JPS6089682A - Dry/wet cooling tower - Google Patents

Dry/wet cooling tower

Info

Publication number
JPS6089682A
JPS6089682A JP58196961A JP19696183A JPS6089682A JP S6089682 A JPS6089682 A JP S6089682A JP 58196961 A JP58196961 A JP 58196961A JP 19696183 A JP19696183 A JP 19696183A JP S6089682 A JPS6089682 A JP S6089682A
Authority
JP
Japan
Prior art keywords
dry
tower
cooling
cooling section
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.)
Granted
Application number
JP58196961A
Other languages
Japanese (ja)
Other versions
JPH041274B2 (en
Inventor
Masao Ezaki
江崎 雅夫
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.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries Co Ltd
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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP58196961A priority Critical patent/JPS6089682A/en
Publication of JPS6089682A publication Critical patent/JPS6089682A/en
Publication of JPH041274B2 publication Critical patent/JPH041274B2/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

Landscapes

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

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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mlの乾式冷却部の設置位置を低くでき、乾式冷NJ
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 type cooling water tower, and in particular, it is possible to lower the installation position of a high ml dry type cooling section consisting of a group of heat transfer tubes, and to improve dry type cooling NJ.
This invention relates to a dry/wet cooling water tower with a smaller and simpler supporting frame.

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、渇
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
冷却塔の従来例が示されている。
Dry/wet cooling towers are devices that cool and process hot water generated in plants such as chemical factories, steel mills, and power plants. , 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 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、
外気の取入口す、cがそれぞれt&Gノられており、塔
a内の中間部には温水を流下させる充填層を有づ°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@0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の充填層を流下づる
温水は、冷水塔a底部の取入口Cからjla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Q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上部の取入口す外側に設けら
れた乾式冷却部りからプレナム部fに高温の乾燥空気を
導入し、上記湿り空気と混合さVて後、排気筒Ω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 include
Outside air intakes (a) and (c) are provided at T&G, respectively, and a wet cooling part (d) having a packed bed through which hot water flows is provided in the middle part of the tower (a). Above the wet cooling part d, a water sprinkler @0 that sprays hot water is arranged. and,
The hot water that is sprayed from the sprinkler pipe e and flows down the packed bed of the wet cooling section d is cooled by direct contact with the outside air that is introduced into JLA from the intake port C at the bottom of the cooling tower a and rises 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 Q, it will generate white smoke and cause a pollution problem. High-temperature dry air is introduced, mixed with the humid air, and then discharged from the exhaust stack Ω to prevent the exhaust from turning into white smoke.

ところで、乾式冷却部1)は温水を移送する多数の伝熱
管群からなり、塔上部のブレナム部[側壁に設置する構
成のため乾式冷却部りの能力を大きくし空気取入面積を
大きくとる場合、ブレナム部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、乾式冷却部りは高重量であるが、上
記従来の冷水塔aにあっては、乾式冷却部りは湿式冷却
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11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 1) consists of a large number of heat exchanger tubes for transferring hot water, and is installed in the brenum section at the top of the tower [because it is installed on the side wall, when increasing the capacity of the dry cooling section and increasing the air intake area. Since it is necessary to increase the height of the plenum part f, the tower height also increases, creating unnecessary space in the plenum part f. Furthermore, although the dry cooling section is heavy, in the conventional cooling tower a described above, the dry cooling section is installed at the top of the tower a above the wet cooling section d. For this reason, the frame i for supporting the dry cooling section 11 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 increase the heat transfer surface area of a dry cooling section consisting of a group of heat transfer tubes to 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 its installation. The purpose of the present invention is to provide a dry/wet cooling tower that can save space.

上記目的は、本発明によれば次の構成ににり達成される
。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渇水を散布す
る散水系を配没し、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渇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 dry water to each of the packed beds divided by the partition wall. During dry/wet operation, dry air from the dry cooling section is directly guided to the upper part of the column without flowing dry water into the packed bed section partitioned by the partition wall.

以下に本発明の好適一実施例を添付図面に従って詳述す
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の土壁
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89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。
In Fig. 2, 1 is a cylindrical cooling water tower.
An air damper 2 is provided on the bottom side wall of the cooling water tower 1, and an exhaust pipe 3 is provided at the center of the earthen wall of the cooling water tower 1 for venting outside air introduced into the tower to the atmosphere. Cooling tower 1 above air damper 2
89 wet cooling sections 4 are installed in the middle of the tower to partition the bottom of the tower and the top of the tower. The wet cooling section 4 includes
A filled layer S is filled with wood and the like and allows hot water to flow down. 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.

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。
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11
部4の充填層Sは、仕切g18により外周部側の充填層
S1とその他の中心部の充@層S+とに分割されている
。また、充填WJ S 1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。
The wet cooling unit 4 is provided with a partition wall 8 that partitions the packed layer S1 on the outer periphery facing the air damper 5.
The filled layer S of the portion 4 is divided by a partition g18 into a filled layer S1 on the outer peripheral side and a filled layer S+ on the other center side. In addition, an air damper 9 is installed at the bottom of the filling WJ S1.
is provided. Above the wet cooling section 4, a water sprinkling pipe T having a water nozzle for spraying hot water sent from a plant or the like to the wet cooling section 4 is arranged.

散水管Tは、充填層S工に温水を散布する散水管T1と
、充填層S)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が設りられ、排気筒3
内には強制排気用のファン11が改番プられている。
The water sprinkling pipe T is branched into a water sprinkling pipe T1 that sprays hot water onto the packed bed S, and a water sprinkling pipe T2 that sprays hot water onto the packed bed S. Further, a cold water tank 10 is provided at the bottom of the cold water tower 1 to store the cooling water that has been cooled in the wet cooling section 4.
A forced exhaust fan 11 is installed inside.

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a3
いでは、エアーダンパ5は閉じられ、エアーダンパ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 water tower 1 divided by the cooling tower axis C in FIG. A3 during normal wet operation
In this case, the air damper 5 is closed, the air damper 9 is opened, and the valve v1 of the water sprinkler pipe T1 is opened.

プラン1−などから送られてきた温水は、散水管T1.
T2から湿式冷却部4の充填層St 、 Stにそれぞ
れ散布され充tat層S1..’Szを仏って流下し、
一方、冷水塔1底部のエアーダンパ2より場内に導入さ
れた外気は充填層Ss 、Stを上昇する。かくして、
充填層S1.St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
The hot water sent from Plan 1- etc. is supplied to the water sprinkler pipe T1.
T2 to the filled layers St and St of the wet cooling section 4, respectively, and the filled tat layer S1. .. 'Buddha of Sz and flowed down,
On the other hand, outside air introduced into the field from the air damper 2 at the bottom of the cooling tower 1 rises through the packed beds Ss and St. Thus,
Filled bed S1. The hot water flowing down St 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 outside air that has cooled the hot water passes through the upper part of the tower. It is exhausted from the exhaust stack 3.

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 and the air damper 9
is closed, and valve V1 is closed.

散水管下1のバルブV1が閉とされるので、充填層S1
には渇水は散布されず、充填層S1は乾燥状態にある。
Since the valve V1 at the bottom 1 of the water sprinkler pipe is closed, the filled bed S1
No water is applied to the packed bed S1, and the packed bed S1 is in a dry state.

従って、乾式冷却部6およびエアーダンパ5を通って充
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St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S+を上昇する間に散水管T2から散布され充
填層S+を流下する温水を冷Fil L、、湿り空気と
なって塔内上部に流入覆る。そしてこの充填層S2から
の湿り空気は、塔内上部において上記充J11層S1か
らの乾燥空気と混合し、排気筒3から大気6(1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。
Therefore, the high-temperature dry air that has flowed into the packed bed S1 through the dry cooling section 6 and the air damper 5 rises through the packed bed St and reaches the upper part of the tower. On the other hand, while the outside air introduced into the tower from the air damper 2 at the bottom of the cooling water tower 1 rises through the packed bed S+, it is sprayed from the water sprinkler pipe T2 and the hot water flowing down the packed bed S+ is converted into cold Fil L, humid air. It flows into the upper part of the tower and covers it. The humid air from the packed bed S2 is mixed with the dry air from the packed bed S1 in the upper part of the tower, and is released into the atmosphere from the exhaust stack 3.The humid air mixes with the dry air, and Since it is discharged after the humidity has decreased, it does not produce white smoke.

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った湿式冷却部4外周の塔側壁を有
効利用(〕、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。従って、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高を高くする事なく
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 makes effective use of the tower side wall around the outer periphery of the wet cooling section 4, which was in a closed state in conventional countercurrent type dry/wet cooling towers. The dry cooling section 6 is provided outside the damper 5. Therefore, the heavy dry cooling section 6 can be installed at a lower position in the middle of the cooling tower 1, at the same level as the wet cooling section 4. Therefore, since the side wall of the packed tank, 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 design freedom is increased without increasing the tower height. The frame 7 that supports the cooling unit 6 can be made small and simple, its construction cost and installation space can be reduced, and the stability of the dry cooling unit 6 can be improved.

以上要するに本発明によれば、広い間口面積を必要とす
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gJ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
る等の優れた効宋を奏する。
In summary, according to the present invention, space can be secured for the dry cooling section which requires a wide frontage 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 gJ section can be made smaller and simpler, and its construction cost and installation space can be reduced, providing excellent benefits.

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

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ず側断面図で
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
、81 ’、S+ は充填層、T。 T1 、T+は散水管である。 特許出願人 石川島播磨重工業株式会社代理人弁理士 
絹 谷 信 雄
FIG. 1 is a side sectional view of a conventional dry/wet type cooling water tower, and FIG. 2 is a side sectional view of an embodiment of the dry/wet type cooling water tower according to the present invention. In the figure, 1 is a cooling tower, 2, 5.9 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
, 81', S+ is a packed bed, T. T1 and T+ are water sprinkler pipes. Patent applicant: Patent attorney representing Ishikawajima-Harima Heavy Industries Co., Ltd.
Nobuo Kinuya

Claims (1)

【特許請求の範囲】[Claims] 塔上部から散布された温水を流下させる充填層を有し塔
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。
A wet cooling section has a packed bed that allows hot water sprayed from the top of the tower to flow down, and 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 provided outside the packed bed of the wet cooling section. a dry cooling section provided in the air tamper, a partition wall that partitions a portion of the packed bed facing the air tamper, and a water sprinkling system disposed to spray hot water to each of the packed beds divided by the partition wall. A dry/wet type cooling water tower.
JP58196961A 1983-10-22 1983-10-22 Dry/wet cooling tower Granted JPS6089682A (en)

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 true JPS6089682A (en) 1985-05-20
JPH041274B2 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)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011056412A3 (en) * 2009-11-04 2012-04-12 Evapco, Inc. Hybrid heat exchange apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011056412A3 (en) * 2009-11-04 2012-04-12 Evapco, Inc. Hybrid heat exchange apparatus
EP2722627A1 (en) * 2009-11-04 2014-04-23 Evapco, INC. Hybrid heat exchange apparatus
US9243847B2 (en) 2009-11-04 2016-01-26 Evapco, Inc. Hybrid heat exchange apparatus

Also Published As

Publication number Publication date
JPH041274B2 (en) 1992-01-10

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