JP2005351610A - Water cooling method, and evaporation cooling type closed or open tube heat exchanger to be used for water cooler and water cooler equipped therewith - Google Patents

Water cooling method, and evaporation cooling type closed or open tube heat exchanger to be used for water cooler and water cooler equipped therewith Download PDF

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JP2005351610A
JP2005351610A JP2005117231A JP2005117231A JP2005351610A JP 2005351610 A JP2005351610 A JP 2005351610A JP 2005117231 A JP2005117231 A JP 2005117231A JP 2005117231 A JP2005117231 A JP 2005117231A JP 2005351610 A JP2005351610 A JP 2005351610A
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water
heat exchanger
pipe
tube heat
meandering
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JP4473168B2 (en
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Tetsuo Sasaki
哲夫 佐々木
Hiroshi Sugawara
博 菅原
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Ebara Refrigeration Equipment and Systems Co Ltd
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Ebara Shinwa Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To improve heat exchanging efficiency and reduce cost while uniformly and reliably carrying spray water onto the surfaces of heat exchange tubes by vertically arranging the meandering face of a tube heat exchanger and vertically setting a water film sheet over heat exchanger tube portions arranged in approximate parallel for guiding the spray water. <P>SOLUTION: Approximately horizontal straight tube portions 13 of the meandering tubes 12 constituting the closed tube heat exchanger 11 to be used for a cross flow type water cooling tower 10 are formed in approximate parallel to each other. The plurality of meandering tubes 12 are arranged at spaces in the cross direction of an outside air intake 14 in the state that the meandering face is located in an approximately vertical plane. The water film sheet 15 is set over the upper and lower straight tube portions 13 of the tube heat exchanger 11. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は水冷却方法と、水冷却器に使用される蒸発冷却式密閉型管熱交換器及びこの密閉型開放型管熱交換器を備える水冷却器に関する。   The present invention relates to a water cooling method, an evaporative cooling type sealed tube heat exchanger used in the water cooler, and a water cooler including the sealed open tube heat exchanger.

従来この種の密閉型熱交換器における蛇行管はU字形状の屈曲部で順次連なった直線部は相互に平行形成されている。
従って蛇行管を含む面を殊に水平方向に設置する場合、蛇行管の出入口の高さに若干の差を設けて、この管内の排水を容易に行なえるようにして設置している(例えば、特許文献1参照)。
更に、上下の蛇行管の直管部間には、合成樹脂製の波板が、複数枚直管部と直交して、かつ垂直で並列して、充填されている。
Conventionally, in this type of hermetic heat exchanger, the meandering pipes are formed in parallel with each other with straight portions that are successively connected with a U-shaped bent portion.
Therefore, when the surface including the meandering pipe is installed in the horizontal direction, the height of the entrance and exit of the meandering pipe is slightly different so that the drainage in the pipe can be easily performed (for example, Patent Document 1).
Further, between the straight pipe portions of the upper and lower meandering pipes, corrugated plates made of synthetic resin are filled perpendicularly in parallel with the plurality of straight pipe portions.

しかしながら、個々の直管部に装填された合成樹脂製の充填板(波板)に向けて散布される散布水は、上下の前記充填板の位置が不一致であると、下段の充填板の壁面に接触することなく、下方に通過したり、また前記充填板の片面のみしか接触せず、全体としての濡壁面積の実効面積が少なくなり、充分に外気との接触することなく、落下することになり、熱交換機能が充分に発揮されない。
また散布水は前記の通り、充填板の表面を伝って流下する流下水であっても前記の各直管部の表面部にすべて供給されるわけではなく、充填板部分のみを伝って流下してしまう散布水も多く、折角気化の潜熱によって温度低下した散布水が有効に前記直管部に作用しない傾向にあった。
また、冬季に、凍結防止対策で水抜をする場合、蛇行面を殊に水平方向に設置したものでは、蛇行管の出入口の高さに若干の差を設けて、この管内の排水を容易に行なえるようにしても、直管部の水抜き勾配は十分ではなく、設置レベルの影響、組み込み精度、変形、汚れなどの影響によって排水が完全にできず、凍結パンク事故が発生する可能性を否定できない。
実公平6−4217号公報
However, the sprayed water sprayed toward the synthetic resin filling plates (corrugated plates) loaded in the individual straight pipe portions has a mismatch between the positions of the upper and lower filling plates and the wall surface of the lower filling plate. Passing downward without touching, or contacting only one side of the filling plate, the effective area of the wet wall area as a whole decreases, and it falls without contact with the outside air sufficiently. Therefore, the heat exchange function is not fully exhibited.
In addition, as described above, even if the sprayed water flows down along the surface of the filling plate, it is not always supplied to the surface portion of each straight pipe portion, and flows down only through the filling plate portion. There was a lot of sprayed water, and the sprayed water whose temperature was lowered by the latent heat of corner vaporization tended to not act on the straight pipe part effectively.
In addition, when draining water to prevent freezing in winter, if the meandering surface is installed horizontally, there is a slight difference in the height of the entrance and exit of the meandering pipe, so that the drainage in this pipe can be performed easily. However, the drainage gradient of the straight pipe part is not sufficient, and the possibility of a freezing puncture accident is denied because drainage cannot be completed completely due to the influence of installation level, installation accuracy, deformation, dirt, etc. Can not.
No. 6-4217

この発明の主目的は、熱交換器を通過する空気の通過抵抗を小さくし、送風動力を低減し、また騒音を低減させることである。
この発明の他の目的は、管熱交換器蛇行面の配置を縦にし、略平行に配置された熱交換器管部に、散布水を案内する充填膜を鉛直方向に張り巡らせることにより、散布水を熱交換器管表面に均一に、しかも確実に流すことができ、熱交換効率の向上と、低コスト化を図ることである。
この発明の更なる目的は、充填膜の一部を水非透過性のシートとすることで、散布水と接触しない空気熱交換部が容易にでき、白煙の発生防止機能を簡易に付ける事ができるようにすることである。
この発明の更なる目的は、熱交換器管内の排水が、確実にできるようにすることである。
The main object of the present invention is to reduce the passage resistance of the air passing through the heat exchanger, to reduce the blowing power, and to reduce the noise.
Another object of the present invention is to disperse the pipe heat exchanger by vertically arranging a meandering surface of the pipe heat exchanger, and by vertically spreading a packed film for guiding the sprayed water on the heat exchanger pipe parts arranged in parallel. It is possible to flow water uniformly and reliably on the surface of the heat exchanger tube, to improve heat exchange efficiency and to reduce costs.
A further object of the present invention is to make a part of the filling membrane a water-impermeable sheet so that an air heat exchanging portion that does not come into contact with the spray water can be easily formed, and a function for preventing the generation of white smoke can be easily added. Is to be able to.
It is a further object of the present invention to ensure that drainage in the heat exchanger tubes is possible.

前記課題を必要充分に解決する発明は、密閉型管熱交換器を構成する蛇行管の略水平なそれぞれの直管部は相互に略平行に形成されて、この蛇行管は蛇行面を略垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいて配列され、各熱交換器における上下の直管部にわたり、散布水案内シートが連ねて張り巡らされている密閉型管熱交換器上に散布水を散布し、前記散布水案内シートに沿い散布水を流し、この流下中に外気流との直接接触により散布水を冷却し、蒸発に伴う潜熱作用で更に冷却し、この冷却された散布水を前記直管部のほゞ全域に前記散布水案内シートにより案内し流下させ、この密閉型管熱交換器内を循環し流下する循環冷却水を間接的に冷却させることを特徴とする水冷却方法としてある。   In the invention that solves the above-mentioned problems sufficiently and sufficiently, the substantially horizontal straight pipe portions of the meandering pipe constituting the sealed pipe heat exchanger are formed substantially parallel to each other, and the meandering pipe has a meandering surface substantially vertical. Sealed in a state where a plurality of pipes are arranged in the plane, spaced apart in the width direction of the outside air intake, and the sprayed water guide sheets are stretched over the straight pipe sections at the top and bottom of each heat exchanger. Sprinkling water is sprayed on the mold tube heat exchanger, and the sprayed water flows along the spray water guide sheet. During this flow, the sprayed water is cooled by direct contact with the external airflow, and further cooled by the latent heat action accompanying evaporation. Then, the cooled sprayed water is guided by the sprayed water guide sheet over the entire area of the straight pipe portion, and the circulating cooling water circulating and flowing through the sealed pipe heat exchanger is indirectly cooled. It is a water cooling method characterized by making it occur.

前記課題を必要充分に解決する関連発明は、上下平行に配置された支持部材にわたり、散水案内シートが連なり張り巡らされてなる開放式熱交換器上に散布水を散布し、散布水をこの散水案内シートに沿い流し、この流下中に外気流と直接接触させ、散布水を冷却することを特徴とする水冷却方法としてある。   A related invention that solves the above-mentioned problem sufficiently spreads sprayed water on an open heat exchanger in which sprinkling guide sheets are continuously stretched over support members arranged in parallel in the vertical direction. The water cooling method is characterized in that the water flows along a guide sheet, directly contacts an external air flow during the flow, and cools the spray water.

前記課題を必要充分に解決する関連発明は、水冷却器に使用される密閉型管熱交換器において、
前記管熱交換器を構成する蛇行管の略水平なそれぞれの直管部は相互に略平行に形成されて、この蛇行管は蛇行面を略垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいてこの熱交換器は配列されていると共に、各熱交換器における上下の直管部にわたり、散布水案内シートが連ねて張り巡らされていることを特徴とする密閉型管熱交換器としてある。
A related invention that solves the above-mentioned problem sufficiently and sufficiently is a sealed pipe heat exchanger used in a water cooler,
The straight horizontal pipe portions of the meandering pipe constituting the pipe heat exchanger are formed substantially in parallel with each other, and the meandering pipe has a plurality of outside air, with the meandering surface positioned in a substantially vertical plane. The heat exchangers are arranged at intervals in the width direction of the intake port, and the sprayed water guide sheets are stretched over the upper and lower straight pipe portions of each heat exchanger. It is a sealed tube heat exchanger.

前記課題を必要充分に解決する関連発明は、水冷却器に使用される密閉型管熱交換器において、
前記管熱交換器における蛇行管はU字形状の屈曲部で順次連った直管部は相互にほゞ平行形成されて、この蛇行面を垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいてこの熱交換器は配列されているとともに、前記熱交換器の少なくとも一側には冷却水の流下路を形成する水膜シートがこの熱交換器の蛇行面に上下方向に連ねて付着乃至添着して配列されていることを特徴とする前記管熱交換器としてある。
A related invention that solves the above-mentioned problem sufficiently and sufficiently is a sealed pipe heat exchanger used in a water cooler,
In the pipe heat exchanger, the meandering pipes, which are successively connected by U-shaped bent parts, are formed substantially parallel to each other, and a plurality of the outside air is provided with the meandering surfaces positioned in the vertical plane. The heat exchangers are arranged at intervals in the width direction of the intake port, and a water film sheet forming a cooling water flow path is provided on at least one side of the heat exchanger. The tube heat exchanger is characterized in that it is arranged attached to or attached in a row in the vertical direction.

前記課題を必要充分に解決する関連発明は、水冷却器に使用される開放型熱交換器において、上下平行に支持部材が配置され、これら支持部材にわたり、散布水案内シートがそれぞれ垂直方向に連ねて張り巡らされていることを特徴とする開放型熱交換器としてある。   A related invention that solves the above-mentioned problems sufficiently is an open type heat exchanger used for a water cooler, in which support members are arranged vertically in parallel, and the sprayed water guide sheets are respectively connected in the vertical direction across the support members. It is an open type heat exchanger characterized by being stretched around.

前記課題を必要充分に解決する発明である関連発明は、請求項3、4、5、6、7又は8記載の発明における前記密閉型管熱交換器をその機枠内に装填されていることを特徴とする水冷却器としてある。
前記課題を必要充分に解決する発明である関連発明は、請求項10記載の発明における前記開放型管熱交換器をその機枠内に装填されていることを特徴とする水冷却器としてある。
In a related invention that is an invention that solves the above-mentioned problem sufficiently and sufficiently, the hermetic tube heat exchanger according to the invention of claim 3, 4, 5, 6, 7 or 8 is loaded in the machine frame. As a water cooler characterized by
A related invention, which is an invention that solves the above-mentioned problem sufficiently and sufficiently, is a water cooler characterized in that the open-type pipe heat exchanger according to the invention of claim 10 is loaded in the machine frame.

請求項1記載の発明である冷却方法においては、密閉型管熱交換器を構成する蛇行管の略水平なそれぞれの直管部は相互に略平行に形成されてこの蛇行管は蛇行面を略垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいて配列され、各熱交換器における上下の直管部にわたり、散布水案内シートが連ねて張り巡らされている密閉型管熱交換器上に散布水を散布し、前記散布水案内シートに沿い散布水を流し、この流下中に外気流との直接接触により散布水を冷却し、蒸発に伴う潜熱作用で更に冷却し、この冷却された散布水を前記直管部のほゞ全域に前記散布水案内シートにより案内し流下させ、この密閉型管熱交換器内を循環し流下する循環冷却水を間接的に冷却させる事により、前記の課題、殊に散布水を熱交換器管表面に均一に、しかも確実に流すことができ、各流下水を殆どすべて、直管部外周面と接触して順次流下し、熱交換効率を向上させ、コストを低減できる。
請求項2記載の発明においては、上下平行に配置された支持部材にわたり、散水案内シートがそれぞれ垂直面方向に連なり張り巡らされてなる開放式熱交換器上に散布水を散布し、散布水をこの散水案内シートに沿い流し、この流下中に外気流と直接接触させ、散布水を冷却することにより、開放式熱交換器を通過する空気の抵抗を小さくし、送風動力を低減できる。
In the cooling method according to the first aspect of the present invention, the substantially horizontal straight pipe portions of the meandering pipe constituting the sealed pipe heat exchanger are formed substantially parallel to each other, and the meandering pipe has a meandering surface substantially omitted. In a state where they are positioned in the vertical plane, a plurality of them are arranged at intervals in the width direction of the outside air intake port, and the sprayed water guide sheets are stretched over the upper and lower straight pipe portions in each heat exchanger. Sprinkling water is sprayed on the sealed tube heat exchanger, and the sprayed water flows along the sprayed water guide sheet. During this flow, the sprayed water is cooled by direct contact with the external airflow. The cooled sprayed water is cooled and guided by the sprayed water guide sheet over the entire area of the straight pipe section, and the circulating cooling water circulating and flowing down in the sealed pipe heat exchanger is indirectly collected. By cooling, the above problems, especially the spray water, It can flow uniformly and surely on the pipe surface, and almost all of the sewage flows in contact with the outer peripheral surface of the straight pipe part and flows down sequentially, improving the heat exchange efficiency and reducing the cost.
In invention of Claim 2, spread water is spread | dispersed on the open-type heat exchanger with which a sprinkling guide sheet | seat is continuously stretched around the support member arrange | positioned in the up-down parallel, respectively, and is spread, By flowing along this watering guide sheet, directly contacting the external airflow during this flow, and cooling the spray water, the resistance of the air passing through the open heat exchanger can be reduced, and the blowing power can be reduced.

請求項3乃至9記載の発明である前記密閉型管熱交換器においては、管熱交換器蛇行面の配置を縦にし、略平行に配置された熱交換器管部に、散布水を案内する散布水案内シート乃至水膜シート充填膜を鉛直方向に張り巡らせることにより、散布水を熱交換器管表面に均一に、しかも確実に流すことができ、かつ、各流下水は殆どすべて、直管部外周面と接触して順次流下し、熱交換効率を向上させ、コストを低減できる。   In the sealed pipe heat exchanger according to any one of claims 3 to 9, the arrangement of the pipe heat exchanger meandering surface is vertical, and the spray water is guided to the heat exchanger pipes arranged substantially in parallel. By spreading the sprayed water guide sheet or the water film sheet filling membrane in the vertical direction, the sprayed water can be made to flow evenly and reliably over the surface of the heat exchanger tube, and almost all the sewage is straight. It is possible to improve the heat exchange efficiency and reduce the cost by sequentially flowing down in contact with the outer peripheral surface of the part.

更に、熱交換器を通過する空気の通過抵抗を小さくし、送風動力を低減し、また騒音を低減させることができる。これに加えて、管熱交換器蛇行面の配置を縦にし、略平行に熱交換器管部同士を配置することで、熱交換器管内の排水が確実にでき、冬期における熱交換器管内に残留する循環冷却水の凍結による熱交換器管の破損を未然に防止出来る。
更に、請求項5記載の発明においては、前記効果に加えて、各前記管熱交換器における上下の直管部間に亘り順次ジクザクに掛合させ屈曲してそれぞれ前記一枚の水膜シートが配列され、水膜シートの幅はほゞ各前記管熱交換器における直管部の長さ寸法としてあり、水膜シートの上端は最上位の直管部位置において、散布水受け部としてくの字に屈曲しており、この水膜シートの下端は最下位の直管部より下方に突出し、下部水槽への散布水案内部としてあるため、散布水を水膜シートの前記上端で安定して受ける事が出来、前記水膜シート全域に一様に散布水を流下できる。更に、前記水膜シート全面を流下してきた散布水を前記水膜シートの下端の散布水案内部により、散布水を前記下水槽に流入し収集することが出来る。
殊に、請求項7記載の発明においては、充填膜の一部を水非透過性のシートとすることで、散布水と接触しない空気熱交換部が容易にでき、白煙の発生防止機能を簡易に付ける事ができる。
請求項10記載の発明においては、請求項2記載の水冷却方法を実施できる。
Furthermore, the passage resistance of the air passing through the heat exchanger can be reduced, the blowing power can be reduced, and the noise can be reduced. In addition to this, by arranging the pipe heat exchanger meander surface vertically and arranging the heat exchanger pipe parts in parallel, drainage in the heat exchanger pipe can be ensured, and in the heat exchanger pipe in winter Damage to the heat exchanger tube due to freezing of the remaining circulating cooling water can be prevented.
Furthermore, in the invention according to claim 5, in addition to the above-mentioned effect, the water film sheets are arranged in a zigzag manner and sequentially bent between the upper and lower straight pipe portions in each of the pipe heat exchangers. The width of the water film sheet is generally the length dimension of the straight pipe part in each of the tube heat exchangers, and the upper end of the water film sheet is a square shape as the spray water receiving part at the uppermost straight pipe part position. The lower end of the water film sheet protrudes downward from the lowest straight pipe part and serves as a spray water guide to the lower water tank, so that the spray water is stably received at the upper end of the water film sheet. The sprayed water can flow uniformly over the entire water film sheet. Furthermore, the spray water flowing down the entire surface of the water film sheet can be collected by flowing the spray water into the sewage tank by the spray water guide at the lower end of the water film sheet.
In particular, in the invention described in claim 7, by forming a part of the filling film as a water-impermeable sheet, an air heat exchanging portion that does not come into contact with the spray water can be easily made, and the function of preventing the generation of white smoke can be achieved. Can be attached easily.
In the invention described in claim 10, the water cooling method described in claim 2 can be implemented.

請求項11乃至13記載の発明である水冷却器においては、前記密閉型管熱交換器の効果を発揮しながら、循環冷却水を冷却できる。
殊に請求項12記載の発明である水冷却器においては、前記水膜シート全面を流下してきた散布水を前記水膜シートの下端の散布水案内部により、散布水を前記下水槽に流入し収集することが出来る。
請求項14記載の発明においては、請求項2記載の水冷却方法を実施できる。
In the water cooler which is invention of Claim 11 thru | or 13, circulating cooling water can be cooled, exhibiting the effect of the said closed tube heat exchanger.
In particular, in the water cooler according to the twelfth aspect of the present invention, the spray water flowing down the entire surface of the water film sheet is caused to flow into the sewage tank by the spray water guide portion at the lower end of the water film sheet. Can be collected.
In the invention described in claim 14, the water cooling method described in claim 2 can be carried out.

実施の形態1
この形態は請求項4、5、6記載の発明および請求項11、12記載の発明の代表的な実施の形態を示す。
Embodiment 1
This embodiment shows typical embodiments of the inventions of claims 4, 5, 6 and claims 11, 12.

図1において、10はクロスフロー型の水冷却塔を示し、内部の熱交換器の構造配列を除いて公知のものと同様であり、ここでの説明は省略する。   In FIG. 1, reference numeral 10 denotes a cross-flow type water cooling tower, which is the same as a known one except for the structural arrangement of the internal heat exchanger, and the description thereof is omitted here.

前記クロスフロー型の水冷却塔10に使用される密閉型管熱交換器11を構成する蛇行管12の略水平なそれぞれの直管部13は相互に略平行に形成されて、この蛇行管12は蛇行面を略垂直面内に位置させた状態で複数本、外気取り入れ口14の幅方向に間隔をおいて配列されている。
各前記熱交換器11における上下の直管部13にわたり、冷却水の流下路を形成する水膜シート15がこの熱交換器11の蛇行面に付着乃至添着して配列されている(図3参照)。より具体的には水膜シート15が各前記熱交換器11における上下の直管部13にわたり、張り巡らされている。
各前記管熱交換器11における上下の直管部13間に亘りジクザクに屈曲して前記一枚の水膜シート15が配列され、この水膜シート15の幅はほゞ各前記管熱交換器11における直管部13の長さ寸法としてあり、この水膜シート15の上端は最上位の直管部13より上方に突出し、散水装置近傍の機枠、または散水ノズル近傍に取り付けられ、散布水受け部としてくの字に屈曲しており、この水膜シート15の下端は最下位の直管部より下方に突出し、下部水槽への散布水案内部として下部水槽側へ内側にくの字に屈曲している。
前記水膜シート15は、編布、不織布、網地など水透過性のシートとしてある。
この水膜シート15は、袋状物からなり場合も有り、この袋状物に対応する前記密閉型管熱交換器11を被覆するように被せられ、止め具で止められる場合もある。
これら水透過性のシートにおいては、これらと一度接触した散布水は、毛細管現象により、充分にこれらシートを濡し、その表面積の広さから、外気流との接触面積は大きく、充分な気化の潜熱により、流下水は冷却され、かつ、一度接触した水はこれらシートから離反せず、確実に前記各直管部13外周面に順次達して、これらを冷却し、前記各直管部13内を流れる循環冷却水を間接的に冷却する(請求項1記載の発明の代表的な実施の形態に対応)。
The substantially horizontal straight pipe portions 13 of the meandering pipe 12 constituting the sealed pipe heat exchanger 11 used in the crossflow type water cooling tower 10 are formed substantially parallel to each other, and the meandering pipe 12 Are arranged in the width direction of the outside air inlet 14 at intervals with the meandering surface positioned in a substantially vertical plane.
Over the upper and lower straight pipe sections 13 in each of the heat exchangers 11, a water film sheet 15 forming a cooling water flow path is attached to or attached to the meandering surface of the heat exchanger 11 (see FIG. 3). ). More specifically, the water film sheet 15 is stretched over the upper and lower straight pipe portions 13 in each of the heat exchangers 11.
The one water film sheet 15 is arranged in a zigzag manner between the upper and lower straight pipe portions 13 in each of the tube heat exchangers 11, and the width of the water film sheet 15 is approximately the width of each of the tube heat exchangers. 11, the upper end of the water film sheet 15 protrudes upward from the uppermost straight pipe portion 13 and is attached to the machine frame near the watering device or the watering nozzle. The water film sheet 15 is bent downwardly as a receiving part, and the lower end of the water film sheet 15 protrudes downward from the lowermost straight pipe part. It is bent.
The water film sheet 15 is a water-permeable sheet such as a knitted fabric, a non-woven fabric, or a net.
The water film sheet 15 may be formed of a bag-like material, and may be covered with the sealed tube heat exchanger 11 corresponding to the bag-like material and stopped with a stopper.
In these water-permeable sheets, the spray water once contacted with them sufficiently wets these sheets by capillary action, and due to the wide surface area, the contact area with the external airflow is large, and sufficient vaporization is achieved. The flowing water is cooled by the latent heat, and the water that has once contacted does not separate from the sheets, but reliably reaches the outer peripheral surface of each straight pipe portion 13 in order, cools them, and in each straight pipe portion 13 The circulating cooling water flowing through is indirectly cooled (corresponding to a representative embodiment of the invention described in claim 1).

実施の形態2
この形態は請求項3記載の発明および請求項11、12記載の発明の代表的な実施の形態を示す。実施の形態1と異なる構成は、各前記熱交換器11における上下の直管部13にわたり、散布水案内シートが張り巡らされていることである。この散布水案内シートは前記水膜シート15のように水透過性に限定されるものではなく、塩ビ製の合成樹脂板に多数の孔を穿孔した多孔板でも良い。
Embodiment 2
This embodiment shows a typical embodiment of the invention described in claim 3 and the invention described in claims 11 and 12. A different configuration from the first embodiment is that a sprayed water guide sheet is stretched over the upper and lower straight pipe sections 13 in each of the heat exchangers 11. The sprayed water guide sheet is not limited to water permeability like the water film sheet 15, and may be a perforated plate in which a large number of holes are formed in a synthetic resin plate made of vinyl chloride.

実施の形態3
この形態は請求項7記載の発明および請求項11、12記載の発明の代表的な実施の形態を示す。実施の形態1と異なる構成は、前記密閉型管熱交換器11は、この熱交換器11の両側に、前記水膜シート15に替えて合成樹脂製で水非透過性の充填膜(図示せず)をこの熱交換器11と並列して略垂直に配列され、散布水と非接触の外気通過流路として、この部分に散布水が散布されない構成とし、白煙防止機能を有する密閉型管熱交換器としてあることである。
Embodiment 3
This embodiment shows a typical embodiment of the invention described in claim 7 and the invention described in claims 11 and 12. The configuration different from that of the first embodiment is that the sealed tube heat exchanger 11 is formed on both sides of the heat exchanger 11 by a synthetic resin made of a synthetic resin instead of the water film sheet 15 (not shown). ) In parallel with the heat exchanger 11 and arranged as a non-contact outdoor air passage that is not in contact with the spray water, so that the spray water is not sprayed on this portion, and is a sealed pipe having a white smoke prevention function It is to be a heat exchanger.

実施の形態4
この形態は請求項11、12記載の実施の形態の一例であり、実施の形態1と異なる構成は、クロスフロー型の水冷却塔ではなく、カウンターフロー型の冷却塔としてある。更に、この水膜シート15の下端は最下位の直管部13より下方に突出し、くの字に曲げられていない。
Embodiment 4
This embodiment is an example of the embodiment described in claims 11 and 12, and the configuration different from the embodiment 1 is not a cross flow type water cooling tower but a counter flow type cooling tower. Further, the lower end of the water film sheet 15 protrudes downward from the lowest straight pipe portion 13 and is not bent into a dogleg shape.

実施の形態5
この形態は請求項8記載の発明の代表的な実施の形態の一例であり、実施の形態1と異なる構成は、前記密閉型管熱交換器はスパイラルコイル16としてあり、上下の各コイル部分間に前記水膜シート15は、この熱交換器のスパイラルコイル16の両側に位置する直管部13に各々上下方向に連ねて付着乃至添着して合計2枚配列されている(図4、図5および図6参照)。
前記スパイラルコイル16は外気取り入れ口14の幅方向に間隔をおいて配列され、隣接する前記スパイラルコイル16は相互に逆向きに旋回して配列する場合もある(図7参照、請求項7記載の代表的な実施の形態に対応)。前記水膜シート15は1つのスパイラルコイル16において、上段部において折り曲げて、2枚折りになっており最上段においては、前記水膜シート15傾斜して張設され、散水装置からの散布水を受ける散水受け部17を形成している。この散水受け部17としては、前記水膜シート15とは別部材の邪魔板を各コイルの最上段の直管部13に設ける場合もある。
この態様においては、このスパイラルコイル16の湾曲部は垂直面に対してある程度角度を為して傾斜しているため、循環冷却水は、実施の形態1の垂直面内に位置する湾曲部の熱交換器に比べて時間をかけて空気流れ方向に対して前後動しつつ流下することとなり、散布水、外気流との接触時間を長くすることができる。
又、隣接する前記スパイラルコイル16は相互に逆向きに旋回しているため、隣接する前記スパイラルコイル16間に前記散水受け部17を確保できる。
また、くの字型に屈曲した各水膜シート15によって、送風通路はハニカム形状に近くなり、外気はこれらに做い水平方向の層流となって流れる効果を奏する。
実施の形態6
この形態は、請求項10記載の発明及び請求項14記載の発明の代表的な実施の形態であり、水冷却器に使用される開放型熱交換器は、上下平行に棒状の支持部材16Aが外気取り入れ口14から奥行方向に配置され、これら支持部材16Aの全長にわたり、散布水案内シート15が連ねてほぼ垂直方向に張り巡らされて構成されている。この開放型管熱交換器を水冷却器の機枠内に装填されている(図8参照)。
各散布水案内シート15の中段部はこれらが通風で振動しないよう、それぞれ数本の水平な中段支持棒13aに対しジグザグに通して張設してある(図8参照)。
その作用は、上下平行に配置された支持部材16Aにわたり、散水案内シート15が連なり張り巡らされてなる開放式熱交換器上に散布水を散布し、散布水をこの散水案内シート15に沿い流し、この流下中に外気流と直接接触させ、散布水を冷却する(請求項2記載の発明の代表的な実施の形態に対応)。
これら散布水案内シート15の中段部は、それぞれ中段支持棒13aに接触させて、張設してあるから、外気流との接触により、吹き寄せられたり、振動して騒音を発しない。
Embodiment 5
This embodiment is an example of a typical embodiment of the invention described in claim 8, and a configuration different from that of the first embodiment is that the hermetic tube heat exchanger is a spiral coil 16 and is arranged between upper and lower coil portions. The water film sheets 15 are attached to or attached to the straight pipe portions 13 located on both sides of the spiral coil 16 of this heat exchanger in the vertical direction, and a total of two sheets are arranged (FIGS. 4 and 5). And FIG. 6).
The spiral coils 16 may be arranged at intervals in the width direction of the outside air intake port 14, and the adjacent spiral coils 16 may be arranged so as to turn in opposite directions (see FIG. 7, claim 7). Corresponding to a typical embodiment). The water film sheet 15 is bent at the upper part of the spiral coil 16 and is folded in two, and the water film sheet 15 is inclined and stretched at the uppermost stage, and the sprayed water from the watering device is supplied. A water spray receiving portion 17 is formed. As the water spray receiving portion 17, a baffle plate which is a member different from the water film sheet 15 may be provided in the straight pipe portion 13 at the uppermost stage of each coil.
In this embodiment, the curved portion of the spiral coil 16 is inclined at an angle with respect to the vertical surface, so that the circulating cooling water is heated by the heat of the curved portion located in the vertical surface of the first embodiment. Compared to the exchanger, it takes time to flow down while moving back and forth in the air flow direction, and the contact time with the spray water and the external airflow can be extended.
Further, since the adjacent spiral coils 16 are pivoted in directions opposite to each other, the water sprinkling portion 17 can be secured between the adjacent spiral coils 16.
Further, the water film sheet 15 bent in a U-shape makes the air passage close to a honeycomb shape, and the outside air has an effect of flowing in a laminar flow in the horizontal direction.
Embodiment 6
This embodiment is a typical embodiment of the invention according to claim 10 and the invention according to claim 14, and the open type heat exchanger used for the water cooler has a bar-like support member 16A in the vertical direction. Arranged in the depth direction from the outside air inlet 14, the spray water guide sheet 15 is connected and stretched in a substantially vertical direction over the entire length of the support member 16 </ b> A. This open pipe heat exchanger is loaded in the frame of the water cooler (see FIG. 8).
The middle portion of each spray water guide sheet 15 is stretched in a zigzag manner with respect to several horizontal middle support rods 13a so that they do not vibrate due to ventilation (see FIG. 8).
The action is to spread the sprayed water on the open heat exchanger in which the watering guide sheets 15 are continuously stretched over the support members 16A arranged in parallel in the vertical direction, and to flow the sprayed water along the watering guide sheets 15. During this flow, the sprayed water is cooled by direct contact with the external airflow (corresponding to a typical embodiment of the invention described in claim 2).
Since the middle part of the spray water guide sheet 15 is in contact with the middle support bar 13a and stretched, it is not blown or vibrated by contact with the external airflow to generate noise.

実施の形態1の一部省略概略正面図である。FIG. 3 is a partially omitted schematic front view of the first embodiment. 図1の一部省略概略右側面図である。FIG. 2 is a partially omitted schematic right side view of FIG. 図1における要部斜視図である。FIG. 2 is a perspective view of main parts in FIG. 実施の形態5の要部斜視図である。FIG. 10 is a perspective view of main parts of a fifth embodiment. 図4におけるスパイラルコイルを示す斜視図である。FIG. 5 is a perspective view showing a spiral coil in FIG. 図4のスパイラルコイルの配列を示す一部省略正面図である。FIG. 5 is a partially omitted front view showing the arrangement of the spiral coils of FIG. 図6のものと異なるスパイラルコイルの配列を示す一部省略正面図である。FIG. 7 is a partially omitted front view showing an arrangement of spiral coils different from that of FIG. 6. 実施の形態6の概略図である。FIG. 10 is a schematic diagram of a sixth embodiment.

符号の説明Explanation of symbols

10 クロスフロー型の水冷却塔
11 管熱交換器
13 直管部
15 水膜シート
DESCRIPTION OF SYMBOLS 10 Cross flow type water cooling tower 11 Tube heat exchanger 13 Straight pipe part 15 Water film sheet

Claims (14)

密閉型管熱交換器を構成する蛇行管の略水平なそれぞれの直管部は相互に略平行に形成されて、この蛇行管は蛇行面を略垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいて配列され、各熱交換器における上下の直管部にわたり、散布水案内シートが連ねて張り巡らされている密閉型管熱交換器上に散布水を散布し、前記散布水案内シートに沿い散布水を流し、この流下中に外気流との直接接触により散布水を冷却し、蒸発に伴う潜熱作用で更に冷却し、この冷却された散布水を前記直管部のほゞ全域に前記散布水案内シートにより案内し流下させ、この密閉型管熱交換器内を循環し流下する循環冷却水を間接的に冷却させることを特徴とする水冷却方法。   The substantially horizontal straight pipe portions of the meandering pipe constituting the hermetic tube heat exchanger are formed substantially parallel to each other, and the meandering pipe has a plurality of meandering faces positioned in a substantially vertical plane, Sprinkling water is spread on a sealed tube heat exchanger that is arranged at intervals in the width direction of the outside air intake and over which the sprinkling water guide sheets are stretched across the upper and lower straight pipe sections of each heat exchanger. The sprayed water is allowed to flow along the sprayed water guide sheet, and the sprayed water is cooled by direct contact with the external airflow during the flow, and further cooled by the latent heat action caused by evaporation. A water cooling method characterized by causing the sprayed water guide sheet to guide and flow down almost all over the tube portion, and indirectly cooling the circulating cooling water circulating and flowing through the sealed pipe heat exchanger. 上下平行に配置された支持部材にわたり、散水案内シートがそれぞれ垂直面方向に連なり張り巡らされてなる開放式熱交換器上に散布水を散布し、散布水をこの散水案内シートに沿い流し、この流下中に外気流と直接接触させ、散布水を冷却することを特徴とする水冷却方法。   Sprinkling water is spread on an open heat exchanger in which sprinkling guide sheets are stretched in a vertical plane over support members arranged in parallel vertically, and the sprinkling water flows along this sprinkling guide sheet. A water cooling method, wherein the sprayed water is cooled by bringing it into direct contact with an external air flow during the flow down. 水冷却器に使用される密閉型管熱交換器において、
前記管熱交換器を構成する蛇行管の略水平なそれぞれの直管部は相互に略平行に形成されて、この蛇行管は蛇行面を略垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいてこの熱交換器は配列されていると共に、各熱交換器における上下の直管部にわたり、散布水案内シートが連ねて張り巡らされていることを特徴とする密閉型管熱交換器。
In closed tube heat exchangers used for water coolers,
The straight horizontal pipe portions of the meandering pipe constituting the pipe heat exchanger are formed substantially in parallel with each other, and the meandering pipe has a plurality of outside air, with the meandering surface positioned in a substantially vertical plane. The heat exchangers are arranged at intervals in the width direction of the intake port, and the sprayed water guide sheets are stretched over the upper and lower straight pipe portions of each heat exchanger. Sealed tube heat exchanger.
水冷却器に使用される密閉型管熱交換器において、
前記管熱交換器における蛇行管はU字形状の屈曲部で順次連った直管部は相互にほゞ平行形成されて、この蛇行面を垂直面内に位置させた状態で複数本、外気取り入れ口の幅方向に間隔をおいてこの熱交換器は配列されていると共に、前記熱交換器の少なくとも一側には冷却水の流下路を形成する水膜シートがこの熱交換器の蛇行面に上下方向に連ねて付着乃至添着して配列されていることを特徴とする前記管熱交換器。
In closed tube heat exchangers used for water coolers,
In the pipe heat exchanger, the meandering pipes, which are successively connected by U-shaped bent parts, are formed substantially parallel to each other, and a plurality of the outside air is provided with the meandering surfaces positioned in the vertical plane. The heat exchangers are arranged at intervals in the width direction of the intake port, and a water film sheet forming a cooling water flow path is provided on at least one side of the heat exchanger. The tube heat exchanger is characterized in that the tube heat exchanger is arranged so as to be attached or attached in a row in the vertical direction.
各前記管熱交換器における上下の直管部間に亘り順次ジクザクに掛合させ屈曲して、それぞれ前記少なくとも一枚の水膜シートが配列され、水膜シートの幅はほゞ各前記管熱交換器における直管部の長さ寸法としてあり、水膜シートの上端は最上位の直管部位置において、散布水受け部としてくの字に屈曲しており、この水膜シートの下端は最下位の直管部より下方に突出し、下部水槽への散布水案内部としてあることを特徴とする請求項4記載の前記管熱交換器。   Each tube heat exchanger is sequentially hooked and bent between the upper and lower straight pipe portions, and each of the at least one water film sheet is arranged, and the width of the water film sheet is approximately the tube heat exchange. The upper end of the water film sheet is bent in a square shape as the spray water receiving part at the position of the uppermost straight pipe part, and the lower end of the water film sheet is the lowest. The said pipe | tube heat exchanger of Claim 4 which protrudes below from the straight pipe part of this, and is used as the spray water guide part to a lower water tank. 前記水膜シートは、編布、不織布、網地など水透過性のシートとしてあることを特徴とする請求項4又は5記載の密閉型管熱交換器。   6. The hermetic tube heat exchanger according to claim 4, wherein the water film sheet is a water permeable sheet such as a knitted fabric, a nonwoven fabric, or a net. 前記密閉型管熱交換器は、熱交換器の両側に、前記水膜シートに替えて合成樹脂製で水非透過性の充填膜をこの熱交換器と並列に略垂直に配列してあり、散布水と非接触の外気通過流路として、この部分に散布水が散布されないことを特徴とする請求項4、5又は6記載の白煙防止機能を有する密閉型管熱交換器。   The sealed tube heat exchanger is arranged on both sides of the heat exchanger with a synthetic resin instead of the water membrane sheet and a water impermeable filling membrane arranged substantially vertically in parallel with the heat exchanger, The sealed pipe heat exchanger having a white smoke prevention function according to claim 4, 5 or 6, wherein the sprayed water is not sprayed on this portion as an outside air passage that is not in contact with the sprayed water. 前記密閉型管熱交換器は前記直管部を有するスパイラルコイルとしてあり、前記水膜シートがニ系列でスパイラルコイルの両側に沿い上下方向に連ねて配設されていることを特徴とする請求項4、5、6または7記載の密閉型管熱交換器。   The sealed tube heat exchanger is a spiral coil having the straight tube portion, and the water film sheet is arranged in series in a vertical direction along both sides of the spiral coil. The closed tube heat exchanger according to 4, 5, 6 or 7. 前記スパイラルコイルは外気取り入れ口の幅方向に間隔をおいて配列され、隣接する前記スパイラルコイルは相互に逆向きに旋回していることを特徴とする請求項8記載の密閉型管熱交換器。   9. The hermetic tube heat exchanger according to claim 8, wherein the spiral coils are arranged at intervals in the width direction of the outside air intake, and the adjacent spiral coils are turned in opposite directions. 水冷却器に使用される開放型熱交換器において、上下平行に支持部材が配置され、これら支持部材にわたり、散布水案内シートがそれぞれ垂直面方向に連ねて張り巡らされていることを特徴とする開放型熱交換器。   In an open heat exchanger used for a water cooler, support members are arranged in parallel in the vertical direction, and the sprayed water guide sheets are stretched around each of the support members in a vertical plane direction. Open heat exchanger. 請求項3、4、5、6、7、8又は9記載の発明における前記密閉型管熱交換器をその機枠内に装填されていることを特徴とする水冷却器。   A water cooler, wherein the sealed pipe heat exchanger according to the invention of claim 3, 4, 5, 6, 7, 8, or 9 is loaded in the machine frame. 請求項3、4、5、6、7、8又は9記載の発明における、蛇行する前記密閉型管熱交換器内の各直管部は、外気流に対して平行としてあるクロスフロー型の熱交換塔としてあり、前記水膜シートおよび前記密閉型管熱交換器へ散布水を散布する散水装置が前記密閉型管熱交換器の上方に配置され、前記水膜シートの下端は最下位の直管部寄り下方に突出し、下部水槽への散布水案内部としてくの字に屈曲していることを特徴とする請求項11記載の水冷却器。   In the invention according to claim 3, 4, 5, 6, 7, 8 or 9, each straight pipe portion in the meandering sealed pipe heat exchanger is parallel to the external airflow. A water spray device is provided as an exchange tower and sprays spray water to the water film sheet and the sealed tube heat exchanger, and is disposed above the sealed tube heat exchanger. The water cooler according to claim 11, wherein the water cooler protrudes downward near the pipe and is bent in a U shape as a spray water guide to the lower water tank. 請求項3、4、5、6、7、8又は9記載の発明における、前記各直管部は外気流に対して直交するカウンターフロー型の熱交換塔としてあり、前記水膜シートおよび前記密閉型管熱交換器へ散布水を散布する散水装置が前記密閉型管熱交換器の上方に配置されていることを特徴とする請求項11記載の水冷却器。   Each straight pipe part in the invention according to claim 3, 4, 5, 6, 7, 8, or 9 is a counter flow type heat exchange tower orthogonal to an external air flow, and the water film sheet and the hermetic seal The water cooler according to claim 11, wherein a water spraying device for spraying sprayed water to the mold tube heat exchanger is disposed above the sealed tube heat exchanger. 請求項10記載の発明における前記開放型管熱交換器をその機枠内に装填されていることを特徴とする水冷却器。   The water cooler, wherein the open-type pipe heat exchanger according to claim 10 is loaded in the machine frame.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014012284A1 (en) * 2012-07-20 2014-01-23 广州市华德工业有限公司 Filler coupling coil pipe evaporative type condenser
WO2014012283A1 (en) * 2012-07-20 2014-01-23 广州市华德工业有限公司 Heat exchange pipe piece used for filler coupling coil pipe evaporative type condenser
CN111141156A (en) * 2020-01-15 2020-05-12 浙江三新科技有限公司 Water distribution system of evaporative condenser

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014012284A1 (en) * 2012-07-20 2014-01-23 广州市华德工业有限公司 Filler coupling coil pipe evaporative type condenser
WO2014012283A1 (en) * 2012-07-20 2014-01-23 广州市华德工业有限公司 Heat exchange pipe piece used for filler coupling coil pipe evaporative type condenser
CN103575146A (en) * 2012-07-20 2014-02-12 广州市华德工业有限公司 Heat exchange tube fin for filler coupling coil evaporative condenser
CN111141156A (en) * 2020-01-15 2020-05-12 浙江三新科技有限公司 Water distribution system of evaporative condenser

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