ID=16264580

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19083696A Pending JPH1038408A (en) 1996-07-19 1996-07-19 Evaporation type cooling liquid generator

Country Status (1)

Country Link
JP (1) JPH1038408A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190019627A (en) * 2017-08-18 2019-02-27 대우조선해양 주식회사 Cooling System based on Cooling Water Tower for Nearshore Floating Plan

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190019627A (en) * 2017-08-18 2019-02-27 대우조선해양 주식회사 Cooling System based on Cooling Water Tower for Nearshore Floating Plan

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