JPH041274B2 - - Google Patents
Info
- Publication number
- JPH041274B2 JPH041274B2 JP58196961A JP19696183A JPH041274B2 JP H041274 B2 JPH041274 B2 JP H041274B2 JP 58196961 A JP58196961 A JP 58196961A JP 19696183 A JP19696183 A JP 19696183A JP H041274 B2 JPH041274 B2 JP H041274B2
- Authority
- JP
- Japan
- Prior art keywords
- tower
- dry
- cooling section
- cooling
- 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
Links
- 238000001816 cooling Methods 0.000 claims description 77
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 41
- 239000000498 cooling water Substances 0.000 claims description 10
- 238000005192 partition Methods 0.000 claims description 10
- 239000007921 spray Substances 0.000 claims description 6
- 238000009434 installation Methods 0.000 description 9
- 239000000779 smoke Substances 0.000 description 5
- 230000000630 rising effect Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
- F28C1/14—Direct-contact trickle coolers, e.g. cooling towers comprising also a non-direct contact heat exchange
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/70—Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating
Landscapes
- 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】
本発明は乾・湿式冷水塔に係り、特に伝熱管群
からなる高重量の乾式冷却部の設置位置を低くで
き、乾式冷却部の支持架構を小型、簡易化し得る
乾・湿式冷水塔に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dry/wet cooling tower, and in particular to a dry cooling tower that can lower the installation position of a heavy dry cooling section consisting of a group of heat transfer tubes, and downsize and simplify the support structure of the dry cooling section.・Regarding wet cooling towers.
乾・湿式冷水塔は、化学工場、製鉄所等のプラ
ントや発電所などで発生する温水を冷却処理する
装置であり、温水と冷気(外気)とを間接熱交換
させて冷却する乾式冷却部と、直接熱交換させて
冷却する湿式冷却部とを備えている。第1図に
は、湿式冷却部を流下する温水に上昇する冷気を
向流させて温水を冷却する向流型の乾・湿式冷水
塔の従来例が示されている。 A dry/wet cooling water tower is a device that cools hot water generated in plants such as chemical factories, steel mills, power plants, etc. It has a dry cooling section that cools hot water and cold air (outside air) by indirect heat exchange , and a wet cooling section that performs direct heat exchange for cooling. FIG. 1 shows a conventional example of a countercurrent type dry/wet cooling water tower that cools hot water by causing cold air rising to flow countercurrently to hot water flowing down a wet cooling section.
図示する如く、冷水塔aの上部側壁と底部側壁
とには、外気の取入口b,cがそれぞれ設けられ
ており、塔a内の中間部には温水を流下させる充
填層を有する湿式冷却部dが設けられている。湿
式冷却部dの上方には、温水を散布する散水管e
が配設されている。そして、散水管eから散布さ
れ湿式冷却部dの充填層を流下する温水は、冷水
塔a底部の取入口cから塔a内に導入され充填層
を上昇する外気と直接接触して冷却される。一
方、湿式冷却部dの充填層を流下する温水を冷却
処理し、湿気を多量に含む湿り空気は、塔a内上
部のプレナム部fに流入する。冬期などにおいて
は、この湿り空気をそのまま排気筒gから大気開
放すると、白煙を生じ公害問題となるので、冷水
塔a上部の取入口b外側に設けられた乾式冷却部
hからプレナム部fに高温の乾燥空気を導入し、
上記湿り空気と混合させて後、排気筒gから排出
するようにして排気の白煙化を防止している。 As shown in the figure, the upper side wall and the bottom side wall of the cooling tower a are provided with outside air intake ports b and c, respectively, and a wet cooling section having a packed bed in which hot water flows down is provided in the middle part of the tower a. d is provided. Above the wet cooling section d, there is a sprinkler pipe e that sprays hot water.
is installed. The hot water that is sprayed from the sprinkler pipe e and flows down the packed bed of the wet cooling section d is introduced into the tower a from the intake port c at the bottom of the cooling tower a, and is cooled by direct contact with the outside air rising up the packed bed. . On the other hand, the hot water flowing down the packed bed of the wet cooling section d is cooled and the humid air containing a large amount of moisture flows into the plenum section f at the upper part of the tower a. In winter, if this humid air is released to the atmosphere from the exhaust stack g, it will generate white smoke and cause a pollution problem. Introducing high temperature dry air,
After being mixed with the moist air, it is discharged from the exhaust stack g to prevent the exhaust from turning into white smoke.
ところで、乾式冷却部hは温水を移送する多数
の伝熱管群からなり、塔上部のプレナム部f側壁
に設置する構成のため乾式冷却部hの能力を大き
くし空気取入面積を大きくとる場合、プレナム部
fの高さを高くする必要から、塔高も高くなり、
プレナム部fに不要な空間を作ることになる。ま
た、乾式冷却部hは高重量であるが、上記従来の
冷水塔aにあつては、乾式冷却部hは湿式冷却部
d上方の塔a上部に設置されている。このため、
乾式冷却部hを支持するための架構iが大型とな
り、建設コストがかさむばかりでなく、広い設置
面積を必要とした。 By the way, the dry cooling section h consists of a large number of heat transfer tube groups for transferring hot water, and is installed on the side wall of the plenum section f at the top of the tower. Therefore, when increasing the capacity of the dry cooling section h and increasing the air intake area, Since it is necessary to increase the height of the plenum part f, the tower height also increases,
This creates unnecessary space in the plenum part f. Furthermore, although the dry cooling section h is heavy, in the conventional cooling tower a described above, the dry cooling section h is installed in the upper part of the tower a above the wet cooling section d. For this reason,
The frame i for supporting the dry cooling section h has become large, which not only increases the construction cost but also requires a large installation area.
本発明は以上の従来の問題点を有効に解決すべ
く創案されたものであり、本発明の目的は、伝熱
管群からなる乾式冷却部の伝熱面積を従来の冷水
塔の高さを変えることなく確保でき、また、高重
量の乾式冷却部の設置位置を、塔内中間部の湿式
冷却部外側まで下げることができ、乾式冷却部の
支持架構の小型・簡易化およびその設置スペース
の削減が図れる乾・湿式冷水塔を提供することに
ある。 The present invention was devised to effectively solve the above-mentioned conventional problems, and an object of the present invention is to change the heat transfer area of a dry cooling section consisting of a group of heat transfer tubes by changing the height of a conventional water cooling tower. In addition, the installation position of the heavy dry cooling section can be lowered to the outside of the wet cooling section in the middle of the tower, making the supporting frame of the dry cooling section smaller and simpler, and reducing its installation space. The purpose of the present invention is to provide a dry/wet type cooling water tower that can achieve this.
上記目的は、本発明によれば次の構成により達
成される。即ち、向流式の冷水塔中間部の湿式冷
却部の外側にエアーダンパを介して乾式冷却部を
設けて乾式冷却部の設置位置を低くし、また、乾
式冷却部からの乾燥空気と湿式冷却部からの湿り
空気とを塔内上部で混合させるべく、エアーダン
パに臨む充填層部分を仕切壁で仕切ると共に仕切
壁で分割された充填層のそれぞれに温水を散布す
る散水系を配設し、乾・湿式運転時には上記仕切
壁で仕切られた充填層部分には温水を流さずに乾
式冷却部からの乾燥空気をそのまま塔内上部に導
くようになしたものである。 According to the present invention, the above object is achieved by the following configuration. In other words, a dry cooling section is installed outside the wet cooling section in the middle of the countercurrent cooling tower via an air damper to lower the installation position of the dry cooling section, and the dry air from the dry cooling section and the wet cooling section are installed at a lower position. In order to mix the moist air from the inside of the tower at the upper part of the tower, the part of the packed bed facing the air damper is separated by a partition wall, and a water spray system is installed to spray hot water to each of the packed beds divided by the partition wall. During dry/wet operation, hot water is not allowed to flow through the packed bed section partitioned by the partition wall, and the dry air from the dry cooling section is directly guided to the upper part of the tower.
以下に本発明の好適一実施例を添付図面に従つ
て詳述する。 A preferred embodiment of the present invention will be described in detail below with reference to the accompanying drawings.
第2図において、1は筒体状の冷水塔であり、
冷水塔1の底部側壁にはエアーダンパ2が、また
冷水塔1の上壁中央には塔内に導入した外気を大
気開放するための排気筒3が設けられている。エ
アーダンパ2上方の冷水塔1内の中間部には、塔
内底部と塔内上部とを仕切るように湿式冷却部4
が設けられている。湿式冷却部4には、木材等が
充填され、温水を流下させる充填層Sが形成され
ている。また、湿式冷却部4を囲む冷水塔1の側
壁部には、エアーダンパ5が設けられ、エアーダ
ンパ5の外側には乾式冷却部6が設けられてい
る。乾式冷却部6は温水を移送する伝熱管群から
なり、基礎上に立設された架構7上に載置されて
いる。 In FIG. 2, 1 is a cylindrical cooling water tower;
An air damper 2 is provided on the bottom side wall of the cooling tower 1, and an exhaust pipe 3 is provided at the center of the upper wall of the cooling tower 1 for venting outside air introduced into the tower to the atmosphere. In the middle of the cooling tower 1 above the air damper 2, there is a wet cooling section 4 that partitions the bottom of the tower and the top of the tower.
is provided. The wet cooling unit 4 is filled with wood or the like to form a packed layer S through which hot water flows. Further, an air damper 5 is provided on the side wall of the cooling tower 1 surrounding the wet cooling section 4, and a dry cooling section 6 is provided outside the air damper 5. The dry cooling unit 6 consists of a group of heat transfer tubes for transferring hot water, and is placed on a frame 7 erected on a foundation.
湿式冷却部4には、エアーダンパ5に臨む外周
部の充填層S1を仕切る仕切壁8が設けられてお
り、湿式冷却部4の充填層Sは、仕切壁8により
外周部側の充填層S1とその他の中心部の充填層S2
とに分割されている。また、充填層S1の底部に
は、エアーダンパ9が設けられている。湿式冷却
部4の上方には、プラントなどから送られてきた
温水を湿式冷却部4に散布するための散水ノズル
を有する散水管Tが配設されている。散水管T
は、充填層S1に温水を散布する散水管T1と、充
填層S2に散布する散水管T2とに分岐されている。
また、冷水塔1底部には、湿式冷却部4で冷却処
理された冷却水を貯留する冷水槽10が設けら
れ、排気筒3内には強制排気用のフアン11が設
けられている。 The wet cooling unit 4 is provided with a partition wall 8 that partitions a packed layer S 1 on the outer periphery facing the air damper 5 . S 1 and other central packed bed S 2
It is divided into. Furthermore, an air damper 9 is provided at the bottom of the packed bed S1 . A water sprinkling pipe T having a water nozzle for spraying hot water sent from a plant or the like to the wet cooling part 4 is disposed above the wet cooling part 4 . Water pipe T
is branched into a water sprinkling pipe T 1 that sprays hot water onto the packed bed S 1 and a water sprinkling pipe T 2 that sprays hot water onto the packed bed S 2 .
Further, a cold water tank 10 is provided at the bottom of the cold water tower 1 to store cooling water cooled by the wet cooling section 4, and a fan 11 for forced exhaust is provided in the exhaust pipe 3.
次に本実施例の作用について述べる。 Next, the operation of this embodiment will be described.
まず、夏期など、冷水塔1からの排気の白煙化
が生じるおそれがない場合の通常湿式運転(温水
の冷却を湿式冷却部4のみで行う)について説明
する。この通常湿式運転時の状況は、第2図の冷
水塔軸心線cで区分される冷水塔1の左半分に示
されている。通常湿式運転時においては、エアー
ダンパ5は閉じられ、エアータダンパ9は開か
れ、更に散水管T1のバルブV1は開成されている。 First, normal wet operation (cooling of hot water is performed only by the wet cooling section 4) when there is no possibility that the exhaust gas from the cooling tower 1 will turn into white smoke, such as during summer, will be described. This situation during normal wet operation is shown in the left half of the cooling tower 1 divided by the cooling tower axis c in FIG. During normal wet operation, the air damper 5 is closed, the air damper 9 is opened, and the valve V 1 of the water sprinkler pipe T 1 is opened.
プラントなどから送られてきた温水は、散水管
T1,T2からの湿式冷却部4の充填層S1,S2にそ
れぞれ散布され充填層S1,S2を伝つて流下し、一
方、冷水塔1底部のエアーダンパ2より塔内に導
入された外気は充填層S1,S2を上昇する。かくし
て、充填層S1,S2を流下する温水は、これを上昇
する外気により冷却され、冷却された冷却水は冷
水槽10に貯留され再びプラント系などに戻さ
れ、他方、温水を冷却処理した外気は塔内上部を
経て排気筒3より排気される。 Hot water sent from plants etc. is sent through sprinkler pipes.
The water is dispersed from T 1 and T 2 to the packed beds S 1 and S 2 of the wet cooling section 4 , respectively, and flows down through the packed beds S 1 and S 2 . The introduced outside air rises through the packed beds S 1 and S 2 . In this way, the hot water flowing down the packed beds S 1 and S 2 is cooled by the rising outside air, and the cooled cooling water is stored in the cold water tank 10 and returned to the plant system, etc. On the other hand, the hot water is subjected to cooling treatment. The outside air is exhausted from the exhaust pipe 3 through the upper part of the tower.
次に冬期など、乾式冷却部4のみの温水冷却で
は排気空気の白煙化を免れない場合の乾・湿式運
転について説明する。この乾・湿式運転時の状況
は、冷水塔1の右半分に示されており、エアーダ
ンパ5は開、エアーダンパ9は閉、バルブV1は
閉とされる。 Next, a description will be given of dry/wet operation when hot water cooling of the dry cooling section 4 alone cannot avoid turning the exhaust air into white smoke, such as during winter. The conditions during this dry/wet operation are shown on the right half of the cooling tower 1, with the air damper 5 open, the air damper 9 closed, and the valve V1 closed.
散水管T1のバルブV1が閉とされるので、充填
層S1には温水は散布されず、充填層S1は乾燥状態
にある。従つて、乾式冷却部6およびエアーダン
パ5を通つて充填層S1に流入してきた高温の乾燥
空気は、そのままの状態で充填層S1を上昇し塔内
上部に至る。一方、冷水塔1底部のエアーダンパ
2より塔内に導入された外気は、充填層S2を上昇
する間に散水管T2から散布され充填層S2を流下
する温水を冷却し、湿り空気となつて塔内上部に
流入する。そしそてこの充填層S2からの湿り空気
は、塔内上部において上記充填層S1からの乾燥空
気と混合し、排気筒3から大気開放される。湿り
空気は乾燥空気と混合し、その湿度低下の後に排
出されるので白煙を生じない。 Since the valve V 1 of the water sprinkler pipe T 1 is closed, hot water is not sprayed onto the packed bed S 1 and the packed bed S 1 is in a dry state. Therefore, the high-temperature dry air that has flowed into the packed bed S 1 through the dry cooling section 6 and the air damper 5 continues to rise through the packed bed S 1 and reach the upper part of the tower. On the other hand, the outside air introduced into the tower from the air damper 2 at the bottom of the cooling water tower 1 cools the hot water that is sprayed from the sprinkler pipe T 2 and flows down the packed bed S 2 while rising up the packed bed S 2 , and It flows into the upper part of the tower. The moist air from the packed bed S 2 is mixed with the dry air from the packed bed S 1 in the upper part of the tower, and is released to the atmosphere from the exhaust stack 3. Humid air mixes with dry air and is discharged after the humidity has decreased, so no white smoke is produced.
このように、本発明では、従来の向流型の乾・
湿式冷水塔では密閉状態であつた湿式冷却部4外
周の塔側壁を有効利用し、ここにエアーダンパ5
を設け、そして更にエアーダンパ5の外側に乾式
冷却部6を設けるようにしている。このため、高
重量の乾式冷却部6を湿式冷却部4と同一レベル
の冷水塔1中間部への設置位置を下げることがで
きる。従つて、側壁面積に占める割合の大きな充
填槽部分の側壁を全面的に利用できるため、乾式
冷却部の伝熱面積が広くとれると共に塔内を高く
する事なく設計の自由度が増す。また、乾式冷却
部6を支持する架構7を小型かつ簡易なものとで
き、その建設コストおよび設置スペースを削減で
きると共に、乾式冷却部6の安定性が向上する。 In this way, the present invention uses the conventional countercurrent drying method.
In a wet cooling tower, the tower side wall around the outer periphery of the wet cooling section 4, which was in a sealed state, is effectively used, and an air damper 5 is installed here.
A dry cooling section 6 is further provided outside the air damper 5. Therefore, the installation position of the heavy dry cooling section 6 in the middle part of the cooling tower 1, which is on the same level as the wet cooling section 4, can be lowered. Therefore, since the side wall of the packed tank portion, which accounts for a large proportion of the side wall area, can be fully utilized, the heat transfer area of the dry cooling section can be widened and the degree of freedom in design is increased without increasing the height of the inside of the column. Further, the frame 7 supporting the dry cooling section 6 can be made small and simple, and the construction cost and installation space can be reduced, and the stability of the dry cooling section 6 can be improved.
以上要するに本発明によれば、広い開口面積を
必要とする乾式冷却部のスペースが確保でき、ま
た、高重量の乾式冷却部の設置位置を塔中間部の
湿式冷却部外側まで下げることができ、乾式冷却
部の支持架構を小型・簡易化でき、その建設コス
トおよび設置スペースを削減できる等の優れた効
果を奏する。 In summary, according to the present invention, space can be secured for the dry cooling section which requires a wide opening area, and the installation position of the heavy dry cooling section can be lowered to the outside of the wet cooling section in the middle of the tower. The support frame of the dry cooling section can be made smaller and simpler, and the construction cost and installation space can be reduced, which is an excellent effect.
第1図は従来の乾・湿式冷水塔の側断面図、第
2図は本発明に係る乾・湿式冷水塔の一実施例を
示す側断面図である。
図中、1は冷水塔、2,5,9はエアーダン
パ、4は湿式冷却部、6は乾式冷却部、7は架
構、8は仕切壁、S,S1,S2は充填層、T,T1,
T2は散水管である。
FIG. 1 is a side sectional view of a conventional dry/wet type cooling water tower, and FIG. 2 is a side sectional view showing an embodiment of the dry/wet type cooling water tower according to the present invention. In the figure, 1 is a cooling tower, 2, 5, and 9 are air dampers, 4 is a wet cooling section, 6 is a dry cooling section, 7 is a frame, 8 is a partition wall, S, S 1 , and S 2 are packed beds, and T , T 1 ,
T 2 is the water pipe.
Claims (1)
層を有し塔底部から流入し上記充填層を上昇する
冷気により温水を冷却する湿式冷却部と、該湿式
冷却部の充填層外側にエアーダンパを介して設け
られた乾式冷却部と、上記エアータンパに臨む充
填層部分を区画する仕切壁と、該仕切壁により分
割された充填層にそれぞれ温水を散布すべく配設
された散水系とを備えたことを特徴とする乾・湿
式冷水塔。1. A wet cooling section that has a packed bed that allows hot water sprayed from the top of the tower to flow down, and that cools the hot water with cold air that flows in from the bottom of the tower and rises above the packed bed, and an air damper is installed outside the packed bed of the wet cooling section. A dry cooling unit provided through the air tamper, a partition wall that partitions a portion of the packed bed facing the air tamper, and a water sprinkling system arranged to spray warm water to each of the packed beds divided by the partition wall. A dry/wet type cooling water tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58196961A JPS6089682A (en) | 1983-10-22 | 1983-10-22 | Dry/wet cooling tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58196961A JPS6089682A (en) | 1983-10-22 | 1983-10-22 | Dry/wet cooling tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6089682A JPS6089682A (en) | 1985-05-20 |
| JPH041274B2 true JPH041274B2 (en) | 1992-01-10 |
Family
ID=16366522
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58196961A Granted JPS6089682A (en) | 1983-10-22 | 1983-10-22 | Dry/wet cooling tower |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6089682A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9243847B2 (en) | 2009-11-04 | 2016-01-26 | Evapco, Inc. | Hybrid heat exchange apparatus |
-
1983
- 1983-10-22 JP JP58196961A patent/JPS6089682A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6089682A (en) | 1985-05-20 |
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