JPH0587468A - White smoke pre ventive device and heat exchanger in cooling tower - Google Patents

White smoke pre ventive device and heat exchanger in cooling tower

Info

Publication number
JPH0587468A
JPH0587468A JP27678491A JP27678491A JPH0587468A JP H0587468 A JPH0587468 A JP H0587468A JP 27678491 A JP27678491 A JP 27678491A JP 27678491 A JP27678491 A JP 27678491A JP H0587468 A JPH0587468 A JP H0587468A
Authority
JP
Japan
Prior art keywords
heat exchanger
cooling tower
air
treated water
white smoke
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
JP27678491A
Other languages
Japanese (ja)
Inventor
Tsugio Yanagihara
次雄 柳原
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.)
Nihon Spindle Manufacturing Co Ltd
Original Assignee
Nihon Spindle Manufacturing 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 Nihon Spindle Manufacturing Co Ltd filed Critical Nihon Spindle Manufacturing Co Ltd
Priority to JP27678491A priority Critical patent/JPH0587468A/en
Publication of JPH0587468A publication Critical patent/JPH0587468A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the white smoke generated from a cooling tower. CONSTITUTION:Processed water that is to be cooled is poured from above to the filling materials 3 and 4 received in the tower body and the outside air is made to go through sideways and perpendicularly to the water. And dry type heat exchangers 13, 14 near the inside of the filling materials 3, 4 that are behind the air flow are provided, keeping the warm water to be cooled and the outside air from making contact mutually. The processed water is supplied to the dry type heat exchangers 13, 14 when the outside temperature falls below the temperature at which the white smoke is generated and the air that passes through the filling materials 3, 4 is heated. All the air passing through the filling materials 3, 4 goes through the dry type heat exchangers 13, 14 and they can heat the air uniformly.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、塔体内に収納した充填
材に上方から冷却すべき処理水を供給し、外部空気を直
交して通過させるクロスフロー形クーリングタワーにお
ける白煙防止装置及び熱交換器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a white smoke prevention device and heat exchange in a cross-flow type cooling tower in which treated water to be cooled is supplied from above to a packing material contained in a tower body and external air is allowed to pass through at right angles. It is related to vessels.

【0002】[0002]

【従来の技術】一般にクーリングタワーにおいて、充填
材表面において処理水と外部空気とを直接接触する湿式
熱交換器は熱交換率が良好であるが、吸気ファンから排
出される排気は湿度が高く、外気温度が高い夏期におい
ては問題はないが、冬季等外気温度が低いときには湿度
が飽和状態に達し白煙となって排出され、問題がある。
このため種々の白煙防止手段が試みられており、その一
例を図7に示す。
2. Description of the Related Art Generally, in a cooling tower, a wet heat exchanger in which treated water and external air are in direct contact with each other on the surface of a filler has a good heat exchange rate, but the exhaust gas discharged from an intake fan has a high humidity and the outside air There is no problem in the summer when the temperature is high, but when the outside temperature is low such as in winter, the humidity reaches a saturated state and is emitted as white smoke, which is a problem.
For this reason, various white smoke preventing means have been tried, and one example thereof is shown in FIG.

【0003】このクーリングタワー50は左右の熱交換
器51,52をそれぞれ上下に区分して上部熱交換器5
1a,52a、下部熱交換器51b,52bとし、上部
熱交換器は処理水と外気とが直接接触しない例えばパイ
プ方式のクローズド式熱交換器とし、下部熱交換器は熱
交換率が良好な充填材による処理水と外部空気とが直接
接触する湿式熱交換器とする。冬期には処理水は開閉弁
53を開き、上下の両充填材に供給して冷却する。
In this cooling tower 50, left and right heat exchangers 51 and 52 are divided into upper and lower parts, respectively, and an upper heat exchanger 5 is provided.
1a, 52a, lower heat exchangers 51b, 52b, the upper heat exchanger is a pipe type closed heat exchanger in which treated water does not come into direct contact with the outside air, and the lower heat exchanger is filled with a good heat exchange rate. A wet heat exchanger in which the treated water from the material and the external air come into direct contact. In winter, the treated water opens the on-off valve 53 and is supplied to both upper and lower fillers to be cooled.

【0004】この方式によるときは、図8に示す如く曲
線ψを飽和曲線とすると、外気の温湿度をa、下部充填
材を通過したときの温湿度をb(但し湿度は飽和状態と
し、従って飽和曲線上にある)とすると、線分abは飽
和曲線ψから上方に位置し、この分が白煙となる。この
とき同時に上部乾式熱交換器を通過した空気の温湿度を
dとすると、この空気湿度は外気湿度で低く、従って両
者が混合し排気ファン54から排出される排気の温湿度
は線分bd上の点eとなり、これにより線分aeは飽和
曲線ψの下方に位置し、白煙の発生が防止される。
In the case of this system, when the curve ψ is a saturation curve as shown in FIG. 8, the temperature and humidity of the outside air are a, and the temperature and humidity when passing through the lower filler are b (however, the humidity is in a saturated state. (Above the saturation curve), the line segment ab is located above the saturation curve ψ, and this portion becomes white smoke. At this time, if the temperature and humidity of the air that has passed through the upper dry heat exchanger is d at the same time, this air humidity is low in the outside air humidity, and therefore the temperature and humidity of the exhaust gas mixed and discharged from the exhaust fan 54 is on the line segment bd. The line segment ae is located below the saturation curve ψ, and the generation of white smoke is prevented.

【0005】[0005]

【発明が解決しようとする課題】しかしこの方式による
ときは、上下の熱交換器を通過した空気を充分に混合す
ることは困難で、白煙発生を確実に防止することはでき
ず、しかも上下2段の熱交換器を設けることは装置の高
さが大となる等の問題がある。
However, with this method, it is difficult to sufficiently mix the air that has passed through the upper and lower heat exchangers, and it is not possible to reliably prevent the generation of white smoke. Providing the two-stage heat exchanger has a problem that the height of the apparatus becomes large.

【0006】本発明は上記の点に鑑みてなされたもの
で、熱交換器として熱交換率良好な充填材を用い、かつ
上下に分割することなく、冬季においても白煙の発生を
防止するクーリングタワーを提供することを目的とす
る。また他の発明は熱交換器として伝熱面積が大きく、
かつ厚みを薄くできるフィルム状のシートを用い、処理
水と外部空気とを接触させることなく、しかも良好な熱
交換率を有する熱交換器を提供することを目的とする。
The present invention has been made in view of the above points, and a cooling tower which uses a filler having a good heat exchange rate as a heat exchanger and which does not divide into upper and lower parts to prevent generation of white smoke even in winter. The purpose is to provide. Another invention has a large heat transfer area as a heat exchanger,
An object of the present invention is to provide a heat exchanger that uses a film-like sheet that can be made thin and does not bring treated water into contact with external air and has a good heat exchange rate.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
の本発明は、上記クロスフロー形クーリングタワーにお
いて、上記充填材の空気流通後方の内側に近接して冷却
すべき温水と外部空気とを非接触とした乾式の熱交換器
を配備し、該乾式熱交換器へ処理水を選択供給するよう
にしたものである。
According to the present invention for achieving the above object, in the cross flow type cooling tower, the hot water and the external air to be cooled are provided in the vicinity of the inner side of the air circulation rear side of the filler. A dry heat exchanger in contact is provided, and treated water is selectively supplied to the dry heat exchanger.

【0008】また第2の発明は、上記乾式熱交換器への
給水回路には開閉弁を備え、クーリングタワーの処理済
液の温度測定用センサまたは外気温・湿度センサによる
測定温度により上記開閉弁の開閉操作を行い、処理水を
選択して乾式熱交換器に供給するようにしたものであ
る。
According to a second aspect of the invention, an on-off valve is provided in the water supply circuit to the dry heat exchanger, and the on-off valve of the on-off valve is controlled according to the temperature measured by the temperature measuring sensor for the treated liquid in the cooling tower or the ambient temperature / humidity sensor. By opening and closing, the treated water is selected and supplied to the dry heat exchanger.

【0009】また第3の発明は、上記乾式熱交換器は、
多数の隔板を微小間隙を存して垂直状に配置し、その間
隙を交互にその上下端及び前後段を閉塞し、前後端を開
放した間隙を空気流通通路、上下端を開放した間隙を処
理水流通通路とし、かつ各隔板は薄膜状の可塑性材料を
以て構成したものである。
According to a third invention, the dry heat exchanger is
A large number of partition plates are arranged vertically with a minute gap, and the gaps are alternately closed by closing the upper and lower ends and the front and rear stages, and the gap with the front and rear ends opened is the air circulation passage, and the gap with the upper and lower ends opened. The treated water flow passage is used, and each partition plate is made of a thin film plastic material.

【0010】[0010]

【作用】冬季等外気温度が低下し白煙を発生するおそれ
のあるときは、乾式熱交換器に処理水を供給する。これ
により充填材を通過した空気はすべて乾式熱交換器を通
過して均等に斑なく加熱され、従って湿度は低下し飽和
曲線以下となり、これにより白煙の発生を防止すること
ができる。また乾式熱交換器は処理水と冷却空気とを直
接接触することなく冷却を行うようにしたもので、冷却
空気は処理水と直交して隔壁の裏側を流通して隔壁を冷
却する。即ち処理水は隔壁を介して冷却される。この
際、隔壁は薄膜状の可塑性材料を以て構成することによ
り熱伝導効率は良好である。
[Function] When there is a possibility that white smoke is generated due to a decrease in outside air temperature such as in winter, treated water is supplied to the dry heat exchanger. As a result, all the air that has passed through the filler passes through the dry heat exchanger and is uniformly and uniformly heated. Therefore, the humidity is lowered and becomes lower than the saturation curve, so that the generation of white smoke can be prevented. The dry heat exchanger is designed to cool the treated water without directly contacting the cooling air, and the cooling air is orthogonal to the treated water and flows through the back side of the partition wall to cool the partition wall. That is, the treated water is cooled via the partition wall. At this time, since the partition wall is made of a thin film plastic material, the heat conduction efficiency is good.

【0011】[0011]

【実施例】図1乃至図6は本発明の実施例を示す。この
クーリングタワー1は塔体2内の左右に充填材3,4を
配備し、その上方には加湿された処理水を充填材に均一
に散布すべく下面に多数の散水孔を穿設した散水樋5,
6を設け、塔体中央上部には排気通路7が形成され、そ
の排気通路7内には排気ファン8が配備される。9は塔
体側部に開口された空気取り入れ口で周知の如く多数の
ルーパ10が取り付けられている。11は塔体下部に設
けられる貯水槽である。
1 to 6 show an embodiment of the present invention. This cooling tower 1 is provided with fillers 3 and 4 on the left and right sides in a tower body 2, and above the sprinkler gutter having a large number of sprinkling holes on its lower surface for uniformly spraying the treated water to the filler. 5,
6, an exhaust passage 7 is formed in the upper center of the tower body, and an exhaust fan 8 is arranged in the exhaust passage 7. Reference numeral 9 denotes an air intake port opened on the side of the tower body, to which a large number of loopers 10 are attached as is well known. Reference numeral 11 is a water storage tank provided at the bottom of the tower.

【0012】12は白煙防止装置であり、上記充填材
3,4の後方、すなわち充填材の空気流通の後方側に設
けられる乾式熱交換器13,14と、それぞれの熱交換
器上方に配備される処理水散水樋15,16を備える。
Numeral 12 is a white smoke prevention device, which is provided behind the fillers 3 and 4, that is, on the rear side of the filler in the air flow direction, and dry heat exchangers 13 and 14, and above the respective heat exchangers. The treated water sprinkling gutters 15 and 16 are provided.

【0013】この乾式熱交換器13,14は処理水と外
気とは直接接触することなく冷却を行うようにしたもの
で、左右の熱交換器13,14は同一構造であり、以下
一方の熱交換器13について説明する。この熱交換器1
3は対をなし微小間隔を存して対向する2枚の隔板20
a,20b(以下総称するときは単に20という)を以
てする単位素子3aを多数並列に設けてなり、それぞれ
の隔板20は薄膜状の可塑性材料を以て構成し、かつ空
気の流通方向と平行に並列し、各隔板20の上下端は外
方に拡開し、前後両端は全長に亘って反対に内方に屈曲
して上下端面、前後端面をそれぞれ接合面a,bとし、
2枚の隔板20a,20bの前後端面b,bを接合して
処理水の流通通路22を形成する。
The dry heat exchangers 13 and 14 are designed to cool the treated water without directly contacting the outside air. The left and right heat exchangers 13 and 14 have the same structure. The exchanger 13 will be described. This heat exchanger 1
Numeral 3 is a pair of two partition plates 20 that face each other with a minute gap.
a, 20b (hereinafter, simply referred to as 20 when collectively referred to) are provided in parallel, and each partition plate 20 is made of a thin film plastic material and is parallel to the air flow direction. Then, the upper and lower ends of each partition plate 20 are expanded outward, and the front and rear ends are bent inward in the opposite direction over the entire length, and the upper and lower end faces and the front and rear end faces are joined faces a and b, respectively.
The front and rear end faces b, b of the two partition plates 20a, 20b are joined to form a flow passage 22 for the treated water.

【0014】また、隣接する単位素子3aの相互間は上
下端の接合面a,aを接合して単位素子3a,3a間の
間隙を空気流通通路21とし、各隔板20は処理水の落
下に抵抗を付すとともに接触面積の増大を計るため、垂
直断面を波状に屈曲した屈曲部23を形成するとともに
水平方向には微細模様の山形のジグザグ部24を形成し
て処理水の水平方向への分配と滞留を向上せしめる。
Between adjacent unit elements 3a, upper and lower joint surfaces a, a are joined to form a gap between the unit elements 3a, 3a as an air passage 21, and each partition plate 20 drops treated water. In order to increase the contact area and the resistance to, the bent portion 23 in which the vertical cross section is bent in a wave shape is formed, and the zigzag portion 24 having a fine pattern in the horizontal direction is formed in the horizontal direction so that the treated water extends in the horizontal direction. Improves distribution and retention.

【0015】上記構成において、散水樋15,16から
供給される加湿された処理水Wは、熱交換器13,14
の処理液流通通路22に流入し、各隔板20に形成した
波状の屈曲部23及び山形のジグザグ部24により図6
において矢符Pに示す如く対向する隔板側に移行し、隔
板の表面を伝って落下する。一方冷却空気は空気流通通
路22を通って上記処理液とは直交してクーリングタワ
ー内方に吸引される。これにより処理液により加熱され
た隔板20は冷却空気により冷却される。すなわち処理
液は隔板を介して冷却空気により冷却される。この場合
隔板20は薄膜状の可塑性材料を以て構成されるから、
フィルム状で伝熱シート厚みを深くできるため伝熱面積
を大きくとれ熱交換効率を向上せしめることが可能とな
った。
In the above structure, the humidified treated water W supplied from the sprinkling gutters 15 and 16 is the heat exchangers 13 and 14.
6 through the corrugated bent portions 23 and the chevron-shaped zigzag portions 24 formed in each partition plate 20.
At the point of, the arrow moves to the opposing partition plate side as indicated by the arrow P, and falls along the surface of the partition plate. On the other hand, the cooling air is sucked into the cooling tower through the air passage 22 at right angles to the processing liquid. Thereby, the partition plate 20 heated by the processing liquid is cooled by the cooling air. That is, the treatment liquid is cooled by the cooling air through the partition plate. In this case, since the partition plate 20 is made of a thin film plastic material,
Since the heat transfer sheet can be made thicker in the form of a film, it is possible to increase the heat transfer area and improve heat exchange efficiency.

【0016】なお散水樋15,16は周知構造と同様に
下面に多数の散水孔を穿孔したもので、図例は充填材
3,4に対する散水樋5,6と一体に形成し、仕切り壁
25,26により区画した例を示したが、これは別個に
設けるようにしてもよい。
The water sprinkling gutters 15 and 16 have a plurality of water sprinkling holes formed on the lower surface similarly to the well-known structure. In the illustrated example, the water spouting gutters 5 and 6 for the fillers 3 and 4 are integrally formed with the partition wall 25. , 26 is shown as an example of partitioning, but this may be provided separately.

【0017】また30,31は処理水供給回路32に設
けた電動式開閉弁で、貯水槽11から排出される冷却液
の水温測定用温度センサ33により作動されるものであ
り、また必要により設けられた外気温・湿度センサによ
って作動させてもよい。上記開閉弁30,31は常時は
閉塞し、貯水槽11から排出される冷却された液温ある
いは冬期で外気温・湿度が所定温度以下に低下したと
き、すなわち夏期設計外気温度以下に低下したとき、こ
れを開路し、乾式熱交換器13,14に給水するように
するものである。図中34,35はオーバフロー管であ
り、乾式熱交換器への給水に当たり、所定の水負荷以上
にならないように散水槽の液の深さを規制しオーバフロ
ーさせるものである。
Further, reference numerals 30 and 31 designate electric open / close valves provided in the treated water supply circuit 32, which are operated by a temperature sensor 33 for measuring the water temperature of the cooling liquid discharged from the water storage tank 11, and are also provided if necessary. It may be operated by an external air temperature / humidity sensor provided. The on-off valves 30 and 31 are normally closed, and when the temperature of the cooled liquid discharged from the water storage tank 11 or the outside air temperature / humidity drops below a predetermined temperature in winter, that is, below the summer design outside air temperature. This is opened to supply water to the dry heat exchangers 13 and 14. In the figure, reference numerals 34 and 35 are overflow pipes which, when supplying water to the dry heat exchanger, regulate the depth of the liquid in the sprinkler tank so that the water does not exceed a predetermined water load and overflow.

【0018】上記構成において、厳寒時において外気温
度が低下し図5において外気温湿度をa点とし、充填材
を通過した空気は熱交換により温度は上昇するが多量の
水分が含まれる。充填材を通過した空気の温湿度をb点
とする。この点は前述の如く水分は飽和状態とすると飽
和曲線ψ上にあり、従って線分abは飽和曲線ψを越え
た状態にあり、白煙を発生する。このときには乾式熱交
換器13,14に処理水を供給することにより、この熱
交換器を通過した空気は、温度は高められるが湿度は低
下している。この点をc点とすると、線分bcは飽和曲
線ψ以下となり、白煙の発生を防止することができる。
In the above structure, the outside air temperature is lowered in a severe cold, the outside air temperature humidity is set to point a in FIG. 5, and the temperature of the air passing through the filler is increased by heat exchange, but a large amount of water is contained. The point b is the temperature and humidity of the air that has passed through the filler. This point is on the saturation curve ψ when the water content is saturated as described above, and therefore the line segment ab exceeds the saturation curve ψ to generate white smoke. At this time, by supplying treated water to the dry heat exchangers 13 and 14, the temperature of the air passing through the heat exchangers is raised but the humidity thereof is lowered. If this point is set as point c, the line segment bc becomes equal to or less than the saturation curve ψ, and white smoke can be prevented from being generated.

【0019】なお、外気温度が比較的高く白煙の発生の
おそれのないときは乾式熱交換器への給水は継続しても
差し支えはないが、熱交換率の良好な充填材側で行うの
が好ましく、通常は停止する。夜間及び冬期で外気温度
が低下したとき、貯水槽11からの排水の温度は低下す
る。温度センサ33または外気温・湿度センサはこれを
検知し、所定温度以下に低下したときは電動式開閉弁3
0,31を作動し、該弁を開き乾式熱交換器13,14
への給水を開始する。これにより白煙の発生の防止を計
ることができる。
When the outside air temperature is relatively high and white smoke is not likely to occur, the water supply to the dry heat exchanger may be continued, but it is performed on the filler side having a good heat exchange rate. Is preferred and usually stopped. When the outside air temperature drops at night and in winter, the temperature of the drainage water from the water storage tank 11 drops. The temperature sensor 33 or the outside air temperature / humidity sensor detects this, and when the temperature falls below a predetermined temperature, the electrically operated on-off valve 3
0, 31 is operated and the valve is opened to dry heat exchangers 13, 14
To supply water to. This can prevent the generation of white smoke.

【0020】[0020]

【発明の効果】以上の如く第1の本発明によるときは、
熱交換率の高い充填材による湿式熱交換器の後方に近接
して乾式熱交換器を配備したから、充填材を通過した空
気はすべて乾式熱交換器を通過するから、均一に温度を
上昇させることができる。従って、排気湿度は飽和湿度
以下となり、白煙の発生を確実に防止することができ
る。この際、乾式熱交換器へは処理水を供給するように
したから、処理水の温度低下を乾式熱交換器によっても
行うことができ効果的である。また乾式熱交換器は湿式
熱交換器の内側に設けたから、塔体は従来と同一の高さ
とすることができる。
As described above, according to the first aspect of the present invention,
Since the dry heat exchanger is placed close to the rear of the wet heat exchanger with the filler having a high heat exchange rate, all the air that has passed through the filler passes through the dry heat exchanger, so the temperature rises uniformly. be able to. Therefore, the exhaust humidity becomes equal to or lower than the saturation humidity, and the generation of white smoke can be reliably prevented. At this time, since the treated water is supplied to the dry heat exchanger, it is effective that the temperature of the treated water can be lowered also by the dry heat exchanger. Further, since the dry heat exchanger is provided inside the wet heat exchanger, the tower body can have the same height as the conventional one.

【0021】また第2の発明によるときは上記乾式熱交
換器の給水回路には開閉弁を設け、貯水槽からの処理済
液の温度を測定しあるいは外気温・湿度が設定以下に降
下したとき、上記開閉弁を開き乾式熱交換器に温度の高
い処理水を供給するようにしたから、白煙の防止を自動
的に行うことができる。
According to the second aspect of the invention, an on-off valve is provided in the water supply circuit of the dry heat exchanger to measure the temperature of the treated liquid from the water storage tank or when the outside air temperature / humidity falls below a set value. Since the on-off valve is opened to supply the high-temperature treated water to the dry heat exchanger, white smoke can be automatically prevented.

【0022】また第3の発明によるときは、上記乾式熱
交換器は多数の隔板を微小間隙を存して垂直状に配置
し、その間隙を交互に空気流通通路、処理水流通通路と
し、かつ各隔板は垂直断面を波状に屈曲したから、構造
簡単でしかも熱交換率の向上を計ることができる。また
上記隔板は薄膜状材料を以て構成したから、熱伝導は良
好であり、かつ熱交換器は板状の隔板を微小間隔を存し
て多数並列して構成されており、これにより限定された
取付空間に隔板を多数収納することができ熱伝導面積は
増大し、熱交換効率の向上を計ることができる。
According to the third aspect of the invention, in the dry heat exchanger, a large number of partition plates are arranged vertically with a minute gap, and the gap is alternately used as an air passage and a treated water passage, In addition, since each partition plate has a vertical cross section bent in a wavy shape, the structure is simple and the heat exchange rate can be improved. Further, since the partition plate is made of a thin film material, the heat conduction is good, and the heat exchanger is composed of a large number of plate-shaped partition plates arranged in parallel with each other at a minute interval. Since a large number of partition plates can be accommodated in the mounting space, the heat transfer area can be increased and the heat exchange efficiency can be improved.

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

【図1】第1実施例の縦断説明図である。FIG. 1 is a vertical cross sectional explanatory view of a first embodiment.

【図2】乾式熱交換器における隔板の組立要領説明図で
ある。
FIG. 2 is an explanatory diagram of a method of assembling a partition plate in a dry heat exchanger.

【図3】乾式熱交換器の縦断面図である。FIG. 3 is a vertical cross-sectional view of a dry heat exchanger.

【図4】乾式熱交換器の平面図である。FIG. 4 is a plan view of a dry heat exchanger.

【図5】本発明の作用説明図である。FIG. 5 is an explanatory view of the operation of the present invention.

【図6】乾式熱交換器の単位素子の正面図である。FIG. 6 is a front view of a unit element of a dry heat exchanger.

【図7】従来例のクーリングタワーの縦断説明図であ
る。
FIG. 7 is a vertical cross-sectional explanatory view of a cooling tower of a conventional example.

【図8】従来例の作用説明図である。FIG. 8 is an operation explanatory view of a conventional example.

【符号の説明】[Explanation of symbols]

1 クーリングタワー 3 充填材 4 充填材 12 白煙防止装置 13 乾式熱交換器 14 乾式熱交換器 20 隔板 21 空気流通間隙 22 処理水流通間隙 23 屈曲部 24 ジグザグ部 30 開閉弁 31 開閉弁 32 処理水回路 33 温度センサ 1 Cooling Tower 3 Filling Material 4 Filling Material 12 White Smoke Prevention Device 13 Dry Heat Exchanger 14 Dry Heat Exchanger 20 Separator 21 Air Flow Gap 22 Treated Water Flow Gap 23 Bent Part 24 Zig Zag 30 Open / Close Valve 31 Open / Close Valve 32 Treated Water Circuit 33 Temperature sensor

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 塔体内に収納する充填材に上方から冷却
すべき処理水を供給し、側方から外部空気を直交して通
過させるクロスフロー形クーリングタワーにおいて、上
記充填材の空気流通後方の内側に近接して冷却すべき温
水と外部空気とを非接触とした乾式の熱交換器を配備
し、該乾式熱交換器へ処理水を選択供給することを特徴
とするクーリングタワーにおける白煙防止装置。
1. A cross-flow type cooling tower in which treated water to be cooled is supplied from above to a packing material contained in a tower body and external air is allowed to pass from the side in a direction orthogonal to the inside of the packing material in the air circulation rear side. A white smoke prevention device in a cooling tower, characterized in that a dry heat exchanger in which hot water to be cooled and external air are not in contact with each other is provided, and treated water is selectively supplied to the dry heat exchanger.
【請求項2】 乾式熱交換器への給水回路には開閉弁を
備え、クーリングタワーの処理済液の温度測定用センサ
または外気温・湿度センサによる測定温度により上記開
閉弁の開度操作を行うことを特徴とする請求項1記載の
クーリングタワーにおける白煙防止装置。
2. A water supply circuit to the dry heat exchanger is provided with an on-off valve, and the opening degree of the on-off valve is controlled by a temperature measuring sensor for the treated liquid in the cooling tower or a temperature measured by an outside air temperature / humidity sensor. The white smoke prevention device in the cooling tower according to claim 1.
【請求項3】 塔体内に収納する充填材に上方から冷却
すべき処理水を供給し、外部空気を側方から直交して通
過させるクロスフロー形クーリングタワーの熱交換器に
おいて、多数の隔板を微小間隙を存して垂直状かつ外部
空気流通方向と平行に配置してなり、それぞれの間隙を
交互にその上下端及び前後端を閉塞し、前後端を開放し
た間隙を空気流通通路、上下端を開放した間隙を処理水
流通通路とし、かつ上記隔板は薄膜状の可塑性の材料を
以て構成し、垂直断面を波状に屈曲したことを特徴とす
るクーリングタワーにおける熱交換器。
3. A heat exchanger of a cross-flow type cooling tower in which treated water to be cooled is supplied from above to a packing material contained in a tower body, and external air is allowed to pass through from a lateral direction so that a large number of partition plates are provided. It is arranged vertically with a minute gap and parallel to the external air circulation direction. Each gap is alternately closed at the upper and lower ends and front and rear ends, and the gap with the front and rear ends opened is the air circulation passage and the upper and lower ends. A heat exchanger in a cooling tower, wherein the open space is used as a treated water flow passage, the partition plate is made of a thin film plastic material, and the vertical cross section is bent in a wave shape.
JP27678491A 1991-09-27 1991-09-27 White smoke pre ventive device and heat exchanger in cooling tower Pending JPH0587468A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27678491A JPH0587468A (en) 1991-09-27 1991-09-27 White smoke pre ventive device and heat exchanger in cooling tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27678491A JPH0587468A (en) 1991-09-27 1991-09-27 White smoke pre ventive device and heat exchanger in cooling tower

Publications (1)

Publication Number Publication Date
JPH0587468A true JPH0587468A (en) 1993-04-06

Family

ID=17574326

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27678491A Pending JPH0587468A (en) 1991-09-27 1991-09-27 White smoke pre ventive device and heat exchanger in cooling tower

Country Status (1)

Country Link
JP (1) JPH0587468A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07280464A (en) * 1994-04-08 1995-10-27 Hitachi Air Conditioning & Refrig Co Ltd White fuming preventing apparatus for sealed cooling tower
JPH08261666A (en) * 1995-03-28 1996-10-11 Nippon Spindle Mfg Co Ltd Control method and apparatus to prevent white fuming of cooling tower
JP2001082882A (en) * 1999-09-09 2001-03-30 Ishikawajima Harima Heavy Ind Co Ltd Cold water tower
US7614613B2 (en) * 2007-05-04 2009-11-10 Equistar Chemicals, Lp Method of operating a cooling fluid system
JP2010084950A (en) * 2008-09-29 2010-04-15 Nippon Spindle Mfg Co Ltd Cooling tower
JP2011099624A (en) * 2009-11-06 2011-05-19 Kobelco Eco-Solutions Co Ltd Cooling tower
CN108662917A (en) * 2018-06-04 2018-10-16 栋梁铝业有限公司 A kind of closed cooling tower

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59134444A (en) * 1983-01-20 1984-08-02 Matsushita Electric Ind Co Ltd Electric water heater
JPS6081959A (en) * 1983-10-12 1985-05-10 Canon Inc Picture processing system
JPS6185920A (en) * 1984-10-03 1986-05-01 株式会社 ニデツク Apparatus for measuring cornea shape

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59134444A (en) * 1983-01-20 1984-08-02 Matsushita Electric Ind Co Ltd Electric water heater
JPS6081959A (en) * 1983-10-12 1985-05-10 Canon Inc Picture processing system
JPS6185920A (en) * 1984-10-03 1986-05-01 株式会社 ニデツク Apparatus for measuring cornea shape

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07280464A (en) * 1994-04-08 1995-10-27 Hitachi Air Conditioning & Refrig Co Ltd White fuming preventing apparatus for sealed cooling tower
JPH08261666A (en) * 1995-03-28 1996-10-11 Nippon Spindle Mfg Co Ltd Control method and apparatus to prevent white fuming of cooling tower
JP2001082882A (en) * 1999-09-09 2001-03-30 Ishikawajima Harima Heavy Ind Co Ltd Cold water tower
US7614613B2 (en) * 2007-05-04 2009-11-10 Equistar Chemicals, Lp Method of operating a cooling fluid system
JP2010084950A (en) * 2008-09-29 2010-04-15 Nippon Spindle Mfg Co Ltd Cooling tower
JP2011099624A (en) * 2009-11-06 2011-05-19 Kobelco Eco-Solutions Co Ltd Cooling tower
CN108662917A (en) * 2018-06-04 2018-10-16 栋梁铝业有限公司 A kind of closed cooling tower

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