JP2903066B2 - Crossflow cooling tower - Google Patents
Crossflow cooling towerInfo
- Publication number
- JP2903066B2 JP2903066B2 JP1309858A JP30985889A JP2903066B2 JP 2903066 B2 JP2903066 B2 JP 2903066B2 JP 1309858 A JP1309858 A JP 1309858A JP 30985889 A JP30985889 A JP 30985889A JP 2903066 B2 JP2903066 B2 JP 2903066B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling tower
- outside air
- spray water
- air intake
- filler
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】 イ.発明の目的 <産業上の利用分野> この発明は直交流式冷却塔、殊に多段に充填材を積み
重ねて本体内に充填した直交流式冷却塔に関する。DETAILED DESCRIPTION OF THE INVENTION BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cross-flow cooling tower, and more particularly to a cross-flow cooling tower in which a filler is stacked in multiple stages and filled in a main body.
<従来の技術> この種の直交流式冷却塔としては、例えば実公平1−
13276号公報がある。<Conventional technology> As this type of cross-flow cooling tower, for example,
There is 13276 publication.
<発明が解決しようとする課題> 従来角形の直交流式冷却塔において、冷却塔の上部散
水槽より散布水を冷却塔の充填材中に散水落下せしめ、
フアンにて外気取入口よりこの充填材内を通過して外気
が吸引される。このため充填材内で散布水はこの吸引し
た空気流にあおられて、充填材の下部に至るにつれて散
水落下する散布水は冷却塔排気口側、即ち冷却塔中心部
へひき寄せられ、下部充填材の外側部分では熱交換が行
なわれてない。これは充填材表面積を熱交換に充分活用
していないことになり、この分だけ冷却塔容積を大きく
する必要がある。<Problems to be Solved by the Invention> In a conventional rectangular cross-flow type cooling tower, the spray water is sprinkled from the upper spray tank of the cooling tower into the filler of the cooling tower, and dropped.
The outside air is sucked from the outside air inlet through the inside of the filler at the fan. For this reason, the spray water in the filling material is flooded by the sucked air flow, and the spray water that falls as it reaches the lower portion of the filler material is drawn to the cooling tower exhaust port side, that is, the center of the cooling tower, and the lower part of the filling material No heat exchange takes place in the outer part of the material. This means that the surface area of the packing material is not sufficiently utilized for heat exchange, and it is necessary to increase the cooling tower volume accordingly.
この発明の目的は充填材中を散水落下される散布水が
排気口側へ吸引されるのを防止して散水状態を充填材全
体に均一になるようにして熱交換率を向上させた直交流
式冷却塔を市場に提供することである。An object of the present invention is to improve the heat exchange rate by preventing the spray water dropped in the filler from being sucked toward the exhaust port so that the spray state is uniform throughout the filler. To provide a market cooling tower.
ロ.発明の構成 <課題を解決するための手段> 前記課題を解決するために、この発明の直交流式冷却
塔は冷却塔の本体内に前記冷却塔の外気取入口に対面し
て複数枚の充填板材が、上下方向で完全に重なって少な
くとも2段充填されており、前記最上段の充填材上部及
び上下の充填材間に通水自在な散布水分配板が配置して
あり、 前記充填材及び散布水分配板は、前記外気取入口側が
冷却塔の排気口側より低位に全体傾斜して配列されて、
前記充填材はフイン付の熱交換コイルからなる間接熱交
換器としてあり、前記フインは前記外気取入口側へ下向
きに傾斜した畝を所定ピッチで相互平行に形成してなる
波板としてあることを特徴とする。B. Configuration of the Invention <Means for Solving the Problems> In order to solve the above problems, a cross-flow type cooling tower of the present invention has a plurality of sheets filled in a main body of the cooling tower facing an outside air intake of the cooling tower. The plate material is completely overlapped in the vertical direction and is filled in at least two stages, and a spraying water distribution plate that allows water to flow freely is arranged between the uppermost filler and the upper and lower fillers, and the filler and The spray water distribution plate is arranged such that the outside air intake side is entirely inclined lower than the exhaust port side of the cooling tower,
The filler is an indirect heat exchanger comprising a heat exchange coil with a fin, and the fin is a corrugated plate formed by forming ridges inclined downward to the outside air intake side at a predetermined pitch and in parallel with each other. Features.
<作用> 前記のように構成したこの発明の直交流式冷却塔の作
用を次に説明する。<Operation> The operation of the cross-flow cooling tower of the present invention configured as described above will be described below.
通常の直交流式冷却塔同様に送風機の作動により前記
外気取入口から外気を冷却塔内に吸い込み、冷却塔に充
填した前記充填材の一種である間接式熱交換器間の空気
通路を水平に通して冷却塔排気口側へ吸引する。Like a normal cross-flow cooling tower, the blower operates to suck outside air from the outside air intake into the cooling tower, and horizontally moves the air passage between the indirect heat exchangers, which are a type of the filler filled in the cooling tower. To the cooling tower exhaust port side.
一方、冷却塔の上部水槽から散布水は各間接熱交換器
上に前記空気流と直交して順次落下し、この落下中に空
気流と直接接触して潜熱作用を受けて冷却されると共
に、負荷部から共通の供給側ヘッドを介して各間接式熱
交換器内に送り込まれてくる工業用プロセス流体を間接
的に冷却する。On the other hand, the spray water from the upper water tank of the cooling tower falls sequentially on each indirect heat exchanger orthogonally to the air flow, and during this fall, it is directly contacted with the air flow to be cooled by the latent heat action, Indirect cooling of the industrial process fluid coming into each indirect heat exchanger from the load via a common feed head.
この冷却された工業用プロセス流体を、この熱交換器
から共通の吐出側ヘッダーを介して負荷部へ供給され、
昇温後に再びこれら熱交換器へ再供給され繰返し冷却さ
れる。The cooled industrial process fluid is supplied from the heat exchanger to the load via a common discharge side header,
After the temperature is raised, the heat is resupplied to these heat exchangers again and repeatedly cooled.
この発明においては、更に前記上部水槽から最上段の
間接式熱交換器への流下以前に散布水分配板上に落下
し、この分配板で一次滞留した後、散布水分配板におい
て一様に再分配、再散布され、次段の熱交換器への散布
も一様に行なわれる。In the present invention, before falling from the upper water tank to the uppermost indirect heat exchanger, it falls on the spraying water distribution plate, and after being temporarily retained by this distribution plate, the spraying water distribution plate uniformly returns. It is distributed and redistributed, and is uniformly distributed to the next heat exchanger.
この際、前記熱交換器及び散布水分配板の前記外気取
込口側を排気側より低位に傾斜して冷却塔内に配列して
あるため、散布水は吹き寄せられる力と傾斜による外気
取入口寄りへの流下力とが相殺されて、散布水は各熱交
換器全面に一様に分配散布されほゞ垂直方向に流下す
る。At this time, since the outside air intake side of the heat exchanger and the spray water distribution plate is arranged in the cooling tower at a lower angle than the exhaust side, the spray water is blown by the outside air inlet by the force and the inclination. The spraying water is evenly distributed and spread over the entire surface of each heat exchanger, and the spraying water flows down in a substantially vertical direction.
前記間接式熱交換器におけるフインが、前記畝のある
波板からなるため、より一層外気取入口側の熱交換器へ
散布水は強制的散布され、かつ空気流との接触面積が拡
大すると共に空気流中に飛散した水滴はこのフインに突
き当たり、捕捉される。Since the fin in the indirect heat exchanger is formed of the corrugated plate having the ridges, the spray water is more forcibly sprayed to the heat exchanger on the side of the outside air intake, and the contact area with the air flow is increased. Water droplets scattered in the air flow strike the fin and are trapped.
<実施例> 次にこの発明の代表的な実施例を説明する。<Example> Next, a typical example of the present invention will be described.
第1図において、Aは密閉型の直交流式冷却塔であ
り、その外気取入口Bに対面してフイン11付きの熱交換
コイル12からなる充填材の一種である間接型熱交換器13
が、複数個上下整列して少なくとも2段、図示のものは
4段、この冷却塔の本体14内に積み重ねられ充填されて
いる。In FIG. 1, reference numeral A denotes a closed type cross-flow cooling tower, and an indirect heat exchanger 13 which is a kind of a filler composed of a heat exchange coil 12 with a fin 11 facing an outside air intake B thereof.
However, at least two stages are arranged vertically and four stages are shown in FIG.
各熱交換器13のフイン11は、外気取入口B側に下向き
に傾斜した畝15を所定ピッチで相互平行に形成してなる
波板からなる(第3図参照)。The fins 11 of the heat exchangers 13 are formed of corrugated sheets having ridges 15 inclined downward at a predetermined pitch toward the outside air inlet B at a predetermined pitch (see FIG. 3).
前記上下段の間接式熱交換器13間には塩化ビニルなど
の合成樹脂製のパンチプレートからなる散布水分配板16
が介在してある。更に冷却塔Aの上部水槽Cと最上段の
間接式熱交換器との間にも、同様な散布水分配板16が配
置されている。A spray water distribution plate 16 made of a punch plate made of a synthetic resin such as vinyl chloride is provided between the upper and lower indirect heat exchangers 13.
Is interposed. Further, a similar spray water distribution plate 16 is disposed between the upper water tank C of the cooling tower A and the uppermost indirect heat exchanger.
前記散布水分配板16は、上下段の間接式熱交換器13間
に位置する散布水分配板16は上段の熱交換器13のフイン
11下端を支持する棚としても使用される。The spray water distribution plate 16 is located between the upper and lower indirect heat exchangers 13 and the spray water distribution plate 16 is
11 It is also used as a shelf to support the lower end.
この散布水分配板16を構成するパンチプレートには、
第2図に示すように、多数の散水孔17があけてあり、散
水孔17の分布状態は、前記外気取入口B側で多く(密)
とし、冷却塔Aの送風機Eが取付けられた排気口D側で
は少なく穿設されている(第2図参照)。The punch plate constituting the spray water distribution plate 16 includes:
As shown in FIG. 2, a large number of water spray holes 17 are provided, and the distribution state of the water spray holes 17 is large (dense) on the side of the outside air intake B.
The cooling tower A is provided with a small amount on the exhaust port D side where the blower E is attached (see FIG. 2).
前記のように多段に積み重ねた間接式熱交換器13と散
布水分配板16は、前記外気取入口B側が前記排気口D側
より低位となる姿勢で全体傾斜してこの冷却塔本体14内
に配列されている。The indirect heat exchanger 13 and the spray water distribution plate 16 stacked in multiple stages as described above are entirely inclined in such a position that the outside air intake B side is lower than the exhaust port D side, and the inside of the cooling tower body 14 is inclined. Are arranged.
18はこれら熱交換器13の供給口が接続する供給側ヘエ
ッダーであり、19はその吐出口が接続する吐出側ヘッダ
ーである。Reference numeral 18 denotes a supply-side header connected to the supply ports of the heat exchanger 13, and reference numeral 19 denotes a discharge-side header connected to the discharge ports.
前記のように構成した実施例の直交流冷却塔Aの作用
は、この発明の作用と同じであるため、ここでの説明を
省略する。The operation of the cross-flow cooling tower A of the embodiment configured as described above is the same as the operation of the present invention, and the description thereof will be omitted.
ハ.発明の効果 前記のように構成し作用するこの発明の直交流式冷却
塔において、前記充填材と散布水分配板全体を、前記外
気取入口側が排気口側より低位となる状態で傾斜して冷
却塔本体内に充填してあるため、散布水を各段の充填材
上に一様に散水でき、従来のように外気取入口側に散布
水が全く散布されないデッドスペースは全く発生せず、
充填材の全面を散布水、循環水の熱交換に充分に活用で
き、冷却塔の容積を大きくせずに、充分な熱交換効率を
達成することができる。C. Effect of the Invention In the cross-flow cooling tower of the present invention configured and operated as described above, the filler and the whole spray water distribution plate are inclined and cooled in a state where the outside air intake side is lower than the exhaust port side. Because it is packed in the tower body, spray water can be evenly sprayed on the packing material of each stage, and there is no dead space where spray water is not sprayed at all on the outside air intake side as in the past,
The entire surface of the filler can be sufficiently utilized for heat exchange of spray water and circulating water, and sufficient heat exchange efficiency can be achieved without increasing the capacity of the cooling tower.
前記充填材がフイン付の熱交換コイルからなる間接熱
交換器としてあるため、間接式熱交換器内を流れる循環
冷却水を、各段の熱交換器外面に沿いに散布流下する散
布水により、その全表面で間接的にかつ能率良く冷却で
きる。Since the filler is an indirect heat exchanger comprising a finned heat exchange coil, the circulating cooling water flowing through the indirect heat exchanger is sprayed down along the outer surface of each stage of the heat exchanger by spray water. The entire surface can be cooled indirectly and efficiently.
前記フインは前記外気取入口側へ下向きに傾斜した畝
を所定ピッチで相互平行に形成してなる波板としてある
ため、フインの表面積を増大でき、フイン上を流下する
散布水と水平に流れる空気流との間の熱交換量を増加で
きると共にその傾斜した畝に沿い散布水を接触的に外気
取入口側へ寄せて流下し、充填材に散布水が散布されな
いデットスペースを減少できる。Since the fin is a corrugated plate formed by forming ridges downwardly inclined toward the outside air intake side at a predetermined pitch, the surface area of the fin can be increased, and spray water flowing down on the fin and air flowing horizontally are formed. The amount of heat exchange with the flow can be increased, and the spray water can be contacted to the outside air inlet side along the inclined ridge to flow down, thereby reducing the dead space in which the spray water is not sprayed on the filler.
<実施例固有の効果> 前記実施例はこの発明と同様の効果を奏する他、散布
水分配板16が塩化ビニールなどの合成樹脂としてあるた
め、金属製のフイン11が電気腐食するのも未然に防ぐこ
とができる。<Effects Specific to the Embodiment> The above-described embodiment has the same effects as the present invention. In addition, since the spray water distribution plate 16 is made of a synthetic resin such as vinyl chloride, the metal fins 11 are prevented from being electrically corroded. Can be prevented.
図はこの発明に係わるもので、第1図はこの発明の代表
的な実施例の概略図、第2図はその散布水分配板の平面
図、第3図は前記熱交換器の一部省略正面図である。 図中の主な符号の説明 12……間接式熱交換器、 16……散布水分配板。1 is a schematic view of a typical embodiment of the present invention, FIG. 2 is a plan view of a spray water distribution plate, and FIG. 3 is a view partially showing the heat exchanger. It is a front view. Description of main symbols in the figure 12: Indirect heat exchanger 16: Sprinkling water distribution plate
フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F28C 1/00 - 1/16 F28F 25/00 - 25/12 Continuation of front page (58) Field surveyed (Int.Cl. 6 , DB name) F28C 1/00-1/16 F28F 25/00-25/12
Claims (1)
に対面して複数枚の充填板材が、上下方向で完全に重な
って少なくとも2段充填されており、前記最上段の充填
材上部及び上下の充填材間に通水自在な散布水分配板が
配置してあり、 前記充填材及び散布水分配板は、前記外気取入口側が冷
却塔の排気口側より低位に全体傾斜して配列されて、前
記充填材はフイン付の熱交換コイルからなる間接熱交換
器としてあり、前記フインは前記外気取入口側へ下向き
に傾斜した畝を所定ピッチで相互平行に形成してなる波
板としてあることを特徴とする直交流式冷却塔。1. A cooling tower body, wherein at least two packing plates are filled with a plurality of filling plate members facing the outside air intake of the cooling tower so as to be completely overlapped in the vertical direction, and the uppermost packing member is provided. A spray water distribution plate that allows water to flow freely is disposed between the upper and lower fillers, and the filler and the spray water distribution plate are arranged such that the outside air intake side is entirely inclined lower than the exhaust port side of the cooling tower. The filler is arranged as an indirect heat exchanger comprising a heat exchange coil with fins, and the fins are corrugated plates formed with ridges inclined downward toward the outside air intake side at a predetermined pitch and in parallel with each other. A cross-flow cooling tower, characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1309858A JP2903066B2 (en) | 1989-11-29 | 1989-11-29 | Crossflow cooling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1309858A JP2903066B2 (en) | 1989-11-29 | 1989-11-29 | Crossflow cooling tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03170794A JPH03170794A (en) | 1991-07-24 |
| JP2903066B2 true JP2903066B2 (en) | 1999-06-07 |
Family
ID=17998144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1309858A Expired - Fee Related JP2903066B2 (en) | 1989-11-29 | 1989-11-29 | Crossflow cooling tower |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2903066B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5036360B2 (en) * | 2007-03-22 | 2012-09-26 | 大阪瓦斯株式会社 | Absorption refrigerator |
| JP6464648B2 (en) * | 2014-10-02 | 2019-02-06 | 栗田工業株式会社 | cooling tower |
| JP6412909B2 (en) * | 2016-11-16 | 2018-10-24 | 株式会社関電エネルギーソリューション | Cooling tower and cooling system |
| CN111879145B (en) * | 2020-06-24 | 2021-11-23 | 洛阳理工学院 | Square water cooling tower |
| CN117516207B (en) * | 2024-01-05 | 2024-05-03 | 广东览讯科技开发有限公司 | Counter-flow tower variable flow device and central air conditioning system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4683101A (en) * | 1985-12-26 | 1987-07-28 | Baltimore Aircoil Company, Inc. | Cross flow evaporative coil fluid cooling apparatus and method of cooling |
-
1989
- 1989-11-29 JP JP1309858A patent/JP2903066B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03170794A (en) | 1991-07-24 |
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