JPH0366592B2 - - Google Patents

Info

Publication number
JPH0366592B2
JPH0366592B2 JP58198115A JP19811583A JPH0366592B2 JP H0366592 B2 JPH0366592 B2 JP H0366592B2 JP 58198115 A JP58198115 A JP 58198115A JP 19811583 A JP19811583 A JP 19811583A JP H0366592 B2 JPH0366592 B2 JP H0366592B2
Authority
JP
Japan
Prior art keywords
air
tower
flow
dry
wet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP58198115A
Other languages
Japanese (ja)
Other versions
JPS6089683A (en
Inventor
Akemasa Horai
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.)
SHINKO PANTETSUKU KK
Original Assignee
SHINKO PANTETSUKU KK
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 SHINKO PANTETSUKU KK filed Critical SHINKO PANTETSUKU KK
Priority to JP58198115A priority Critical patent/JPS6089683A/en
Publication of JPS6089683A publication Critical patent/JPS6089683A/en
Publication of JPH0366592B2 publication Critical patent/JPH0366592B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C1/00Direct-contact trickle coolers, e.g. cooling towers
    • F28C1/14Direct-contact trickle coolers, e.g. cooling towers comprising also a non-direct contact heat exchange
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、冷却塔から排出される空気が白煙状
となることを防止する乾湿併用形冷却塔の改良構
造に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to an improved structure of a wet/dry cooling tower that prevents air discharged from the cooling tower from becoming white smoke-like.

(従来の技術) 湿式冷却塔から排出される飽和湿り空気が外気
条件により冷却され可視プルーム(霧)、いわゆ
る白煙の状態となることは公害原因の1つでもあ
るので、乾式冷却部を併用しそれからの乾き空気
を混合して白煙防止を図る乾湿併用形冷却塔が各
種提案されている。第1図は従来の乾湿併用形冷
却塔を示し、湿式冷却部Wと乾式冷却部Dとの配
列およびそれらを通つて塔内に吸引される空気流
の方向によつて次の3種に大別される。
(Prior technology) Saturated humid air discharged from a wet cooling tower is cooled by outside air conditions and becomes a visible plume (fog), so-called white smoke, which is one of the causes of pollution, so a dry cooling section is also used. Various dry/wet cooling towers have been proposed that mix the dry air from the dry air to prevent white smoke. Figure 1 shows a conventional dry/wet cooling tower, which can be divided into three types depending on the arrangement of the wet cooling section W and dry cooling section D and the direction of the air flow drawn into the tower through them. Separated.

(1) W,D直交配置の交叉流型式(第1図イ) (2) W,D対交配置の対向流型式(第1図ロ) (3) W,D交互配置または上下配置の並流型式
(第1図ハ,ニ) (発明が解決しようとする課題) これらの従来型式は吸引フアン前の塔内空間す
なわちプレナム室での両空気の混合が充分に行わ
れず、乾き空気流と湿り空気流とが層状となつて
排出されるため、フアンシリンダの上方に可視プ
ルーム(霧)層が不可視空気流層とはつきり分離
された状態で発生するので、白煙発生は所期どお
りには防止されない。すなわち湿り空気線図によ
り可視プルームを発生しない乾湿空気温度および
比率が決算上ではできていても、実際には両空気
の混合が不充分であることにより不充分な結果し
か得られない。
(1) Cross-flow type with W and D orthogonal arrangement (Figure 1 A) (2) Counter-flow type with W and D opposite arrangement (Figure 1 B) (3) W and D alternating arrangement or vertical arrangement Flow type (Fig. 1 c, d) (Problem to be solved by the invention) In these conventional types, the two types of air are not sufficiently mixed in the column space in front of the suction fan, that is, the plenum room, resulting in a dry air flow and a dry air flow. Since the moist air flow is discharged in a layered manner, a visible plume (fog) layer is generated above the fan cylinder that is distinctly separated from the invisible air flow layer, so white smoke is not generated as expected. is not prevented. That is, even if the dry and wet air temperature and ratio that do not generate a visible plume can be calculated according to the moist psychrometric diagram, in reality, only an unsatisfactory result is obtained because the mixing of both air is insufficient.

さらに、フイン付チユーブによる間接熱伝達交
換の乾式冷却の冷却効果が充填材部での気水直接
接触による蒸発潜熱の湿式冷却に較べて原理的に
冷却効果が小さく、その上、従来型式の乾湿併用
形冷却塔では乾式冷却部が垂直側面設置のため、
湿式冷却部との関連配置ならびに構造面で種々の
制約を受け、同容量の湿式冷却塔と較べる数段上
のサイズのクラスの塔を選定することが必要とな
り、コスト的に不利を免れない。
Furthermore, the cooling effect of dry cooling using indirect heat transfer using finned tubes is theoretically smaller than that of wet cooling using the latent heat of vaporization due to direct contact with air and water in the filling material. In combined cooling towers, the dry cooling section is installed vertically on the side, so
Due to various restrictions in terms of the arrangement and structure in relation to the wet cooling section, it is necessary to select a tower that is several steps larger in size than a wet cooling tower of the same capacity, which is unavoidable in terms of cost.

(課題を解決するための手段) 本発明は、従来型式の乾式冷却塔の上記諸困難
を解決するためになされたものであつて、本発明
の乾湿併用形冷却塔は、上位の温水分配槽から定
置されている充填材部を通して下位の冷水槽に流
下する温水と吸引フアンによつて充填材部の外側
から塔内空間に吸引される空気流とを充填材部で
交叉流直接接触させて温水を冷却する湿式交叉流
式冷却塔部に対し、塔内空間への吸引空気を間接
加熱する空気加熱器を組込んで塔内空間からの排
出空気の白煙化を防止する乾湿併用形冷却塔にお
いて、前記冷水槽を充填材部からの流下水を受入
可能な幅に縮小して通風可能な基礎上に設置する
ことにより塔底免に空気吸引可能な開口部を生ぜ
しめ、この塔底開口部に前記空気加熱器を組込む
とともに、その上位に空気加熱器を通つて塔内空
間に吸引される高温乾燥空気の流れを充填材部寄
りに偏向させかつ塔内空間からの落下水滴を受止
めて排出するための下縁に受水樋を形成した複数
のダンパー翼を充填材部の方向に傾けて列設した
風量調節がダンパーを設けたことを特徴とする。
(Means for Solving the Problems) The present invention has been made to solve the above-mentioned difficulties of conventional dry cooling towers. The hot water flowing down through the stationary packing material section into the lower cold water tank and the air flow sucked into the column internal space from outside the packing material section by a suction fan are brought into direct cross-flow contact at the packing material section. Wet and dry type cooling incorporates an air heater that indirectly heats the air drawn into the tower space into the wet cross-flow cooling tower section that cools hot water to prevent the air discharged from the tower space from turning into white smoke. In the tower, by reducing the width of the cold water tank to a width that can receive the flowing water from the filling material section and installing it on a foundation that allows ventilation, an opening that can suck air is created at the bottom of the tower. The air heater is installed in the opening, and the air heater is installed above the air heater to deflect the flow of high-temperature dry air sucked into the column internal space toward the packing material part, and to receive falling water droplets from the column internal space. The damper is characterized in that a plurality of damper blades each having a water receiving gutter formed at the lower edge for stopping and discharging water are arranged in a row and tilted in the direction of the filling material part.

(作用) 本発明によると、交叉流方式の湿式冷却部から
吸引される飽和湿り空気と乾式冷却部から上向き
に吸引される乾き空気とが塔内空間(プレナム
室)で概略交叉流して緊密に混合され、特に湿り
空気流の不均一分布に向け上向流乾き空気を偏向
流させて混合効果が助長されるので、可視プルー
ムの発生の防止が確実になされる。この場合に塔
内空間からの落下水滴はダンパー翼によつて受止
められ排出されるので、乾き空気が湿らされるこ
とは極小となる。
(Function) According to the present invention, the saturated humid air sucked from the cross-flow type wet cooling section and the dry air sucked upward from the dry cooling section roughly cross-flow in the tower interior space (plenum room) and are tightly cooled. The prevention of visible plumes is ensured since the mixing effect is enhanced, especially by deflecting the upstream dry air towards the non-uniform distribution of the humid air flow. In this case, since the falling water droplets from the inner space of the tower are caught and discharged by the damper blades, the amount of moisture in the dry air is minimized.

構造上、乾式冷却部の併設のためには、湿式冷
却部は冷水槽の幅を必要最小限に近付けて縮小し
基礎を通風可能の構造として塔底面空気吸引開口
を設け、乾き空気の吸引のためフアン容量を大き
くするだけで済むので、冷却機能は湿式冷却部の
上部構造、サイズおよび定格容量を従来の湿式冷
却塔と同等にすることができ、コストを特に増加
させたり、設置地積の増大を招いたりしない。白
煙の発生する気象条件になければ、乾式冷却部を
閉じて湿式冷却部の有利な冷却機能を利用する運
転が可能である。
Structurally, in order to install a dry cooling section, the width of the cold water tank for the wet cooling section should be reduced to the minimum necessary, and the foundation should be structured to allow ventilation, with air suction openings on the bottom of the tower to prevent the suction of dry air. Therefore, the cooling function can be made similar to conventional wet cooling towers in terms of superstructure, size and rated capacity of the wet cooling section, since only the fan capacity needs to be increased, which does not particularly increase costs or increase the installation area. I don't invite anyone. If the weather conditions do not produce white smoke, it is possible to close the dry cooling section and utilize the advantageous cooling function of the wet cooling section.

(実施例) 以下、本発明を第2図乃至第4図に示す実施例
により具体的かつ詳細に説明する。第2および3
図は湿式冷却部をダブルフロー形の交叉流方式冷
却塔として構成した実施例であり、第4図は同じ
くシングルフロー形の実施例である。
(Example) Hereinafter, the present invention will be explained specifically and in detail with reference to the examples shown in FIGS. 2 to 4. 2nd and 3rd
The figure shows an embodiment in which the wet cooling section is constructed as a double-flow cross-flow type cooling tower, and FIG. 4 shows an embodiment in which the wet cooling section is also a single-flow type.

第2および第3図において、湿式交叉流冷却塔
部分は、地上直接ではなく、地上に間隔を隔てて
立設したコンクリート基礎1およびその上に間隔
を隔てて列設した形鋼架台2等からなる通風可能
な架台上に設置され上部の湿式冷却部を構成す
る。通風可能な架台は地下、半地下配置とするこ
ともできる。
In Figures 2 and 3, the wet cross-flow cooling tower part is not directly on the ground, but has a concrete foundation 1 erected on the ground at intervals, and shaped steel frames 2, etc. installed in a row at intervals on top of the concrete foundation 1. It is installed on a pedestal that allows ventilation and constitutes the upper wet cooling section. The ventilation frame can also be placed underground or semi-underground.

架台上の両側には中間をプレナム室3として充
填材部4が設けられ、塔上部デツキにはフアン
5、減速器6、モータ7、フアンシリンダ8から
なる吸引通風装置は設け、フアン5により空気を
充填材部4を通してプレナム室3に吸引しフアン
シリンダ8から上方に排出するようにする。充填
材部4の空気取入面にはルーパ9を、空気流出面
にはエリミネータ10を設ける。
A filling material section 4 is provided on both sides of the pedestal with a plenum chamber 3 in the middle, and a suction ventilation device consisting of a fan 5, a speed reducer 6, a motor 7, and a fan cylinder 8 is provided on the upper deck of the tower. is sucked into the plenum chamber 3 through the filler part 4 and discharged upward from the fan cylinder 8. A looper 9 is provided on the air intake surface of the filler portion 4, and an eliminator 10 is provided on the air outlet surface.

冷却すべき温水は各充填材部4上の温水分配槽
11に温水管12、散水箱13を経て供給され充
填材部4を分散して空気との直接接触により冷却
され下方の冷水槽14に向かつて流下する。
The hot water to be cooled is supplied to the hot water distribution tank 11 above each filling material section 4 via hot water pipes 12 and water sprinkler box 13, disperses the filling material section 4, is cooled by direct contact with air, and flows into the cold water tank 14 below. It flows down towards the direction.

本発明では上記流下水量を制御する温水管12
の出口部に流量調節弁15を設け、また冷水槽1
4は従来のように底面の全面とせずに各充填材部
4の下方に限定して2分し充填材部から落下する
調節量の冷却水が全て受水できるだけの有効幅に
縮小し、かくして生じた両冷水槽14間の間隔に
プレナム室3の下方に塔底面空気吸引開口16を
開設する。平面面積の縮小した各冷水槽14は冷
水を溢流させないだけの深さを与え、速やかにサ
ンプ26を経て冷水取出口17から冷水を取り出
すようにする。
In the present invention, the hot water pipe 12 that controls the amount of flowing water
A flow control valve 15 is provided at the outlet of the cold water tank 1.
4 is not formed on the entire bottom surface as in the past, but is limited to the lower part of each filling material section 4 and is divided into two parts, reducing the effective width to enough to receive all the adjusted amount of cooling water that falls from the filling material section. An air suction opening 16 at the bottom of the column is opened below the plenum chamber 3 in the gap between the two cold water tanks 14 created. Each cold water tank 14 with a reduced plane area is given enough depth to prevent cold water from overflowing, and the cold water is quickly taken out from a cold water outlet 17 via a sump 26.

塔底面空気開口16にはフイン付チユーブの管
群からなる空気加熱器18を設け、その入口配管
19から前記温水管12と関連する温水または他
の水源からの高温水を流入して流過させるように
する。25は空気加熱器出口配管を示す。空気加
熱器18の上位には、概略J字形断面のダンパー
翼21の列からなるダンパー21を設け、その通
過気流の方向が充填材部4の内側面のエリミネー
タ10に向かつて偏流するようダンパー翼20の
傾きを与える。こうしてフアン5により、前記の
通風可能な基礎1,2から前記充填材部通過空気
と並流の関係に外部から吸引さる空気は空気加熱
器18を通つて加熱されダンパー21を通つてプ
レナム室3に点線矢印dで示すように充填材部4
の内側面に向かつて偏らされて流れ、充填材部
4、エリミネータ10を通つた実線矢印wで示す
空気と概略交叉流する。
An air heater 18 consisting of a group of finned tubes is installed in the tower bottom air opening 16, and hot water associated with the hot water pipe 12 or high temperature water from another water source flows through the inlet pipe 19 thereof. Do it like this. 25 indicates the air heater outlet piping. A damper 21 consisting of a row of damper blades 21 having a roughly J-shaped cross section is provided above the air heater 18. Give a slope of 20. In this way, the air drawn in from the outside by the fan 5 from the ventilation-permeable foundations 1 and 2 in a parallel flow relationship with the air passing through the filling material section is heated through the air heater 18 and passed through the damper 21 into the plenum chamber 3. As shown by the dotted arrow d, the filling material portion 4
The flow is biased toward the inner surface of the air, and approximately crossflows with the air shown by the solid arrow w that has passed through the filler portion 4 and the eliminator 10.

複数のダンパー翼20はエリミネータ10を通
過した湿り空気w中の通り抜け水滴が合一して生
ずる落下水滴を全て受入れるように隣接翼間に上
下方向の重なりを有するようにし、またJ字形断
面翼の下縁は翼面流下水の受水樋22に形成し受
水樋22に集水された水は端部に流れダンパー2
1の端部の集水樋23を経て塔底面空気吸引開口
16の領域から排除されるようにし空気加熱器1
8からの乾き空気が湿らされることを極力少なく
する。
The plurality of damper blades 20 are designed to have vertical overlap between adjacent blades so as to receive all the falling water droplets that are generated by the coalescence of the passing water droplets in the moist air w that has passed through the eliminator 10, and also have J-shaped cross-section blades. The lower edge is formed into a water receiving gutter 22 for the sewage flowing from the wing surface, and the water collected in the water receiving gutter 22 flows to the end and damper 2.
Air heater 1
Minimize as much as possible the dry air from 8 being moistened.

充填材部4を通過する空気の流速は通常2〜4
m/secであるが、エリミネータ10を通過した
湿り空気wの流れは決して一様ではなく場所によ
つて著しく異なる。第5図イに示すように充填材
部4およびエリミネータ10は支柱24によつて
水平方向に多数のスパンに区劃され、それらの支
柱24の下流の部分では第5図ロの流速分布図に
示すように湿り空気の流れが殆ど存在しない。従
つて前記の概略交叉流する湿り空気wと乾き空気
dとの間においては、エリミネータ10に向かつ
て偏流させられる乾き空気dが湿り空気の流れが
殆ど存在しない個所に入り込み、こうして両空気
流の相互接触拡散面積が大きくなるので、従来形
式の乾湿併用形冷却塔と較べてより良好な塔内空
気混合効果が得られる。
The flow rate of air passing through the filling material part 4 is usually 2 to 4
m/sec, but the flow of humid air w passing through the eliminator 10 is by no means uniform and varies significantly depending on the location. As shown in FIG. 5A, the filler part 4 and the eliminator 10 are horizontally divided into a number of spans by support columns 24, and the flow velocity distribution diagram shown in FIG. As shown, there is almost no flow of humid air. Therefore, between the humid air w and the dry air d that roughly cross-flow, the dry air d that is deflected toward the eliminator 10 enters the area where there is almost no flow of humid air, and thus the flow of both air flows is reduced. Since the mutual contact diffusion area is increased, a better air mixing effect within the tower can be obtained compared to the conventional type cooling tower that combines dry and wet cooling towers.

第4図は本発明の他の実施例を示し、湿式冷却
塔をシングルフロー形とし一側のみに充填材部4
を設けたものである。第2および3図の実施例と
均等の各部は図中、同一符号を記入して指摘し、
説明の重複を省略する。
FIG. 4 shows another embodiment of the present invention, in which the wet cooling tower is of a single-flow type with a packing material section 4 on only one side.
It has been established. Parts that are equivalent to the embodiments in FIGS. 2 and 3 are indicated by the same reference numerals in the figures, and
Omit duplicate explanations.

(発明の効果) 本発明の乾湿併用形冷却塔の構成作用は以上の
とおりであつて、本発明によれば次の諸効果が得
られる。
(Effects of the Invention) The structural functions of the wet and dry cooling tower of the present invention are as described above, and the present invention provides the following effects.

塔内における飽和湿り空気と乾き空気との湿合
は前記のようにして極めて緊密に行われるので排
出空気からの可視プルームの発生は効果的に防止
される。混合促進のため特別な混合室を設ける必
要はない。通常の冷却塔では利用され得なかつた
塔底面を乾き空気供給のための空気加熱器の設置
場所としたので床面積の有効利用が計れる。ま
た、従来の乾湿併用形冷却塔では乾式部が垂直側
面装置のため、配置上、構造上種々の制約を受
け、通常の湿式冷却塔に較べて数段容量が上のク
ラスの塔型を選定することが必要となり、必然的
にコストアツプを余儀なくされていた。これに対
し本発明では乾式部の設置場所の制約等が軽減さ
れ、塔型式のクラスアツプの必要は最小となり、
対応は乾き空気の吸引のためフアン容量を大きく
する程度で済むので、コスト面で有利となる。
The wetting of the saturated moist air and the dry air within the column is thus very intimate, so that the formation of visible plumes from the exhaust air is effectively prevented. There is no need to provide a special mixing chamber to facilitate mixing. Since the bottom of the tower, which cannot be used in a normal cooling tower, is used as a place to install an air heater for supplying dry air, effective use of floor space can be achieved. In addition, in conventional wet/dry cooling towers, the dry section is a vertical side device, so there are various restrictions in terms of layout and structure, so we selected a tower type with several stages higher capacity than a normal wet cooling tower. This inevitably led to an increase in costs. In contrast, in the present invention, restrictions on the installation location of the dry section are alleviated, and the need for class-up of the tower type is minimized.
The only solution is to increase the capacity of the fan to suck in dry air, which is advantageous in terms of cost.

また、従来の乾湿併用形冷却塔では列設して多
セル構造とするのに空気取入れの関係から制約が
あつた。本発明では各セルの熱量に見合つた容量
の空気加熱器を塔底面にならべるので列設の妨げ
とならず多セル構造とすることが容易である。空
気取入れについては形鋼架台およびコンクリート
基礎が空気流入の妨げにならぬよう配慮がなされ
ていれば問題はない。
In addition, with conventional dry/wet cooling towers, there are restrictions on air intake when arranging them in a row to create a multi-cell structure. In the present invention, air heaters with a capacity commensurate with the amount of heat of each cell are arranged at the bottom of the tower, so it is easy to form a multi-cell structure without interfering with the arrangement in rows. There will be no problem with air intake as long as consideration is taken to ensure that the steel frame and concrete foundation do not impede air inflow.

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

第1図は従来の乾湿併用形冷却塔の各部配置図
を示し、第1図イは交叉流型の平面配置図、第1
図ロは対向流型の平面配置図、第1図ハは並流型
の一例の平面配置図、第1図ニは並流型の他例の
側面配置図である。第2図は本発明の1実施例の
乾湿併用形冷却塔の縦断側面図、第3図はその2
セルの部分横断平面図、第4図は本発明の他の実
施例の乾湿併用形冷却塔の縦断側面図、第5図イ
は充填材部の空気流出面の支柱の配列を示す平面
図、第5図ロはそれに対応する流通状況を示し横
軸に支柱の場所、縦軸下向正に流速をとり湿り空
気流速分布曲線を示すものである。 1……コンクリート基礎、2……形鋼架台、3
……プレナム室、4……充填材部、5……フア
ン、6……減速機、7……モータ、8……フアン
シリンダ、9……ルーパ、10……エリミネー
タ、11……温水分配槽、12……温水管、13
……散水箱、14……冷水槽、15……流量調節
弁、16……塔底面空気吸気吸引開口、17……
冷水取出口、18……空気加熱器、19……入口
配管、20……ダンパー翼、21……ダンパー、
22……受水樋、23……集水樋、24……支
柱、25……出口配管、26……サンプ、W……
湿式冷却部、D……乾式冷却部、w……湿り空気
流、d……乾き空気流。
Figure 1 shows the layout of each part of a conventional combined dry/wet type cooling tower.
FIG. 1B is a plan layout of a counter-current type, FIG. 1C is a plan layout of an example of a parallel flow type, and FIG. FIG. 2 is a longitudinal cross-sectional side view of a wet and dry cooling tower according to one embodiment of the present invention, and FIG.
FIG. 4 is a vertical cross-sectional side view of a wet/dry cooling tower according to another embodiment of the present invention; FIG. FIG. 5B shows the corresponding flow situation, and shows a moist air flow velocity distribution curve, with the horizontal axis representing the location of the support and the vertical axis representing the flow velocity in the downward direction. 1...Concrete foundation, 2...Shaped steel frame, 3
... Plenum chamber, 4 ... Filler section, 5 ... Fan, 6 ... Reduction gear, 7 ... Motor, 8 ... Fan cylinder, 9 ... Looper, 10 ... Eliminator, 11 ... Hot water distribution tank , 12...Hot water pipe, 13
... Watering box, 14 ... Cold water tank, 15 ... Flow rate control valve, 16 ... Tower bottom air intake suction opening, 17 ...
Cold water outlet, 18... Air heater, 19... Inlet piping, 20... Damper blade, 21... Damper,
22...Water receiving gutter, 23...Water collection gutter, 24...Strut, 25...Outlet piping, 26...Sump, W...
Wet cooling section, D...Dry cooling section, w...Moist air flow, d...Dry air flow.

Claims (1)

【特許請求の範囲】[Claims] 1 上位の温水分配槽から定置されている充填材
部を通つて下位の冷水槽に流下する温水と吸引フ
アンによつて充填材部の外側から塔内空間に吸引
される空気流とを充填材部で交叉流直接接触させ
て温水を冷却する湿式交叉流式冷却塔部に対し、
塔内空間への吸引空気を間接加熱する空気加熱器
を組み込んで塔内空間からの排出空気の白煙化を
防止する乾湿併用形冷却塔において、前記冷水槽
を充填材部からの流下水を受入可能な幅に縮小し
て通風可能な基礎上に設置することにより塔底面
に空気吸引可能な開口部を生ぜしめ、この塔底開
口部に前記空気加熱器を組み込むとともに、その
上位に空気加熱器を通つて塔内空間に吸引される
高温乾燥空気の流れを充填材部寄りに偏向させか
つ塔内空間からの落下水滴を受止めて排出するた
めの下縁に受水樋を形成した複数のダンパー翼を
充填材部の方向に傾けて列設した風量調節ダンパ
ーを設けたことを特徴とする乾湿併用形冷却塔。
1 The hot water flowing from the upper hot water distribution tank through the stationary filling part to the lower cold water tank and the air flow sucked into the column internal space from outside the packing part by a suction fan are combined into the filling material. In contrast to the wet cross-flow cooling tower section, which cools hot water by direct contact with cross-flow at the
In a wet/dry cooling tower that incorporates an air heater that indirectly heats the air drawn into the tower interior space to prevent the air discharged from the tower interior space from becoming white smoke, the cold water tank is connected to the water flowing from the filling material section. By reducing the width to an acceptable width and installing it on a foundation that allows ventilation, an opening is created at the bottom of the tower through which air can be sucked.The air heater is built into this opening at the bottom of the tower, and an air heater is installed above it. A plurality of water-receiving gutters are formed at the lower edge to deflect the flow of high-temperature dry air sucked into the tower interior space through the container toward the packing material part, and to catch and discharge falling water droplets from the tower interior space. What is claimed is: 1. A cooling tower for both dry and wet use, characterized by having air volume adjusting dampers arranged in rows with damper blades tilted in the direction of the filling material section.
JP58198115A 1983-10-21 1983-10-21 Cooling tower of wet and dry composite type Granted JPS6089683A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58198115A JPS6089683A (en) 1983-10-21 1983-10-21 Cooling tower of wet and dry composite type

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58198115A JPS6089683A (en) 1983-10-21 1983-10-21 Cooling tower of wet and dry composite type

Publications (2)

Publication Number Publication Date
JPS6089683A JPS6089683A (en) 1985-05-20
JPH0366592B2 true JPH0366592B2 (en) 1991-10-17

Family

ID=16385714

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58198115A Granted JPS6089683A (en) 1983-10-21 1983-10-21 Cooling tower of wet and dry composite type

Country Status (1)

Country Link
JP (1) JPS6089683A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10113326B2 (en) 2015-08-07 2018-10-30 Spx Cooling Technologies, Inc. Modular heat exchange tower and method of assembling same

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51130143U (en) * 1975-03-05 1976-10-20
JPS5792689A (en) * 1980-11-29 1982-06-09 Ishikawajima Harima Heavy Ind Co Ltd Method to flow air into mixing chamber of cooling tower of dry and wet air type

Also Published As

Publication number Publication date
JPS6089683A (en) 1985-05-20

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