JPH11166793A - Crossflow cooling tower - Google Patents

Crossflow cooling tower

Info

Publication number
JPH11166793A
JPH11166793A JP33326097A JP33326097A JPH11166793A JP H11166793 A JPH11166793 A JP H11166793A JP 33326097 A JP33326097 A JP 33326097A JP 33326097 A JP33326097 A JP 33326097A JP H11166793 A JPH11166793 A JP H11166793A
Authority
JP
Japan
Prior art keywords
outside air
tower
gas
liquid contact
air
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
JP33326097A
Other languages
Japanese (ja)
Inventor
Masatomi Ikeda
正富 池田
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.)
TOWA KENSETSU KOGYO KK
Takasago Thermal Engineering Co Ltd
Original Assignee
TOWA KENSETSU KOGYO KK
Takasago Thermal Engineering 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 TOWA KENSETSU KOGYO KK, Takasago Thermal Engineering Co Ltd filed Critical TOWA KENSETSU KOGYO KK
Priority to JP33326097A priority Critical patent/JPH11166793A/en
Publication of JPH11166793A publication Critical patent/JPH11166793A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To suppress the height of a crossflow cooling tower having white smoke preventing function. SOLUTION: A gas-liquid contact heat exchanging sections 5, 5 are disposed in the opposite sides of a tower body 3 and a pair of heaters 12, 12 are disposed in the air passage 9, i.e., the space between the sections 5, 5. The space between the heaters 12, 12 serves as an outer air introduction passage 14. On the side wall 7 of the tower body 3 where the gas-liquid contact heat exchanging section 5 is not disposed, an outer air introduction port 15 with damper 16 communicating with the outer air introduction passage 14 is provided. When there is a possibility of providing white smoke, outer air is introduced by opening the damper 16 and discharged to time air passage 9 after being heated through the heater 12. Heated air passed through the heater 12 and the heated and humidified air passed through the gas-liquid contact heat exchanging section 5 are mixed and stirred in the air passage 9 before being discharged from an exhaust port 10 to the atmosphere.

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、被冷却水と空気と
を塔内において直交させるように流して被冷却水を冷却
する直交流型冷却塔に関し、特に、白煙を防止し得る直
交流型冷却塔に係るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cross-flow type cooling tower for cooling water to be cooled by flowing water to be cooled and air in the tower so as to be orthogonal to each other. It relates to a mold cooling tower.

【0002】[0002]

【従来の技術と発明が解決しようとする課題】冷却塔の
運転に際して、特に冬季においては、冷却塔内を通過し
て暖められ湿度上昇した空気が塔外に排気として排出さ
れると、この排気が冷たい外気と接触して、排気中の水
蒸気が液化して霧状になり、見た目には白煙の状態とな
り、いかにも出火時の白煙のように見られたり、あるい
は有害な排気ガスを排出して環境を汚染しているかのよ
うに見られたりする虞れがあり、また、広大な白煙が発
生すると視界を遮り交通の障害になる虞れがある。
2. Description of the Related Art During operation of a cooling tower, especially in winter, when air that has been heated and increased in humidity after passing through the cooling tower is discharged as exhaust gas outside the tower, the exhaust gas is discharged. When it comes into contact with cold outside air, the water vapor in the exhaust gas liquefies and becomes mist, it looks like white smoke, and it looks like white smoke at the time of fire, or emits harmful exhaust gas The environment may be seen as if it is polluting the environment, and if a large amount of white smoke is generated, the visibility may be obstructed and traffic may be obstructed.

【0003】このような白煙の発生を防止するため、従
来の直交流型冷却塔では、図7に示すように、間接加熱
コイル21を気液接触熱交換部22上に設置する方式が
使用されてきた。この方式は、冷却水の戻り水の熱を熱
源として用いて余分な熱を要しないようにし、かつ一部
の空気を間接加熱コイル21に通過させることによって
空気に顕熱は与えるが、潜熱の上昇は起こさないように
したものである。このように顕熱の付与された空気と、
気液接触熱交換部22を通過させて顕熱とともに潜熱の
上昇した空気、すなわち温度と湿度が上昇した空気とを
混合すると、混合空気全体の湿度は後者の空気の湿度よ
りも低下するため、排出される混合空気が冷たい外気と
接触したとしても白煙が発生しないようにすることがで
きる。尚、その際、例えば、外気の温湿度条件により間
接加熱をする空気量を調節する操作などが行われる。
In order to prevent such generation of white smoke, a conventional cross-flow type cooling tower employs a system in which an indirect heating coil 21 is installed on a gas-liquid contact heat exchange section 22, as shown in FIG. It has been. This system uses the heat of the return water of the cooling water as a heat source so that no extra heat is required, and sensible heat is given to the air by passing a part of the air through the indirect heating coil 21. The rise was not to occur. With the air to which the sensible heat is applied,
When air passing through the gas-liquid contact heat exchange section 22 and mixing sensible heat and air whose latent heat has risen, that is, air whose temperature and humidity have risen, are mixed, the humidity of the whole mixed air is lower than the humidity of the latter air. Even if the discharged mixed air comes into contact with cold outside air, white smoke can be prevented from being generated. At this time, for example, an operation of adjusting the amount of air to be indirectly heated according to the temperature and humidity conditions of the outside air is performed.

【0004】しかしながら、この方式は、塔高が高くな
り、装置が大型化する上に、冷却塔の構造上、一般的に
間接加熱コイル21の設置位置が左右に制約され、前後
方向など他の方向には設置が困難であり、また、排気用
ファンによる気流の捻れが18゜程度に制約されてしま
うため、空気の良好な撹拌混合が得られにくく、十分な
白煙防止効果が得られないという欠点がある。
However, in this method, the tower height is increased, the size of the apparatus is increased, and the installation position of the indirect heating coil 21 is generally restricted to the left and right due to the structure of the cooling tower. It is difficult to install in the direction, and twisting of the airflow by the exhaust fan is restricted to about 18 °, so that it is difficult to obtain good stirring and mixing of air, and it is not possible to obtain sufficient white smoke prevention effect. There is a disadvantage that.

【0005】また、特公平4−1273号公報に開示さ
れた直交流型冷却塔では、対向配置された一対の気液接
触熱交換部の間の塔中央部に、間接加熱コイルを立設
し、一方の気液接触熱交換部と間接加熱コイルの間の塔
上部に流路切替用のダンパ(第1のダンパ)を設け、さ
らに、間接加熱コイルへの空気の流通を許可あるいは遮
断するダンパ(第2のダンパ)を設けている。この直交
流型冷却塔では、両ダンパの開閉により空気の流路を切
り替えることによって、白煙が発生する虞れがない時の
運転では、両気液接触熱交換部に空気を通し間接加熱コ
イルには空気を通さずに塔外に排気し、白煙が発生する
虞れがある時の運転では、一方の気液接触熱交換部の冷
却機能を停止させた上でこの気液接触熱交換部を通った
空気を間接加熱コイルに通し、この間接加熱コイルを通
った空気と冷却機能を有する他方の気液接触熱交換部を
通った空気を混合して塔外に排気するようにしている。
[0005] In the cross-flow cooling tower disclosed in Japanese Patent Publication No. 4-1273, an indirect heating coil is provided upright at the center of the tower between a pair of gas-liquid contact heat exchangers arranged opposite to each other. A damper (first damper) for switching the flow path is provided at the top of the tower between the one gas-liquid contact heat exchange section and the indirect heating coil, and further, a damper for permitting or blocking the flow of air to the indirect heating coil. (A second damper). In this cross-flow type cooling tower, by switching the air flow path by opening and closing both dampers, when there is no danger of generating white smoke, air is passed through both gas-liquid contact heat exchange parts and the indirect heating coil During the operation when there is a risk of generating white smoke without passing air through the tower, the cooling function of one of the gas-liquid contact heat exchange units must be stopped before this gas-liquid contact heat exchange The air passing through the indirect heating coil is passed through the indirect heating coil, and the air passing through the other gas-liquid contact heat exchange unit having a cooling function is mixed with the air passing through the indirect heating coil and discharged outside the tower. .

【0006】この直交流型冷却塔の場合には、前記従来
の直交流型冷却塔よりも塔高を低くすることができる
が、白煙が発生する虞れのない時の運転でも空気を前記
第1のダンパに通さなければならない構造になっている
ため、圧力損失が大きく動力費の点で不利である。
In the case of this cross-flow cooling tower, the tower height can be made lower than that of the conventional cross-flow cooling tower. Since the structure must pass through the first damper, pressure loss is large and power consumption is disadvantageous.

【0007】さらに、この直交流型冷却塔において白煙
が発生する虞れのある時の運転では、前記一方の気液接
触熱交換部の冷却機能を停止させてしまうので、処理水
量が低下するという欠点がある。その上、間接加熱コイ
ルと気液接触熱交換部がほぼ同じ高さ位置に設けられて
いて、かつ直ぐその上が排気口になっている構造である
ため、間接加熱コイルを通った空気と前記他方の気液接
触熱交換部を通った空気との混合撹拌が不十分になり、
白煙発生防止効果が十分に得られない場合もある。
Further, in the operation when there is a risk of generating white smoke in the cross-flow type cooling tower, the cooling function of the one gas-liquid contact heat exchange section is stopped, so that the amount of treated water decreases. There is a disadvantage that. In addition, since the indirect heating coil and the gas-liquid contact heat exchange part are provided at substantially the same height position, and the structure is such that the air outlet is located immediately above, the air passing through the indirect heating coil and the air Mixing and agitation with air that passed through the other gas-liquid contact heat exchange section became insufficient,
In some cases, the effect of preventing white smoke is not sufficiently obtained.

【0008】本発明はこのような従来の技術の問題点に
鑑みてなされたものであり、塔高を低くでき、しかも白
煙防止に優れる直交流型冷却塔を提供することを目的と
する。
[0008] The present invention has been made in view of such problems of the conventional technology, and an object of the present invention is to provide a cross-flow cooling tower that can reduce the tower height and is excellent in preventing white smoke.

【0009】[0009]

【課題を解決するための手段】本発明は前記課題を解決
するために、以下の手段を採用した。本発明は、塔上部
に排気用ファンを有する排気口を設け、塔側部の少なく
とも一部に、塔側方から外気を流入しこの外気を上方か
ら散水される被冷却水と接触させて熱交換する気液接触
熱交換部を設け、前記排気口と前記気液接触熱交換部と
の間に位置する塔内部の中空部を空気通路とした直交流
型冷却塔において、塔側部あるいは塔上部に、前記気液
接触熱交換部とは別に外気導入口を設け、前記中空部内
に、空気と熱媒とを非接触状態で熱交換させる加熱体
と、前記外気導入口から導入した外気を前記加熱体に導
く外気導入通路とを設け、前記気液接触熱交換部を通っ
て加熱された外気と、前記外気導入口から導入され前記
加熱体を通って加熱された外気を前記中空部で混合可能
にしたことを特徴とする。
The present invention has the following features to attain the object mentioned above. According to the present invention, an exhaust port having an exhaust fan is provided at the top of a tower, and outside air is introduced into at least a part of the tower side from the side of the tower, and the outside air is contacted with water to be cooled sprayed from above to generate heat. In a cross-flow type cooling tower provided with a gas-liquid contact heat exchange section to be exchanged and having a hollow portion inside the tower located between the exhaust port and the gas-liquid contact heat exchange section as an air passage, a tower side or a tower In the upper part, an outside air introduction port is provided separately from the gas-liquid contact heat exchange section, and a heating element for exchanging heat between the air and the heat medium in a non-contact state, and outside air introduced from the outside air introduction port are provided in the hollow section. Providing an outside air introduction passage leading to the heating body, the outside air heated through the gas-liquid contact heat exchanging section, and the outside air introduced from the outside air introduction port and heated through the heating body, in the hollow portion. It is characterized in that it can be mixed.

【0010】外気導入口から流入した外気は、外気導入
通路を通り加熱体を通って塔内部の中空部に放出され
る。この空気は加熱体を通る際に加熱される。気液接触
熱交換部を通った外気は加熱加湿されて塔内部の中空部
に放出され、この中空部において、加熱体を通った前記
加熱空気と混合撹拌され、排気口から大気に排気され
る。加熱体を塔内部の中空部内に設置したので、冷却塔
の塔高を低く抑えることができる。
The outside air flowing from the outside air introduction port passes through the outside air introduction passage, passes through the heating element, and is discharged into the hollow portion inside the tower. This air is heated as it passes through the heating element. The outside air that has passed through the gas-liquid contact heat exchange unit is heated and humidified and released into the hollow portion inside the tower, where the air is mixed and stirred with the heated air that has passed through the heating element, and exhausted to the atmosphere from the exhaust port. . Since the heating element is installed in the hollow portion inside the tower, the tower height of the cooling tower can be kept low.

【0011】加熱体は、空気と熱媒とを非接触状態で熱
交換させ、空気に顕熱を与えるが潜熱の上昇は起こさな
いものであれば、その構造等に制限はなく、例えば、板
状体、螺旋状体、渦巻状体、蛇行管状態などを例示でき
る。加熱体における熱媒は、液体、気体、蒸気等を例示
できる。
[0011] The structure of the heating element is not limited as long as it causes heat exchange between the air and the heating medium in a non-contact state and gives sensible heat to the air but does not increase latent heat. Examples include a shape, a spiral, a spiral, and a meandering tube. The heat medium in the heating element can be exemplified by liquid, gas, vapor and the like.

【0012】気液接触熱交換部は、流入する外気と散水
される被冷却水とを接触させて熱交換するものであれ
ば、その構造等に特に限定はなく、内部に充填材を充填
して被冷却水を上方から下方に散布するタイプのもの
や、充填材を設けずに水を噴霧して直接気液接触させる
タイプのものなどを例示することができる。さらに、被
冷却水の散水状態についても特に限定はなく、液膜状、
飛沫状、スプレー状、あるいはこれらの共存状態にして
もよい。
The gas-liquid contact heat exchanging section is not particularly limited in its structure and the like, as long as it is capable of exchanging heat by bringing the inflowing outside air into contact with the water to be cooled. And a type in which water to be cooled is sprayed downward from above, and a type in which water is sprayed without providing a filler and brought into direct gas-liquid contact can be exemplified. Further, there is no particular limitation on the state of spraying the water to be cooled.
It may be in the form of a droplet, a spray, or a coexistence thereof.

【0013】外気導入口は、ダンパ等による開閉手段を
備えるのが好ましい。このようにすれば、白煙発生の虞
れのある時にだけ外気導入口を開放することができる。
It is preferable that the outside air inlet is provided with opening / closing means such as a damper. In this way, the outside air inlet can be opened only when there is a risk of generating white smoke.

【0014】[0014]

【発明の実施の形態】以下、本発明の直交流型冷却塔の
実施の形態を図1から図6の図面に基いて説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a cross-flow cooling tower according to the present invention will be described below with reference to FIGS.

【0015】〔第1の実施の形態〕図1及び図2に示す
ように、第1の実施の形態の直交流型冷却塔1は平面視
略矩形をなし、水槽2の上方に塔本体3を設置してな
る。
First Embodiment As shown in FIGS. 1 and 2, a cross-flow type cooling tower 1 according to a first embodiment has a substantially rectangular shape in plan view, and a tower body 3 is provided above a water tank 2. Is installed.

【0016】塔本体3の底部には支床4が設けられ、塔
本体3において対向する側部には一対の気液接触熱交換
部5が支床4の上に設置され、各気液接触熱交換部5の
上部には散水槽6が設置されている。
A support 4 is provided at the bottom of the tower body 3, and a pair of gas-liquid contact heat exchangers 5 are installed on the support 4 on opposite sides of the tower body 3. A watering tank 6 is provided above the heat exchange unit 5.

【0017】支床4と気液接触熱交換部5,5が設けら
れていない塔本体3の側壁7,7と気液接触熱交換部
5,5と塔本体3の天板部8とで囲まれた塔本体3の内
部は中空になっていて、空気通路9を構成している。そ
して、天板部8からは、空気通路9に連なる円筒状の排
気口10が立設されており、この排気口10は排気用フ
ァン11を備えている。
The support 4, the side walls 7, 7 of the tower body 3 where the gas-liquid contact heat exchange sections 5, 5 are not provided, the gas-liquid contact heat exchange sections 5, 5 and the top plate section 8 of the tower body 3. The inside of the enclosed tower body 3 is hollow, and forms an air passage 9. From the top plate 8, a cylindrical exhaust port 10 connected to the air passage 9 is provided upright. The exhaust port 10 includes an exhaust fan 11.

【0018】気液接触熱交換部5は、その側面が外気導
入口5aになっていて、内部には、空気と液体の接触面
積を大きくするための充填材(図示せず)が充填されて
いる。そして、排気用ファン11を回転すると、外気導
入口5aから導入された外気が、気液接触熱交換部5を
通過して空気通路9内に流入する。また、散水槽6の底
部には多数の散水孔が設けられており、この散水孔から
気液接触熱交換部5に被冷却水が散水される。この気液
接触熱交換部5内において、下方に流れる被冷却水と略
水平に流れる外気とが接触して熱交換を行い、被冷却水
は冷却され、外気は暖められると共に湿度が上昇する。
この温度と湿度が上昇した空気が空気通路9を通り、排
気口10から外部に排気される。
The gas-liquid contact heat exchange section 5 has a side surface serving as an outside air inlet 5a, and the inside thereof is filled with a filler (not shown) for increasing the contact area between air and liquid. I have. Then, when the exhaust fan 11 is rotated, the outside air introduced from the outside air introduction port 5 a passes through the gas-liquid contact heat exchange unit 5 and flows into the air passage 9. Further, a large number of water spray holes are provided at the bottom of the water spray tank 6, and water to be cooled is sprayed from the water spray holes to the gas-liquid contact heat exchange unit 5. In the gas-liquid contact heat exchange unit 5, the water to be cooled that flows downward and the outside air that flows substantially horizontally contact each other to exchange heat, and the water to be cooled is cooled, the outside air is warmed, and the humidity rises.
The air having the increased temperature and humidity passes through the air passage 9 and is exhausted from the exhaust port 10 to the outside.

【0019】また、空気通路9内のほぼ中央には一対の
加熱体12,12が設置されている。両加熱体12は、
その下部を支床4に接地させ、一方の側壁7から他方の
側壁7に至るまで下方が末広がりの「ハ」の字状に傾斜
させて対向設置されている。両加熱体12の上端部は、
空気通路9の高さのほぼ中間に位置していて、閉塞板1
3によって連結されている。そして、両加熱体12,1
2と支床4と閉塞板13によって囲まれた空間は外気導
入通路14になっている。
A pair of heaters 12, 12 are installed at substantially the center of the air passage 9. Both heating elements 12
The lower part is grounded to the supporting floor 4, and the lower part is oppositely installed from the one side wall 7 to the other side wall 7 in such a manner that the lower part is inclined in the shape of "C". The upper ends of both heating elements 12
The obstruction plate 1 is located at approximately the middle of the height of the air passage 9.
3 are connected. And both heating bodies 12, 1
A space surrounded by the support 2, the floor 4, and the closing plate 13 is an outside air introduction passage 14.

【0020】さらに、塔本体3の各側壁7の中央下部に
は、外気導入通路14に連なる外気導入口15が設置さ
れている。この外気導入口15には、必要に応じてこの
外気導入口15を閉塞するためのダンパ16が設けられ
ている。
Further, an outside air introduction port 15 connected to the outside air introduction passage 14 is provided at the lower center of each side wall 7 of the tower body 3. The outside air inlet 15 is provided with a damper 16 for closing the outside air inlet 15 as needed.

【0021】加熱体12はコイル式のもので、コイル内
に熱媒としての温水を流し、コイルとコイルの間を空気
が通過する際に、空気が湿度上昇を伴わずに加熱される
ようになっている。すなわち、加熱体12は、空気に顕
熱は与えるが潜熱の上昇を起こさないようにした非接触
式の熱交換器である。
The heating element 12 is of a coil type, in which hot water as a heat medium flows in the coil so that when the air passes between the coils, the air is heated without increasing the humidity. Has become. That is, the heating element 12 is a non-contact type heat exchanger that gives sensible heat to the air but does not increase latent heat.

【0022】外気導入口15から流入する外気は外気導
入通路14を通り、加熱体12を通過して空気通路9に
流れ出る。また、支床4において外気導入通路14を除
く部分には多数の水抜き孔が設けられていて、散水槽6
から散水され気液接触熱交換部5を流れ落ちた被冷却水
はこの水抜き孔を通って水槽2に流れるようになってい
る。尚、支床4に水抜き孔を設ける代わりに、支床4を
側縁に向けて下り傾斜させて設置してもよい。
The outside air flowing from the outside air introduction port 15 passes through the outside air introduction passage 14, passes through the heater 12, and flows out to the air passage 9. A large number of drain holes are provided in the support floor 4 except for the outside air introduction passage 14.
The water to be cooled which has been sprinkled from the water and has flowed down the gas-liquid contact heat exchange section 5 flows into the water tank 2 through the drain hole. In addition, instead of providing the drainage hole in the support floor 4, the support floor 4 may be installed to be inclined downward toward the side edge.

【0023】次に、この実施の形態の冷却塔1の作用を
説明する。冷却塔1の排気口10から排気を流出した時
に白煙が生じる虞れがない場合には、外気導入口15の
ダンパ16を閉ざして冷却塔1を運転する。ダンパ16
を閉ざして排気用ファン11を回転すると、側壁7に設
けた外気導入口15からの外気の流入が阻止され、外気
は気液接触熱交換部5の外気導入口5aからだけ冷却塔
1内に流入する。流入した外気は、気液接触熱交換部5
を通過する際に散水槽6から散水される被冷却水と接触
して熱交換を行い、被冷却水を冷却する。この熱交換に
より外気は暖められるとともに、一部の被冷却水の蒸発
により湿度を上昇させる。加熱加湿された空気は空気通
路9内を上昇し排気口10から大気中に排気される。加
熱体12は、気液接触熱交換部5から離れて、空気通路
9の下部中央に位置しているので、加熱体12が空気通
路9内の空気の流れを邪魔することはない。
Next, the operation of the cooling tower 1 of this embodiment will be described. When there is no possibility that white smoke will be generated when the exhaust gas flows out from the exhaust port 10 of the cooling tower 1, the cooling tower 1 is operated with the damper 16 of the outside air inlet 15 closed. Damper 16
Is closed and the exhaust fan 11 is rotated, the inflow of outside air from the outside air introduction port 15 provided in the side wall 7 is prevented, and the outside air enters the cooling tower 1 only from the outside air introduction port 5a of the gas-liquid contact heat exchange unit 5. Inflow. The inflowing outside air is supplied to the gas-liquid contact heat exchange section 5.
When passing through, water is cooled by contacting the water to be cooled sprinkled from the water spray tank 6 to cool the water to be cooled. This heat exchange warms the outside air and raises the humidity by evaporating some of the water to be cooled. The heated and humidified air rises in the air passage 9 and is exhausted to the atmosphere from an exhaust port 10. Since the heating element 12 is located at the lower center of the air passage 9 away from the gas-liquid contact heat exchange section 5, the heating element 12 does not obstruct the flow of air in the air passage 9.

【0024】一方、冬季など、冷却塔1の排気口10か
ら排気を流出した時に白煙が生じる虞れがある場合に
は、外気導入口15のダンパ16を開いて冷却塔1を運
転する。ダンパ16を開いて排気用ファン11を回転す
ると、外気は、気液接触熱交換部5の外気導入口5aか
らだけでなく、側壁7に設けた外気導入口15からも冷
却塔1内に流入するようになる。気液接触熱交換部5の
外気導入口5aから流入した外気は前述と同様に気液接
触熱交換部5で加熱加湿されて空気通路9内に流入し、
空気通路9内を上昇する。また、外気導入口15から流
入した外気は、外気導入通路14から加熱体12を通過
して空気通路9内に流入し、加熱体12を通過する際に
加熱される。そして、加熱体12を通った加熱空気と、
気液接触熱交換部5を通過して加熱加湿された空気は、
空気通路9内において十分に撹拌混合され排気口10か
ら大気に排気されるので、排気の際に白煙が生じない。
On the other hand, when there is a possibility that white smoke may be generated when exhaust gas flows out of the exhaust port 10 of the cooling tower 1 such as in winter, the cooling tower 1 is operated by opening the damper 16 of the outside air inlet 15. When the exhaust fan 11 is rotated by opening the damper 16, the outside air flows into the cooling tower 1 not only from the outside air inlet 5 a of the gas-liquid contact heat exchange unit 5 but also from the outside air inlet 15 provided on the side wall 7. I will be. The outside air flowing from the outside air inlet 5a of the gas-liquid contact heat exchange unit 5 is heated and humidified by the gas-liquid contact heat exchange unit 5 as described above, and flows into the air passage 9.
It rises in the air passage 9. The outside air flowing from the outside air introduction port 15 passes through the heating body 12 from the outside air introduction passage 14, flows into the air passage 9, and is heated when passing through the heating body 12. And the heating air which passed through the heating body 12,
The air heated and humidified after passing through the gas-liquid contact heat exchange section 5 is
Since the mixture is sufficiently stirred and mixed in the air passage 9 and exhausted to the atmosphere from the exhaust port 10, white smoke is not generated at the time of exhaust.

【0025】ここで、空気通路9の高さが加熱体12の
高さよりも高く、加熱体12の上端から排気口10の入
口までに相当の距離があること、及び、加熱体12と気
液接触熱交換部5が同じ範囲(すなわち、側壁7,7
間)に設置されていることから、加熱体12を通った加
熱空気と、気液接触熱交換部5を通過して加熱加湿され
た空気とが接触し混合する機会が多くなり、これが両空
気を十分に混合撹拌することとなる。
Here, the height of the air passage 9 is higher than the height of the heating element 12, and there is a considerable distance from the upper end of the heating element 12 to the entrance of the exhaust port 10. The contact heat exchanger 5 has the same area (that is, the side walls 7, 7).
In this case, the heated air passing through the heating element 12 and the air heated and humidified through the gas-liquid contact heat exchange section 5 come into contact and mix with each other. Will be sufficiently mixed and stirred.

【0026】また、加熱体12を気液接触熱交換部5,
5間の空気通路9内に設置しているので、冷却塔1の塔
高が高くならずに済み、冷却塔1のコンパクト化、及び
コストダウンを図ることができる。
The heating element 12 is connected to the gas-liquid contact heat exchanging section 5,
Since the cooling tower 1 is installed in the air passage 9 between the cooling towers 5, the tower height of the cooling tower 1 does not need to be high, and the cooling tower 1 can be made compact and the cost can be reduced.

【0027】〔第2の実施の形態〕次に、第2の実施の
形態の冷却塔1について、図3及び図4に基いて説明す
る。尚、以下の第2の実施の形態の説明では、第1の実
施の形態の冷却塔1と同一態様部分には同一符号を付し
て説明を省略し、第1の実施の形態との相違点だけを説
明する。
[Second Embodiment] Next, a cooling tower 1 according to a second embodiment will be described with reference to FIGS. In the following description of the second embodiment, the same components as those of the cooling tower 1 of the first embodiment will be denoted by the same reference numerals, and description thereof will be omitted, and differences from the first embodiment will be omitted. Only points will be explained.

【0028】第2の実施の形態の冷却塔1においては、
気液接触熱交換部が設けられている側面の四隅下方に4
つの外気導入口15が設けられている。対向する外気導
入口15,15同士はそれぞれ側壁7に沿って設けられ
た外気通路17によって連なっており、さらに各外気通
路17は加熱体12,12間の外気導入通路14に連通
している。尚、外気通路17は亜鉛鉄板、塩化ビニルラ
イニング鋼板、塩化ビニル板、ステンレス鋼板などで形
成することができる。
In the cooling tower 1 according to the second embodiment,
4 below the four corners of the side where the gas-liquid contact heat exchange part is provided
Two outside air inlets 15 are provided. The opposed outside air introduction ports 15 are connected to each other by an outside air passage 17 provided along the side wall 7, and each outside air passage 17 communicates with an outside air introduction passage 14 between the heating elements 12. The outside air passage 17 can be formed of a zinc iron plate, a vinyl chloride lining steel plate, a vinyl chloride plate, a stainless steel plate, or the like.

【0029】気液接触熱交換部は、外気通路17,17
間に設けられた気液接触熱交換部5Aと、外気通路17
の上方に設けられた気液接触熱交換部5Bから構成され
ており、気液接触熱交換部5Aは第1の実施の形態の場
合と同様に支床4から塔本体3の天板部8までの高さを
有している。
The gas-liquid contact heat exchanging section is connected to the outside air passages 17, 17.
The gas-liquid contact heat exchange section 5A provided between the
The gas-liquid contact heat exchanging section 5A is provided above the base plate 4 and the top plate section 8 of the tower main body 3 from the supporting floor 4 in the same manner as in the first embodiment. Up to the height.

【0030】この実施の形態の場合には、外気導入口1
5のダンパ16が開かれていると、外気導入口15から
流入した外気は、外気通路17から外気導入通路14に
流入し、加熱体12を通過するようになる。
In the case of this embodiment, the outside air inlet 1
When the damper 16 is opened, the outside air flowing from the outside air inlet 15 flows into the outside air introduction passage 14 from the outside air passage 17 and passes through the heating element 12.

【0031】この第2の実施の形態の冷却塔1において
も、第1の実施の形態の冷却塔1と同様の作用効果が得
られる。
In the cooling tower 1 of the second embodiment, the same operation and effect as those of the cooling tower 1 of the first embodiment can be obtained.

【0032】〔第3の実施の形態〕次に、第3の実施の
形態の冷却塔1について、図5及び図6に基いて説明す
る。尚、以下の第3の実施の形態の説明では、第1の実
施の形態の冷却塔1と同一態様部分には同一符号を付し
て説明を省略し、第1の実施の形態との相違点だけを説
明する。
Third Embodiment Next, a cooling tower 1 according to a third embodiment will be described with reference to FIGS. In the following description of the third embodiment, the same components as those of the cooling tower 1 of the first embodiment will be denoted by the same reference numerals, and description thereof will be omitted, and differences from the first embodiment will be omitted. Only points will be explained.

【0033】第3の実施の形態の冷却塔1においては、
外気導入口15が、気液接触熱交換部5,5の間であっ
て排気口10の両側に位置する天板部8に設けられてい
る。そして、空気通路9内に垂直に設けられた外気通路
18によって、外気導入口15は外気導入通路14に接
続されている。尚、外気通路18は亜鉛鉄板、塩化ビニ
ルライニング鋼板、塩化ビニル板、ステンレス鋼板など
で形成することができる。
In the cooling tower 1 according to the third embodiment,
An outside air inlet 15 is provided in the top plate 8 between the gas-liquid contact heat exchangers 5 and 5 and on both sides of the outlet 10. The outside air inlet 15 is connected to the outside air introduction passage 14 by an outside air passage 18 provided vertically in the air passage 9. The outside air passage 18 can be formed of a zinc iron plate, a vinyl chloride lining steel plate, a vinyl chloride plate, a stainless steel plate, or the like.

【0034】この実施の形態の場合には、外気導入口1
5のダンパ16が開かれていると、外気導入口15から
流入した外気は、外気通路18を下降して外気導入通路
14に流入し、加熱体12を通過するようになる。
In the case of this embodiment, the outside air inlet 1
When the damper 16 is opened, the outside air flowing from the outside air inlet 15 descends through the outside air passage 18, flows into the outside air introduction passage 14, and passes through the heating element 12.

【0035】この第3の実施の形態の冷却塔1において
も、第1の実施の形態の冷却塔1と同様の作用効果が得
られる。
In the cooling tower 1 of the third embodiment, the same operation and effect as those of the cooling tower 1 of the first embodiment can be obtained.

【0036】[0036]

【発明の効果】以上説明したように、本発明によれば、
塔上部に排気用ファンを有する排気口を設け、塔側部の
少なくとも一部に、塔側方から外気を流入しこの外気を
上方から散水される被冷却水と接触させて熱交換する気
液接触熱交換部を設け、前記排気口と前記気液接触熱交
換部との間に位置する塔内部の中空部を空気通路とした
直交流型冷却塔において、塔側部あるいは塔上部に外気
導入口を設け、前記中空部内に、空気と熱媒とを非接触
状態で熱交換させる加熱体と、前記外気導入口から導入
した外気を前記加熱体に導く外気導入通路とを設け、前
記気液接触熱交換部を通って加熱された外気と、前記外
気導入口から導入され前記加熱体を通って加熱された外
気を前記中空部で混合可能にしたので、排気の際の白煙
の発生を確実に防止することができ、しかも、塔高を低
く抑えることができる、冷却塔のコンパクト化やコスト
ダウンを達成することができる。
As described above, according to the present invention,
An exhaust port having an exhaust fan is provided at the top of the tower, and outside air flows into the tower side from at least a part of the tower side, and the outside air comes into contact with the water to be cooled sprayed from above to perform heat exchange. In a cross-flow cooling tower provided with a contact heat exchange section and having a hollow portion inside the tower located between the exhaust port and the gas-liquid contact heat exchange section as an air passage, outside air is introduced into the tower side or the top of the tower. A heating element for exchanging heat between the air and the heat medium in a non-contact state, and an outside air introduction passage for guiding outside air introduced from the outside air introduction port to the heating element, wherein the gas-liquid Since the outside air heated through the contact heat exchange section and the outside air introduced from the outside air introduction port and heated through the heating body can be mixed in the hollow portion, generation of white smoke at the time of exhaustion is reduced. Can be reliably prevented, and the tower height can be kept low. That it can achieve compactness and cost reduction of the cooling tower.

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

【図1】 本発明の直交流型冷却塔の第1の実施の形態
の縦断面図である。
FIG. 1 is a longitudinal sectional view of a first embodiment of a cross-flow cooling tower according to the present invention.

【図2】 上記第1の実施の形態の直交流型冷却塔の横
断面図である。
FIG. 2 is a cross-sectional view of the cross-flow cooling tower according to the first embodiment.

【図3】 本発明の直交流型冷却塔の第2の実施の形態
の縦断面図であり、図4においてI−I線に沿った図で
ある。
FIG. 3 is a longitudinal sectional view of a second embodiment of a cross-flow cooling tower according to the present invention, and is a view along the line II in FIG.

【図4】 上記第2の実施の形態の直交流型冷却塔の横
断面図である。
FIG. 4 is a cross-sectional view of the cross-flow cooling tower according to the second embodiment.

【図5】 本発明の直交流型冷却塔の第3の実施の形態
の縦断面図である。
FIG. 5 is a longitudinal sectional view of a third embodiment of a cross-flow cooling tower according to the present invention.

【図6】 上記第3の実施の形態の直交流型冷却塔の横
断面図である。
FIG. 6 is a cross-sectional view of the cross-flow cooling tower according to the third embodiment.

【図7】 従来の直交流型冷却塔の縦断面図である。FIG. 7 is a longitudinal sectional view of a conventional cross-flow cooling tower.

【符号の説明】[Explanation of symbols]

1 直交流型冷却塔 5 気液接触熱交換部 7 側壁 8 天板部 9 空気通路(中空部) 10 排気口 11 排気用ファン 12 加熱体 14 外気導入通路 15 外気導入口 DESCRIPTION OF SYMBOLS 1 Cross-flow cooling tower 5 Gas-liquid contact heat exchange part 7 Side wall 8 Top plate part 9 Air passage (hollow part) 10 Exhaust port 11 Exhaust fan 12 Heating body 14 Outside air introduction path 15 Outside air introduction port

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 塔上部に排気用ファンを有する排気口を
設け、塔側部の少なくとも一部に、塔側方から外気を流
入しこの外気を上方から散水される被冷却水と接触させ
て熱交換する気液接触熱交換部を設け、前記排気口と前
記気液接触熱交換部との間に位置する塔内部の中空部を
空気通路とした直交流型冷却塔において、 塔側部に、前記気液接触熱交換部とは別に外気導入口を
設け、 前記中空部内に、空気と熱媒とを非接触状態で熱交換さ
せる加熱体と、前記外気導入口から導入した外気を前記
加熱体に導く外気導入通路とを設け、 前記気液接触熱交換部を通って加熱された外気と、前記
外気導入口から導入され前記加熱体を通って加熱された
外気を前記中空部で混合可能にしたことを特徴とする直
交流型冷却塔。
An exhaust port having an exhaust fan is provided at an upper part of a tower, and outside air is introduced into at least a part of the tower side from a side of the tower, and the outside air is brought into contact with water to be cooled sprayed from above. In a cross-flow type cooling tower provided with a gas-liquid contact heat exchanging section for heat exchange and having a hollow portion inside the tower located between the exhaust port and the gas-liquid contact heat exchanging section as an air passage, An outside air introduction port is provided separately from the gas-liquid contact heat exchange section, and a heating element for exchanging heat between air and a heat medium in a non-contact state in the hollow portion; and heating the outside air introduced from the outside air introduction port to the heating section. Providing an outside air introduction passage leading to the body, and mixing the outside air heated through the gas-liquid contact heat exchange section with the outside air introduced from the outside air introduction port and heated through the heating body in the hollow portion; A cross-flow type cooling tower characterized in that:
【請求項2】 塔上部に排気用ファンを有する排気口を
設け、塔側部の少なくとも一部に、塔側方から外気を流
入しこの外気を上方から散水される被冷却水と接触させ
て熱交換する気液接触熱交換部を設け、前記排気口と前
記気液接触熱交換部との間に位置する塔内部の中空部を
空気通路とした直交流型冷却塔において、 塔上部に外気導入口を設け、 前記中空部内に、空気と熱媒とを非接触状態で熱交換さ
せる加熱体と、前記外気導入口から導入した外気を前記
加熱体に導く外気導入通路とを設け、 前記気液接触熱交換部を通って加熱された外気と、前記
外気導入口から導入され前記加熱体を通って加熱された
外気を前記中空部で混合可能にしたことを特徴とする直
交流型冷却塔。
2. An exhaust port having an exhaust fan is provided at the top of the tower, and outside air is introduced into at least a part of the tower side from the side of the tower, and the outside air is contacted with water to be cooled sprayed from above. In a cross-flow type cooling tower provided with a gas-liquid contact heat exchanging section for heat exchange and having a hollow portion inside the tower located between the exhaust port and the gas-liquid contact heat exchanging section as an air passage, An inlet is provided, a heating element for exchanging heat between the air and the heat medium in a non-contact state, and an external air introduction passage for guiding external air introduced from the external air inlet to the heating element are provided in the hollow portion. A cross-flow cooling tower characterized in that the outside air heated through the liquid contact heat exchange section and the outside air introduced from the outside air introduction port and heated through the heating body can be mixed in the hollow portion. .
JP33326097A 1997-12-03 1997-12-03 Crossflow cooling tower Pending JPH11166793A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33326097A JPH11166793A (en) 1997-12-03 1997-12-03 Crossflow cooling tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33326097A JPH11166793A (en) 1997-12-03 1997-12-03 Crossflow cooling tower

Publications (1)

Publication Number Publication Date
JPH11166793A true JPH11166793A (en) 1999-06-22

Family

ID=18264129

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33326097A Pending JPH11166793A (en) 1997-12-03 1997-12-03 Crossflow cooling tower

Country Status (1)

Country Link
JP (1) JPH11166793A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102103926B1 (en) * 2018-12-19 2020-04-23 주식회사 경인기계 Cooling tower of cross flow type for reducing white smoke
KR102350169B1 (en) * 2021-08-30 2022-01-17 한상신 Hybrid multi cooling tower for preventing plume

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102103926B1 (en) * 2018-12-19 2020-04-23 주식회사 경인기계 Cooling tower of cross flow type for reducing white smoke
KR102350169B1 (en) * 2021-08-30 2022-01-17 한상신 Hybrid multi cooling tower for preventing plume

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