JPS62280590A - Ball washing method for condenser and device thereof - Google Patents

Ball washing method for condenser and device thereof

Info

Publication number
JPS62280590A
JPS62280590A JP12109586A JP12109586A JPS62280590A JP S62280590 A JPS62280590 A JP S62280590A JP 12109586 A JP12109586 A JP 12109586A JP 12109586 A JP12109586 A JP 12109586A JP S62280590 A JPS62280590 A JP S62280590A
Authority
JP
Japan
Prior art keywords
outlet
screen
condenser
ball
cooling water
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
JP12109586A
Other languages
Japanese (ja)
Inventor
Katsumoto Otake
大嶽 克基
Yoshio Sumiya
住谷 吉男
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP12109586A priority Critical patent/JPS62280590A/en
Publication of JPS62280590A publication Critical patent/JPS62280590A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To enable economical management of the contaminating state of the cooling pipe of the condenser of a steam generating plant by using a thermal power or an atomic power, by a method wherein opening and closing control of a screen and the charging position of a washing material are switched according to an adhering state of a foreign matter to a screen and the contaminating state of the outlet and inlet of a cooling pipe. CONSTITUTION:Ball collection and prescreens 10 and 14 have screen's function of removing a foreign matter 36 in cooling water from a curculating pump 6, and meanwhile, the side, facing an outlet water chamber 12, of an outlet water chamber 11 of a condenser has ball collector's function of catching a washing material 37 in cooling water. By means of outputs from differential pressure gauges 40 and 45, the degree of adhesion of a foreign matter to the collectors 10 and 14 is detected, and through promotion of screen driving machines 31, 32, 33, and 34, collection of a foreign matter to the screen and back washing motion are effected. Further, outputs from heat flow sensors 60 and 65 are compared with each other through the working of an arithmetic unit 200, a motion instruction to ball recovery valves 17 and 26 and ball charge valves 23 and 28 are issued from a control oscillating device so that ball washing is effected by back washing beginning with the outlet side on which the degree of contamination is high.

Description

【発明の詳細な説明】 3、発明の詳細な説明 〔発明の利用分野〕 本発明は、火力または原子力等による蒸気発生プラント
において使用される復水器の冷却管の洗浄方法支びその
装置に関する。
Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Application of the Invention] The present invention relates to a method and apparatus for cleaning cooling pipes of a condenser used in a thermal or nuclear steam generation plant.

〔発明の背景〕[Background of the invention]

従来の装置は、実開昭59−158894号公報に記載
のように、要取水機器側の流入管路と排出管路を開閉操
作可能なスクリーンを設け、流入・排出管路と取水・放
水管路との間に逆洗弁を設け、スクリーンの前後差圧を
検知し、閉側のスクリーンが設定差圧に達した時に逆洗
弁を切換え、他方の開側のスクリーンを閉に、さらに閉
側のスクリーンを開に切えるられるようになっていた。
As described in Japanese Utility Model Application Publication No. 59-158894, the conventional device is equipped with a screen that can open and close the inflow pipe and the discharge pipe on the side of the equipment that requires water intake, and the inflow/discharge pipe and the water intake/discharge pipe are A backwash valve is installed between the screen and the screen, and the pressure difference across the screen is detected. When the screen on the closed side reaches the set pressure difference, the backwash valve is switched, the screen on the other open side is closed, and then the screen is closed again. The side screen could be opened.

しかし、スクリーンを通過した海水の汚れ(スライム。However, the dirt (slime) in the seawater that passed through the screen.

海棲生蜀の付着等)に対する冷却管のボール洗浄、特に
、冷却管の入口側・出口側の汚れの程度によって正洗浄
、るるいは、逆洗浄によってボール洗浄が出来るように
なっておらず、さらI/’C,#I4時的に大量の異物
がスクリーンに流入した場合の保護対策について考慮さ
れていなかった。
Cleaning the balls of cooling pipes to prevent the adhesion of marine insects, etc. In particular, depending on the degree of dirt on the inlet and outlet sides of the cooling pipes, it is not possible to clean the balls by forward cleaning, circular cleaning, or back cleaning. , I/'C, #I4 No consideration was given to protection measures in the event that a large amount of foreign matter occasionally flows into the screen.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、スクリーンへの異物の付着状態および
復水器の運転(性能)状態の変化に追従し、冷却管群の
汚れ状態に応じた洗浄体の投入位置切換えが可能な復水
器ボール洗浄運転方法および装置を提供するにある。
An object of the present invention is to create a condenser that can follow changes in the state of foreign matter adhering to the screen and the operating (performance) state of the condenser, and can change the position of the cleaning body in accordance with the state of contamination of the cooling pipe group. The present invention provides a ball cleaning operating method and device.

〔発明の概要〕[Summary of the invention]

本発明の要点は、復水器の冷却水出入口系にボール捕集
器兼プレスクリーンを設け、スクリーンの前説差圧を検
出し、冷却水の入口系と出口系との間に逆洗弁を設けて
連絡し、復水器冷却管の出入口部の管外壁における熱流
束を検出し、その熱流束と復水器温度変化とから冷却管
の管清浄度を評価し得る手段を備え、スクリーンの異物
の付着状態および冷却管出入口の汚れ状態に応じて、ス
クリーンの開閉操作訃よび洗浄体の投入位置を切り換え
ることを特徴とした復水器ボール洗浄運転方法および装
置である。
The key points of the present invention are to provide a ball collector and pre-screen in the cooling water inlet and outlet system of the condenser, to detect the aforementioned differential pressure of the screen, and to install a backwash valve between the cooling water inlet and outlet systems. It is equipped with a means to detect the heat flux on the outer wall of the condenser cooling pipe inlet and outlet, and to evaluate the pipe cleanliness of the cooling pipe from the heat flux and the condenser temperature change. A condenser ball cleaning operation method and apparatus characterized in that the opening/closing operation of the screen and the input position of the cleaning body are changed according to the adhesion state of foreign matter and the contamination state of the cooling pipe inlet/outlet.

〔発明の実施例〕[Embodiments of the invention]

本発明の実施例を図面に基づいて説明する。 Embodiments of the present invention will be described based on the drawings.

第3図から第7図は本発明の一実施例を示す。3 to 7 show one embodiment of the present invention.

第3図は基本系統図でるる。復水器1の冷却水入口系9
および冷却水出口系13にボール捕Jk器兼プレスクリ
ーン10.14を設ける。ボール捕集器兼プレスクリー
ン10.14は、循環水ポンプ6からの冷却水流入側お
よび流出側が冷却水中の異物36を除去するスクリーン
の機能を持ち、一方、復水器入口水室11の出口水室1
2に面した側が冷却水中の洗浄体37をキャッチするこ
との出来るボール捕集器の機能を持ったものでろる。
Figure 3 shows the basic system diagram. Cooling water inlet system 9 of condenser 1
A ball catcher and pre-screen 10.14 is provided in the cooling water outlet system 13. The ball collector/pre-screen 10.14 has the function of a screen to remove foreign matter 36 from the cooling water on the inflow and outflow sides of the cooling water from the circulating water pump 6, and on the other hand, the ball collector/prescreen 10.14 has the function of a screen to remove foreign matter 36 from the cooling water. Water chamber 1
The side facing 2 has the function of a ball collector that can catch the cleaning body 37 in the cooling water.

ボール捕集器兼プレスクリーン(以降捕集装置と呼称)
10.14には前後差圧を検出する差圧計40.45を
設け、検出値Δp1.  Δp、は信号人力装置100
に入力される。
Ball collector and pre-screen (hereinafter referred to as collection device)
10.14 is provided with a differential pressure gauge 40.45 for detecting the differential pressure between the front and rear, and the detected value Δp1. Δp is the signal human power device 100
is input.

復水器1における複数の冷却管2の入口部および出口部
の外壁に熱流センサ60,65を装着し、その検知出力
e、、e、および器内蒸気温度t。
Heat flow sensors 60 and 65 are attached to the outer walls of the inlet and outlet portions of the plurality of cooling pipes 2 in the condenser 1, and their detection outputs e, , e, and internal steam temperature t are measured.

あるいは器内真空度p、を検出する検出器70が一般け
られている。また、冷却水入口系9および冷−5却水出
口系13にも冷却求人ロ二度tli出口温度t、を検出
する検出器50.55がそれぞれ設けられている。また
冷却水入口系7には冷却水流iG、を検出するfi、X
検出器35が設けられてお)、すべて信号入力装glo
oに人力される。さらに、信号入力装置100では計画
条件(例えば。
Alternatively, a detector 70 for detecting the internal vacuum degree p is generally used. Further, the cooling water inlet system 9 and the cooling water outlet system 13 are also provided with detectors 50 and 55, respectively, for detecting the cooling water outlet temperature t. In addition, the cooling water inlet system 7 has fi,
A detector 35 is provided), all signal input devices are
It is man-powered by o. Furthermore, the signal input device 100 further includes a planning condition (for example).

計!iIiJg清浄度、計画管清浄度比率2.計画捕集
装置差圧等)aも入力できる。次K、これらの入力デー
タを基に演算装置200で演算され、各捕集装置の差圧
Δp+、  Δpゆが設定値jp、と比較され、冷却管
出入口部の管清浄度C+、C−が演算され、設定値C1
と比較される。そして、制御発信装fii300に指令
を与え、制御信号の発振を行なうことができる。すなわ
ち、差圧計40.45の出力Δpl、Δp、によって各
捕集装置10゜14の異物付着度合いを検知し、制御発
信装置からの信号す、o、−wb、が発信され、捕集装
置10.14のスクリーン駆動機31,32.33゜3
4の動作を促して、スクリーンへの異物回収、逆洗動作
をなし得る。さらに、熱流センサ60゜65の出力e、
、e。によって冷却管入口部、出口部の汚れ度合いを検
知して制御装置からの信号b5〜b、が発信され、ボー
ル循環ポンプ19、ボール回収弁17,26、ボール投
入fP23゜28の動作を促して、冷却W2の汚れによ
る器内真空度低下の回復をなし得る。さらに、運転条件
(タービン負荷、流量、温度等)の変化により復水器冷
却管内面のスケール付着量を調査した結果、第6図に示
すように、冷却管の入口部と出口部の汚れ度合も画一的
なものではなく、出口部の方が汚れが大きい、傾向がる
るため、熱流センサ60゜65からの出力e1.e、を
演算装置200で比較し、制御発信装置300から、特
に、汚れ度合の大きい出口側からの逆洗によりボール洗
浄を行なうよう、ボール回収弁17,26、および、ボ
ール投入弁23.28の動作指令も可能となっている。
Total! iIiJg cleanliness, planned pipe cleanliness ratio 2. Planned collection device differential pressure, etc.) a can also be input. Next, the calculation device 200 calculates based on these input data, and the differential pressures Δp+ and ΔpY of each collection device are compared with the set value jp, and the pipe cleanliness C+ and C- at the entrance and exit of the cooling pipe are determined. Calculated, set value C1
compared to Then, a command can be given to the control transmitter fii300 to oscillate a control signal. That is, the degree of adhesion of foreign matter to each collection device 10 14 is detected by the outputs Δpl and Δp of the differential pressure gauge 40.45, and signals s, o, -wb are transmitted from the control transmitter, and the collection device 10 .14 screen drive machine 31, 32.33゜3
By prompting the operation 4, foreign matter can be collected into the screen and a backwash operation can be performed. Furthermore, the output e of the heat flow sensor 60°65,
, e. detects the degree of contamination at the inlet and outlet of the cooling pipe and sends signals b5 to b from the control device, prompting the operation of the ball circulation pump 19, ball recovery valves 17 and 26, and ball input fP23°28. , it is possible to recover from a decrease in the degree of vacuum inside the vessel due to contamination of the cooling W2. Furthermore, as a result of investigating the amount of scale adhesion on the inner surface of the condenser cooling pipe due to changes in operating conditions (turbine load, flow rate, temperature, etc.), we found that the degree of contamination at the inlet and outlet of the cooling pipe was as shown in Figure 6. is not uniform and tends to be more contaminated at the outlet, so the output e1. from the heat flow sensor 60°65. e, are compared by the arithmetic unit 200, and the control transmitter 300 selects the ball recovery valves 17, 26 and the ball input valves 23, 28 so that the balls are cleaned by backwashing from the outlet side where the degree of contamination is particularly high. Operation commands are also possible.

また、ボールの洗浄時間と汚れの回復率を演算装置20
0で演算しておき、制御発信装置300からの発信によ
り冷却管の出入口の汚れ度合に見合ってボール投入時間
(逆洗時間)と信号す、b、〜b9の発振によりボール
回収弁17゜26およびボール投入弁23.28の開閉
を制御動作することも可能である。
In addition, the calculation device 20 calculates the cleaning time of the ball and the dirt recovery rate.
0, and a signal is sent from the control transmitter 300 to signal the ball input time (backwash time) according to the degree of contamination at the entrance and exit of the cooling pipe. It is also possible to control the opening and closing of the ball input valves 23 and 28.

すなわち、冷却管2の外壁に装着した熱流センサ60,
65からの出力eI、e、は、一般Ki、mv電圧とし
て検出されるが、これらの熱流センサ60.65の出力
e、、e、(e、、!:総称)、!:冷却管2の管壁を
通過する熱流束qt t  qa (qmと総称)との
関係は実測データによればIJ ニアにあるという特性
かぁ〕、この特性を演算装置200に入力データとして
入れておき、実測熱流束q。
That is, the heat flow sensor 60 attached to the outer wall of the cooling pipe 2,
The output eI, e, from 65 is detected as a general Ki, mv voltage, but the output e,,e, (e,,!: generic term),! of these heat flow sensors 60.65 is detected as a general Ki,mv voltage. :According to actual measurement data, the relationship between the heat flux qt t qa (generally referred to as qm) passing through the pipe wall of the cooling pipe 2 is near IJ], and input this characteristic into the calculation device 200 as input data. Then, the measured heat flux q.

を演算する。Calculate.

qmocK−ea       ・・・・・・・・・・
・・(1)但しに:係数 検出器70からは器内蒸気温度t、、または、器内真空
度p、が検出される。器内真空度p、を検出する場合に
は、演算装置200にてそれ罠相当する飽和温度t、を
換算し、冷却水入口温度検出器50の出力1.と冷却水
出口温度検出器55の出力【、とから実測対数平均温度
差θmの演算を行なう。
qmocK-ea・・・・・・・・・・・・
(1) However: The coefficient detector 70 detects the internal steam temperature t or the internal vacuum degree p. When detecting the internal vacuum degree p, the arithmetic unit 200 converts the corresponding saturation temperature t, and calculates the output 1. The actually measured logarithmic average temperature difference θm is calculated from the output of the cooling water outlet temperature detector 55 [,].

(1)式と(2)式から実測熱通過率J−+、 J−(
J−と総称)を演算する。
From equations (1) and (2), the measured heat transfer rates J-+, J-(
(collectively referred to as J-).

J、、=(1,/θm       ・・・・・・・・
・・・・(3)次に、予め設定されている運転条件、す
なわち、タービン負荷、冷却水流量、冷却水入口温度お
よび復水器の仕様によって、計画点熱通過率Jdを計算
しておき、熱通過率比R+、 几、(R1と総称)を演
算する。
J,,=(1,/θm...
(3) Next, calculate the design point heat transfer rate Jd based on preset operating conditions, that is, turbine load, cooling water flow rate, cooling water inlet temperature, and condenser specifications. , heat transfer rate ratio R+, 几, (generally referred to as R1) is calculated.

几、 =J 、 、 IJ d       ・・・・
・・・・・(4)ここでJdは冷却管が汚れる前の値で
あるから冷却管の汚れによる性能低下がめった場合、%
別な場合を除き一般K J −(J−+ (J dの関
係で検知して算出される。
几、=J、、IJd・・・・・・
・・・・・・(4) Here, Jd is the value before the cooling pipe becomes dirty, so if the performance decreases due to cooling pipe dirt rarely occurs, the %
Unless otherwise specified, it is detected and calculated using the general K J -(J-+ (J d) relationship.

ついで、(4)式で得られた熱通過率比几3.R6)と
計画時、管清浄度C1とから運転時における冷9却管清
浄度C’ +、 C’ −(C’、と総称)を演算する
C’、 =Ca −R,・・・・・・・・・・・俤)さ
らに、運転時管清浄度C’+、 C’s  と計画時管
清浄度Caとから管清浄度比率01,0゜(0゜と総称
)を演算する。
Next, the heat transfer rate ratio obtained by equation (4) 3. Calculate the cooling pipe cleanliness C' +, C' - (collectively referred to as C') during operation from R6) and the pipe cleanliness C1 at the planning time, = Ca - R,... . . .) Further, a pipe cleanliness ratio of 01.0° (generally referred to as 0°) is calculated from the operating pipe cleanliness C'+, C's and the planned pipe cleanliness Ca.

(5)式および(6)式よシ冷却管の入口側および出口
側の汚れを熱流束を検知して管理することができる。冷
却管2の入口側および出口側について上記管清浄度C’
 + z C’ @、ろるいは、管清浄任率01゜0、
をもって、あらかじめ設定したそれぞれの許容値Ca、
■、にろるか否かを演算装置200で分析し1例えば、
冷却管2からの熱流センサ60゜65の出力eI、e、
によって分析した結果が設定管清浄度Ca 1あるいは
、設定管清浄度比率0、ニジ低下した場合には、直ちに
、復水器ボール洗浄装置にON指令が出される。具体例
で示すと、第7rgJにおいて、冷却管内面のスケール
付着量g+、g−が実線の状態から破線の状態に増えた
場合、それに併い熱流束e、、e、が降下し、管清浄度
C+、C−も低下し、冷却管出口側の管清浄度C0がC
,<C,となシボール洗浄装置がオンとなる。
According to equations (5) and (6), contamination on the inlet and outlet sides of the cooling pipe can be managed by detecting heat flux. The above pipe cleanliness C' for the inlet and outlet sides of the cooling pipe 2
+ z C' @, Rouiwa, pipe cleaning rate 01゜0,
and each preset allowable value Ca,
■Analyze whether or not it is cloudy using the arithmetic unit 200.1 For example,
Outputs eI, e, of the heat flow sensor 60°65 from the cooling pipe 2
If the result of the analysis is that the set pipe cleanliness Ca is 1 or the set pipe cleanliness ratio is 0, an ON command is immediately issued to the condenser ball cleaning device. To give a specific example, in the seventh rgJ, when the amount of scale adhesion g+, g- on the inner surface of the cooling tube increases from the solid line to the broken line, the heat fluxes e, , e decrease accordingly, and the tube cleansing becomes more difficult. The degree of cleanliness C+ and C- also decreased, and the pipe cleanliness C0 on the outlet side of the cooling pipe decreased to C.
, <C, the shibor cleaning device is turned on.

第8図は本発明の洗浄運転方法の具体的な例を示すフロ
ーチャートでアシ、各検出器からの入力データのうち、
特に、捕集装置10,14の差圧ΔpI、Δp、に基づ
き、正洗、あるいは、逆洗の判別を行ない、それぞれ、
Δp+(Δp 、。
FIG. 8 is a flowchart showing a specific example of the cleaning operation method of the present invention.
In particular, based on the differential pressures ΔpI and Δp between the collection devices 10 and 14, forward washing or backwashing is determined, respectively.
Δp+(Δp,.

Δp*(」paを満足させた後、前記のように、管清浄
度C+*  Ceおよび管清浄度比率(81,、(9゜
を演算し、性能分析を行なう。即ち、冷却管の入口側の
管清浄度C1と出口側の管清浄度C0との比較に基づき
洗浄装置の操作方法の選択を行ない、設定管清浄度Ca
との比較により洗浄装置の0N10FF操作がなされる
After satisfying Δp*('pa, as described above, calculate the pipe cleanliness C+* Ce and the pipe cleanliness ratio (81,, (9°) and perform performance analysis. In other words, the inlet side of the cooling pipe The operating method of the cleaning device is selected based on the comparison between the pipe cleanliness level C1 of
0N10FF operation of the cleaning device is performed by comparison with .

第1図は捕集装置10のみがプレスクリーンとして機能
し、ボール洗浄装置が運用されていない正洗の状態を示
すものであシ、ボール循環ポンプ19は停止し、ボール
回収弁17,26、および、ボール投入弁23.28は
閉止の状態にある。
FIG. 1 shows a normal washing state in which only the collection device 10 functions as a pre-screen and the ball cleaning device is not operated, the ball circulation pump 19 is stopped, and the ball recovery valves 17, 26, And the ball input valves 23 and 28 are in a closed state.

第2図は差圧計40がΔp、<<Δp、であシ、管清浄
度がC+ >C−、C−’−C−の場合であシ、捕集装
置14がボール捕集器の機能を果し、正洗のボール洗浄
運転状態を示す。
Fig. 2 shows the case where the differential pressure gauge 40 is Δp, <<Δp, the pipe cleanliness is C+ >C-, C-'-C-, and the collection device 14 functions as a ball collector. This shows the ball cleaning operation status of normal cleaning.

第3図は、差圧計40がΔp1≧Δp、となった場合を
示し、逆洗弁8が逆洗位置にセットされ。
FIG. 3 shows a case where the differential pressure gauge 40 indicates Δp1≧Δp, and the backwash valve 8 is set to the backwash position.

捕集装置10が逆洗状態に、捕集装置14がプレスクリ
ーンの機能を果しているっ 第4図は第2図とは全く逆の状態でろシ、逆洗状態にお
けるボール洗浄運転を示す。
The collecting device 10 is in a backwashing state, and the collecting device 14 is functioning as a pre-screen. FIG. 4 shows a bowl cleaning operation in a filter and backwashing state, which is completely opposite to FIG. 2.

第5図は、第1図の状態で、瞬時的に大量の異物が捕集
装置10に流入した場合には、差圧Δl)+がΔp、を
はるかにオーバーし、捕集装置の強度にも影響するため
、捕集装置10を開き、捕集装置10のスクリーンに付
着する異物36を一担、復水器水室11側に開放させた
状態を示す。この後、第3図の状態で逆洗することで、
捕集装置10は保護される。
FIG. 5 shows that in the state shown in FIG. 1, when a large amount of foreign matter instantly flows into the collection device 10, the differential pressure Δl)+ far exceeds Δp, and the strength of the collection device is The state in which the collection device 10 is opened and the foreign matter 36 adhering to the screen of the collection device 10 is partially released to the condenser water chamber 11 side is shown because this also has an effect. After this, by backwashing as shown in Figure 3,
The collection device 10 is protected.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、冷却管の汚n状態の管理が可能となり
、冷却管の運転(性能)状態の変化に追従し、冷却管の
汚れ状態に応じた洗浄体の投入位置切換えが可能になる
According to the present invention, it becomes possible to manage the contamination state of the cooling pipe, follow changes in the operation (performance) state of the cooling pipe, and switch the insertion position of the cleaning body according to the contamination state of the cooling pipe. .

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

tg1図ないし第5図は本発明の一実施例の系統図、第
6図は冷却管内直スケール付着量の調査実績図、第7図
は冷却管出入口の運転状態値の変化順向を示す特性図、
第8図は洗浄運転方法の内容を示す70−チャート、第
9図は公知の異物除去装置の系統図、第10図は′i4
9図の作用説明図である。 1・・・復水器。
Figures 1 to 5 are system diagrams of an embodiment of the present invention, Figure 6 is a diagram showing the results of investigation of the amount of direct scale deposited inside cooling pipes, and Figure 7 is a characteristic showing the direction of change in operating status values at the entrance and exit of cooling pipes. figure,
Fig. 8 is a 70-chart showing the details of the cleaning operation method, Fig. 9 is a system diagram of a known foreign matter removal device, and Fig. 10 is 'i4
9 is an explanatory diagram of the action of FIG. 9. 1... Condenser.

Claims (1)

【特許請求の範囲】 1、復水器の冷却管入口部及び出口部の管外壁に取付け
た熱流センサで熱流束を、および器内蒸気温度または器
内真空度、冷却水出入口温度を検出し、併せて、冷却水
出入口系に設けたボール洗浄装置兼プレスクリーンの前
後差圧を検出し、その検出値を演算装置に入力し、冷却
管出入口部の管清浄度を演算し、管清浄度または前後差
圧と、予め設定された計画値とを比較し、冷却管の出入
口部の汚れ状態、または、ボール洗浄装置兼プレスクリ
ーンの差圧状態に応じて洗浄体の投入位置を切り換える
ことを特徴とする復水器のボール洗浄方法。 2、復水器の冷却管入口部及び出口部の管外壁に取付け
た熱流センサと、器内蒸気温度または器内真空度、冷却
水出入口温度の検出器と、冷却水出入口系に設けたボー
ル捕集器兼プレスクリーンと、その前後差圧を検出する
差圧計と、その検出値の信号入力装置と、前記冷却管の
出入口部の管清浄度を演算し、前記管清浄度または前記
前後差圧を、予め設定された計画値と比較する演算装置
と、その出力により洗浄方向を切換える制御発信装置と
、逆洗弁とを設けたことを特徴とする復水器のボール洗
浄装置。 3、冷却水入口系に冷却水量を検出する流量計を設けた
ことを特徴とする特許請求の範囲第2項記載の復水器の
ボール洗浄装置。
[Claims] 1. A heat flux sensor attached to the outer wall of the cooling pipe inlet and outlet of the condenser detects the heat flux, the internal steam temperature or the internal vacuum degree, and the cooling water inlet and outlet temperature. In addition, the differential pressure across the ball cleaning device and pre-screen installed in the cooling water inlet and outlet system is detected, and the detected value is input to a calculation device to calculate the pipe cleanliness of the cooling pipe inlet and outlet. Alternatively, compare the differential pressure across the front and rear with a preset plan value, and switch the cleaning body loading position depending on the dirt condition at the entrance and exit of the cooling pipe or the differential pressure condition of the ball cleaning device and pre-screen. A distinctive condenser ball cleaning method. 2. Heat flow sensors installed on the outer walls of the cooling pipe inlet and outlet of the condenser, detectors for internal steam temperature or internal vacuum, cooling water inlet/outlet temperature, and balls installed in the cooling water inlet/outlet system. A collector and pre-screen, a differential pressure gauge that detects the differential pressure across the front and back, a signal input device for the detected value, and a pipe cleanliness at the inlet and outlet of the cooling pipe is calculated, and the pipe cleanliness or the front and back difference is calculated. A ball cleaning device for a condenser, comprising: a calculation device that compares the pressure with a preset plan value; a control transmission device that switches the cleaning direction based on the output of the calculation device; and a backwash valve. 3. The condenser ball cleaning device according to claim 2, characterized in that the cooling water inlet system is provided with a flow meter for detecting the amount of cooling water.
JP12109586A 1986-05-28 1986-05-28 Ball washing method for condenser and device thereof Pending JPS62280590A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12109586A JPS62280590A (en) 1986-05-28 1986-05-28 Ball washing method for condenser and device thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12109586A JPS62280590A (en) 1986-05-28 1986-05-28 Ball washing method for condenser and device thereof

Publications (1)

Publication Number Publication Date
JPS62280590A true JPS62280590A (en) 1987-12-05

Family

ID=14802751

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12109586A Pending JPS62280590A (en) 1986-05-28 1986-05-28 Ball washing method for condenser and device thereof

Country Status (1)

Country Link
JP (1) JPS62280590A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6332298A (en) * 1986-07-24 1988-02-10 Ebara Corp Heat transfer pipe cleaning device for heat exchanger
JP2006343003A (en) * 2005-06-08 2006-12-21 Kawasaki Thermal Engineering Co Ltd Absorption water cooler/heater system and its operation method
JP2014114993A (en) * 2012-12-07 2014-06-26 Asahi Kokusai Techneion Co Ltd Heat exchanger operating device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6332298A (en) * 1986-07-24 1988-02-10 Ebara Corp Heat transfer pipe cleaning device for heat exchanger
JP2006343003A (en) * 2005-06-08 2006-12-21 Kawasaki Thermal Engineering Co Ltd Absorption water cooler/heater system and its operation method
JP2014114993A (en) * 2012-12-07 2014-06-26 Asahi Kokusai Techneion Co Ltd Heat exchanger operating device

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