[go: up one dir, main page]

JPH01266496A - Process plant - Google Patents

Process plant

Info

Publication number
JPH01266496A
JPH01266496A JP63094445A JP9444588A JPH01266496A JP H01266496 A JPH01266496 A JP H01266496A JP 63094445 A JP63094445 A JP 63094445A JP 9444588 A JP9444588 A JP 9444588A JP H01266496 A JPH01266496 A JP H01266496A
Authority
JP
Japan
Prior art keywords
cooling
heat exchanger
heat transfer
cooling water
tube
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.)
Pending
Application number
JP63094445A
Other languages
Japanese (ja)
Inventor
Shinichiro Monno
門野 真一郎
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP63094445A priority Critical patent/JPH01266496A/en
Publication of JPH01266496A publication Critical patent/JPH01266496A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin

Landscapes

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

Abstract

PURPOSE:To permit effective continuous washing in a tube and reduce the cost for installation, by a method wherein the heat transfer tube of a heat exchanger for cooling an auxiliary machine is formed so as to be a straight tube and the tube is connected in parallel to the heat transfer tube of a main condenser in a cooling water line to circulate washing balls. CONSTITUTION:A heat exchanger 28 for cooling an auxiliary machine is formed so as to be a single path type and titanium made straight heat transfer tubes 30 are received in a horizontal type cylinder 29. Sea water in a water intake pit 21 is distributed into respective main condensers 26 and respective beat exchangers 25 for cooling auxiliary machines respectively through a sea water screen 22, respective water intake pumps 24, respective cooling water lines 23 and respective ball washing devices 25 to cool and condense exhaust steam in respective main condensers 20 and cools auxiliary machine cooling water in the heat exchanger 28 for cooling respective auxiliary machines. Washing balls supplied from respective ball washing devices 25 into respective cooling water lines 23 are branched respectively to respective heat transfer tubes of respective main condensers 26 and respective heat transfer tubes 30 of heat exchangers 25 for cooling respective auxiliary machines and are circulated repeatedly through a ball washing unit 25 whereby the inner walls of the heat transfer tubes 30 may be washed.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は火力発電プラントや原子力発電プラント等のプ
ロセスプラントに係り、特に主復水器冷却系の一部を補
機冷却系に共用したプロセスプラン1−に関する。
[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to process plants such as thermal power plants and nuclear power plants, and in particular, to cooling a part of the main condenser cooling system to auxiliary equipment. This relates to process plan 1 shared by the system.

(従来の技術) 従来の原子力発電プラントは第5図(A)で示す主復水
器冷却系1と第5図(B)で示す補機冷却系11とを互
いに独立させて、それぞれ設けている。
(Prior Art) In a conventional nuclear power plant, a main condenser cooling system 1 shown in FIG. 5(A) and an auxiliary equipment cooling system 11 shown in FIG. 5(B) are provided independently of each other. There is.

主復水器冷却系1は図示しない蒸気タービンで仕事をし
た排出蒸気を冷却する複数台の主復水器2.2.2のチ
タン製の伝熱管を冷却水ライン3゜3.3の途中にそれ
ぞれ介装すると共に、各冷却水ライン3には各主復水器
2の上流側にて取水ポンプ4.4.4とボール洗浄装置
5.5.5とをそれぞれ介装している。
The main condenser cooling system 1 connects titanium heat transfer tubes of a plurality of main condensers 2.2.2 to cool the exhaust steam that has been worked by a steam turbine (not shown) along a cooling water line 3. In addition, each cooling water line 3 is provided with a water intake pump 4.4.4 and a ball cleaning device 5.5.5 on the upstream side of each main condenser 2, respectively.

各冷却水ライン3は海水を冷W水として通水させるもの
であり、取水ビットに張設された異物除去用の海水スク
リーン6により浄化した例えば海水を各取水ポンプ4に
より汲み上げ、これを冷却水として各ボール洗浄装置5
に通水させてから、各主復水器2の伝熱管を通水させて
冷却し、各ボール洗浄装置5の洗浄ボールを冷却水の流
れに従って伝熱管内を循環させ、洗浄してから放水口1
7より放水するようになっている。
Each cooling water line 3 is for passing seawater as cold W water, and for example, seawater purified by a seawater screen 6 for removing foreign matter attached to a water intake bit is pumped up by each water intake pump 4, and then converted into cooling water. As each ball cleaning device 5
After that, water is passed through the heat transfer tubes of each main condenser 2 for cooling, and the cleaning balls of each ball cleaning device 5 are circulated through the heat transfer tubes according to the flow of cooling water, cleaned, and then released. Mizuguchi 1
Water will be sprayed from 7 onwards.

各ボール洗浄装置5は例えば第6図に示すようにそれぞ
れ構成され、複数本の直管状の伝熱管2aを内蔵する主
復水器2の入口側水室2bに接続された冷却水ライン3
の途中にボール供給管5aを接続している。
Each ball cleaning device 5 is configured as shown in FIG. 6, for example, and has a cooling water line 3 connected to an inlet side water chamber 2b of the main condenser 2 containing a plurality of straight heat transfer tubes 2a.
A ball supply pipe 5a is connected to the middle of the ball supply pipe 5a.

また、主復水器2の出口側氷室2Cに接続された冷却水
ライン3の途中にボール回収管5bを接続し、これらボ
ール供給管5aとボール回収管5bとをスポンジ状の洗
浄ボール5Cを回収供給するボール回収装置5dを介し
て接続している。
In addition, a ball recovery pipe 5b is connected to the middle of the cooling water line 3 connected to the outlet side ice chamber 2C of the main condenser 2, and a sponge-like cleaning ball 5C is connected to the ball supply pipe 5a and the ball recovery pipe 5b. They are connected via a ball recovery device 5d that collects and supplies the balls.

すなわち、ボール洗浄装置5は洗浄ボール5Cを冷却水
ライン3内の冷却水の流れにより主復水i?s2の伝熱
管2a内を繰り返し循環させることにより伝熱管2a内
を洗浄するものであり、ボール供給管5aから冷却水ラ
イン3に複数の洗浄ボール5Cが供給される。
That is, the ball cleaning device 5 cleans the cleaning balls 5C with the main condensate i? by the flow of cooling water in the cooling water line 3. The inside of the heat exchanger tube 2a is cleaned by repeatedly circulating the inside of the heat exchanger tube 2a of s2, and a plurality of cleaning balls 5C are supplied to the cooling water line 3 from the ball supply pipe 5a.

このために、洗浄ボール5Cは図中太線矢印で示す冷却
水の流れに従って主復水器2の入口側水室2bに流入さ
れ、さらに、各伝熱管2a内を流れて、各伝熱管2aの
内壁に付着した汚物8を洗浄ボール5Cにより除去し、
出口側氷室2cの冷却水ライン3内で張設された捕集ネ
ット5fににり洗浄ボール5Cを捕集する。
For this purpose, the cleaning balls 5C flow into the inlet side water chamber 2b of the main condenser 2 according to the flow of cooling water indicated by thick arrows in the figure, and further flow inside each heat exchanger tube 2a, and flow into each heat exchanger tube 2a. The dirt 8 adhering to the inner wall is removed by the cleaning ball 5C,
The cleaning balls 5C are collected by a collection net 5f stretched within the cooling water line 3 of the outlet side ice compartment 2c.

捕集された洗浄ボール5Cはボール回収管5bを通って
ボール循環ポンプ5eにより昇圧して再びボール回収装
置5dに戻すと共に、再びボール供給管5aを介して冷
却水ライン3に供給し、以後これを繰り返して伝熱管2
a内を洗浄する。
The collected cleaning balls 5C pass through the ball recovery pipe 5b, are pressurized by the ball circulation pump 5e, are returned to the ball recovery device 5d, and are again supplied to the cooling water line 3 via the ball supply pipe 5a. Repeat heat transfer tube 2
Clean inside a.

一方、補機冷却系11は第5図(B)に示すように構成
され、例えば海水を取水する取水ピット12内に張設さ
れた海水スクリーン13により異物を除去し、浄化した
海水を冷却水として複数台の取水ポンプ14,14.1
4により汲み上げる。
On the other hand, the auxiliary equipment cooling system 11 is configured as shown in FIG. As multiple water intake pumps 14, 14.1
Pump up by 4.

この汲み上げた海水を補機冷却水ライン15゜15.1
5により輸送して、さらに複数台の海水ストレーナ15
a、15a、15aにより浄化し、図示しない原子炉補
機を冷却する補機冷却水を冷却する複数台の補機冷却用
熱交換器16.16゜16を冷却してから放出ピット1
7へ放水する。
This pumped seawater is transferred to the auxiliary cooling water line 15°15.1
5, and then transported to multiple seawater strainers 15.
a, 15a, and 15a, and a plurality of auxiliary equipment cooling heat exchangers 16.16°16 that cool the auxiliary equipment cooling water that cools the reactor auxiliary equipment (not shown) are cooled, and then the discharge pit 1
Spray water on 7.

各補機冷却用熱交換器16は第7図に示すように構成さ
れ、横置き型の1117内に収容された耐食性の良好な
アルミニウム黄銅製等の複数本の伝熱管18内に海水を
図中破線矢印で示すように通水させる一方、各伝熱管1
8の外側のrIA17内に淡水の補機冷却水を図中実線
矢印で示すように通水させ、海水の冷却水により伝熱管
18を介して補橢冷却水を冷却するようになっている。
Each auxiliary equipment cooling heat exchanger 16 is constructed as shown in FIG. While passing water as shown by the middle broken line arrow, each heat exchanger tube 1
Freshwater auxiliary cooling water is made to flow into the rIA 17 outside the RIA 17 as shown by the solid line arrow in the figure, and the auxiliary cooling water is cooled by the seawater cooling water via the heat transfer tube 18.

このような補機冷却用熱交換器16は胴17内の図中上
部にある各伝熱管18内を通水する海水の流れを水室1
9により下部にある各伝熱管18側へ反転させるように
複数パスに構成するので、上下の伝熱管18同士を直線
状に連結する単一パスのものに比して胴の小型化を図る
ことができる。
Such an auxiliary equipment cooling heat exchanger 16 converts the flow of seawater passing through each heat transfer tube 18 located at the upper part of the figure in the shell 17 into the water chamber 1.
Since the structure is configured in multiple passes so as to be reversed toward the lower heat transfer tubes 18 by 9, the body can be made smaller compared to a single pass structure in which the upper and lower heat transfer tubes 18 are connected in a straight line. I can do it.

そして、主復水器冷却系1の各主復水器2および各取水
ポンプ4と補機冷却系11の各取水ポンプ14および補
機冷却用熱交換器16とは例えば第8図に示すように1
フロア−にまとめて配置されることが多く、補機冷却用
熱交換器16としては小型の上記復水バス型のものが多
用される。
Each main condenser 2 and each water intake pump 4 of the main condenser cooling system 1 and each water intake pump 14 and auxiliary equipment cooling heat exchanger 16 of the auxiliary equipment cooling system 11 are configured as shown in FIG. 8, for example. to 1
They are often arranged together on the floor, and the small condensing bus type mentioned above is often used as the auxiliary equipment cooling heat exchanger 16.

(発明が解決しようとする課題) しかしながら、このような従来のプロセスブラン]・で
は主復水器冷却系1と補機冷却系11とを別個にそれぞ
れ設けているので、コスト高であるうえに、補機冷却用
熱交換器16の伝熱管18の管内洗浄が困難であるとい
う課題がある。
(Problem to be Solved by the Invention) However, in such a conventional process bran, the main condenser cooling system 1 and the auxiliary equipment cooling system 11 are provided separately, which results in high cost and However, there is a problem in that it is difficult to clean the inside of the heat transfer tubes 18 of the heat exchanger 16 for cooling auxiliary equipment.

補機冷却用熱交換7A16は複数バス型であり、各伝熱
管18内を流れる海水を水室19により反転させている
ので、第5図で示すボール洗浄装置5によりこれら伝熱
管18内を洗浄しようとすると、洗浄ボール5Cが水室
19内に溜って伝熱管18内を循環せず、洗浄できない
というおそれがある。
The heat exchanger 7A16 for cooling auxiliary equipment is a multi-bus type, and the seawater flowing inside each heat transfer tube 18 is reversed by the water chamber 19, so the inside of these heat transfer tubes 18 is cleaned by the ball cleaning device 5 shown in FIG. If you try to do so, there is a possibility that the cleaning balls 5C will accumulate in the water chamber 19 and will not circulate within the heat transfer tubes 18, making it impossible to clean them.

このために、伝熱管18内に腐食防止剤等の薬剤を注入
することも考えられるが、これでは水源の薬物汚染等の
新たな問題が発生するおそれがある。
For this purpose, it is possible to inject a chemical such as a corrosion inhibitor into the heat exchanger tube 18, but this may cause new problems such as drug contamination of the water source.

そこで本発明は上記事情を考慮してなされたもので、そ
の目的は補機冷却用熱交換器の伝熱管内を連続して有効
に洗浄することができ、しかも、コスト低減を図ること
ができるプロセスプラントを提供することにある。
Therefore, the present invention has been made in consideration of the above-mentioned circumstances, and its purpose is to be able to continuously and effectively clean the inside of the heat transfer tubes of a heat exchanger for cooling auxiliary equipment, and to reduce costs. Our goal is to provide process plants.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) 本発明は主復水器を冷却する主復水器冷却系と補機冷却
系とは相互に重複するラインや装置が多いことに着目し
てなされたものであり、主復水器冷却系の一部を補機冷
却系で共用するようにしたものである。
(Means for Solving the Problems) The present invention was made by focusing on the fact that the main condenser cooling system that cools the main condenser and the auxiliary equipment cooling system have many overlapping lines and devices. A part of the main condenser cooling system is shared by the auxiliary cooling system.

すなわち本発明は、冷却水を通水させる冷却水ラインと
、この冷却水ラインに介装せしめた伝熱管により排出蒸
気を冷却凝縮させる主復水器と、この主復水器の伝熱管
内に洗浄ボールを循環させて洗浄するボール洗浄装置と
、プラント補機を冷却する冷却水を冷却する補機冷却用
熱交換器とを有するプロセスプラントにおいて、上記補
機冷却用熱交換器の伝熱管を、上記冷却水ラインに上記
主復水器の伝熱管に対して並列に接続すると共に、上記
ボール洗浄装置の洗浄ボールを循環させるように直管状
に形成したことを特徴とする。
That is, the present invention includes a cooling water line through which cooling water flows, a main condenser that cools and condenses exhaust steam using a heat exchanger tube installed in the cooling water line, and a heat exchanger tube in the main condenser. In a process plant that has a ball cleaning device that circulates and cleans the cleaning balls and an auxiliary equipment cooling heat exchanger that cools cooling water that cools plant auxiliary equipment, the heat exchanger tube of the auxiliary equipment cooling heat exchanger is The cooling water line is connected in parallel to the heat exchanger tube of the main condenser, and is formed in a straight pipe shape so as to circulate the cleaning balls of the ball cleaning device.

(作用) 冷却水ラインを通水する冷却水は主復水器と補機冷却用
熱交換器の各伝熱管とに分流されて、これらを冷却する
(Function) The cooling water flowing through the cooling water line is divided into the main condenser and the heat exchanger tubes of the auxiliary equipment cooling heat exchanger to cool them.

また、冷却水ラインの冷却水の流れに従ってボール洗浄
装置の洗浄ボールが主復水器と補機冷却用熱交換器にそ
れぞれ供給され、これらの各伝熱管内を洗浄ボールが循
環してそれぞれ洗浄する。
In addition, the cleaning balls of the ball cleaning device are supplied to the main condenser and the auxiliary equipment cooling heat exchanger according to the flow of cooling water in the cooling water line, and the cleaning balls circulate inside each of these heat transfer tubes to clean each one. do.

したがって、本発明によれば、冷却水ラインやボール洗
浄装置等を主復水器と補機冷却用熱交換器とにより共用
するので、コスト低減を図ることができる。
Therefore, according to the present invention, the main condenser and the auxiliary equipment cooling heat exchanger share the cooling water line, the ball cleaning device, etc., so that costs can be reduced.

また、ボール洗浄装置により補機冷却用熱交換器の伝熱
管を洗浄することができるので、これら伝熱管内の汚物
の腐食に起因する伝熱管の腐食や潰食等を防止すること
ができる。
Further, since the heat exchanger tubes of the heat exchanger for cooling auxiliary equipment can be cleaned by the ball cleaning device, it is possible to prevent corrosion and erosion of the heat exchanger tubes caused by corrosion of dirt inside these heat exchanger tubes.

(実施例) 以下本発明の実施例を第1図〜第4図に基づいて説明す
る。
(Example) Examples of the present invention will be described below based on FIGS. 1 to 4.

第1図は本発明の一実施例の要部系統構成を示し、例え
ば海水を取水する取水ビット21には海水スクリーン2
2が張設され、この海水スクリーン22により海水から
異物を除去するようになっている。
FIG. 1 shows the main system configuration of an embodiment of the present invention. For example, a seawater screen 2 is attached to a water intake bit 21 that takes in seawater.
2 is stretched, and this seawater screen 22 removes foreign substances from seawater.

取水ビット21内に取水口を開口する複数本の冷却水ラ
イン23.23.23には上流側から下流側に向けて取
水ポンプ24.24.24、ボール洗浄装置25.25
.25、図示しない蒸気タービン等で仕事をした排出蒸
気を冷却凝縮する主復水器26.26.26の各伝熱管
がそれぞれ介装され、各主復水器26.26.26の下
流側の冷却水ライン23.23.23が1本に集合され
、その集合管の放水口端部が放出ビット27内の海水中
に開口されている。各ボール洗浄装置25は第6図で示
す従来例とほぼ同様に構成され、各主復水器26の伝熱
管の入口側に複数個のスポンジ状の洗浄ボールを供給す
る一方、伝熱管の出口側でこれら洗浄ボールを捕集し、
洗浄ボールに各伝熱管内を繰り返し循環させ、洗浄する
ようになっている。
A plurality of cooling water lines 23, 23, 23 that open water intake ports in the water intake bit 21 are equipped with a water intake pump 24, 24, 24, and a ball cleaning device 25, 25 from the upstream side to the downstream side.
.. 25. Each heat transfer tube of the main condenser 26, 26, 26 that cools and condenses the exhaust steam that has done work in a steam turbine (not shown) is installed, and the downstream side of each main condenser 26, 26, 26 is installed. The cooling water lines 23, 23, 23 are collected into one, and the water outlet end of the collecting pipe is opened into the seawater in the discharge bit 27. Each ball cleaning device 25 is constructed almost in the same way as the conventional example shown in FIG. Collect these cleaning balls on the side,
The cleaning ball is repeatedly circulated inside each heat transfer tube to clean it.

そして、各冷却水ライン23,23.23′kmは各補
機冷却用熱交換!28.28.28の各伝熱管が各主復
水器27.27.27に対して並列にそれぞれ接続され
、各補機冷却用熱交換器28により冷却された補機冷W
水が図示しない原子か補機を冷却して、再び各補機冷却
用熱交換器28へ戻るようになっている。
And, each cooling water line 23, 23.23'km exchanges heat for cooling each auxiliary machine! Each of the heat exchanger tubes of 28.28.28 is connected in parallel to each main condenser 27.27.27, and the auxiliary cooling W cooled by each auxiliary cooling heat exchanger 28.
The water cools the auxiliary equipment (not shown) and returns to the heat exchanger 28 for cooling each auxiliary equipment.

したがって本実施例では、第5図(B)で示す従来の補
機冷却系11のうち、取水ビット12、海水スクリーン
13、複数台の取水ポンプ14゜14.14、複数本の
補機冷却水ライン15,15.15、海水ストレーナ1
5a、、15a、15a1放水ビツト17を省略するこ
とができ、大幅なコスト低減を図ることができる。
Therefore, in this embodiment, the conventional auxiliary cooling system 11 shown in FIG. 5(B) includes a water intake bit 12, a seawater screen 13, a plurality of water intake pumps 14, Line 15, 15.15, seawater strainer 1
5a, 15a, 15a1 water discharge bits 17 can be omitted, resulting in a significant cost reduction.

上記補機冷却用熱交換器28は第2図に示すように単一
バス型に構成され、横置型の胴29内にチタン製の複数
の直管状の伝熱管30を収容し、その両開口端側方には
海水入口水室31aと海水出口氷室31bとが各伝熱管
30にそれぞれ連通させて配設されている。
The auxiliary equipment cooling heat exchanger 28 is configured in a single bus type as shown in FIG. A seawater inlet water chamber 31a and a seawater outlet ice chamber 31b are disposed at the end sides so as to communicate with each heat exchanger tube 30, respectively.

胴29の軸方面画端部には海水入口水室31aに連通す
る海水人口32、海水出口氷室31bに連通ずる海水出
口33がそれぞれ開口される一方、各伝熱管30の外側
の1129内を淡水の補機冷却水が通水するように、I
!29には補機冷却水人口34と補機冷却水出口35が
それぞれ開口され、胴29内を図中実線矢印方向に流れ
る補機冷却水を、各伝熱管30内を図中破線矢印方向に
流れる冷却水(海水)により冷却するようになっている
A seawater outlet 32 communicating with the seawater inlet water chamber 31a and a seawater outlet 33 communicating with the seawater outlet ice chamber 31b are opened at the axial end of the shell 29, while fresh water is provided inside 1129 on the outside of each heat transfer tube 30. I so that the auxiliary cooling water of
! 29, an auxiliary cooling water outlet 34 and an auxiliary cooling water outlet 35 are opened, and the auxiliary cooling water flows inside the shell 29 in the direction of the solid line arrow in the figure, and in each heat transfer tube 30 in the direction of the broken line arrow in the figure. It is designed to be cooled by flowing cooling water (seawater).

各伝熱管30が直管状であり、第7図で示す従来例のよ
うに水室19で冷却水の通水方向を反転させないので、
ボール洗浄装置25から補機冷却用熱交換器28に供給
されるスポンジ状の洗浄ボールが各伝熱管30内を冷却
水の流れに従って流れ、胴29内に溜るのを防止するこ
とができる。
Each heat transfer tube 30 has a straight tube shape, and the direction of cooling water flowing in the water chamber 19 is not reversed as in the conventional example shown in FIG.
The sponge-like cleaning balls supplied from the ball cleaning device 25 to the auxiliary cooling heat exchanger 28 flow inside each heat transfer tube 30 according to the flow of cooling water, and can be prevented from accumulating in the shell 29.

したがって、洗浄ボールにより各伝熱管30内を有効に
洗浄することができるので、各伝熱管30内の汚物の腐
食等による各伝熱管30の腐食や酒食の防止を図ること
ができる。
Therefore, since the inside of each heat exchanger tube 30 can be effectively cleaned by the cleaning ball, it is possible to prevent corrosion of each heat exchanger tube 30 due to corrosion of contaminants inside each heat exchanger tube 30 and prevention of alcohol consumption.

次に本実施例の作用を説明する。Next, the operation of this embodiment will be explained.

取水ビット21内の海水は海水スクリーン22により異
物が除去されてから各取水ポンプ24により汲み上げら
れ、さらに、冷却水として各冷却水ライン23を通水し
て各ボール洗浄装置25を経て各主復水器26と各補機
冷却用熱交換器28とにそれぞれ分流される。
The seawater in the water intake bit 21 is pumped up by each water intake pump 24 after foreign matter is removed by a seawater screen 22, and is further passed through each cooling water line 23 as cooling water, passed through each ball cleaning device 25, and then sent to each main return tank. The water is divided into the water container 26 and each auxiliary equipment cooling heat exchanger 28.

したがって、各主復水器26の各伝熱管と各補機冷却用
熱交換器28の各伝熱管30とに海水が冷却水としてそ
れぞれ分流され、各主復水器26内の排出蒸気を冷却凝
縮すると共に、各補機冷却用熱交換器28の補機冷却水
を冷却することができる。
Therefore, seawater is branched as cooling water to each heat exchanger tube of each main condenser 26 and each heat exchanger tube 30 of each auxiliary equipment cooling heat exchanger 28, and cools the exhaust steam in each main condenser 26. At the same time as being condensed, the auxiliary cooling water in each auxiliary cooling heat exchanger 28 can be cooled.

また、各主復水器26の各伝熱管と各補機冷却用熱交換
器28の各伝熱管30とには各ボール洗浄装置25から
各冷却水ライン23に供給された複数個の洗浄ボールが
それぞれ分流され、しかも、ボール洗浄装置25を介し
て繰り返し循環され、これら伝熱管30の内壁が洗浄さ
れる。
In addition, each heat exchanger tube of each main condenser 26 and each heat exchanger tube 30 of each auxiliary equipment cooling heat exchanger 28 are provided with a plurality of cleaning balls supplied from each ball cleaning device 25 to each cooling water line 23. are separated and repeatedly circulated through the ball cleaning device 25 to clean the inner walls of these heat transfer tubes 30.

したがって、各主復水器26の各伝熱管と各補機冷却用
熱交換828の各伝熱管30の腐食や酒食を防止するこ
とができる。
Therefore, corrosion and corrosion of each heat transfer tube of each main condenser 26 and each heat transfer tube 30 of each auxiliary equipment cooling heat exchanger 828 can be prevented.

そして、本実施例によれば第3図に示すように取水ポン
プ24、主復水器26、補機冷却用熱交換器28を1フ
ロア−にまとめて配置することができるので、これらの
配置スペースの節約を図ることができる。
According to this embodiment, as shown in FIG. 3, the water intake pump 24, main condenser 26, and auxiliary equipment cooling heat exchanger 28 can be arranged together on one floor. Space can be saved.

さらに、各主復水器26および各補機冷却用熱交換器2
8の伝熱管30をチタンによりそれぞれ製造することが
できるので、各伝熱管30の寿命を延長させることがで
きる。
Furthermore, each main condenser 26 and each auxiliary equipment cooling heat exchanger 2
Since each of the eight heat exchanger tubes 30 can be manufactured from titanium, the life of each heat exchanger tube 30 can be extended.

第4図は本発明の他の実施例の一系統を示しており、本
実施例が上記実施例と相違する点は、主復水器26の胴
に補機冷却用熱交換器28の!1129を一体的に結合
し、この胴肉には主復水器26と補機冷却用熱交換器2
8の各伝熱管30に海水である冷却水を通水させる共通
の氷室40.41を形成した点にある。
FIG. 4 shows a system of another embodiment of the present invention, and the difference between this embodiment and the above embodiment is that an auxiliary cooling heat exchanger 28 is provided in the body of the main condenser 26! 1129 are integrally connected, and the main condenser 26 and the auxiliary equipment cooling heat exchanger 2 are installed in this body.
The point is that a common ice chamber 40, 41 is formed through which cooling water, which is seawater, is passed through each of the heat exchanger tubes 30 of 8.

これによれば、主復水器26に補機冷却用熱交換器28
を一体的に結合したので、これらの小型化を図ることが
できる。
According to this, the auxiliary equipment cooling heat exchanger 28 is connected to the main condenser 26.
Since they are integrally combined, they can be made smaller.

なお、上記主復水器26にはその伝熱管内を流れる冷却
水の通水方向を逆転させて、その管内を洗浄する逆洗装
置(図示せず)を付設したものがあり、この場合にはこ
の逆洗装置を各補機冷却用熱交換器28で共用するよう
に構成してもよい。
Note that some of the main condensers 26 are equipped with a backwashing device (not shown) that reverses the direction of cooling water flowing inside the heat transfer tubes to clean the insides of the tubes. The backwashing device may be configured to be shared by each auxiliary equipment cooling heat exchanger 28.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明は、主復水器冷却系の一部を
補機冷却系により共用するので、コスト低減を図ること
ができ、しかも、補機冷却系の補機冷却用熱交換器の伝
熱管を主復水器冷却系のボール洗浄装置により洗浄する
ことができるので、その伝熱管の腐食や潰食を防止する
ことができる。
As explained above, the present invention shares a part of the main condenser cooling system with the auxiliary equipment cooling system, thereby making it possible to reduce costs. Since the heat transfer tubes can be cleaned by the ball cleaning device of the main condenser cooling system, corrosion and erosion of the heat transfer tubes can be prevented.

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

第1図は本発明に係るプロセスプラントの−実流側の要
部系統構成図、第2図は第1図で示す補機冷却用熱交換
内の構成を示す図、第3図は第1図で示す実施例の機器
配置図、第4図は本発明の他の実施例の要部を一系統だ
け示す要部系統構成図、第5図(A>は従来の主復水器
冷却系の系統構成図、第5図(B)は従来の補機冷却系
の系統構成図、第6図は第5図(A)で示すボール洗浄
装置の構成と作用を説明するための図、第7図は第5図
(B)で示す補機冷却系の補機冷却用熱交換器の構成図
、第8図は第5図(A)、(B)でそれぞれ示す従来の
主復水器冷却系と補機冷却系の機器配置図である。 23・・・冷却水ライン、25・・・ボール洗浄装置、
26・・・主復水器、28・・・補機冷却用熱交換器、
30・・・伝熱管。 代理人弁理士  則 近  憲 先 回        第  子  丸   健F5 第1図 第2図 第4図 第7図 第8図
Fig. 1 is a system configuration diagram of main parts on the actual flow side of a process plant according to the present invention, Fig. 2 is a diagram showing the configuration inside the heat exchanger for cooling auxiliary equipment shown in Fig. Fig. 4 is a main part system configuration diagram showing only one main part of another embodiment of the present invention, Fig. 5 (A> is a conventional main condenser cooling system) 5(B) is a system configuration diagram of a conventional auxiliary equipment cooling system. FIG. 6 is a diagram for explaining the configuration and operation of the ball cleaning device shown in FIG. 5(A). Figure 7 is a block diagram of the accessory cooling heat exchanger of the accessory cooling system shown in Figure 5 (B), and Figure 8 is the conventional main condenser shown in Figures 5 (A) and (B), respectively. It is an equipment layout diagram of the cooling system and the auxiliary equipment cooling system. 23... Cooling water line, 25... Ball cleaning device,
26... Main condenser, 28... Auxiliary equipment cooling heat exchanger,
30... Heat exchanger tube. Representative Patent Attorney Nori Chika Ken Previously Ken Komaru F5 Figure 1 Figure 2 Figure 4 Figure 7 Figure 8

Claims (1)

【特許請求の範囲】[Claims] 冷却水を通水させる冷却水ラインと、この冷却水ライン
に介装せしめた伝熱管により排出蒸気を冷却凝縮させる
主復水器と、この主復水器の伝熱管内に洗浄ボールを循
環させて洗浄するボール洗浄装置と、プラント補機を冷
却する冷却水を冷却する補機冷却用熱交換器とを有する
プロセスプラントにおいて、上記補機冷却用熱交換器の
伝熱管を、上記冷却水ラインに上記主復水器の伝熱管に
対して並列に接続すると共に、上記ボール洗浄装置の洗
浄ボールを循環させるように直管状に形成したことを特
徴とするプロセスプラント。
A cooling water line through which cooling water flows, a main condenser that cools and condenses exhaust steam using a heat transfer tube installed in this cooling water line, and a cleaning ball that circulates within the heat transfer tube of this main condenser. In a process plant that has a ball cleaning device that cleans the balls by cleaning the auxiliary equipment, and an auxiliary equipment cooling heat exchanger that cools cooling water that cools the plant auxiliary equipment, the heat exchanger tubes of the auxiliary equipment cooling heat exchanger are connected to the cooling water line. A process plant characterized in that the process plant is connected in parallel to the heat exchanger tube of the main condenser and formed in a straight tube shape so as to circulate the cleaning balls of the ball cleaning device.
JP63094445A 1988-04-19 1988-04-19 Process plant Pending JPH01266496A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63094445A JPH01266496A (en) 1988-04-19 1988-04-19 Process plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63094445A JPH01266496A (en) 1988-04-19 1988-04-19 Process plant

Publications (1)

Publication Number Publication Date
JPH01266496A true JPH01266496A (en) 1989-10-24

Family

ID=14110460

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63094445A Pending JPH01266496A (en) 1988-04-19 1988-04-19 Process plant

Country Status (1)

Country Link
JP (1) JPH01266496A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0577600U (en) * 1992-03-27 1993-10-22 東京瓦斯株式会社 Adhesion prevention device for water intake pit screen

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0577600U (en) * 1992-03-27 1993-10-22 東京瓦斯株式会社 Adhesion prevention device for water intake pit screen

Similar Documents

Publication Publication Date Title
CN102094211B (en) Acid washing system of low-temperature multi-effect seawater desalting equipment
CA1055479A (en) Descaling of heat exchanger
CA1277877C (en) Device for degassing the condensate in the cycle of an electricity generating plant
CN210833227U (en) Descaling device of heat exchanger
JPH01266496A (en) Process plant
JP4095738B2 (en) Nuclear power generation equipment
CN114940521A (en) Modularized horizontal pipe type evaporator unit, cleaning device, evaporator and cleaning application method
JPH06194071A (en) Residence preventing device for cleaning ball in heat exchanger
SU1506252A1 (en) Closed circuit water system
JPS63238397A (en) Condenser cooling pipe cleaning device
DE4307608C2 (en) Method and device for using energy from flue gases in coal-fired power plants
KR20020050861A (en) Scale removal apparatus for plate heat changers with the ability of continuous heat changing
CN105152363A (en) Modified utilization system for circulating water
CN216815174U (en) Hydraulic pressure station heat exchanger with clean function
JPH0791883A (en) Cleaning device for condenser, cooler and cooling pipe
CN114602878B (en) On-line cleaning system of evaporative crystallization device
CN209128465U (en) It is a kind of to disappear the system of white haze and flushing cinder wastewater treatment for flushing cinder steam exhaust
RU1791693C (en) Heat exchanger cleaning system
CN220103790U (en) Tubular heat exchanger
CN220931828U (en) Heat exchanger for high-humidity sludge drying carrier gas
CN210512774U (en) Automatic cleaning device for closed water cooler of coastal power plant
CN212902846U (en) Be used for condenser scale deposit purifier
JP3888894B2 (en) Condensate treatment system and condensate treatment method
KR20020050860A (en) Scale removal apparatus for plate heat changers
JPH03181895A (en) Device of sea water system for cooling auxiliary equipment