JP3958222B2 - Cleaning method in plant - Google Patents

Cleaning method in plant Download PDF

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Publication number
JP3958222B2
JP3958222B2 JP2003015845A JP2003015845A JP3958222B2 JP 3958222 B2 JP3958222 B2 JP 3958222B2 JP 2003015845 A JP2003015845 A JP 2003015845A JP 2003015845 A JP2003015845 A JP 2003015845A JP 3958222 B2 JP3958222 B2 JP 3958222B2
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Prior art keywords
water
cleaning
blow
condenser
deaerator
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JP2004226026A (en
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英昭 林
光男 山田
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Chugoku Electric Power Co Inc
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Chugoku Electric Power Co Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、プラントにおける貯槽、機器と配管が組み合わされた系の水流による洗浄技術に係り、特に発電所等の起動時に系内の洗浄処理を要するプラントにおける洗浄方法に関するものである。
【0002】
【従来の技術】
一般に、火力発電所等の発電プラントの運転においては、その給水中に不純物が混入してはならない。そこで、図から図10のプラントの系統図に示すように、貯槽、機器と配管が組み合わされた発電プラントの系では、その起動時に洗浄処理を行う必要がある。例えば、貫流ボイラ等を洗浄処理するときは、系のブロー洗浄を行うと共に、系の途中に設けた脱塩装置に通水し循環洗浄することにより洗浄処理を行っていた。
【0003】
例えば、復水クリーンアップするときは、図の系統図に示すように復水ポンプ3を運転し、ブロー弁B2を「開」にしてブロータンク5へブロー洗浄していた。次に、復水器2と配管内の水質が安定した後に、弁(CV−2)を「開」にして循環運転していた。このとき脱塩装置4への通水を開始し、以後の工程では全て水質処理を行っていた。図示例では、「太い実線」はブロー洗浄を示し、「太い破線」は循環洗浄を示している。
【0004】
低圧クリーンアップするときは、図の系統図に示すように、低圧ヒータ6から脱気器7まで通水し、ブロー弁B4、ブロー弁B5を「開」にしてブロータンク5へブロー洗浄していた。次に、低圧ヒータ6と脱気器7内の水質が安定した後に、弁V6を「開」にして循環運転していた。
【0005】
高圧クリーンアップするときは、図の系統図に示すように、低圧クリーンアップ系統で脱気器7へ通水し、給水ポンプ8を運転し、高圧ヒータ9へ通水し、ブロー弁B5を「開」にしてブロータンク5へブロー洗浄していた。次に、高圧ヒータ9内の水質が安定した後に弁V6を「開」にして循環運転していた。
【0006】
ボイラクリーンアップするときは、図10の系統図に示すように、高圧クリーンアップ系統でボイラ1へ通水し、フラッシュタンク10へ水を張り、ブロー弁B7を「開」にしてブロータンク5へブロー洗浄していた。次に、ボイラ1と配管内の水質が安定した後に、弁(CV−3)を「開」にして循環運転していた。
【0007】
【発明が解決しようとする課題】
定期点検等でボイラを停止する場合、貯槽、機器および配管内には停止時からの残留水や、工事による塵埃または腐食防止用薬品等が混入している場合がある。しかし、上記従来の洗浄方法では、貯槽、機器および配管中の不純物を不必要に系内循環させ脱塩装置4で吸着除去させるため、その処理時間が長くなるという問題を有していた。例えば、プラントの系内の洗浄に要する時間が11時間から12時間程度を要していた。ここで、最近の電力需要は、冷暖房機器をはじめとする数々の電気機器の普及に伴い、需要家の産業活動や気温等の気象条件により急激に増減する傾向にある。その急激な需要変化に対応するため、発電プラントのレスポンスは給電運用上の重要な位置づけとなっており、起動指令から全負荷までの時間短縮が望まれていた。
【0008】
また、脱塩装置4を再生させるための洗浄頻度の増加及び樹脂の劣化が進行するという問題を有していた。
【0009】
更に、貯槽、機器に水張りしながらブロー洗浄を行うために、大量の洗浄水が必要であるという問題を有していた。例えば、発電機出力が700MWクラスの1発電プラントの系内の洗浄に要する洗浄水が2500トンから2700トン程度であった。
【0010】
本発明は、かかる問題点を解決するために創案されたものである。すなわち、本発明の目的は、最初に復水器、脱気器といった系の中で保水容量の大きい貯槽、機器に一旦水を張った後ブローし、その後、脱気器までの系における貯槽、機器と配管内の不純物をブロー洗浄のみで処理することにより、洗浄工程途中における循環洗浄工程を省略でき、短時間に洗浄処理すると共に、その洗浄に用いる使用する水量を減少させることができるプラントにおける洗浄方法を提供することにある。
【0011】
【課題を解決するための手段】
本発明の第1の洗浄方法によれば、発電プラントにおける復水器(2)、脱気器(7)及び脱塩装置(4)を配管組み合わた系を洗浄処理する洗浄方法であって、前記復水器(2)と前記脱気器(7)に一旦水を張った後、該復水器(2)と該脱気器(7)内の水質が基準値に達するまで水張りとブローを繰り返し、次に、再度前記復水器(2)に水を張った後、復水器(2)から前記脱気器(7)までの間の機器と配管を、復水ポンプ(3)により洗浄水を供給しつつブロー洗浄し、その水質が基準値に達した後、脱塩装置(4)へ通水する、ことを特徴とするプラントにおける洗浄方法が提供される。
【0012】
第2の洗浄方法は、発電プラントの復水器(2)、脱気器(7)、低圧ヒータ(6)及び脱塩装置(4)を配管組み合わた系を洗浄処理する洗浄方法であって、前記復水器(2)と前記脱気器(7)に一旦水を張った後、該復水器(2)と該脱気器(7)内の水質が基準値に達するまで水張りとブローを繰り返し、次に、再度前記復水器(2)に水を張った後、復水ポンプ(3)により該復水器(2)を、洗浄水を供給しつつブロー洗浄し、前記低圧ヒータ(6)をバイパスして脱気器(7)へ通水し、該脱気器(7)へ再度水を張った後ブローを行い、前記脱気器(7)を洗浄水を供給しつつブロー洗浄し、同時に低圧ヒータ(6)も洗浄水を供給しつつブロー洗浄し、その水質が基準値に達した後、脱塩装置(4)へ通水する方法である。
【0013】
上記方法では、最初に発電プラントを構成する復水器(2)、脱気器(7)等といった系の中で保水容量の大きい貯槽や機器に一旦水を張った後この貯水のみでブローを行うことにより、これらの貯槽や機器内にある不純物を直近の弁から排出するものであるため、洗浄処理に要する時間を短縮することができる。しかも、使用水量が従来の循環洗浄とブロー洗浄を併用した洗浄方法と比較して低減することができる。
【0014】
また、本発明は、貯槽、機器と配管が接続された系を洗浄する際に、洗浄工程途中の循環洗浄工程を省略するものであるために、従来は脱塩装置内で吸着除去していた不純物が、この脱塩装置内を通水しないことで樹脂の劣化を防ぐことができる。
【0015】
【発明の実施の形態】
以下、本発明の好ましい実施の形態を図面を参照して説明する。
図1は本発明のプラントにおける洗浄方法を実施する発電プラントの系統図である。図から図は洗浄方法を示す発電プラントの系統図である。図示例では、「太い実線」はブローまたはブロー洗浄を、「太い破線」は循環洗浄を示している。
本発明の洗浄方法は、先ず、復水器2と脱気器7に一旦水を張った後ブローを行い、その水質が基準値に達するまでこれらを繰り返し、再度復水器2に水を張った後、復水ポンプ3によりブロー洗浄し、低圧ヒータ6をバイパスして脱気器7へ通水し、脱気器7へ再度水を張った後ブローし、脱気器7をブロー洗浄しながら低圧ヒータ6内をブロー洗浄し、その水質が基準値に達した後、脱塩装置4へ通水する。
ここで「ブロー」とは、洗浄水を供給しないで、貯水のみでブローを行うことをいい、「ブロー洗浄」とは、洗浄水を供給しつつブローを行うことをいう。
【0016】
図2は復水クリーンアップの洗浄方法を示す発電プラントの系統図である。
先ず、系の中で保水容量の大きな貯槽、機器である復水器2と脱気器7へ一旦水を張った後ブローするときは、図示するように、復水器2については、ブロー弁B1を「開」にしてブロータンク5へブローする。また、脱気器7についてはブロー弁B4、ブロー弁B5を「開」にしてブロータンク5へブローする。例えば、復水器2の水張りとブローは、サンプリング配管を介した水質検出器で測定したブロー水質が基準値に達するまで実施し、必要があれば複数回繰り返す。ブロー完了後はブロー弁B1,B4,B5を閉止する。
【0017】
図3は復水クリーンアップの洗浄方法を示す発電プラントの系統図である。
次に、復水クリーンアップをするときは、図示するように、復水器2に水を張った後、復水ポンプ3を運転し、ブロー弁B2を「開」にしてブロータンク5へブロー洗浄する。即ち、復水器2に再度水張り後、弁V1及びブロー弁B2を開け、復水器2を経由した洗浄水による配管のブロー洗浄を行う。この時、復水器2へは適宜洗浄水を供給する。配管のブロー洗浄は、サンプリング配管を介した水質検出器で測定したブロー洗浄水質が基準値に達するまで実施する。
【0018】
水質検出器による測定は、その系の目的によって検査項目が異なる。発電所の場合では、濁度、鉄、ヒドラジン又は溶存酸素が検査項目となる。濁度と鉄に強い相関関係を示す系では、濁度の代わりに鉄を測定することができる。水質は自動測定のみならず、手分析による測定とすることもできる。
【0019】
また、手分析や水質検出器による測定に代えて、洗浄時間の管理により実施することができる。この洗浄時間は、その洗浄対象装置の種類と停止時間に応じて設定する。例えば、短時間で洗浄工程が終了することがあらかじめ経験則としてわかっている場合は、タイマーを使用して洗浄時間を管理し、次工程へ進めることができる。
【0020】
図4は低圧ヒータバイパスクリーンアップの洗浄方法を示す発電プラントの系統図である。図5は低圧ヒータクリーンアップの洗浄方法を示す発電プラントの系統図である。
脱気器7と低圧ヒータ6とをクリーンアップするときは、まず図4の系統図に示すように、低圧ヒータ6をバイパスし、脱気器7へ通水し、この脱気器7に再度水を張った後、ブロー弁B4、ブロー弁B5を「開」にしてブロータンク5へブローする。次に、図5の系統図に示すように、この脱気器7のクリーンアップを実施しながら弁V4、ブロー弁B3を「開」にして低圧ヒータ6内を押出してブロー洗浄する。
【0021】
図6は低圧ヒータクリーンアップ後の循環方法を示す発電プラントの系統図である。
脱気器7と低圧ヒータ6のクリーンアップにともない、系の水質が基準値に達した後、図示するように、脱塩装置4へ通水し循環工程を行う。
【0022】
従来の発電プラントの系について、その起動時にブロー洗浄と循環洗浄を併用した方法では、11時間程度の洗浄時間が必要であった。本発明による脱気器および低圧ヒータの洗浄が完了するまで、即ち洗浄工程途中における循環洗浄を省略する洗浄方法では、系内で保水容量の大きな貯槽又は機器について一旦水を張った後ブローするために、その系内の不純物を直近の弁から排出することができるので8時間程度で洗浄が終了した。
また、使用する水量については、ブロー、ブロー洗浄と循環洗浄を併用した方法では約2500トン必要であったが、本発明の洗浄方法では約1500トンで洗浄できた。
【0023】
なお、貯槽、機器及び配管については、この様に順次洗浄する方法だけでなく、機器と配管等、複数装置を同時に洗浄することも可能である。また、各工程での洗浄が未完のまま次工程へ進むことも可能である。この様に順次洗浄するか、同時に洗浄するかは、洗浄水の供給容量や排水容量等を考慮して決定する。この場合、同時に洗浄を進行させることにより、より迅速に洗浄を完了させることができる。
【0024】
本発明は上述した発明の実施の形態に限定されず、最初に主に系内で保水容量の大きな復水器2、脱気器7のような貯槽又は機器について一旦水を張った後ブローすることにより不純物を直近の弁B1,B4,B5等から排出し、下流側の装置を順次ブロー、ブロー洗浄し、洗浄工程途中における循環洗浄を不要とする洗浄方法であれば、本発明の要旨を逸脱しない範囲で種々変更できることは勿論である。
【0025】
【発明の効果】
本発明のプラントにおける洗浄方法は、最初に復水器、脱気器といった系の中で保水容量の大きい機器に一旦水を張った後ブローを行い、その後、再度水を張り、下流側の貯槽、機器、配管を順次ブロー洗浄し、従来実施していた脱気器および低圧ヒータの洗浄が完了するまで、即ち洗浄工程途中における循環洗浄工程を省略する方法であるため、洗浄処理に要する時間を短縮することができる。そこで、火力発電所等のプラントの起動までに要する時間を短縮することができ、給電の運用性の向上に貢献することができる。
【0026】
また、本発明の洗浄方法によれば、プラント洗浄に使用する水量を従来の循環洗浄とブロー洗浄を併用した方法と比較して低減することができる。
【0027】
更に、本発明の洗浄方法は脱気器および低圧ヒータの洗浄が完了するまでの、最も脱塩装置への負荷が高い各クリーンアップ時に脱塩装置による水質処理を行わないことから、その装置について化学洗浄を実施する回数を低減させることが可能となるために、洗浄薬品のコストダウンや環境負荷を低減させると共に、不純物を系内で循環させないために、機器等の故障率が低下する、等の効果がある。
【図面の簡単な説明】
【図】本発明のプラントにおける洗浄方法を実施する発電プラントの系統図である。
【図】復水クリーンアップの洗浄方法を示す発電プラントの系統図である。
【図】復水クリーンアップの洗浄方法を示す発電プラントの系統図である。
【図】低圧ヒータバイパスクリーンアップの洗浄方法を示す発電プラントの系統図である。
【図】低圧ヒータクリーンアップの洗浄方法を示す発電プラントの系統図である。
【図】低圧ヒータクリーンアップ後の循環方法を示す発電プラントの系統図である。
【図】従来の火力発電所等の発電プラントの復水クリーンアップする洗浄方法を示す発電プラントの系統図である。
【図】従来の火力発電所等の発電プラントの低圧クリーンアップする洗浄方法を示す発電プラントの系統図である。
【図】従来の火力発電所等の発電プラントの高圧クリーンアップする洗浄方法を示す発電プラントの系統図である。
【図10】従来の火力発電所等の発電プラントのボイラクリーンアップする洗浄方法を示す発電プラントの系統図である。
【符号の説明】
1 ボイラ
2 復水器
3 復水ポンプ
4 脱塩装置
6 低圧ヒータ
7 脱気器
8 給水ポンプ
9 高圧ヒータ
10 フラッシュタンク
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a cleaning technique using a water flow in a system in which storage tanks, equipment and piping in a plant are combined, and more particularly to a cleaning method in a plant that requires a cleaning process in the system when a power plant or the like is started.
[0002]
[Prior art]
Generally, in the operation of a power plant such as a thermal power plant, impurities should not be mixed in the water supply. Therefore, as shown in the system diagrams of the plants in FIGS. 7 to 10 , in the system of the power plant in which the storage tank, the equipment, and the piping are combined, it is necessary to perform a cleaning process at the time of activation. For example, when a once-through boiler or the like is subjected to a cleaning process, the system is blow-cleaned, and the cleaning process is performed by circulating water through a desalting apparatus provided in the middle of the system.
[0003]
For example, when condensate cleanup is performed, the condensate pump 3 is operated as shown in the system diagram of FIG. 7 , and the blow valve B <b> 2 is set to “open” to perform blow cleaning to the blow tank 5. Next, after the water quality in the condenser 2 and the piping was stabilized, the valve (CV-2) was opened and the circulation operation was performed. At this time, water flow to the desalting apparatus 4 was started, and water quality treatment was performed in all subsequent steps. In the illustrated example, “thick solid line” indicates blow cleaning, and “thick broken line” indicates circulation cleaning.
[0004]
When performing low-pressure cleanup, as shown in the system diagram of FIG. 8 , water is passed from the low-pressure heater 6 to the deaerator 7, and the blow valve B 4 and the blow valve B 5 are set to “open” and blow-washed into the blow tank 5. It was. Next, after the water quality in the low pressure heater 6 and the deaerator 7 was stabilized, the valve V6 was opened and the circulation operation was performed.
[0005]
When performing high pressure cleanup, as shown in the system diagram of FIG. 9 , water is passed to the deaerator 7 in the low pressure cleanup system, the feed water pump 8 is operated, water is passed to the high pressure heater 9, and the blow valve B5 is turned on. The blow tank 5 was blow-washed with “open”. Next, after the water quality in the high-pressure heater 9 was stabilized, the valve V6 was opened and the circulation operation was performed.
[0006]
When the boiler cleanup is performed, as shown in the system diagram of FIG. 10 , water is passed to the boiler 1 through the high-pressure cleanup system, water is applied to the flash tank 10, the blow valve B 7 is opened, and the blow tank 5 is opened. Blow cleaning. Next, after the water quality in the boiler 1 and the piping was stabilized, the valve (CV-3) was opened and the circulation operation was performed.
[0007]
[Problems to be solved by the invention]
When the boiler is stopped during regular inspections, the storage tank, equipment, and piping may contain residual water from the time of stoppage, dust from construction, or chemicals for preventing corrosion. However, the conventional cleaning method has a problem that the processing time is long because impurities in the storage tank, equipment and piping are unnecessarily circulated in the system and adsorbed and removed by the desalting apparatus 4. For example, the time required for cleaning the plant system is about 11 to 12 hours. Here, the recent demand for electric power tends to increase or decrease rapidly depending on the consumer activities such as the industrial activities and the weather conditions such as the temperature with the spread of various electric devices such as air conditioning equipment. In order to respond to the sudden change in demand, the response of the power plant has become an important position in power supply operation, and it has been desired to shorten the time from the start command to the full load.
[0008]
Moreover, there existed a problem that the washing | cleaning frequency for reproducing | regenerating the desalinization apparatus 4 increased, and deterioration of resin advanced.
[0009]
Furthermore, there is a problem that a large amount of washing water is required to perform blow washing while filling the storage tank and equipment. For example, the washing water required for washing in the system of one power plant with a generator output of 700 MW class was about 2500 to 2700 tons.
[0010]
The present invention has been developed to solve such problems. That is, the object of the present invention is to first store a tank having a large water retention capacity in a system such as a condenser and a deaerator, blow once after water is applied to the device, and then store in the system up to the deaerator, By treating the impurities in the equipment and piping only by blow cleaning, the circulation cleaning step in the middle of the cleaning process can be omitted, and in the plant that can be cleaned in a short time and the amount of water used for the cleaning can be reduced It is to provide a cleaning method.
[0011]
[Means for Solving the Problems]
According to the first method of cleaning of the present invention, the condenser in a power plant (2), there at deaerator (7) and desalination device (4) a cleaning method for cleaning a system that combines a pipe Te, until after once filled with water to the condenser (2) and the deaerator (7), 該復condenser (2) and the dehydration-aerator (7) water quality in reaches the reference value the water filling and repeating the blow, then, after filled with water again the condenser (2), the equipment and piping between from the condenser (2) to said deaerator (7), a condensate pump According to (3) , there is provided a cleaning method in a plant characterized in that blow cleaning is performed while supplying cleaning water , and the water quality reaches a reference value and then water is passed to a desalting apparatus (4).
[0012]
The second method of cleaning, condenser of a power plant (2), deaerator (7), the low-pressure heater (6) and demineralizer (4) in the cleaning method of cleaning a system that combines a pipe there, after once filled with water to the condenser (2) and the deaerator (7), until 該復condenser (2) and the dehydration-aerator (7) water quality in reaches the reference value Repeated water filling and blowing, and then watered the condenser (2) again , and then the condenser (2) was blow-washed while supplying cleaning water by the condensate pump (3), the Rohm & low pressure heater (6) bypass to deaerator to (7), followed by blow after stretched again with water to dehydration-aerator (7), said deaerator wash water (7) in the method while supplying blowing washed, blown washed while supplying low pressure heater (6) washing water at the same time, the water flow that water quality after reaching the reference value, the desalter (4) That.
[0013]
In the above method, the water tank or equipment having a large water holding capacity in the system such as the condenser (2) and deaerator (7) constituting the power plant is first filled with water and then blown only with this water storage. By doing so, impurities in these storage tanks and equipment are discharged from the nearest valve, so that the time required for the cleaning process can be shortened. In addition, the amount of water used can be reduced as compared with a conventional cleaning method using both circulation cleaning and blow cleaning.
[0014]
Further, in the present invention, when washing a system in which a storage tank, equipment and piping are connected, the circulation washing step in the middle of the washing step is omitted. Impurities can prevent deterioration of the resin by not passing water through the desalting apparatus.
[0015]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a system diagram of a power plant that performs the cleaning method in the plant of the present invention. 2 to 6 are system diagrams of the power plant showing the cleaning method. In the illustrated example, “thick solid line” indicates blow or blow cleaning, and “thick broken line” indicates circulation cleaning.
In the cleaning method of the present invention, first, the condenser 2 and the deaerator 7 are once filled with water and then blown, and these are repeated until the water quality reaches a reference value, and then the condenser 2 is filled with water again. After that, the condensate pump 3 is blow-washed, the low-pressure heater 6 is bypassed, water is passed to the deaerator 7, water is refilled to the deaerator 7 and then blown, and the deaerator 7 is blow-washed. However, the inside of the low-pressure heater 6 is blow-cleaned, and after the water quality reaches the reference value, the water is passed through the desalting apparatus 4.
Here, “blow” refers to blowing with only stored water without supplying cleaning water, and “blow cleaning” refers to performing blowing while supplying cleaning water.
[0016]
FIG. 2 is a system diagram of a power plant showing a cleaning method for condensate cleanup.
First, when the water is blown after the water is once put in the condenser 2 and the deaerator 7 which are storage tanks and devices having a large water holding capacity in the system , as shown in FIG. B1 is opened and blown into the blow tank 5. The deaerator 7 is blown into the blow tank 5 by opening the blow valve B4 and the blow valve B5. For example, water filling and blowing of the condenser 2 are performed until the blow water quality measured by the water quality detector via the sampling pipe reaches the reference value, and is repeated a plurality of times if necessary. After the blow is completed, the blow valves B1, B4, B5 are closed.
[0017]
FIG. 3 is a system diagram of a power plant showing a cleaning method for condensate cleanup.
Next, when performing condensate cleanup, as shown in the figure, after the condenser 2 is filled with water, the condensate pump 3 is operated, the blow valve B2 is opened, and the blow tank 5 is blown. Wash. That is, after refilling the condenser 2 again, the valve V1 and the blow valve B2 are opened, and the pipe is blow-washed with the wash water passing through the condenser 2. At this time, cleaning water is appropriately supplied to the condenser 2. Pipe blow cleaning is performed until the blow cleaning water quality measured by the water quality detector through the sampling pipe reaches the reference value.
[0018]
The measurement items of the water quality detector vary depending on the purpose of the system. In the case of a power plant, turbidity, iron, hydrazine or dissolved oxygen are inspection items. In a system showing a strong correlation between turbidity and iron, iron can be measured instead of turbidity. Water quality can be measured not only automatically but also manually.
[0019]
Moreover, it can replace with a manual analysis and the measurement by a water quality detector, and can implement by management of the washing | cleaning time. This cleaning time is set according to the type of the device to be cleaned and the stop time. For example, when it is known as a rule of thumb that the cleaning process is completed in a short time, it is possible to manage the cleaning time using a timer and proceed to the next process.
[0020]
FIG. 4 is a system diagram of a power plant showing a cleaning method for low-pressure heater bypass cleanup. FIG. 5 is a system diagram of a power plant showing a cleaning method for low-pressure heater cleanup.
When cleaning up the deaerator 7 and the low-pressure heater 6, first, as shown in the system diagram of FIG. 4 , the low-pressure heater 6 is bypassed and water is passed to the deaerator 7. After filling the water, the blow valve B4 and the blow valve B5 are opened and blown into the blow tank 5. Next, as shown in the system diagram of FIG. 5, while the deaerator 7 is being cleaned up, the valve V4 and the blow valve B3 are opened, and the low pressure heater 6 is extruded and blow cleaned.
[0021]
FIG. 6 is a system diagram of the power plant showing the circulation method after the low-pressure heater cleanup.
As the deaerator 7 and the low-pressure heater 6 are cleaned up, the water quality of the system reaches a reference value, and then, as shown in the figure, the water is passed through the demineralizer 4 to perform a circulation process.
[0022]
In a conventional power plant system, a cleaning time of about 11 hours was required in a method using blow cleaning and circulation cleaning at the time of startup. In the cleaning method in which the cleaning of the deaerator and the low-pressure heater according to the present invention is completed, i.e., the circulation cleaning in the middle of the cleaning process is omitted, a water tank or device having a large water holding capacity is once filled with water and then blown. In addition, since the impurities in the system can be discharged from the latest valve, cleaning was completed in about 8 hours.
As for the amount of water to be used, about 2500 tons were required in the method using blow, blow cleaning and circulating cleaning in combination, but in the cleaning method of the present invention, cleaning was possible at about 1500 tons.
[0023]
In addition, about a storage tank, an apparatus, and piping, it is also possible to wash | clean multiple apparatuses simultaneously, such as not only the method to wash | clean sequentially but in this way. It is also possible to proceed to the next step without completing the cleaning in each step. Whether the cleaning is performed sequentially or simultaneously is determined in consideration of the supply capacity and drainage capacity of the cleaning water. In this case, the cleaning can be completed more quickly by proceeding with the cleaning at the same time.
[0024]
The present invention is not limited to the embodiment of the invention described above. First, the storage tank or equipment such as the condenser 2 or deaerator 7 having a large water retention capacity is first filled in the system and then blown. Thus, the gist of the present invention can be obtained if it is a cleaning method that discharges impurities from the latest valves B1, B4, B5, etc., and sequentially blows and blow-cleans downstream devices, and eliminates the need for circulating cleaning during the cleaning process. Of course, various changes can be made without departing from the scope.
[0025]
【The invention's effect】
In the washing method in the plant of the present invention, first, water is once applied to a device having a large water holding capacity in a system such as a condenser and a deaerator, then blown, and then water is added again, and a downstream storage tank This is a method that eliminates the circulation cleaning process until the cleaning of the deaerator and the low-pressure heater, which has been performed in the past, is completed, that is, the circulation cleaning process in the middle of the cleaning process. It can be shortened. Therefore, it is possible to shorten the time required for starting up a plant such as a thermal power plant, and it is possible to contribute to the improvement of power supply operability.
[0026]
Moreover, according to the cleaning method of the present invention, the amount of water used for plant cleaning can be reduced as compared with a conventional method using both circulation cleaning and blow cleaning.
[0027]
Furthermore, since the cleaning method of the present invention does not perform water quality treatment by the desalting apparatus at the time of each cleanup with the highest load on the desalting apparatus until the cleaning of the deaerator and the low-pressure heater is completed. Since it is possible to reduce the number of times chemical cleaning is performed, the cost of cleaning chemicals and environmental impact are reduced, and impurities are not circulated in the system, so the failure rate of equipment, etc. decreases. There is an effect.
[Brief description of the drawings]
FIG. 1 is a system diagram of a power plant that performs a cleaning method in a plant of the present invention.
FIG. 2 is a system diagram of a power plant showing a cleaning method for condensate cleanup.
FIG. 3 is a system diagram of a power plant showing a cleaning method for condensate cleanup.
FIG. 4 is a system diagram of a power plant showing a cleaning method for low-pressure heater bypass cleanup.
FIG. 5 is a system diagram of a power plant showing a cleaning method for low-pressure heater cleanup.
FIG. 6 is a system diagram of a power plant showing a circulation method after cleanup of a low-pressure heater.
FIG. 7 is a system diagram of a power plant showing a cleaning method for cleaning up condensate in a conventional power plant such as a thermal power plant.
FIG. 8 is a system diagram of a power plant showing a cleaning method for performing low-pressure cleanup of a power plant such as a conventional thermal power plant.
FIG. 9 is a system diagram of a power plant showing a cleaning method for performing high-pressure cleanup of a power plant such as a conventional thermal power plant.
FIG. 10 is a system diagram of a power plant showing a cleaning method for cleaning up a boiler of a power plant such as a conventional thermal power plant.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Boiler 2 Condenser 3 Condensate pump 4 Desalination apparatus 6 Low pressure heater 7 Deaerator 8 Water supply pump 9 High pressure heater 10 Flash tank

Claims (2)

発電プラントにおける復水器(2)、脱気器(7)及び脱塩装置(4)を配管組み合わた系を洗浄処理する洗浄方法であって、
前記復水器(2)と前記脱気器(7)に一旦水を張った後、該復水器(2)と該脱気器(7)内の水質が基準値に達するまで水張りとブローを繰り返し、
次に、再度前記復水器(2)に水を張った後、復水器(2)から前記脱気器(7)までの間の機器と配管を、復水ポンプ(3)により洗浄水を供給しつつブロー洗浄し、
その水質が基準値に達した後、脱塩装置(4)へ通水する、ことを特徴とするプラントにおける洗浄方法。
Condenser in a power plant (2), a deaerator (7) and desalination device (4) a cleaning method for cleaning a system that combines a pipe,
After once filled with water to the condenser (2) and the deaerator (7), the water filling and blow up 該復condenser (2) and the dehydration-aerator (7) Water quality in reaches the reference value Repeat
Then washed, filled with water again the condenser (2), the equipment and piping between from the condenser (2) to said deaerator (7), the condensate pump (3) Blow cleaning while supplying water ,
A washing method in a plant, wherein the water quality reaches a reference value and then water is passed to a desalinator (4).
発電プラントの復水器(2)、脱気器(7)、低圧ヒータ(6)及び脱塩装置(4)を配管組み合わた系を洗浄処理する洗浄方法であって、
前記復水器(2)と前記脱気器(7)に一旦水を張った後、該復水器(2)と該脱気器(7)内の水質が基準値に達するまで水張りとブローを繰り返し、
次に、再度前記復水器(2)に水を張った後、復水ポンプ(3)により該復水器(2)を、洗浄水を供給しつつブロー洗浄し、
前記低圧ヒータ(6)をバイパスして脱気器(7)へ通水し、該脱気器(7)へ再度水を張った後ブローを行い、
前記脱気器(7)を洗浄水を供給しつつブロー洗浄し、同時に低圧ヒータ(6)も洗浄水を供給しつつブロー洗浄し、
その水質が基準値に達した後、脱塩装置(4)へ通水する、ことを特徴とするプラントにおける洗浄方法。
Condenser of the power plant (2), deaerator (7), a cleaning method for cleaning a system that combines a pipe low pressure heater (6) and demineralizer (4),
After once filled with water to the condenser (2) and the deaerator (7), the water filling and blow up 該復condenser (2) and the dehydration-aerator (7) Water quality in reaches the reference value Repeat
Next, after watering the condenser (2) again, the condenser (2) is blow-washed while supplying washing water by the condenser pump (3),
The Rohm & low pressure heater (6) Bypass to deaerator to (7), followed by blow after stretched again with water to dehydration-aerator (7),
The deaerator (7) is blow-washed while supplying cleaning water, and at the same time the low-pressure heater (6) is blow-washed while supplying cleaning water ,
A washing method in a plant, wherein the water quality reaches a reference value and then water is passed to a desalinator (4).
JP2003015845A 2003-01-24 2003-01-24 Cleaning method in plant Expired - Fee Related JP3958222B2 (en)

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