JPH0129430Y2 - - Google Patents

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Publication number
JPH0129430Y2
JPH0129430Y2 JP7535885U JP7535885U JPH0129430Y2 JP H0129430 Y2 JPH0129430 Y2 JP H0129430Y2 JP 7535885 U JP7535885 U JP 7535885U JP 7535885 U JP7535885 U JP 7535885U JP H0129430 Y2 JPH0129430 Y2 JP H0129430Y2
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JP
Japan
Prior art keywords
refrigerant
heat exchange
exhaust port
heat
water tank
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
Application number
JP7535885U
Other languages
Japanese (ja)
Other versions
JPS61192170U (en
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 filed Critical
Priority to JP7535885U priority Critical patent/JPH0129430Y2/ja
Publication of JPS61192170U publication Critical patent/JPS61192170U/ja
Application granted granted Critical
Publication of JPH0129430Y2 publication Critical patent/JPH0129430Y2/ja
Expired legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【考案の詳細な説明】 <利用される技術分野> この考案は、直交流式熱交換塔殊にその雨水、
雪、霰、雹などが冷媒若しくは熱媒に混入するの
を防止する技術に関するものである。
[Detailed description of the invention] <Utilized technical field> This invention is applicable to cross-flow heat exchange towers, especially rainwater,
This invention relates to technology for preventing snow, hail, hail, etc. from getting mixed into refrigerant or heating medium.

<従来技術及びその問題点> 従来、この種の直交流式熱交換塔における雨水
などの混入防止装置は、その排気口上にエルボ型
のダクトを取付けたものが一般的であるが、この
ダクトが風上を向いた時には、雨水などが排気口
より熱交換塔内に吹き込み、かつ排気損失が大き
くなり、このダクトに隣接して起立壁のある場合
には、排気にも支障をきたす。
<Prior art and its problems> Conventionally, devices for preventing rainwater from entering this type of cross-flow heat exchange tower have generally had an elbow-shaped duct installed above the exhaust port. When the duct faces upwind, rainwater etc. blow into the heat exchange tower through the exhaust port, increasing exhaust loss, and if there is an upright wall adjacent to this duct, this also poses a problem for exhaust.

更に、冷媒若しくは熱媒が不凍液の場合には、
侵入した雨水によりこの不凍液の濃度が低下し、
所期の冷凍効果を上げることが出来ない。
Furthermore, if the refrigerant or heating medium is antifreeze,
The concentration of this antifreeze decreases due to rainwater entering,
The desired freezing effect cannot be achieved.

このような現象は、排気口に設けた送風機の運
転停止時により顕著となる。
Such a phenomenon becomes more noticeable when the blower provided at the exhaust port stops operating.

<問題を解決するための手段> この考案は、液体受け皿を冷却塔本体内に配置
することにより、即ち、上部水槽より充填材上に
冷媒若しくは熱媒の流下路に対し直交して、本体
内部に形成したエア室内へ外気を導きこのエア室
の真下の上部排気口より排気し、この外気と冷媒
若しくは熱媒間で熱交換を行い、熱交換した冷媒
若しくは熱媒を前記エア室の下部に設置した下部
水槽に収集する直交流式熱交換塔において、 この上部排気口真下の下部水槽の水面のみを覆
うに充分な大きさの液体受け皿がこの水面上に配
置してあり、この受け皿内に滞留した液体を冷媒
若しくは熱媒系路外へ排出自在としてあることを
特徴とする直交流式熱交換塔とすることにより、
前記問題点を解決し、雨水などが冷媒若しくは熱
媒に混入するのを低減させた直交流式熱交換塔を
提供することを目的とする。
<Means for solving the problem> This invention has been developed by arranging the liquid receiver inside the cooling tower body, that is, by disposing the liquid receiver inside the cooling tower body, from the upper water tank onto the filling material, orthogonally to the flow path of the refrigerant or heating medium. Outside air is introduced into the air chamber formed in the air chamber and exhausted from the upper exhaust port directly below the air chamber, heat is exchanged between the outside air and the refrigerant or heating medium, and the heat exchanged refrigerant or heating medium is sent to the lower part of the air chamber. In a cross-flow heat exchange tower that collects liquid in a lower water tank installed, a liquid receiving tray large enough to cover only the water surface of the lower water tank directly below this upper exhaust port is placed above this water surface. By using a cross-flow type heat exchange tower, which is characterized in that the stagnant liquid can be freely discharged to the outside of the refrigerant or heat medium system,
It is an object of the present invention to provide a cross-flow type heat exchange tower that solves the above-mentioned problems and reduces the mixing of rainwater and the like into a refrigerant or a heat medium.

次に、本件考案の代表的な実施態様を図に基ず
き説明する。
Next, a typical embodiment of the present invention will be explained based on the drawings.

第1図において、Aは2方向から外気を吸込む
直交流式熱交換塔であり、上部排気口18の左右
両側に上部水槽11が熱交換塔本体12上部に設
置され、この上部水槽11の真下で外気取入口1
3近傍に充填材の一種である波板状の充填板15
が装填してあり、各充填板15の二次側にエリミ
ネータ部材(図示せず)が設けてあり、外気取入
口13より充填板15間を通りエリミネータ部材
を通過した外気が流入し寄り集まるエア室17
が、この本体12の中央に形成してあり、このエ
ア室17の真上には、冷媒若しくは熱媒と熱交換
を終了した空気を外部へ排気する前記上部排気口
18が設けてあり、この上部排気口18内に送風
機18aが設置してある。前記充填板15を流下
中に外気との間で熱交換された冷媒若しくは熱媒
をエア室17の下部で収集し、冷凍機などのプラ
ントへ戻す下部水槽19が設置されている。前記
エア室17は、前記本体12の中央でなく片寄り
してもよい。
In FIG. 1, A is a cross-flow type heat exchange tower that sucks outside air from two directions. Upper water tanks 11 are installed above the heat exchange tower main body 12 on both left and right sides of the upper exhaust port 18, and directly below the upper water tanks 11. outside air intake 1
A corrugated filling plate 15, which is a type of filling material, is placed near 3.
is loaded, and an eliminator member (not shown) is provided on the secondary side of each filling plate 15, and outside air flows in from the outside air intake port 13, passes between the filling plates 15, passes through the eliminator member, and collects the air. Room 17
is formed in the center of the main body 12, and the upper exhaust port 18 is provided directly above the air chamber 17 for exhausting the air that has completed heat exchange with the refrigerant or heat medium to the outside. A blower 18a is installed inside the upper exhaust port 18. A lower water tank 19 is installed to collect the refrigerant or heat medium exchanged with outside air while flowing down the filling plate 15 at the lower part of the air chamber 17 and return it to a plant such as a refrigerator. The air chamber 17 may not be located at the center of the main body 12 but may be located off-center.

この種熱交換塔Aは、公知のものと同じであり
本件考案の熱交換塔においては、更に上部排気口
18真下の前記下部水槽19の水面のみを覆うに
充分な大きさの液体受け皿20が、この水面上に
略水平に配置してあり、この受け皿20の中心部
に集められた雨水、雪、及び霰、雹など融解液を
前記下部水槽へ排出する排水管21が、この受皿
20の中心部に連通されている。
This type of heat exchange tower A is the same as the known one, and the heat exchange tower of the present invention further includes a liquid receiving tray 20 large enough to cover only the water surface of the lower water tank 19 directly below the upper exhaust port 18. A drain pipe 21 is disposed approximately horizontally on the water surface, and drains rainwater, snow, and melting liquid such as sleet and hail collected in the center of the receiving tray 20 to the lower water tank. It is connected to the center.

前記上部排気口18が、前記本体12の長手方
向に2〜3個並設してあるものにおいては、これ
ら排気口18の真下に位置する下部水槽17の水
面は、この長手方向へ長い平面矩形の前記受け皿
20により覆われている。
In the case where two or three upper exhaust ports 18 are arranged in parallel in the longitudinal direction of the main body 12, the water surface of the lower water tank 17 located directly below these exhaust ports 18 has a rectangular plane that is long in the longitudinal direction. It is covered by the said saucer 20 of.

必要に応じて第2図に示す如く、前記排気口1
8には、排気ダクト22が取付けられるが、本件
考案ではこの排気ダクト22のないものもこの技
術範囲に入いることは云うまでもない。
If necessary, as shown in FIG.
8 is attached with an exhaust duct 22, but it goes without saying that a device without this exhaust duct 22 also falls within the technical scope of the present invention.

この排気ダクト22は、多数枚の矩形状の板2
3をルーバー状に隣接し、前記上部排気口18を
これら板23で覆い隣接する板23間に排気可能
な間隙を形成し、各板23をその幅方向へ傾斜し
その下縁を長手方向亘り排水樋24とし、隣接す
る板23の下側にその下縁が位置する形態で、前
記ルーバ状にこれら、板23を配列してなるもの
であり、上部排気口18に対して各板23の一端
は、他端よりも高く設けてあり、各板23は全体
として片流れ型で、各排水樋24の一端は、前記
上部排気口18外の外部まで延在している(第3
図、第4図参照)。
This exhaust duct 22 consists of a large number of rectangular plates 2
3 are adjacent to each other in a louver shape, the upper exhaust port 18 is covered with these plates 23, and a gap is formed between the adjacent plates 23 to allow exhaust air, each plate 23 is inclined in its width direction, and its lower edge is extended in the longitudinal direction. The drain gutter 24 is formed by arranging the plates 23 in the louver shape, with the lower edge of the drain gutter 24 located below the adjacent plate 23. One end is provided higher than the other end, each plate 23 is of a single-flow type as a whole, and one end of each drainage gutter 24 extends to the outside outside the upper exhaust port 18 (the third
(See Figure 4).

前記板23aの形状、配列の他の態様としては
第5図、第6図のように、円形の上部排気口18
に、各板23aを放射状に配列し、各板23aの
外端が末広がりとなる末広形状に各板23aが形
成してある。
Other aspects of the shape and arrangement of the plate 23a include a circular upper exhaust port 18 as shown in FIGS. 5 and 6.
The plates 23a are arranged radially, and each plate 23a is formed in a wide-end shape with the outer end of each plate 23a widening at the end.

即ち、前記板23aの外端ほど若干低く各板2
3aは傾斜し、隣接する前記板23と一部重合し
多数枚の板23aが、前記上部排気口18の円周
方向に追い廻し形状に配列され、各板23a間に
排気可能な間隙が形成されて、排気ダクト22a
を構成し、前記各板23aの外端は、上部排気口
18外に臨在している(第5図参照)。
That is, each plate 2 is slightly lower toward the outer end of the plate 23a.
3a is inclined and partially overlaps the adjacent plate 23, and a large number of plates 23a are arranged in a circular shape in the circumferential direction of the upper exhaust port 18, and a gap is formed between each plate 23a to allow exhaust air. and the exhaust duct 22a
The outer ends of each plate 23a are located outside the upper exhaust port 18 (see FIG. 5).

<作用及び効果> 前記のように構成した本件考案の作用を効果と
併せ次に説明する。
<Operations and Effects> The functions and effects of the present invention configured as described above will be explained below.

本件考案の直交流式熱交換塔Aの冷媒若しくは
熱媒と外気間の熱交換は、従来この種の熱交換塔
のものと同様に行なわれる。
Heat exchange between the refrigerant or heat medium and outside air in the cross-flow type heat exchange tower A of the present invention is carried out in the same manner as in conventional heat exchange towers of this type.

送風機18aの運転及び停止時において、上部
排気口18より前記エア室17内に侵入した雨水
雪、霰、雹などは落下し前記受け皿20内に落下
収集され、雪、霰、雹は融解後、下部水槽19内
の冷媒若しくは熱媒に混入することなく、排水管
21を経て、冷媒若しくは熱媒系路外へ排出され
るため、冷媒、熱媒の濃度が雨水などにより薄め
られることはなく、殊に冷媒、熱媒が不凍液の場
合には、雨水などの混入による氷結事故を未然に
防止することが出来、例えば寒冷地又は冬期に使
用される暖房装置の加熱塔に最適である。
During operation and stop of the blower 18a, rainwater, snow, hailstones, etc. that enter the air chamber 17 through the upper exhaust port 18 fall and are collected in the tray 20, and after melting, the snow, hailstones, hailstones, etc. Since it is discharged outside the refrigerant or heat medium system path through the drain pipe 21 without mixing with the refrigerant or heat medium in the lower water tank 19, the concentration of the refrigerant or heat medium will not be diluted by rainwater, etc. In particular, when the refrigerant or heating medium is antifreeze, it is possible to prevent freezing accidents due to contamination with rainwater, etc., and it is ideal for heating towers of heating devices used in cold regions or in winter, for example.

上部排気口18は上向きとしてあるため、排気
口18に方向性がなく、排気口18より背の高い
起立壁があつても、排気に支障なく、前記雨水な
どの混入防止効果を有する冷却塔Aを、周囲の環
境に左右されずに自由に設置できる。
Since the upper exhaust port 18 faces upward, there is no directionality in the exhaust port 18, and even if there is a standing wall that is taller than the exhaust port 18, there is no problem with the exhaust air, and the cooling tower A has the effect of preventing rainwater from entering. can be freely installed without being affected by the surrounding environment.

前記受け皿20は、上部排気口18真下の下部
水槽19の水面のみを覆つているため、充填材1
5を流下した冷媒若しくは熱媒は、支障なく従来
通り下部水槽19内へ流入収集することができ、
再循環利用出来る。
Since the saucer 20 covers only the water surface of the lower water tank 19 directly below the upper exhaust port 18, the filler 1
The refrigerant or heat medium that has flowed down through the lower water tank 19 can be flowed and collected in the lower water tank 19 as before without any hindrance.
Can be recycled and used.

実施態様の効果を次に説明する。 The effects of the embodiment will be explained next.

多数の上部排気口18を並設してなる熱交換塔
においても、全ての排気口18の真下の下部水槽
19の水面は、平面矩形の単一の受け皿21によ
り覆われているため、どれか一つの排気口18に
設けた送風機18aを停止し他の排気口18の送
風機18aを運転する形式でも、適切に雨水など
をこの受け皿20で受け、冷媒若しくは熱媒への
混入を防止できる。
Even in a heat exchange tower having a large number of upper exhaust ports 18 arranged in parallel, the water surface of the lower water tank 19 directly below all the exhaust ports 18 is covered by a single tray 21 having a rectangular planar shape. Even in the case where the blower 18a provided at one exhaust port 18 is stopped and the blower 18a of the other exhaust port 18 is operated, rainwater and the like can be appropriately received in the tray 20 and prevented from mixing with the refrigerant or heat medium.

前記受け皿20を具備すると共に上部排気口1
8に前記排気ダクト22を接続した実施態様にお
いては、(第2図乃至第6図参照)この排気ダク
ト22上に降り注ぐ雨水などは、各板23(=2
3a)で一度捕捉された後、その排水樋24に集
められた後、この排水樋24に沿い板23(=2
3a)の一端(外端)に向け移動し、前記上部排
気口18外の外部へ排出され、上部排気口18よ
り冷却塔本体12内に殆んど落下せず、受け皿2
0上へ落下する雨水等の量を大幅に削減でき、仮
に少量の雨水などが外風により隣接する板23間
の間隙を通りエア室17内へ侵入しても、前記受
け皿20により受け取ることができ、ほゞ完壁に
雨水などが冷媒又は熱媒に混入するのを、受け皿
20の容量を大きくすることなく防止でき、受け
皿20を小型化できる。
The upper exhaust port 1 is provided with the receiving tray 20 and the upper exhaust port 1.
In the embodiment in which the exhaust duct 22 is connected to the exhaust duct 22 at the plate 23 (see FIGS.
3a) and collected in the drainage gutter 24, the plate 23 (=2
3a) moves toward one end (outer end), is discharged to the outside outside the upper exhaust port 18, hardly falls into the cooling tower main body 12 from the upper exhaust port 18, and the receiving tray 2
The amount of rainwater etc. falling onto the air chamber 17 can be significantly reduced, and even if a small amount of rainwater etc. enters the air chamber 17 through the gap between the adjacent plates 23 due to the outside wind, it can be received by the receiving tray 20. Therefore, it is possible to almost completely prevent rainwater or the like from mixing with the refrigerant or heat medium without increasing the capacity of the tray 20, and the tray 20 can be made smaller.

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

図は、この考案に係るもので、第1図は、この
考案の代表的な実施態様の概略図、第2図は排気
ダクトを第1図のものに組込んだ態様を示す概略
図、第3図は第2図のダクト部分の破断斜視図、
第4図は、その板の斜視図、第5図は、排気ダク
トの他の実施態様の半断面図、第6図は、第5図
の排気ダクトの一部破断平面図、第7図は、従来
のエルボ型ダクト付き直交流熱交換塔の概略図で
ある。 図中の主な記号の説明、17…エア室、18…
上部排気口、19…下部水槽、20…雨水受け
皿。
The figures relate to this invention; FIG. 1 is a schematic diagram of a typical embodiment of this invention, FIG. 2 is a schematic diagram showing an embodiment in which an exhaust duct is incorporated into the one in FIG. Figure 3 is a cutaway perspective view of the duct part in Figure 2;
FIG. 4 is a perspective view of the plate, FIG. 5 is a half-sectional view of another embodiment of the exhaust duct, FIG. 6 is a partially cutaway plan view of the exhaust duct of FIG. 5, and FIG. , is a schematic diagram of a conventional elbow-type ducted cross-flow heat exchange tower. Explanation of main symbols in the diagram, 17...air chamber, 18...
Upper exhaust port, 19...lower water tank, 20...rainwater tray.

Claims (1)

【実用新案登録請求の範囲】 1 上部水槽より充填材上に冷媒若しくは熱媒を
散水し、冷媒若しくは熱媒の流下路に対し直交
して、本体内部に形成したエア室内へ外気を導
きこのエア室の真上の上部排気口より排気し、
この外気と冷媒若しくは熱媒間で熱交換を行
い、熱交換した冷媒若しくは熱媒を前記エア室
の下部に設置した下部水槽に収集する直交流式
熱交換塔において、 この上部排気口真下の下部水槽の水面のみを
覆うに充分な大きさの液体受け皿がこの水面上
に配置してあり、この受け皿内に滞留した液体
を冷媒若しくは熱媒系路外へ排出自在としてあ
ることを特徴とする直交流式熱交換塔。 2 前記冷媒若しくは熱媒は不凍液としてある実
用新案登録請求の範囲第1項記載の直交流式熱
交換塔。 3 上部排気口が、長手方向に多数並設してある
実用新案登録請求の範囲第1項又は第2項記載
の直交流式熱交換塔。
[Scope of Claim for Utility Model Registration] 1. Sprinkling refrigerant or heating medium onto the filling material from the upper water tank, and directing outside air into the air chamber formed inside the main body orthogonally to the flow path of the refrigerant or heating medium. Exhaust air from the upper exhaust port directly above the chamber.
In a cross-flow heat exchange tower that exchanges heat between this outside air and a refrigerant or heat medium, and collects the heat-exchanged refrigerant or heat medium in a lower water tank installed at the bottom of the air chamber, the lower part directly below this upper exhaust port is used. A liquid receiving tray large enough to cover only the water surface of the water tank is placed above the water surface, and the liquid stagnant in this receiving tray can be freely discharged to the outside of the refrigerant or heat medium system path. AC heat exchange tower. 2. The cross-flow heat exchange tower according to claim 1, wherein the refrigerant or heating medium is an antifreeze liquid. 3. The cross-flow type heat exchange tower according to claim 1 or 2, wherein a large number of upper exhaust ports are arranged in parallel in the longitudinal direction.
JP7535885U 1985-05-21 1985-05-21 Expired JPH0129430Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7535885U JPH0129430Y2 (en) 1985-05-21 1985-05-21

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7535885U JPH0129430Y2 (en) 1985-05-21 1985-05-21

Publications (2)

Publication Number Publication Date
JPS61192170U JPS61192170U (en) 1986-11-29
JPH0129430Y2 true JPH0129430Y2 (en) 1989-09-07

Family

ID=30616506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7535885U Expired JPH0129430Y2 (en) 1985-05-21 1985-05-21

Country Status (1)

Country Link
JP (1) JPH0129430Y2 (en)

Also Published As

Publication number Publication date
JPS61192170U (en) 1986-11-29

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