JPH0429243Y2 - - Google Patents

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Publication number
JPH0429243Y2
JPH0429243Y2 JP1986085920U JP8592086U JPH0429243Y2 JP H0429243 Y2 JPH0429243 Y2 JP H0429243Y2 JP 1986085920 U JP1986085920 U JP 1986085920U JP 8592086 U JP8592086 U JP 8592086U JP H0429243 Y2 JPH0429243 Y2 JP H0429243Y2
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JP
Japan
Prior art keywords
air
hot water
flow
cooling tower
heat exchanger
Prior art date
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Expired
Application number
JP1986085920U
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Japanese (ja)
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JPS62198367U (en
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Publication of JPS62198367U publication Critical patent/JPS62198367U/ja
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Description

【考案の詳細な説明】 イ 考案の目的 (産業上の利用分野) この考案は直交流式冷却塔に使用される熱交換
器に関する。
[Detailed description of the invention] A. Purpose of the invention (industrial application field) This invention relates to a heat exchanger used in a cross-flow cooling tower.

(従来の技術) この種冷却塔から排出される空気は、高温多湿
であつて、冬期のように外気温の低い時には、排
気される空気中の湿気は凝固し、白煙状態となつ
て排気口より排出される。
(Prior art) The air discharged from this type of cooling tower is hot and humid, and when the outside temperature is low, such as in winter, the moisture in the exhausted air solidifies and becomes white smoke when it is exhausted. Excreted from the mouth.

この白煙の発生を防止する従来技術として、排
出空気に高温乾燥空気を混合させ、減湿と排気温
度の上昇を計つた冷却塔が、特公昭59−16200号
公報、特公昭60−45798号公報及び特開昭60−
82780号公報に各々記載されている。
As a conventional technology to prevent the generation of white smoke, a cooling tower that mixes high temperature dry air with exhaust air to reduce humidity and increase the exhaust temperature is disclosed in Japanese Patent Publication No. 59-16200 and Japanese Patent Publication No. 60-45798. Official gazette and Japanese Patent Application Publication 1986-
Each is described in Publication No. 82780.

前記3つの公知例のうち、第1番目の公報記載
の冷却塔においては、充填材間の全ての間隙に外
気が流通し、一つおきの間隙に被冷却水分配器に
より冷却水を供給し濡れ壁を形成し、充填材間の
吐出口より、乾燥予熱された空気流と、多湿の空
気流がほゞ一対一の割合で吐出するため、冬期に
おいて全充填材を被冷却水の冷却に有効に使用す
ることができず、通常の直交流式冷却塔が常備し
ている上部水槽に代えて、特殊構造の前記被冷却
水分配器を必要とし、冷却塔全体としての熱交換
性能が低下し、その構造が複雑すると共に、前記
2種の空気流を均一に混合し難い。
Of the three known examples above, in the cooling tower described in the first publication, outside air flows through all the gaps between the packing materials, and cooling water is supplied to every other gap by a cooled water distributor to keep them wet. Since the dry preheated air flow and the humid air flow are discharged from the outlet between the fillers in a nearly one-to-one ratio, all the fillers are effective in cooling the water to be cooled in winter. The cooling tower cannot be used as a cooling tower, and requires a specially constructed water distribution device to be cooled in place of the upper water tank that is normally provided in a normal cross-flow cooling tower, which reduces the heat exchange performance of the cooling tower as a whole. The structure is complicated, and it is difficult to mix the two types of air flows uniformly.

また、第2番目公報記載の冷却塔においては、
充填材に何ら手を加えず、冷却塔排気通路に主ダ
クトと分岐ダクトからなる高温乾燥空気分配機構
を配備し、この分配機構の主ダクトを高温乾燥空
気発生装置に連結し、冬期における白煙の発生を
防止しており、通常の直交流式冷却塔の他に高温
乾燥空気発生装置と、前記分配機構を別途配備し
なければならず全体として大型となり、占有面積
が拡大する。
In addition, in the cooling tower described in the second publication,
A high-temperature dry air distribution mechanism consisting of a main duct and branch ducts is installed in the cooling tower exhaust passage without any modification to the filler, and the main duct of this distribution mechanism is connected to a high-temperature dry air generator to reduce white smoke in winter. In addition to the normal cross-flow type cooling tower, a high-temperature dry air generator and the above-mentioned distribution mechanism must be separately provided, resulting in a larger overall size and an increased occupied area.

第3番目公報記載の気液間接接触型の熱交換器
は徒に構造が複雑で、かつ、外気流通路の断面積
が狭く、熱交換効率が低いものであつた。
The gas-liquid indirect contact type heat exchanger described in the third publication had an unnecessarily complicated structure, and the cross-sectional area of the outside air passage was narrow, resulting in low heat exchange efficiency.

ロ 考案の構成 (課題を解決するための手段) この考案は、上部水槽とこの真下に位置する充
填材間に装填自在の直交流式冷却塔用の気液間接
接触型の熱交換器において、 充填材間を通る空気流れ方向とほゞ平行な空気
専用流路が、多数並列してトンネル状に貫通して
形成してあり、隣接する空気専用流路間には、狭
幅の温水流下専用通路が非透水性で熱交換自在の
壁板で仕切られて形成してあり、これら温水流下
専用通路の空気流れ方向の両端は閉塞してあると
共に、温水流下専用通路の上端は、上部水槽から
流下する温水の流入口としてあり、その下端は、
前記充填材への温水の散水口としてあり、前記温
水流下通路専用通路の狭幅とは、空気専用流路の
幅の2分の1乃至3分の1寸法としてあることを
特徴とする直交流式冷却塔用の熱交換器とする。
B. Structure of the invention (means for solving the problem) This invention is a gas-liquid indirect contact heat exchanger for a cross-flow cooling tower that can be freely loaded between an upper water tank and a filler located directly below it. A large number of air-only channels, which are approximately parallel to the air flow direction passing between the fillers, are formed in parallel to form a tunnel-like structure. The passages are partitioned with water-impermeable wall plates that allow for free heat exchange.Both ends of these hot water flow passages in the air flow direction are closed, and the upper ends of the hot water flow passages are separated from the upper water tank. It serves as an inlet for flowing hot water, and its lower end is
The cross flow is provided as a sprinkling port for hot water to the filling material, and the narrow width of the dedicated hot water flow path is 1/2 to 1/3 of the width of the air dedicated flow path. This is a heat exchanger for type cooling towers.

(作用) 前記構成の本件考案である熱交換器の作用をそ
の使用方法と共に次に説明する。
(Function) The function of the heat exchanger of the present invention having the above structure will be explained below along with its usage method.

既存の直交流式冷却塔における上部水槽と、充
填材の間にこの熱交換器を、前記空気専用流路の
吐出口が冷却塔排気通路内に開口し、その吸入口
が冷却塔外気取入口に向く状態で組み付ける。
This heat exchanger is installed between the upper water tank and the filler in an existing cross-flow type cooling tower, and the discharge port of the air-only flow path opens into the cooling tower exhaust passage, and the inlet port opens into the cooling tower outside air intake. Assemble it so that it is facing.

前記上部水槽内の温水は、その底部に設けた小
孔群から流出し、前記熱交換器における温水流下
専用通路の流入口より各温水流下専用通路内に流
れ込み、その下端の散水口から下方の充填材上へ
散布する。
The hot water in the upper water tank flows out from a group of small holes provided at its bottom, flows into each hot water flow dedicated passage from the inlet of the hot water flow dedicated passage in the heat exchanger, and flows downward from the water sprinkling port at the lower end. Spray on the filler.

これら充填材表面上、及び充填材間を流下中の
温水は通常の直交流式冷却塔同様に、この温水流
下方向と直交する状態に吸い込まれた気流と接触
し、一部が蒸発して、その潜熱作用で冷却され
る。この温水を冷却済みの昇温した空気は高温多
湿の状態で排気口に向け上昇する。
The hot water flowing down on the surface of these fillers and between the fillers comes into contact with the airflow sucked in perpendicularly to the direction of flow of the hot water, as in a normal cross-flow cooling tower, and a portion of it evaporates. It is cooled by its latent heat action. The heated air that has cooled this hot water rises toward the exhaust port in a hot and humid state.

一方、この温水流下式の熱交換器の空気専用流
路内に流入した外気は、幅が狭い温水流下専用通
路内を流下中の温水とは直接接触せず、この流路
内を移動中に、この気流は非透水性の壁板を介し
てこの流下中の温水により絶対湿度の上昇を伴わ
ずに加熱され、高温乾燥空気としてこの空気専用
流路の吐出口より冷却塔排気通路内へ吐出され
る。
On the other hand, the outside air that flows into the air-only flow path of this hot water flow-down type heat exchanger does not come into direct contact with the hot water flowing through the narrow hot water flow-only flow path, and while moving within this flow path, This airflow is heated through the non-water permeable wall plate by the flowing hot water without increasing the absolute humidity, and is discharged as high-temperature dry air from the outlet of this air-only flow path into the cooling tower exhaust passage. be done.

この充填材を通り上昇してくる高温多湿の気流
と、前記空気専用流路の吐出口から吐出する高温
乾燥空気とは、排風機の吸引側で混合し、湿度が
低下するも冬期においては白煙とならずに排気さ
れる。
The high-temperature and humid airflow rising through this filling material and the high-temperature dry air discharged from the outlet of the air-only flow path mix on the suction side of the exhaust fan, and although the humidity decreases, it remains white in winter. Exhaust without producing smoke.

(実施例) 次に、本件考案の代表的な実施例を図に基ずき
説明する。
(Example) Next, a typical example of the present invention will be described based on the drawings.

第1図、第2図において、Aは熱交換器であ
り、全体箱形機枠10を有し、この箱形機枠10
内には、複数個の温水流下専用通路11と、これ
ら温水流下専用通路11間に形成したほゞ水平な
トンネル状の空気専用流路12がその幅方向に交
互に配列されている。
In FIG. 1 and FIG. 2, A is a heat exchanger, which has a box-shaped machine frame 10 as a whole, and this box-shaped machine frame 10.
Inside, a plurality of passages 11 exclusively for hot water flow and approximately horizontal tunnel-shaped air passages 12 formed between these passages 11 exclusively for hot water flow are arranged alternately in the width direction.

前記空気専用流路12は各々箱形機枠10の長
手方向に貫通して形成され、その一端は吸入口1
3に、また他端は吐出口14としてある。隣接す
る温水流下専用通路11と空気専用流路12と
は、非透水性で熱交換自在の例えば合成樹脂製の
壁板15により相互に仕切られている。
Each of the air-only channels 12 is formed to pass through the box-shaped machine frame 10 in the longitudinal direction, and one end thereof is connected to the inlet port 1.
3, and the other end serves as a discharge port 14. The adjacent hot water flow passage 11 and air exclusive flow passage 12 are separated from each other by a water-impermeable wall plate 15 made of, for example, synthetic resin and capable of free heat exchange.

これら温水流下専用通路11の空気流れ方向の
両端16,17は、前記機枠10の端板18,1
9により各々閉塞され、これら温水専用通路11
の上端は温水流入口20に、またその下端は散水
口21としてある。
Both ends 16 and 17 of the hot water flow dedicated passage 11 in the air flow direction are connected to end plates 18 and 1 of the machine frame 10.
9, and these hot water dedicated passages 11
The upper end is provided as a hot water inlet 20, and the lower end is provided as a water spout 21.

前記温水流下専用流路11の幅bは空気専用流
路12の幅B0の2分の1乃至3分の1程度の寸
法としてあり、温水流下専用流路11及び空気専
用流路12は、上下方向に亘り波状に蛇行して形
成されている。
The width b of the hot water flow path 11 is approximately 1/2 to 1/3 of the width B 0 of the air flow path 12, and the hot water flow path 11 and the air flow path 12 are as follows: It is formed in a wavy meandering manner in the vertical direction.

これら空気専用流路12の天井壁は隣接する温
水流下専用通路11の温水流入口20同士を連ね
る上向きに凸の丸天井壁22としてある。
The ceiling walls of these air flow passages 12 are formed as upwardly convex round ceiling walls 22 that connect the hot water inlets 20 of the adjacent hot water flow passages 11.

前記空気専用流路12の吐出口14側には、全
ての空気専用流路12の吐出口14を一斉に開閉
する開閉ダンパ23が設けてあり、この開閉ダン
パ23はその開放時に上端24が直交流式冷却塔
Aの排気通路30内へ、前記機枠10にヒンジ結
合されたその下端25より張り出す形状としてあ
る。
An opening/closing damper 23 is provided on the discharge port 14 side of the air-only flow path 12 to open and close the discharge ports 14 of all the air-only flow paths 12 at the same time. It has a shape that projects into the exhaust passage 30 of the AC cooling tower A from its lower end 25 which is hinged to the machine frame 10.

前記開閉ダンパ23を2、3個分分割し、前記
吐出口14からの空気流量を段階的に切り替え可
能としても、この考案としては同一である。
Even if the opening/closing damper 23 is divided into two or three parts and the air flow rate from the discharge port 14 can be changed in stages, the invention remains the same.

また、前記蛇行形状に代えて、前記温水流下専
用通路11及び空気専用流路12をストレートに
形成しても良く、かつ開閉ダンパ23を取付けな
くても、この考案としては同一の技術的範囲に属
する。
Moreover, instead of the meandering shape, the hot water flow dedicated passage 11 and the air dedicated flow passage 12 may be formed straight, and even if the opening/closing damper 23 is not installed, the same technical scope can be achieved as this invention. belong to

この温水流下式の熱交換器Aは単体として予め
製造され、使用に際しては、既設の直交流式冷却
塔Aの本体31内に充填された充填材32の最上
部と、上部水槽33の散水底面間に装填、組み付
けられる。
This hot water flow-down type heat exchanger A is manufactured in advance as a single unit, and when used, it is attached to the top of the filler 32 filled in the main body 31 of the existing cross-flow type cooling tower A and the bottom surface of the water spraying tank 33. Loaded and assembled in between.

この組み付け時に、前記空気専用流路12の吸
入口13は前記本体31の側壁に設けた外気取入
口34側に開口し、その吐出口14は冷却塔Bの
排気通路30内に開口していると共に、前記温水
流下専用通路11の温水流入口20は上部水槽3
3の散水底面の下方に一し、その下端の散水口2
1は、充填材32側に開口する。
At the time of this assembly, the intake port 13 of the air-only flow path 12 opens to the outside air intake port 34 provided on the side wall of the main body 31, and the discharge port 14 thereof opens into the exhaust passage 30 of the cooling tower B. At the same time, the hot water inlet 20 of the hot water flow dedicated passage 11 is connected to the upper water tank 3.
The water sprinkling port 2 is located below the bottom of the water sprinkling hole 2 at the bottom of the
1 opens on the filling material 32 side.

このように前記熱交換器Aを組み込んだ既設の
直交流式冷却塔Bの排風機35を作動し温水の冷
却をするにあたり、夏期のように外気の温度が高
い時には前記開閉ダンパ23を閉じ、前記空気専
用流路12の吐出口14を全て閉塞する。
In order to cool hot water by operating the exhaust fan 35 of the existing cross-flow cooling tower B incorporating the heat exchanger A, the opening/closing damper 23 is closed when the outside air temperature is high, such as in the summer. All the discharge ports 14 of the air-only flow path 12 are closed.

この状態で前記上部水槽33内の温度の高い温
水をこの熱交換器Aの温水流下専用通路11上へ
落下させ、この温水流下専用通路11内を蛇行し
つつ流下させて、その下端の散水口21から下方
の充填材32上へ均等に散布し、充填材32表面
を流下させる。
In this state, the high-temperature hot water in the upper water tank 33 is dropped onto the hot water flow dedicated passage 11 of the heat exchanger A, and is caused to flow down the hot water flow dedicated passage 11 in a meandering manner, and is caused to flow down through the water spout at the lower end thereof. 21 onto the filler material 32 below, and flow down the surface of the filler material 32.

一方、排風機35の作動により外気取入口34
から前記本体31内に外気を取り込む。
On the other hand, due to the operation of the exhaust fan 35, the outside air intake port 34
Outside air is drawn into the main body 31 from the air.

この際、前記吐出口24は閉塞されているため
排風記35の外気吸引作用は、この熱交換器Aに
は及ばず、前記空気専用流路12内において空気
流は発生せず、空気はこの空気専用流路22内に
滞留し、この熱交換器Aにおいては温水と空気間
で間接的に熱交換は殆ど行われない。
At this time, since the discharge port 24 is closed, the outside air suction action of the exhaust port 35 does not reach the heat exchanger A, and no air flow is generated in the air-only flow path 12, and the air The air remains in the air-only flow path 22, and in this heat exchanger A, almost no indirect heat exchange is performed between the hot water and the air.

この結果、夏期においては、通常通り充填材3
2表面を流下し濡壁となる温水と空気流の接触に
伴う熱交換が行われ、温水を冷却し自身昇温した
空気は排風機35を取付けた排気口36より排気
されるが、外気の温度が高いため従来同様排気さ
れた空気は白煙化しない。
As a result, in the summer, the filling material 3
Heat exchange occurs due to the contact between the hot water flowing down the 2 surfaces and forming a wet wall, and the air that cools the hot water and raises its own temperature is exhausted from the exhaust port 36 to which the exhaust fan 35 is attached. Because the temperature is high, the exhausted air does not turn into white smoke like before.

次に、春、夏、冬期のように外気温度の低い時
には、前記開閉ダンパ23を、その下端25のヒ
ンジ軸周りに回動させ、その上端24を前記冷却
塔Bの排気通路30内へ張り出し、この熱交換器
Aにおける空気専用流路12の吐出口14全てを
全開する。
Next, when the outside air temperature is low, such as in spring, summer, and winter, the opening/closing damper 23 is rotated around the hinge axis of the lower end 25, and the upper end 24 is extended into the exhaust passage 30 of the cooling tower B. , all the discharge ports 14 of the air-only flow path 12 in this heat exchanger A are fully opened.

この結果、排風機35の吸引作用により、外気
取入口34から取り込んだ外気の一部は、この空
気専用流路12内へその吸入口13から流入しこ
の流路12内を移動中に、隣接する前記温水流下
専用通路11中を流下中の冷却塔A中で最も高温
の温水の熱伝導により前記壁板15を介して間接
的にこの空気流は外部から加熱され、換言すれば
温水は冷却され、絶対湿度はそのままとして高温
となつた乾燥空気は前記吐出口14から前記冷却
塔Bの排気通路30内へ吹き出される。
As a result, due to the suction action of the exhaust fan 35, a part of the outside air taken in from the outside air intake port 34 flows into this air-only flow path 12 from its intake port 13, and while moving within this flow path 12, some of the outside air is Due to the heat conduction of the hottest water in the cooling tower A flowing down through the hot water flow dedicated passage 11, this air flow is indirectly heated from the outside via the wall plate 15, in other words, the hot water is cooled. The high temperature dry air is blown out from the discharge port 14 into the exhaust passage 30 of the cooling tower B with the absolute humidity unchanged.

この空気流を間接的に加熱し自身は若干降した
温水は、夏期同様にこの熱交換器Aの温水流下専
用通路11を経て充填材32上へ均一に散布さ
れ、外気取入口34から取り込んだ残部の外気流
と接触し、従来同様に冷却される。この温水を冷
却し自身昇温した空気流は、高温多湿の空気流と
なつて前記排気口36に向け吸引上昇する。この
上昇する空気流は、前記開放したダンパ23によ
り形成された排気通路16の絞り部分において、
排気口36に到達する流量を制御され、前記吐出
口14より吹きだされる側方空気流と混合され、
排気口36から外部へ排気される。この混合によ
り、前記排気口36から排気される空気の湿度よ
り減少し、排気後、低温の外気に触れても、直ち
に排気した空気中の水分は凝固せず、白煙となら
ない。
The hot water that indirectly heats this air flow and cools down slightly is uniformly spread onto the filling material 32 through the hot water flow dedicated passage 11 of this heat exchanger A, as in the summer, and is taken in from the outside air intake port 34. The remaining part is brought into contact with the outside air flow and cooled in the conventional manner. The airflow, which cools the hot water and raises its own temperature, becomes a high-temperature and humid airflow and is sucked upward toward the exhaust port 36. This rising airflow is caused by the narrowed portion of the exhaust passage 16 formed by the opened damper 23.
The flow rate reaching the exhaust port 36 is controlled, and the air is mixed with the side air flow blown out from the discharge port 14,
The air is exhausted to the outside from the exhaust port 36. Due to this mixing, the humidity is lower than that of the air exhausted from the exhaust port 36, and even if it comes into contact with low-temperature outside air after being exhausted, the moisture in the exhausted air will not immediately solidify and will not turn into white smoke.

この高温多湿の空気に対する吐出口14からの
高温乾燥空気の混合率は、外気状態に応じてダン
パ23の開閉度により調整される。
The mixing ratio of the hot dry air from the discharge port 14 to the hot and humid air is adjusted by the opening/closing degree of the damper 23 depending on the outside air condition.

前記ダンパ23を具備しない実施態様ににおい
ては、四季を通して、外気取り入れ口34から取
り込んだ外気の一部は、前記吸入口13から空気
専用流路12内を通り、常時吐出口14から前記
冷却塔Bの排気通路30内へ吹き出す。
In an embodiment that does not include the damper 23, a part of the outside air taken in from the outside air intake port 34 passes through the air-only flow path 12 from the suction port 13 throughout the four seasons, and is constantly supplied to the cooling tower from the discharge port 14. It blows out into the exhaust passage 30 of B.

ハ 考案の効果 前記のように構成し作用する本件考案において
は、既設の直交流式冷却塔を大幅に改造すること
なく、本件熱交換器を、上部水槽と充填材間に装
填し組み込むだけで、冬期のように外気の湿度が
低い時期における白煙発生を有効に防止でき、か
つ従来同様の温水の冷却能力を維持することがで
きる。
C. Effects of the invention In the present invention, which is structured and operates as described above, the heat exchanger can be simply loaded and incorporated between the upper water tank and the filler without significantly modifying the existing cross-flow cooling tower. , it is possible to effectively prevent the generation of white smoke during periods when the humidity of the outside air is low, such as in winter, and to maintain the same hot water cooling capacity as in the past.

殊に温水流下専用通路の幅はそれぞれ外気が流
れる空気専用通路の1/2〜1/3と狭いため、温度の
高い流下水は、空気を介在させずに、これを満た
し全壁板と接触して流下し、壁板を介して空気流
と熱交換が行われる。
In particular, the width of the hot water flow passage is narrow, 1/2 to 1/3 of the air passage through which outside air flows, so the high-temperature flowing water fills it and comes into contact with all wall panels without intervening air. The air flows down and exchanges heat with the air flow through the wall plate.

(実施例固有の効果) 前記温水流下専用通路11の幅bを、前記各空
気専用流路12の幅の2分の1乃至3分の1程度
の寸法とすることにより、温水流下専用通路11
内を空気流の混入なく温度の高い温水で満たし、
これを通過した温水を充填材32上に散布できる
と共に、温水流下熱交換器Aにおいて被冷却水の
水量と無関係な量の気流を単位時間当たり流すこ
とができ、この結果冬期において外気を充分に温
めることができ、白煙の発生を有効に防止でき
る。
(Effects Unique to the Embodiment) By setting the width b of the hot water flow dedicated passage 11 to a dimension of approximately 1/2 to 1/3 of the width of each air dedicated flow passage 12, the hot water flow dedicated passage 11
Fill the inside with high temperature water without mixing air flow,
The hot water that has passed through this can be sprayed onto the filler 32, and an amount of air that is independent of the amount of water to be cooled can be flowed per unit time in the hot water downflow heat exchanger A. As a result, sufficient outside air can be supplied in winter. It can be heated and effectively prevent the generation of white smoke.

前記温水流下専用通路11及び空気専用流路1
2を、上下方向にわたり波状に蛇行して形成した
実施例においては、温水及び外気に間接的な接触
面積がより広くなり、温水による取り入れ空気の
加熱が効率良く行え、白煙の発生を防止できると
共に被冷却流下専用通路21に下端から上端に向
け外気が混入するおそれなく、温水が泡立つこと
はなく外気との間に支障なく熱交換を行える。
The hot water flow dedicated passage 11 and the air dedicated flow passage 1
In the embodiment in which 2 is formed in a wave-like meandering manner in the vertical direction, the indirect contact area between the hot water and the outside air is wider, the intake air can be efficiently heated by the hot water, and the generation of white smoke can be prevented. At the same time, there is no fear that outside air will be mixed into the cooled downstream passage 21 from the lower end to the upper end, and the hot water will not bubble, allowing heat exchange with the outside air without any trouble.

前記空気専用通路12の吐出口14に前記開閉
ダンパ23を取り付け、このダンパ23の開放時
にその上端33を前記冷却塔Bの排気通路30内
に張り出す実施例においては、冬期のように外気
の温度の低い時にこのダンパ23を開くことで、
前記吐出口14より吹出される高温乾燥の空気を
前記冷却塔Bの排気通路30中を充填材32側か
ら上昇してくる高温多湿の空気中に適量混合する
ことができ、排気口36から湿度を減少した混合
することができ、排気口36から湿度を減少した
混合空気を排気でき、白煙化を防止できると共
に、この開放したダンパ23により前記冷却塔B
の排気通路30の一部を絞ることができ、この絞
られた部分を通過中に充填材32側から上昇吸引
される高温多湿の空気量を制御し、前記吐出口1
4よりの高温の空気と合流し、更に排風機15に
より混合させて排気できる。また、このダンパ2
3の開閉度を調整することにより、全体の風量を
ほゞ一定に保ちながら高温多湿の空気に対する吐
出口14からの高温乾燥空気の混合割合を一操作
で無段階調節できる。
In an embodiment in which the opening/closing damper 23 is attached to the discharge port 14 of the air-only passage 12 and the upper end 33 of the damper 23 is extended into the exhaust passage 30 of the cooling tower B when the damper 23 is opened, it is possible to By opening this damper 23 when the temperature is low,
An appropriate amount of high-temperature dry air blown out from the discharge port 14 can be mixed with the high-temperature and humid air rising from the filling material 32 side in the exhaust passage 30 of the cooling tower B, and the humidity is removed from the exhaust port 36. The mixed air with reduced humidity can be exhausted from the exhaust port 36, and white smoke can be prevented.
A part of the exhaust passage 30 of the exhaust passage 30 can be constricted, and the amount of hot and humid air sucked upward from the filler 32 side while passing through this constricted part is controlled.
It joins with the high temperature air from air 4, and can be further mixed and exhausted by the exhaust fan 15. Also, this damper 2
By adjusting the opening/closing degree of No. 3, the mixing ratio of the hot dry air from the discharge port 14 to the hot and humid air can be adjusted steplessly with a single operation while keeping the overall air volume almost constant.

このダンパ23を夏期のように外気の温度が高
い時には閉じて、前記吐出口14を閉止すること
で、温水流下式の熱交換器Aの機能を中止させる
ことができ、従来同様、温水を各温水流下専用通
路11より下方の全充填材32へ散布し、温水を
外気取入口34より吸引した外気で充分に冷却で
きる。
By closing this damper 23 when the outside air temperature is high, such as in the summer, and closing the discharge port 14, the function of the hot water flow-down type heat exchanger A can be stopped. The warm water is sprayed onto all the filling materials 32 below from the hot water flow dedicated passage 11, and the hot water can be sufficiently cooled with outside air sucked through the outside air intake port 34.

このダンパ23を設けてない吐出口14を有す
る温水流式の熱交換器Aを具備する直交流式冷却
塔の実施例においては、ダンパ23の開閉操作を
要することな、構造簡易にして白煙の発生を防止
できる。
In this embodiment of the cross-flow type cooling tower equipped with the hot water flow type heat exchanger A having the discharge port 14 without the damper 23, the structure is simplified and white smoke is generated without requiring the opening/closing operation of the damper 23. can be prevented from occurring.

前記各温水流下専用通路21及び空気専用流路
12がストレートに形成してある実施例において
は渦流を伴わずに被冷却水空気が通過できると共
にその構造を簡略にできる。
In the embodiment in which the hot water flow passages 21 and the air flow passages 12 are straight, the cooled water air can pass through without swirling, and the structure can be simplified.

前記空気専用流路12の天井壁を形成する上向
きの凸の丸天井壁22で、隣接する温水流下専用
通路11の温水流入口20同士を相互に連ねた実
施例においては、空気専用流路12内に流れる空
気流を乱すことなく円滑に流すことができると共
に温水流下専用通路11内に滞留することなく上
部水槽33内の温水を分配供給できる。
In an embodiment in which hot water inlets 20 of adjacent hot water flow passages 11 are connected to each other by an upwardly convex vaulted ceiling wall 22 forming a ceiling wall of the air flow passage 12, It is possible to smoothly flow the airflow without disturbing the airflow, and the hot water in the upper water tank 33 can be distributed and supplied without stagnation in the passage 11 exclusively for hot water flow.

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

図は、この考案に係るもので、第1図は代表的
実施例の側面図、第2図は第1図の2−2線に沿
う総断面図、第3図は第1図の3−3線に沿う縦
断面図及び第4図は第1図に示す熱交換器を装填
した直交流式冷却塔の概略図である。 図中の主な符号の説明、A……熱交換器、11
……温水流下専用通路、12……空気専用流路。
The drawings are related to this invention: Fig. 1 is a side view of a typical embodiment, Fig. 2 is a general sectional view taken along line 2-2 in Fig. 1, and Fig. 3 is a 3-- A longitudinal sectional view taken along line 3 and FIG. 4 are schematic diagrams of a cross-flow cooling tower loaded with the heat exchanger shown in FIG. 1. Explanation of main symbols in the figure: A...Heat exchanger, 11
... Passage exclusively for hot water flow, 12... Channel exclusively for air.

Claims (1)

【実用新案登録請求の範囲】 1 上部水槽と、この真下に位置する充填材間に
装填自在の直交流式冷却塔用の気液間接接触型
の熱交換器において、 充填材間を通る空気流れ方向とほゞ平行な空
気専用流路が、多数並列してトンネル状に貫通
して形成してあり、隣接する空気専用流路間に
は、狭幅の温水流下専用通路が非透水性で熱交
換自在の壁板で仕切られて形成してあり、これ
ら温水流下専用通路の空気流れ方向の両端は閉
塞してあると共に、温水流下専用通路の上端
は、上部水槽から流下する温水の流入口として
あり、その下端は、前記充填材への温水の散水
口としてあり、前記温水流下通路専用通路の狭
幅とは、空気専用流路の幅の2分の1乃至3分
の1寸法としてあることを特徴とする直交流式
冷却塔用の熱交換器。 2 前記温水流下専用通路及び空気専用流路は上
下方向に亘り波状に蛇行して形成されている実
用新案登録請求の範囲第1項記載の直交流式冷
却塔用の熱交換器。 3 前記空気専用流路の天井壁は、隣接する温水
流下専用通路の上端で形成される温水流入口同
士を連ねる上向きに凸の丸天井壁としてある実
用新案登録請求の範囲第2項記載の直交流式冷
却塔用の熱交換器。 4 前記空気専用流路の吐出口は、下端がヒンジ
結合された開閉ダンパを有する吐出口としてあ
り、この開閉ダンパの開放時にその上端が下端
より冷却塔排気通路内へ張出す形状に前記開閉
ダンパは形成してある実用新案登録請求の範囲
第1項又は第2項記載の直交流式冷却塔用の熱
交換器。
[Scope of Claim for Utility Model Registration] 1. In a gas-liquid indirect contact type heat exchanger for a cross-flow cooling tower that can be freely loaded between an upper water tank and a packing material located directly below, air flow passing between the packing materials. A large number of air-only channels that are approximately parallel to the direction are formed in a tunnel-like manner, and between adjacent air-only channels, there are narrow hot water flow channels that are impermeable and heat-resistant. They are partitioned by replaceable wall plates, and both ends of these hot water flow passages in the air flow direction are closed, and the upper end of the hot water flow passage serves as an inlet for hot water flowing down from the upper water tank. The lower end serves as a hot water sprinkling port for the filling material, and the narrow width of the dedicated hot water flow path is 1/2 to 1/3 of the width of the air dedicated flow path. A heat exchanger for cross-flow cooling towers featuring: 2. The heat exchanger for a cross-flow cooling tower according to claim 1, wherein the hot water flow dedicated passage and the air dedicated flow passage are formed to meander in a wave-like manner in the vertical direction. 3. The ceiling wall of the air-only flow path is an upwardly convex round ceiling wall that connects the hot water inlets formed at the upper ends of the adjacent hot water flow-only paths. Heat exchanger for type cooling tower. 4. The outlet of the air-only flow path has an opening/closing damper whose lower end is hinged, and when the opening/closing damper is opened, the opening/closing damper is shaped so that its upper end extends from the lower end into the cooling tower exhaust passage. is a heat exchanger for a cross-flow cooling tower according to claim 1 or 2 of the registered utility model.
JP1986085920U 1986-06-05 1986-06-05 Expired JPH0429243Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1986085920U JPH0429243Y2 (en) 1986-06-05 1986-06-05

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1986085920U JPH0429243Y2 (en) 1986-06-05 1986-06-05

Publications (2)

Publication Number Publication Date
JPS62198367U JPS62198367U (en) 1987-12-17
JPH0429243Y2 true JPH0429243Y2 (en) 1992-07-15

Family

ID=30941763

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1986085920U Expired JPH0429243Y2 (en) 1986-06-05 1986-06-05

Country Status (1)

Country Link
JP (1) JPH0429243Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001082882A (en) * 1999-09-09 2001-03-30 Ishikawajima Harima Heavy Ind Co Ltd Cold water tower

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6082780A (en) * 1983-10-12 1985-05-10 Ishikawajima Harima Heavy Ind Co Ltd Dry and wet type cooling tower

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6082780A (en) * 1983-10-12 1985-05-10 Ishikawajima Harima Heavy Ind Co Ltd Dry and wet type cooling tower

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001082882A (en) * 1999-09-09 2001-03-30 Ishikawajima Harima Heavy Ind Co Ltd Cold water tower

Also Published As

Publication number Publication date
JPS62198367U (en) 1987-12-17

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