JPS6242307Y2 - - Google Patents

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Publication number
JPS6242307Y2
JPS6242307Y2 JP8395183U JP8395183U JPS6242307Y2 JP S6242307 Y2 JPS6242307 Y2 JP S6242307Y2 JP 8395183 U JP8395183 U JP 8395183U JP 8395183 U JP8395183 U JP 8395183U JP S6242307 Y2 JPS6242307 Y2 JP S6242307Y2
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JP
Japan
Prior art keywords
water
cooling tower
heat exchanger
double
pipe
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
JP8395183U
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Japanese (ja)
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JPS59191094U (en
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
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Priority to JP8395183U priority Critical patent/JPS59191094U/en
Publication of JPS59191094U publication Critical patent/JPS59191094U/en
Application granted granted Critical
Publication of JPS6242307Y2 publication Critical patent/JPS6242307Y2/ja
Granted legal-status Critical Current

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Description

【考案の詳細な説明】 〔産業分野〕 この考案は、被冷却水が大気と遮断した状態で
その内部を流れる密閉型熱交換器を装備した冷却
塔に関する。
[Detailed Description of the Invention] [Industrial Field] This invention relates to a cooling tower equipped with a closed heat exchanger through which water to be cooled flows while being isolated from the atmosphere.

〔従来技術〕[Prior art]

本件出願以前におけるこの種の冷却塔において
密閉型熱交換器を散水装置下に配置し、この密閉
型熱交換器内を流れる被冷却水を前記熱交換器の
表面に散布され流下する散布水で冷却している冷
却塔が周知であるが、常に被冷却水より循環する
散布水の温度を低く維持せねばならず、散水装置
の下に充填板を配置してなる開放型冷却塔に比較
し、被冷却水の気化の潜熱による冷却効果が全く
期待し得ないため、開放型冷却塔と同等の熱交換
率を得るには装置が大型化する欠点があると共
に、密閉型熱交換器外面を通り外部へ排出される
空気の圧力損失は、充填材のそれに比べ一般に高
く送風機の負荷が大きく(約2倍)なり、騒音が
高くなる欠点がある。
In a cooling tower of this type prior to the filing of this application, a closed heat exchanger is placed under a water sprinkler, and the water to be cooled flowing inside the closed heat exchanger is sprayed on the surface of the heat exchanger and is sprayed with water flowing down. Cooling towers are well known, but the temperature of the circulating spray water must always be maintained lower than the water to be cooled, and compared to open cooling towers that have a filling plate placed below the water sprinkler. , since no cooling effect can be expected from the latent heat of vaporization of the water to be cooled, there is a disadvantage that the equipment will be larger to obtain the same heat exchange rate as an open type cooling tower, and the outer surface of the closed type heat exchanger must be The pressure loss of the air discharged to the outside is generally higher than that of the filler, which increases the load on the blower (approximately twice as much) and increases noise.

前記密閉型熱交換器の熱交換率を補充するため
に、密閉型熱交換器の下側で下部水槽に一部が水
没して充填板を配置した冷却塔が、実開昭52−
75955号公報に記載されているが送風機の回転に
伴う騒音はいまだ解決されず、散布水と被冷却水
間の熱交換率にもまだ改良の余地がある。
In order to supplement the heat exchange efficiency of the hermetic heat exchanger, a cooling tower was developed in 1972, in which a filling plate was placed partially submerged in the lower water tank below the hermetic heat exchanger.
Although it is described in Publication No. 75955, the noise caused by the rotation of the blower has not yet been solved, and there is still room for improvement in the heat exchange rate between the spray water and the water to be cooled.

本件出願人会社名義である特開昭51−60047号
においては、密閉型熱交換器を上下に分割し、高
熱側の下部熱交換器(プレートコイル)を下部水
槽に埋設し、下部水槽外の上部熱交換器(プレー
トコイル)の上側で、散布水装置下に充填材を配
置した冷却塔が記載され、密閉型熱交換器内を流
れる被冷却水と散布水との間接的な接触位置、接
触時間を多くしその熱交換率の向上を図つている
が、熱交換器が大型化し、冷却塔の大型化を招く
と共に、いまだ送風機から生じる騒音を充分に低
減化してない欠点がある。
In JP-A No. 51-60047, which is in the name of the applicant company, a closed heat exchanger is divided into upper and lower parts, the lower heat exchanger (plate coil) on the high-temperature side is buried in the lower water tank, and the lower heat exchanger (plate coil) on the high temperature side is buried in the lower water tank. Above the upper heat exchanger (plate coil), a cooling tower with a filling material placed below the spray water device is described, and the position of indirect contact between the water to be cooled flowing inside the closed heat exchanger and the spray water, Efforts have been made to increase the heat exchange efficiency by increasing the contact time, but this leads to an increase in the size of the heat exchanger, which leads to an increase in the size of the cooling tower, and there is a drawback that the noise generated from the blower has not yet been sufficiently reduced.

〔目 的〕〔the purpose〕

この考案は、前記先行技術の欠点を解消し、開
放型冷却塔の充填板に関する利点を密閉型冷却塔
に取入れ、熱交換器の構造、配置に工夫を施し、
効果的に散布水と被冷却水間との熱交換を行うと
共に、散布水を常に低温に維持し、低騒音運転を
行なえるようにした冷却塔を提供することを主目
的とする。
This invention eliminates the drawbacks of the prior art, incorporates the advantages of the packed plate of an open cooling tower into a closed cooling tower, and devises the structure and arrangement of the heat exchanger,
The main object is to provide a cooling tower which can effectively exchange heat between sprayed water and cooled water, keep sprayed water at a constant low temperature, and perform low-noise operation.

〔構 成〕〔composition〕

この考案は、冷却塔の散水装置と冷却塔外筐に
設けた外気取入口間でこの本体内に熱交換板が複
数枚並設充填してあり、下部水槽の水面近傍に
は、大気と遮断した状態で冷却される被冷却水と
この散水装置から散布される散布水の内外2重通
路を有する2重管式熱交換器が配置してあり、こ
の被冷却水と散布水の流通方向は相反しており、
この熱交換器における散布水用の管の吸込口に
は、前記下部水槽の散布水中に位置するストレー
ナが接続し、その吐出側は、前記散水装置に揚水
ポンプ、揚水管を介して接続し、散布水の循環系
路を形成していることを特徴とする冷却塔により
前記主目的の総てを達成する冷却塔である。
In this design, multiple heat exchange plates are installed in parallel inside the main body between the cooling tower water sprinkler and the outside air intake provided in the outer casing of the cooling tower, and the area near the water surface of the lower water tank is isolated from the atmosphere. A double pipe heat exchanger is installed, which has dual passages inside and outside for the cooled water to be cooled and the sprayed water from this sprinkler, and the direction of flow of the cooled water and the sprayed water is It is contradictory,
A strainer located in the spray water of the lower water tank is connected to the suction port of the spray water pipe in this heat exchanger, and its discharge side is connected to the sprinkler device via a water pump and a water pump, This cooling tower achieves all of the above main objectives by using a cooling tower that is characterized by forming a circulation system for sprayed water.

次に、この考案の代表的な実施態様を図に基ず
き説明する。
Next, a typical embodiment of this invention will be explained based on the drawings.

第1図乃至第3図において、10は向流式冷却
塔の外筐であり、この外筐10の上端排風口に
は、送風機11が設けてあり、前記外筐10中に
は上方よりエリミネータ12、散水装置13、充
填材14が配置され、外筐10下端部は下部水槽
15に形成され、この下部水槽15と充填材下端
間で外筐10の周壁には、外気取入口16が設け
てある。
1 to 3, reference numeral 10 denotes an outer casing of a countercurrent cooling tower. A blower 11 is provided at the upper end of the outer casing 10, and an eliminator is inserted into the outer casing 10 from above. 12. A watering device 13 and a filler 14 are arranged, a lower water tank 15 is formed at the lower end of the outer casing 10, and an outside air intake port 16 is provided on the peripheral wall of the outer casing 10 between the lower water tank 15 and the lower end of the filler. There is.

前記下部水槽15の散布水内には、冷凍機等を
流通循環する被冷却水と散水装置13から充填材
14上に散布される散布水の内外2重通路17、
18を有する2重管式熱交換器19が、その通路
17、18が水平となる状態で完全に沈設されて
いる。
In the sprayed water of the lower water tank 15, there is a double passage 17 for cooled water that circulates through a refrigerator and the like, and for sprayed water that is sprayed onto the filler 14 from the water sprinkler 13.
A double tube heat exchanger 19 with 18 is completely submerged with its passages 17, 18 horizontal.

前記散布水通路17を形成する内管20は、水
平面内で蛇行屈曲し、内管20の一端である吸込
口20aには、下部水槽15内に落下収集される
散布水中に位置するストレーナ21が接続してあ
り、この内管20の吐出側20bは、前記散水装
置13に揚水ポンプP、揚水管22を介し接続
し、散布水の循環系路を形成している。
The inner pipe 20 forming the spray water passage 17 is meanderingly bent in a horizontal plane, and a suction port 20a, which is one end of the inner pipe 20, has a strainer 21 located in the spray water that falls into the lower water tank 15 and is collected. The discharge side 20b of this inner pipe 20 is connected to the water sprinkling device 13 via a water pump P and a water pump 22, forming a circulation system for sprayed water.

前記蛇行屈曲する内管20の各直線部に、両端
が閉じられた中空管23が間隙をおいて嵌合し、
隣接する中空管23は、ジグザグの被冷却水通路
18が内管外周に形成される形態に中空短管24
で相互にその端部で連通している。
A hollow tube 23 with both ends closed is fitted into each straight portion of the meandering and bent inner tube 20 with a gap,
The adjacent hollow tubes 23 are formed into hollow short tubes 24 having a zigzag cooled water passage 18 formed on the outer periphery of the inner tube.
and communicate with each other at their ends.

前記通路18内を流れる被冷却水の流れ方向
は、通路17を流れる散布水の流れ方向と相向う
方向としてあり、被冷却水通路18の一端18a
は、冷凍機内などを循環し高熱化した被冷却水を
受入れる供給口としてあり、その他端18bは散
布水で間接的に冷却された被冷却水を冷凍機など
へ戻す吐出口としてある。
The flow direction of the cooled water flowing in the passage 18 is opposite to the flow direction of the sprayed water flowing in the passage 17, and one end 18a of the cooled water passage 18
18b serves as a supply port for receiving high-temperature water to be cooled that circulates within the refrigerator, and the other end 18b serves as a discharge port for returning the water indirectly cooled by the sprayed water to the refrigerator or the like.

前記実施態様においては、前記熱交換器19を
下部水槽15内に水平に配置したが、その通路1
7、18が垂直となる態様で熱交換器19を下部
水槽15内に配置して、水面上に熱交換器19が
あつてもこの考案としては同一であり、その2重
通路のうち外側通路を被冷却水通路とし、内側通
路を散布水通路としても良く、要は、一つの熱交
換器19に、被冷却水通路と散布水通路が管壁を
介し併存してあれば、熱交換器の輪郭形状は問わ
ない。ただし、下部水槽15中に熱交換器19を
沈設する場合は必ず外側が被冷却水通路となる。
In the embodiment, the heat exchanger 19 is arranged horizontally in the lower water tank 15, but the passage 1
Even if the heat exchanger 19 is arranged in the lower water tank 15 in such a manner that 7 and 18 are vertical, and the heat exchanger 19 is placed above the water surface, this device is the same; may be used as the cooled water passage, and the inner passage may be used as the sprayed water passage.In short, if the cooled water passage and the sprayed water passage coexist in one heat exchanger 19 via the pipe wall, the heat exchanger The shape of the outline does not matter. However, when the heat exchanger 19 is placed in the lower water tank 15, the outside always becomes the water passage to be cooled.

〔作 用〕[Effect]

前記構成のこの考案の冷却塔の作用を説明す
る。
The operation of the cooling tower of this invention having the above configuration will be explained.

先ず下部水槽15に水張をし、冷凍機の冷凍管
路などを、2重管式熱交換器19の被冷却水通路
18の供給口端18aと吐出口端18bに接続
し、供給口端18aから吐出端18bに向け被冷
却水を通路18内にジグザグ蛇行し流す。一方、
ポンプPの始動により、下部水槽15内の水をス
トレーナ21を通し内管内に導き、被冷却水の流
れ方向と逆向きでジグザグに蛇行しつつこの内管
20内を流通させる。この蛇行し流れる間に、散
布水と、被冷却水は管壁を介して間接的に接触し
両者間で熱の授受が行なわれ、散布水に熱を奪わ
れ冷却された被冷却水は冷凍機などへ戻され、循
環する。一方熱を吸収し、若干暖められた水は、
揚水管22を介してポンプPの作用により上方の
散水装置13へ汲み上げられた後、この散水装置
13から充填材14上に散布される。この充填材
14の壁面を伝つて流れる間に、送風機11の駆
動により外気取入口16から外筐10内に吸込ま
れた外気との接触と、暖められた散布水の蒸発に
よる気化の潜熱によつて、散布水は急速に温度低
下し、下部水槽15上へ自然落下し、循環する。
First, the lower water tank 15 is filled with water, and the freezing pipe of the refrigerator is connected to the supply port end 18a and the discharge port end 18b of the cooled water passage 18 of the double tube heat exchanger 19, and the supply port end The water to be cooled flows in a meandering zigzag manner into the passage 18 from 18a toward the discharge end 18b. on the other hand,
When the pump P is started, the water in the lower water tank 15 is guided into the inner pipe through the strainer 21, and is caused to flow through the inner pipe 20 while meandering in a zigzag manner in the opposite direction to the flow direction of the water to be cooled. During this meandering flow, the sprayed water and the water to be cooled come into indirect contact through the pipe wall, and heat is exchanged between them. It is returned to the machine and circulated. On the other hand, water that absorbs heat and becomes slightly warmer,
The water is pumped up through the water lift pipe 22 to the water sprinkler 13 located above by the action of the pump P, and then sprayed onto the filling material 14 from the water sprinkler 13 . While flowing along the wall surface of the filler 14, it comes into contact with the outside air sucked into the outer casing 10 from the outside air intake port 16 by the drive of the blower 11, and due to the latent heat of vaporization due to the evaporation of the warmed spray water. As a result, the temperature of the sprayed water decreases rapidly, naturally falls onto the lower water tank 15, and is circulated.

〔効 果〕〔effect〕

前記のように構成し作用する本件考案において
は、前記被冷却水槽15内から散水装置13へ汲
み上げられ充填材14に散布され再び下部水槽1
5へ落下収集され循環使用される散布水と被冷却
水は、前記2重管式熱交換器19の内外通路1
7,18を通過時に、その流れ方向が相対向する
状態で流れるため、間接的に管壁を介して熱の授
受を行い内外通路17,18の各部において、被
冷却水と散布水との温度差が大きくとれ、かつそ
の接触区域も従来の冷却塔に比べ大きな面積を占
めるため、効率よく高温の被冷却水の熱を散布水
に吸収でき、密閉型熱交換器を散布装置13の真
下近傍の通風路域には全く設けずに、前記充填材
14のみ散布装置13真下に配置するのみで、前
記通風域に密閉型熱交換器を配した密閉型冷却塔
と同等若しくはそれ以上の熱交換率を得ることが
でき、かつ送風機11の作動により外筐10内に
吸入された空気は充填材充填域のみを向流又は直
交流とし、外気へ排気されるだけであるから圧力
損失が低減でき送風機11の駆動により発生する
騒音をより低く抑えることができる。
In the present invention constructed and operated as described above, water is pumped up from the inside of the cooled water tank 15 to the water sprinkler 13, sprinkled on the filler 14, and then returned to the lower water tank 1.
Sprayed water and water to be cooled are collected and circulated through the inner and outer passages 1 of the double-tube heat exchanger 19.
7 and 18, the flow directions are opposite to each other, so heat is transferred indirectly through the pipe walls, and the temperature of the cooled water and the sprayed water decreases in each part of the inner and outer passages 17 and 18. Since the difference is large and the contact area occupies a larger area than that of conventional cooling towers, the heat of the high-temperature water to be cooled can be efficiently absorbed into the spray water, and the closed heat exchanger can be installed near the bottom of the spray device 13. By simply arranging only the filler 14 directly below the dispersion device 13 without providing it at all in the ventilation area, heat exchange is equivalent to or better than that of a closed cooling tower with a closed heat exchanger arranged in the ventilation area. In addition, the air sucked into the outer casing 10 by the operation of the blower 11 flows counter-currently or cross-currently only in the filler-filled area and is exhausted to the outside air, reducing pressure loss. Noise generated by driving the blower 11 can be suppressed to a lower level.

前記2重管式熱交換器19は前記構造をしてい
るため、最小能力の冷却塔の大きさに併せてその
外形寸法を予じめ製造しておけば、これをユニツ
トとして、他の能力の冷却塔の大きさに応じて、
複数個組合せ、例えば下部水槽15内に段積み、
又は並列に接続し敷設することにより、被冷却水
の冷却を行うことができ、前記熱交換器19の製
造、保守管理が容易となる。
Since the double-tube heat exchanger 19 has the above-described structure, if its external dimensions are manufactured in advance to match the size of the cooling tower with the minimum capacity, it can be used as a unit to accommodate other capacities. Depending on the size of the cooling tower,
Combining multiple pieces, for example, stacking them in the lower water tank 15,
Alternatively, by connecting and installing them in parallel, the water to be cooled can be cooled, and the manufacture and maintenance of the heat exchanger 19 can be facilitated.

実施態様の効果としては、下部水槽14の水面
上に水平に2重管式熱交換器19が配置した場合
には、充填材14から落下してくる散布水は、一
度この熱交換器19に滴下し、この熱交換器19
の外周面に沿い流れた後、下部水槽15内に流下
するため、滴下水が直接下部水槽の液面を強打せ
ず、滴下音も清粛となり、外側通路18が被冷却
水通路となつている時には、被冷却水を内、外か
らより効果的に冷却できる下部水槽15内に2重
式熱交換器19の少くとも一部が沈設してある場
合には、被冷却水通路の外壁は、下部水槽15内
のストレーナ14に向け流れる散布水により洗わ
れ、内管17を通り流れる散布水との共働により
内外から被冷却水は冷却されると共に、2重管式
熱交換器表面に付着する水あかなどを流れる散布
水により、洗い流すことができこれらの表面に余
り附着しない。
As an effect of the embodiment, when the double-pipe heat exchanger 19 is arranged horizontally above the water surface of the lower water tank 14, the sprayed water falling from the filler 14 is once transferred to the heat exchanger 19. This heat exchanger 19
After flowing along the outer circumferential surface of the cooling water tank, the water flows down into the lower water tank 15, so that the dripping water does not directly hit the liquid surface of the lower water tank, the dripping sound is quieter, and the outer passage 18 becomes a cooled water passage. When at least a part of the double heat exchanger 19 is submerged in the lower water tank 15 that can cool the water to be cooled more effectively from inside and outside, the outer wall of the water passage to be cooled is The water to be cooled is washed by the spray water flowing toward the strainer 14 in the lower water tank 15, and in cooperation with the spray water flowing through the inner pipe 17, the water to be cooled is cooled from inside and outside, and the water is cooled on the surface of the double-pipe heat exchanger. The adhering water scale can be washed away by the flowing spray water, so that it does not adhere much to these surfaces.

2重管式熱交換器19を水平に配置した時に
は、冷却塔の高さを高くせずに、被冷却水を効果
的に冷却でき、下部水槽15の水面に直角に起立
させて下部水槽15内に沈設した時には、下部水
槽の種々の配管を避けて、多数の2重管式熱交換
器19を並設し使用することが容易にできる。
When the double-tube heat exchanger 19 is arranged horizontally, the water to be cooled can be effectively cooled without increasing the height of the cooling tower. When the heat exchanger 19 is submerged in the tank, a large number of double-tube heat exchangers 19 can be easily installed and used in parallel, avoiding various piping in the lower water tank.

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

図は、この考案の代表的実施態様を示すもの
で、第1図は、その概略的全体図、第2図は2重
管式熱交換器の一例を示す平面図、および第3図
は第2図の3−3線に沿う拡大縦断面図である。 図中の主な記号の説明、13……散水装置、1
4……充填材、15……下部水槽、19……2重
管式熱交換器。
The figures show a typical embodiment of this invention; FIG. 1 is a schematic overall view thereof, FIG. 2 is a plan view showing an example of a double tube heat exchanger, and FIG. FIG. 3 is an enlarged longitudinal sectional view taken along line 3-3 in FIG. 2; Explanation of main symbols in the diagram, 13... Watering device, 1
4...Filling material, 15...Lower water tank, 19...Double pipe heat exchanger.

Claims (1)

【実用新案登録請求の範囲】 1 冷却塔の散水装置と冷却塔外筐に設けた外気
取入口間でこの本体内に熱交換板が複数枚並設
充填してあり、下部水槽の水面近傍には、大気
と遮断した状態で冷却される被冷却水とこの散
水装置から散布される散布水の内外2重通路を
有する2重管式熱交換器が配置してあり、この
被冷却水と散布水の流通方向は相反しており、
この熱交換器における散布水用の管の吸込口に
は、前記下部水槽の散布水中に位置するストレ
ーナが接続し、その吐出側は、前記散水装置に
揚水ポンプ、揚水管を介して接続し、散布水の
循環系路を形成していることを特徴とする冷却
塔。 2 前記2重管式熱交換器は、下部水槽の水面上
に水平に配置されている実用新案登録請求の範
囲第1項記載の冷却塔。 3 前記2重管式熱交換器は、下部水槽の散布水
内に少なくとも一部が沈設してある実用新案登
録請求の範囲第1項記載の冷却塔。 4 前記2重管式熱交換器の内外2重管のうち、
内管が前記散布水の通路に形成され、この内管
を囲撓し蛇行する外管が前記被冷却水の通路に
形成されている実用新案登録請求の範囲第1項
記載の冷却塔。 5 前記2重管式熱交換器は、下部水槽の水面に
対し直角に起立して、下部水槽の散布水内に沈
没されている実用新案登録請求の範囲第1項記
載の冷却塔。 6 前記2重管式熱交換器が、下部水槽内に階層
的に複数個配列され相互連結されている実用新
案登録請求の範囲第2項、第3項又は第4項記
載の冷却塔。
[Scope of Claim for Utility Model Registration] 1. A plurality of heat exchange plates are installed in parallel in the cooling tower body between the water sprinkler system of the cooling tower and the outside air intake provided in the outer casing of the cooling tower, and near the water surface of the lower water tank. The system is equipped with a double-pipe heat exchanger that has double passages inside and outside for the cooled water that is cooled while isolated from the atmosphere and the sprayed water from this water spraying device. The direction of water flow is opposite,
A strainer located in the spray water of the lower water tank is connected to the suction port of the spray water pipe in this heat exchanger, and its discharge side is connected to the sprinkler device via a pump and a pump pipe, A cooling tower characterized by forming a circulation system path for sprayed water. 2. The cooling tower according to claim 1, wherein the double-pipe heat exchanger is arranged horizontally above the water surface of the lower water tank. 3. The cooling tower according to claim 1, wherein the double-pipe heat exchanger is at least partially submerged in the sprayed water of the lower water tank. 4 Of the inner and outer double pipes of the double pipe heat exchanger,
2. The cooling tower according to claim 1, wherein an inner pipe is formed in the passage for the sprayed water, and an outer pipe that surrounds the inner pipe and meanderes is formed in the passage for the water to be cooled. 5. The cooling tower according to claim 1, wherein the double-tube heat exchanger stands perpendicular to the water surface of the lower water tank and is submerged in the sprayed water of the lower water tank. 6. The cooling tower according to claim 2, 3, or 4, wherein a plurality of the double-tube heat exchangers are hierarchically arranged in a lower water tank and interconnected.
JP8395183U 1983-06-03 1983-06-03 cooling tower Granted JPS59191094U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8395183U JPS59191094U (en) 1983-06-03 1983-06-03 cooling tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8395183U JPS59191094U (en) 1983-06-03 1983-06-03 cooling tower

Publications (2)

Publication Number Publication Date
JPS59191094U JPS59191094U (en) 1984-12-18
JPS6242307Y2 true JPS6242307Y2 (en) 1987-10-29

Family

ID=30213905

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8395183U Granted JPS59191094U (en) 1983-06-03 1983-06-03 cooling tower

Country Status (1)

Country Link
JP (1) JPS59191094U (en)

Also Published As

Publication number Publication date
JPS59191094U (en) 1984-12-18

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