JPH0829074A - White smoke preventing device for closed cross flow cooling tower - Google Patents
White smoke preventing device for closed cross flow cooling towerInfo
- Publication number
- JPH0829074A JPH0829074A JP18097694A JP18097694A JPH0829074A JP H0829074 A JPH0829074 A JP H0829074A JP 18097694 A JP18097694 A JP 18097694A JP 18097694 A JP18097694 A JP 18097694A JP H0829074 A JPH0829074 A JP H0829074A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- water tank
- air
- water
- cooling tower
- 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.)
- Granted
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】空調設備、工業設備等の冷却水の
冷却用として冷却塔が幅広く用いられているが、このう
ち年間運転設備等に使用されている冷却塔においては、
外気温が低下すると冷却塔からの排出空気が白煙となり
問題となる。本発明は、この白煙を防止するためになさ
れた密閉式直交流形冷却塔の白煙防止装置に関するもの
である。[Industrial application] Cooling towers are widely used for cooling cooling water for air-conditioning equipment, industrial equipment, etc.
When the outside air temperature decreases, the air discharged from the cooling tower becomes white smoke, which is a problem. The present invention relates to a white smoke prevention device for a closed cross-flow cooling tower designed to prevent the white smoke.
【0002】[0002]
【従来の技術】空調設備、工業設備等における冷却水の
冷却用として冷却塔が使用される。この冷却塔から排出
される空気は、高温多湿であって冬期等外気温が低いと
きには排出空気中の湿気は白煙状態となって排出され、
交通の障害となったり、また夜間においてはこれに光が
当たると火災と見間違う恐れがある。この白煙を発生を
防止するため、従来の技術としては充填物と熱交換器を
併設して、乾式熱交換器(プレートフィンコイル)を配
した冷却塔または充填物部分に樹脂製熱交換器を組み込
んだ冷却塔がある。2. Description of the Related Art A cooling tower is used for cooling cooling water in air conditioning equipment, industrial equipment and the like. The air discharged from this cooling tower is hot and humid, and when the outside air temperature is low such as in winter, the humidity in the discharged air is discharged as white smoke.
There is a risk that it will be a traffic obstacle and that it may be mistaken for a fire if it is exposed to light at night. In order to prevent the generation of this white smoke, the conventional technology is to install a packing and a heat exchanger together, and a resin heat exchanger in the cooling tower or the packing part where the dry heat exchanger (plate fin coil) is arranged. There is a cooling tower that incorporates.
【0003】[0003]
【発明が解決しようとする課題】従来の密閉式冷却塔に
おいて、乾式熱交換器を配したものは乾式熱交換器を組
み込むためのスペースを必要とするため大型化し、また
空気圧損も大きくなり送風機の動力アップとなる。さら
に乾式熱交換器の接続配管、温調弁等が必要で、特別な
構造としなければならず特別な塔本体を必要とする。一
方充填物に樹脂製熱交換器を組み込んだものは、構造上
複雑になると共に、また冬期において著しく冷却能力が
低下し、大きな塔体を必要とし、また冬期においては水
温が低下し過冷却となるため、乾き空気の割合に対し湿
り空気の割合が多くなり白煙が発生しやすくなる。さら
に充填物、熱交換器を通過してきた空気は、整流されて
いて塔内では充分混合されていないため、送風機により
外気へ放出時、湿り空気部分において白煙を生ずる等の
問題がある。The conventional closed type cooling tower with the dry heat exchanger is large in size because it requires a space for incorporating the dry heat exchanger, and the air pressure loss is large, so that a blower is required. Power up. Furthermore, a connecting pipe for the dry heat exchanger, a temperature control valve, etc. are required, and a special structure is required and a special tower body is required. On the other hand, the one in which the resin heat exchanger is incorporated in the packing becomes complicated in structure, and the cooling capacity is remarkably lowered in the winter season, which requires a large tower body, and the water temperature is lowered in the winter season to cause overcooling. Therefore, the ratio of moist air is higher than the ratio of dry air, and white smoke is likely to be generated. Further, since the air that has passed through the packing and the heat exchanger is rectified and not sufficiently mixed in the tower, there is a problem that white smoke is generated in the moist air portion when discharged to the outside air by the blower.
【0004】本発明は密閉式直交流形冷却塔において冬
期でも確実に白煙の発生を防止することを目的とする。An object of the present invention is to reliably prevent the generation of white smoke in a closed cross-flow type cooling tower even in winter.
【0005】[0005]
【課題を解決するための手段】前記課題を解決するため
に、この発明の冷却塔は送風機、上部水槽、充填物、熱
交換器、下部水槽、散布水ポンプ、三方弁及び混合板等
で構成され、上部水槽は空気吸込口側から見て任意の位
置にて仕切られていて上部水槽A,Bとして形成してあ
る。散布水は散布水ポンプにより送水されるが、下部水
槽〜散布水ポンプ〜上部水槽へと配管されていて、その
途中に各々三方弁が設けられ、散布水をバイパス配管よ
り直接下部水槽にバイパスされるようになっている。三
方弁はワックス式温調弁で水温により自動開閉し、水温
が高くなるとバイパス側を閉じ、低くなると開ける構造
のものである。このうち上部水槽A用の三方弁は水温が
低くなるとバイパス側全開となり全量バイパスされる。
上部水槽B用の三方弁は水温が低くなるとバイパス側1
00%未満〜50%くらい開となり、これに相当する水
量がバイパスされる。充填物、熱交換器は一段または二
段以上設けられ、各段に設けられる熱交換器は上部水槽
の仕切りの位置で分割されており、隣り合った熱交換器
は配管で接続されていて、プロセス水は熱交換器Aで冷
却された後、熱交換器Bで冷却される方式となってい
る。また充填物の空気吹出し側または熱交換器の吹出し
側には、混合板が設けられていて、充填物及び熱交換器
からの吹出し空気を塔内で混合されるよう形成してあ
る。この混合板は固定式または回転式があり、固定式の
V形形状で充填物または熱交換器からの空気の流れに対
して並行に導かれ、単体または複数個で構成されてい
る。回転式の場合、回転軸に取り付けられた2枚以上の
複数個の羽根が送風機によって風を受け回転するよう形
成されている。In order to solve the above problems, the cooling tower of the present invention comprises a blower, an upper water tank, a packing, a heat exchanger, a lower water tank, a spray water pump, a three-way valve and a mixing plate. The upper water tank is partitioned at arbitrary positions when viewed from the air suction port side, and is formed as upper water tanks A and B. The spray water is sent by a spray water pump, but it is piped from the lower water tank to the spray water pump to the upper water tank, and a three-way valve is installed in the middle of each, and the spray water is bypassed directly to the lower water tank through the bypass pipe. It has become so. The three-way valve is a wax-type temperature control valve that automatically opens and closes according to the water temperature, closes the bypass side when the water temperature rises, and opens it when the water temperature falls. Of these, the three-way valve for the upper water tank A is fully opened on the bypass side when the water temperature becomes low, and the entire amount is bypassed.
The three-way valve for upper water tank B is on the bypass side 1 when the water temperature becomes low.
Open from less than 00% to about 50%, and the amount of water equivalent to this is bypassed. Packings, heat exchangers are provided in one stage or two or more stages, the heat exchangers provided in each stage are divided at the position of the partition of the upper water tank, and adjacent heat exchangers are connected by piping. The process water is cooled in the heat exchanger A and then in the heat exchanger B. Further, a mixing plate is provided on the air blowing side of the packing or on the blowing side of the heat exchanger so that the packing and the air blown from the heat exchanger are mixed in the tower. The mixing plate may be of a fixed type or a rotary type, and has a fixed V-shape, which is guided in parallel to the air flow from the packing or the heat exchanger, and is composed of a single unit or a plurality of units. In the case of the rotary type, two or more blades attached to the rotary shaft are formed so as to rotate by receiving the wind by the blower.
【0006】[0006]
【作 用】本発明の冷却塔において、負荷からの冷却水
(プロセス水)は塔内各段左右の熱交換器7A,7Bの
管内を通過し、冷却された後再び負荷に送水される。ま
た下部水槽の水は散布水ポンプにて上部水槽に送水さ
れ、左右に仕切られた各槽へと水が送水され、散水孔よ
り散水される。この散水された水は充填物内で送風機に
よって吸引された外気と直角に交叉し、水と空気が直接
接触により熱交換し、水は冷却され、空気は加熱加湿さ
れる。次に熱交換器部では充填物内で冷却された水が管
外表面を伝わって流れ、管内のプロセス水を冷却する。
この時送風機によって吸引された外気と散布水が直接接
触し、水の蒸発蓄熱により散布水及び管内のプロセス水
を冷却する。熱交換器部を通過した散布水は下段の充填
物、熱交換器を通過し、下部水槽に集められる。空気は
充填物、熱交換器を通過した際、加熱加湿され混合板に
よって混合された後、送風機により塔外に排出される。
冬期等において外気温が低下すると、散布水温も低下
し、散布水ポンプから上部水槽への配管途中に設けられ
た三方弁が作動し、一方の三方弁では全量バイパスさ
れ、他方の三方弁では全量の100%未満〜50%くら
いまでバイパスされる。このため一方の上部水槽4A側
には水は送水されず、他方の上部水槽B側には50%〜
100%の間で送水され散水孔より散水される。散布水
が流れない上部水槽4A側において、充填物内は水が流
れず空気のみ通過し、一方の熱交換器7Aでは管外表面
を外気が通過し、管内のプロセス水と熱交換(顕熱によ
り熱交換)し、外気は加熱されるだけで湿度は低下し、
プロセス水は冷却される。他方の上部水槽4B側では、
散布水が少ないものの夏期と同様の熱交換が行われる。
この場合、散布水量の少ないぶん湿度の割合が少なくな
る。一方の充填物6Aを通過した空気、熱交換器7Aを
通過した高温低湿の空気、他方の充填物6B、熱交換器
7Bを通過した高温多湿の空気が混合板により混合され
た後、送風機によって排気され、低温の外気にさらされ
ても高温低湿のため白煙とはならない。[Operation] In the cooling tower of the present invention, the cooling water (process water) from the load passes through the tubes of the heat exchangers 7A and 7B on the left and right of each stage in the tower, is cooled, and is then sent to the load again. Further, the water in the lower water tank is sent to the upper water tank by a spray water pump, and the water is sent to each of the tanks partitioned on the left and right, and is sprayed from the water spray holes. The sprinkled water intersects with the outside air sucked by the blower at a right angle in the filling, the water and the air exchange heat by direct contact, the water is cooled, and the air is heated and humidified. Next, in the heat exchanger part, the water cooled in the filling flows along the outer surface of the pipe to cool the process water in the pipe.
At this time, the outside air sucked by the blower comes into direct contact with the sprayed water, and the sprayed water and the process water in the pipe are cooled by the evaporation heat of water. The sprayed water that has passed through the heat exchanger section passes through the lower packing material and the heat exchanger and is collected in the lower water tank. When the air passes through the packing and the heat exchanger, it is heated and humidified, mixed by a mixing plate, and then discharged outside the tower by a blower.
When the outside air temperature decreases in winter etc., the spray water temperature also drops, and the three-way valve installed in the middle of the pipe from the spray water pump to the upper water tank operates. Bypassing from less than 100% to about 50%. Therefore, no water is sent to the one upper water tank 4A side, and 50% to the other upper water tank B side.
Water is sent between 100% and water is sprayed from the water spray holes. On the side of the upper water tank 4A where the sprayed water does not flow, water does not flow in the filling and only air passes, and the outside air passes through the outer surface of the pipe in the heat exchanger 7A, and heat exchange with the process water in the pipe (sensible heat). Heat exchange), the outside air is only heated and the humidity drops,
The process water is cooled. On the other side of the upper water tank 4B,
Although the amount of sprayed water is small, heat exchange is performed as in summer.
In this case, the proportion of humidity with a small amount of sprayed water decreases. After the air passing through one of the packings 6A, the high temperature and low humidity air passing through the heat exchanger 7A, and the other packing 6B and the hot and humid air passing through the heat exchanger 7B are mixed by the mixing plate, the air is blown by the blower. Even if it is exhausted and exposed to low temperature outside air, it does not turn into white smoke due to high temperature and low humidity.
【0007】[0007]
【実施例】以下本発明密閉式直交流形冷却塔の白煙防止
装置を図面に示す実施例にもとづいて説明する。図1、
図2において1は密閉式直交流形の冷却塔であり、この
塔体2の相対する両面は空気吸込口3となっており、上
部水槽4は仕切板19で左右2つに仕切られて、一方の
上部水槽4Aと他方の上部水槽4Bとに分けられてい
る。塔体2の内部には充填物6も上部水槽4と同じよう
に左右に分けられ、上部水槽4Aの下部に充填物6A
を、上部水槽4Bの下方に充填物6Bを、熱交換器7も
同様に分割されて熱交換器7A,7Bが分けられて一段
または複数段設けられている。下部には水を集める下部
水槽8を設けている。塔体2の上部には送風機16と送
風機16を駆動するための電動機17が設けられてい
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A white smoke prevention device for a closed crossflow type cooling tower according to the present invention will be described below with reference to the embodiments shown in the drawings. Figure 1,
In FIG. 2, reference numeral 1 is a closed cross-flow type cooling tower, both opposing surfaces of the tower body 2 are air inlets 3, and the upper water tank 4 is divided into two left and right by a partition plate 19, It is divided into one upper water tank 4A and the other upper water tank 4B. In the inside of the tower body 2, the packing 6 is also divided into the right and left like the upper water tank 4, and the packing 6A is placed below the upper water tank 4A.
In the same manner, the filler 6B is provided below the upper water tank 4B, and the heat exchanger 7 is also divided in the same manner to provide the heat exchangers 7A and 7B in one or more stages. A lower water tank 8 for collecting water is provided in the lower part. A blower 16 and an electric motor 17 for driving the blower 16 are provided on the upper portion of the tower body 2.
【0008】プロセス配管14,15は熱交換器7A,
7Bを介して配管されており、また左右の熱交換器7A
と7Bとは図2に示す如く接続配管で接続されている。The process pipes 14 and 15 are heat exchangers 7A,
7B, and the left and right heat exchangers 7A
2 and 7B are connected by a connecting pipe as shown in FIG.
【0009】次に散布水配管10,11は、下部水槽8
より散布水ポンプ9を経て散布水配管10、散布水配管
11にて上部水槽4へと接続されており、この散布水配
管10,11に三方弁12、三方弁13が組み込まれて
いる。Next, the spray water pipes 10 and 11 are connected to the lower water tank 8.
Further, it is connected to the upper water tank 4 through a spray water pump 9 and a spray water pipe 10 and a spray water pipe 11, and the spray water pipes 10 and 11 have a three-way valve 12 and a three-way valve 13 incorporated therein.
【0010】また塔体2内には図1、図2に示すように
固定式の混合板18が設けている。この混合板を回転式
とする場合は図3〜図6に示すようになす。A fixed mixing plate 18 is provided in the tower body 2 as shown in FIGS. When this mixing plate is of the rotary type, it is formed as shown in FIGS.
【0011】次に上述の如く構成される、本発明による
冷却塔の動作を説明する。下部水槽8に貯められた水
(散布水)は、散布水ポンプ9によって散布水配管1
0,11内を流れ、上部水槽4A,4Bに各々供給され
る。散布水は上部水槽4A,4Bの散水孔より散水さ
れ、充填物6A,6B、熱交換器7A,7Bを通って下
部水槽8に集められる。外気は送風機16により吸い込
まれ、充填物6A,6B内では水と空気との直接接触に
より熱交換が行われ散布水は冷却され、空気は加熱高湿
となり、熱交換器7A,7B部ではプロセス水の通る管
外表面を散布水が流れ、散布水と空気の直接接触による
熱交換がおこなれると共に、主として水の蒸発蓄熱によ
り熱交換器内のプロセス水を冷却する。これら高温多湿
の空気は、混合板18により混合させられた後、送風機
16により塔外に排出される。Next, the operation of the cooling tower according to the present invention constructed as described above will be described. The water (spray water) stored in the lower water tank 8 is sprayed by the spray water pump 9 to the spray water pipe 1.
It flows through the inside of 0 and 11, and is supplied to upper water tanks 4A and 4B, respectively. The sprayed water is sprayed from the spray holes of the upper water tanks 4A and 4B, passes through the fillers 6A and 6B and the heat exchangers 7A and 7B, and is collected in the lower water tank 8. The outside air is sucked in by the blower 16, heat is exchanged by direct contact between water and air in the fillers 6A, 6B, the sprayed water is cooled, the air becomes heated and humid, and the heat exchangers 7A, 7B process The sprayed water flows on the outer surface of the pipe through which water flows, heat is exchanged by direct contact between the sprayed water and air, and the process water in the heat exchanger is cooled mainly by the evaporation heat of water. The hot and humid air is mixed by the mixing plate 18, and then discharged by the blower 16 to the outside of the tower.
【0012】冬期になり外気温が低下すると、三方弁1
2はバイパス側に全開となり、上部水槽4Aには散布水
が送水されない。三方弁13は一部(50%〜100未
満%)がバイパス側に流れ、残りの水は上部水槽4Bに
送水される。When the outside temperature decreases in winter, the three-way valve 1
No. 2 is fully opened to the bypass side, and spray water is not sent to the upper water tank 4A. A part (50% to less than 100%) of the three-way valve 13 flows to the bypass side, and the remaining water is sent to the upper water tank 4B.
【0013】上部水槽4A側では散水されないため、充
填物6Aを通過した空気は外気と同じ状態で、熱交換器
7Aを通過した空気は管内を流れるプロセス水の高温側
と間接的に熱交換(顕熱による熱交換)し、空気は絶対
湿度が一定のままで加熱され、高温低湿空気となる。次
に上部水槽4B側では散布水量が減少の状態で散水さ
れ、充填物6Bを通過した空気は水と直接接触による熱
交換し高温多湿となり、熱交換器7Bを通過した空気は
水と直接接触による熱交換を行い、そのときの蒸発蓄熱
によりプロセス水を冷却すると共に、散布水も冷却され
空気は高温多湿となる。Since the water is not sprinkled on the side of the upper water tank 4A, the air passing through the filling 6A is in the same state as the outside air, and the air passing through the heat exchanger 7A indirectly exchanges heat with the high temperature side of the process water flowing in the pipe ( Heat is exchanged by sensible heat), and the air is heated at a constant absolute humidity to become high-temperature low-humidity air. Next, in the upper water tank 4B side, the amount of sprayed water is sprinkled in a reduced state, the air passing through the filler 6B directly exchanges heat with the water to become hot and humid, and the air passing through the heat exchanger 7B comes into direct contact with the water. The heat is exchanged with the process water, and the process water is cooled by the evaporation heat at that time, and the spray water is also cooled, and the air becomes hot and humid.
【0014】各充填物6A,6B、熱交換器7A,7B
を通過した空気は混合板18により混合し、低湿の空気
となって送風機16により低温の外気に放出されても、
過飽和空気とならず白煙を生じない。Each packing 6A, 6B, heat exchanger 7A, 7B
The air that has passed through is mixed by the mixing plate 18 to become low-humidity air and is discharged to the low temperature outside air by the blower 16,
Does not produce super-saturated air and does not generate white smoke.
【0015】[0015]
【発明の効果】本発明においては、冬期一方の上部水槽
A側では三方弁の働きにより水は全量バイパスされ散水
されないため、一方の充填物を通過した空気は外気温の
ままで温度のみ上昇した乾き空気となる。また他方の上
部水槽B側では三方弁の働きにより水は50%〜100
%未満バイパスされ、夏期に比べ散水量が少ないため、
この上部水槽側の充填物、熱交換器を通過した空気は中
温多湿の空気となる。従ってこれらの吹出し空気は混合
板により塔内で混合された後、送風機によって気温が低
下している外気へ排出しても過飽和空気とならないの
で、白煙を生じない。さらに乾式熱交換器(プレートフ
ィンコイル)を組み込まないため、据付面積が少なくて
すみ、乾式熱交換器の配管等が不要で特別な塔体を必要
としない。また散布水配管途中に三方弁の組み込みと上
部水槽を任意の位置で仕切ると共に、混合板を組み込む
ことにより、安価な塔体が利用でき、かつ容量に応じた
上部水槽の仕切と三方弁の選定により、冷却性能の確保
と白煙防止機能を満足することができる。According to the present invention, in the winter, one side of the upper water tank A side bypasses the entire amount of water due to the operation of the three-way valve and is not sprayed. It becomes dry air. On the other hand, on the side of the upper water tank B, the water is 50% to 100% due to the function of the three-way valve.
Bypassing less than%, the amount of water sprinkled is smaller than in the summer, so
The air that has passed through the filling material on the upper water tank side and the heat exchanger becomes medium-temperature and high-humidity air. Therefore, even if these blown-out air is mixed in the tower by the mixing plate and then discharged to the outside air whose temperature is lowered by the blower, it does not become supersaturated air, so that white smoke is not generated. Further, since the dry heat exchanger (plate fin coil) is not incorporated, the installation area is small, the piping of the dry heat exchanger is unnecessary, and no special tower body is required. Also, by incorporating a three-way valve in the middle of the spray water pipe and partitioning the upper water tank at any position, and by incorporating a mixing plate, an inexpensive tower can be used, and the partition of the upper water tank and selection of the three-way valve according to the capacity As a result, the cooling performance can be secured and the white smoke prevention function can be satisfied.
【図1】本発明密閉式直交流形冷却塔の白煙防止装置の
一実施例を示す縦断面図である。FIG. 1 is a vertical cross-sectional view showing an embodiment of a white smoke prevention device for a closed crossflow type cooling tower of the present invention.
【図2】同側面図である。FIG. 2 is a side view of the same.
【図3】異なる実施例の縦断面図である。FIG. 3 is a vertical sectional view of a different embodiment.
【図4】同横断平面図である。FIG. 4 is a transverse plan view of the same.
【図5】ヘッダー部の詳細図である。FIG. 5 is a detailed view of a header section.
【図6】混合板の正面図である。FIG. 6 is a front view of a mixing plate.
1 密閉式直交流形冷却塔 2 塔体 3 空気吸込口 4 上部水槽 5 分流槽 6 充填物 7 熱交換器 8 下部水槽 9 散布水ポンプ 10 散布水配管 11 散布水配管 12 三方弁 13 三方弁 16 送風機 17 電動機 18 混合板 19 仕切板 20 水量調節弁 21 接続配管 30 ヘッダー 32 固定板 33 軸受台 34 回転軸 35 軸受 36 軸受 37 摺動部 1 Closed cross flow type cooling tower 2 Tower body 3 Air suction port 4 Upper water tank 5 Dividing tank 6 Filling material 7 Heat exchanger 8 Lower water tank 9 Spraying water pump 10 Spraying water piping 11 Spraying water piping 12 Three-way valve 13 Three-way valve 16 Blower 17 Electric motor 18 Mixing plate 19 Partition plate 20 Water amount control valve 21 Connection pipe 30 Header 32 Fixing plate 33 Bearing base 34 Rotating shaft 35 Bearing 36 Bearing 37 37 Sliding part
Claims (4)
下部水槽、散布水ポンプ等で構成され、吸込面は一面ま
たは二面吸い込みとし、負荷からの水(以下プロセス水
という)は、熱交換器部において散布水と空気により冷
却され、散布水は充填物内で空気と直接接触により冷却
される密閉式直交流形冷却塔において、上部水槽を空気
吸込口側から見て任意の位置にて仕切ると共に、仕切ら
れた各上部水槽には分流槽を設け、入口側には散布水ポ
ンプの出口側と配管で接続され、一方の配管には途中に
バイパス配管を設けて下部水槽へと直接流れ出るように
なすと共に、バイパス配管と散布水配管の分岐部にはワ
ックス式三方弁を組み込まれていることを特徴とする密
閉式直交流形冷却塔の白煙防止装置。1. A blower, an upper water tank, a packing, a heat exchanger,
It consists of a lower water tank, spray water pump, etc. The suction surface is one side or two sides suction, the water from the load (hereinafter referred to as process water) is cooled by the spray water and air in the heat exchanger section, and the spray water is filled. In a closed cross-flow type cooling tower that is cooled by direct contact with air inside an object, the upper water tank is partitioned at an arbitrary position as seen from the air suction port side, and a dividing tank is provided for each partitioned upper water tank. , The inlet side is connected to the outlet side of the spray water pump by piping, and one pipe is provided with a bypass pipe on the way to directly flow out to the lower water tank, and at the branch part of the bypass pipe and the spray water pipe. Is a white smoke prevention device for a closed cross flow type cooling tower, which is equipped with a wax type three-way valve.
は、単段または2段以上で構成し、熱交換器の各段は上
部水槽の仕切板の位置で分割され、各段毎に熱交換器同
志が接続されていることを特徴とする請求項1記載の密
閉式直交流形冷却塔の白煙防止装置。2. The packing constituting the cooling tower and the heat exchanger are constituted by a single stage or two or more stages, and each stage of the heat exchanger is divided at the position of the partition plate of the upper water tank, and each stage is divided. The white smoke prevention device for a closed cross-flow cooling tower according to claim 1, wherein each heat exchanger is connected to each other.
換器出口部分に混合板を設け、充填物または熱交換器か
らの空気の流れに対して並行V字形に置かれ、単体また
は複数個以上で構成されていて充填物及び熱交換器から
の出口空気を混合させることを特徴とする請求項1記載
の密閉式直交流形冷却塔の白煙防止装置。3. A mixing plate is provided immediately below the blower at the packing outlet or the heat exchanger outlet, and is placed in a V-shape parallel to the flow of air from the packing or the heat exchanger. 2. The white smoke prevention device for a closed cross-flow cooling tower according to claim 1, wherein the mixture and the outlet air from the heat exchanger are mixed with each other.
換器出口部分に混合板を設け、回転軸に取り付けられた
2枚以上の複数個の羽根が送風機によって風を受け回転
し、充填物及び熱交換器からの出口空気を混合させるこ
とを特徴とする請求項1記載の密閉式直交流形冷却塔の
白煙防止装置。4. A mixing plate is provided immediately below the blower at the filling material outlet portion or the heat exchanger outlet portion, and two or more blades attached to the rotary shaft rotate by receiving the wind by the blower, The white smoke prevention device for a closed cross-flow cooling tower according to claim 1, wherein the outlet air from the heat exchanger is mixed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18097694A JP3220597B2 (en) | 1994-07-08 | 1994-07-08 | White smoke prevention device for hermetic cross-flow cooling tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18097694A JP3220597B2 (en) | 1994-07-08 | 1994-07-08 | White smoke prevention device for hermetic cross-flow cooling tower |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0829074A true JPH0829074A (en) | 1996-02-02 |
JP3220597B2 JP3220597B2 (en) | 2001-10-22 |
Family
ID=16092576
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18097694A Expired - Fee Related JP3220597B2 (en) | 1994-07-08 | 1994-07-08 | White smoke prevention device for hermetic cross-flow cooling tower |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3220597B2 (en) |
-
1994
- 1994-07-08 JP JP18097694A patent/JP3220597B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP3220597B2 (en) | 2001-10-22 |
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