JP2006183902A - Method for collective chemical cleaning of once-through boiler and system therefor - Google Patents

Method for collective chemical cleaning of once-through boiler and system therefor Download PDF

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JP2006183902A
JP2006183902A JP2004375538A JP2004375538A JP2006183902A JP 2006183902 A JP2006183902 A JP 2006183902A JP 2004375538 A JP2004375538 A JP 2004375538A JP 2004375538 A JP2004375538 A JP 2004375538A JP 2006183902 A JP2006183902 A JP 2006183902A
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cleaning
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Yutaka Sakurai
裕 櫻井
Setsuo Moriya
節雄 守谷
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Ebara Industrial Cleaning Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method capable of cleaning tubes of a superheater, a reheater, steam tubes and the like in a once-through boiler in a collective and simultaneous manner without cutting them. <P>SOLUTION: The method for collective chemical cleaning of a once-through boiler includes using a superheater inlet valve as a cleaning fluid inlet and a main steam stop valve as a cleaning fluid outlet, and cleaning a portion therebetween by means of a cleaning device by causing circulation of a chemical cleaning solution containing a chelating compound, an organic acid and a reducing agent, the cleaning device comprising a sludge collector, a chemical cleaning solution injection device, and a circulating pump. The method also includes using a reheater inlet valve as a cleaning solution inlet and a reheated steam stop valve as a cleaning solution outlet, and cleaning a portion therebetween by means of the cleaning device by causing circulation of the chemical cleaning solution containing the chelating compound, the organic acid, and the reducing agent, the cleaning device comprising the sludge collector, the chemical cleaning solution injection device, and the circulating pump. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、火力発電プラントや一般産業用ボイラーに使用される貫流型ボイラーの一括化学洗浄方法およびそのためのシステムに関する。   The present invention relates to a batch chemical cleaning method for a once-through boiler used in a thermal power plant or a general industrial boiler, and a system therefor.

貫流型ボイラーをはじめとするボイラーでは、プラント運転中に主蒸気管、過熱器、再熱器等の内面に水蒸気酸化スケール(以下、「スケール」ということがある)が生成されることがある。そして、この生成したスケールが蒸気とともにタービンに飛散すると、ノズル・エロージョンを起こし、タ−ビンの健全性をそこねるという問題があった。   In boilers such as once-through boilers, steam oxidation scales (hereinafter sometimes referred to as “scales”) may be generated on the inner surfaces of main steam pipes, superheaters, reheaters and the like during plant operation. When the generated scale is scattered along with the steam to the turbine, there is a problem that nozzle erosion is caused and the soundness of the turbine is lost.

従来、このような問題を避けるため、予め主蒸気管等の配管中のスケールを化学洗浄により除去することが行われているが、この化学洗浄方法は、例えば、過熱器出口配管を切断し、これを洗浄液入り口として、また、主蒸気止め弁または再熱蒸気入り口止め弁を洗浄液出口として取り合い、この間を洗浄装置により洗浄液を循環させることにより行われるのが一般的であった。   Conventionally, in order to avoid such a problem, it has been performed in advance to remove the scale in the piping such as the main steam pipe by chemical cleaning, this chemical cleaning method, for example, by cutting the superheater outlet piping, In general, this is performed by using this as a cleaning liquid inlet and a main steam stop valve or a reheat steam inlet stop valve as a cleaning liquid outlet, and circulating the cleaning liquid between them using a cleaning device.

しかしながら、過熱器等の出口配管は高温、高圧となるため、配管肉厚が数十ミリと厚く、この切断には多大な労力及び費用を要するという問題があった。また、これを切断するためには、規制当局の認可が必要であり、更に当該配管復旧後にも規制当局の検査を受ける必要があるなど、これらに関わる労力、費用もまた多大であった。   However, since the outlet pipe of a superheater or the like has a high temperature and a high pressure, the thickness of the pipe is as thick as several tens of millimeters, and there has been a problem that much labor and cost are required for this cutting. Moreover, in order to cut this, the approval of a regulatory authority is required, and also after the said piping restoration | repair, it is necessary to carry out the inspection of a regulatory authority, The labor and expense concerning these were also great.

これらの労力を回避するため、主蒸気管安全弁より風船型閉止治具を挿入し、安全弁上流側に当該閉止治具を装着し、安全弁フランジ部より洗浄液入り口座として取り合い、洗浄を行う方法も検討されてきた。しかし、この方法では過熱器部の洗浄が出来ず十分目的を達成できないという問題があった。   In order to avoid these efforts, a balloon-type closing jig is inserted from the main steam pipe safety valve, the closing jig is installed upstream of the safety valve, and a cleaning liquid account is taken into account from the safety valve flange and cleaning is also considered. It has been. However, this method has a problem that the superheater section cannot be cleaned and the purpose cannot be achieved sufficiently.

また、仮に過熱器入り口配管を切断し、取り合い洗浄を行っても、除去されたスラッジ分を回収することが難しく、洗浄目的を完全に達成することが出来ないという問題があり、更には、過熱器はUチューブなどの屈曲管があり、当該部分のスラッジ除去効果を洗浄中に確認することが不可能であるという問題もあった。   In addition, even if the superheater inlet pipe is cut and washed together, there is a problem that it is difficult to recover the removed sludge, and the cleaning purpose cannot be achieved completely. There is also a problem that the vessel has a bent tube such as a U tube, and it is impossible to confirm the sludge removal effect of the portion during cleaning.

本発明は、上記課題を解決することを目的とするものであり、過熱器、再熱器、各蒸気管等を切断することなく一括で同時に洗浄することができる方法の提供をその課題とするものである。   The present invention aims to solve the above-mentioned problems, and an object of the present invention is to provide a method capable of simultaneously cleaning the superheater, the reheater, each steam pipe and the like without cutting them. Is.

本発明者らは、上記課題を解決すべく鋭意検討を行った結果、貫流ボイラーの所定の位置を洗浄液入り口および洗浄液出口として取り合い、この間を特定の組成を有する洗浄液で循環洗浄することにより、スラッジを微粉状の状態で除去排出でき、従来、そのままでは化学洗浄が困難とされていた過熱器中も洗浄可能であることを見出し、本発明を完成した。   As a result of intensive studies to solve the above-mentioned problems, the present inventors have taken a predetermined position of the once-through boiler as a cleaning liquid inlet and a cleaning liquid outlet, and circulated and cleaned between them with a cleaning liquid having a specific composition. The present invention has been completed by finding that it can be removed and discharged in a fine powder state and can be cleaned even in a superheater that has been conventionally difficult to perform chemical cleaning.

すなわち本発明は、過熱器入口弁を洗浄液入口、主蒸気止め弁を洗浄液出口として取り合い、この間をスラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置を用い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄することを特徴とする貫流型ボイラーの一括化学洗浄方法である。   That is, the present invention uses a superheater inlet valve as a cleaning liquid inlet and a main steam stop valve as a cleaning liquid outlet, and uses a cleaning apparatus equipped with a sludge collecting device, a chemical cleaning liquid injection device and a circulation pump in the meantime, It is a collective chemical cleaning method for a once-through boiler, characterized by circulating cleaning with a chemical cleaning agent containing an organic acid and a reducing agent.

また本発明は、再熱器入口弁を洗浄液入口、再熱蒸気止め弁を洗浄液出口として取り合い、この間をスラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置を用い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄することを特徴とする貫流型ボイラーの一括化学洗浄方法である。   The present invention also uses a reheater inlet valve as a cleaning liquid inlet and a reheat steam stop valve as a cleaning liquid outlet, and uses a cleaning apparatus equipped with a sludge collecting device, a chemical cleaning liquid injection device and a circulation pump in the meantime, to form a chelate. A batch chemical cleaning method for a once-through boiler, characterized by circulating cleaning with a chemical cleaning agent containing a compound, an organic acid and a reducing agent.

更に本発明は、スラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置で、過熱器入口弁を洗浄液入口、主蒸気止め弁を洗浄液出口として取り合い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄可能としてなる貫流型ボイラーの一括化学システムである。   Furthermore, the present invention is a cleaning device equipped with a sludge trapping device, a chemical cleaning liquid injection device and a circulation pump, wherein a superheater inlet valve is used as a cleaning liquid inlet and a main steam stop valve is used as a cleaning liquid outlet. This is a collective chemical system for a once-through boiler that can be circulated and cleaned with a chemical cleaning agent containing a reducing agent.

更にまた本発明は、スラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置で、再熱器入口弁を洗浄液入口、再熱蒸気止め弁を洗浄液出口として取り合い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄可能としてなる貫流型ボイラーの一括化学洗浄システムである。   Furthermore, the present invention is a cleaning device equipped with a sludge collecting device, a chemical cleaning liquid injection device, and a circulation pump, wherein a reheater inlet valve is used as a cleaning liquid inlet and a reheat steam stop valve is used as a cleaning liquid outlet, and a chelate forming compound, This is a collective chemical cleaning system for a once-through boiler that can be circulated and cleaned with a chemical cleaning agent containing an organic acid and a reducing agent.

本発明によれば、過熱器、再熱器、主蒸気管、高・低温再熱蒸気管を多大なる費用と労力要する切断作業を行わず、一括で洗浄することができ、これら配管に付着堆積したスケールを同時に除去することが可能であり、特に、過熱器や再熱器の中の屈曲管に存在するスケールをも除去することができる。   According to the present invention, the superheater, the reheater, the main steam pipe, and the high / low temperature reheat steam pipe can be cleaned in a lump without performing costly and labor-intensive cutting work, and deposited on these pipes. It is possible to remove the scales at the same time, and in particular, it is possible to remove scales present in the bent pipes in the superheater and the reheater.

従って、本発明方法により、上記配管を一括化学洗浄することにより、ボイラー起動時や停止時などに上記スケールが剥離脱落し、これがタービンへの飛散、流入することを防ぎ、ノズル・エロージョンの発生を防止し、タービンの健全性を保つことが可能である。   Therefore, by the method of the present invention, the above-mentioned piping is subjected to batch chemical cleaning, whereby the scale is peeled and dropped when the boiler is started or stopped, and this prevents the scale from being scattered and flowing into the turbine, thereby generating nozzle erosion. It is possible to prevent and maintain the soundness of the turbine.

本発明は、過熱器(二次過熱器)入口弁を洗浄液入口、主蒸気止め弁を洗浄液出口として取り合い、この間をスラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置を用い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄する貫流型ボイラーの化学洗浄方法(以下、「第一態様発明」という)および再熱器入口弁を洗浄液入口、再熱蒸気止め弁を洗浄液出口として取り合い、この間をスラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置を用い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄する貫流型ボイラーの化学洗浄方法(以下、「第一態様発明」という)を含むものである。   The present invention uses a superheater (secondary superheater) inlet valve as a cleaning liquid inlet and a main steam stop valve as a cleaning liquid outlet, and uses a cleaning device equipped with a sludge collecting device, a chemical cleaning liquid injection device and a circulation pump in the meantime, A chemical cleaning method for a once-through boiler that circulates and cleans with a chemical cleaning agent containing a chelate-forming compound, an organic acid and a reducing agent (hereinafter referred to as "first aspect invention") and a reheater inlet valve as a cleaning liquid inlet, reheat A steam stop valve is used as a cleaning liquid outlet, and a cleaning apparatus equipped with a sludge collector, chemical cleaning liquid injection apparatus, and circulation pump is used for this period, and a circular cleaning is performed with a chemical cleaning agent containing a chelating compound, an organic acid and a reducing agent. And a chemical cleaning method for a once-through boiler (hereinafter referred to as “first aspect invention”).

以下、いくつかの図面と共に、本発明の第一態様発明および第二態様発明について説明を行う。   Hereinafter, the first aspect invention and the second aspect invention of the present invention will be described with some drawings.

図1は、第一態様発明の洗浄系統を模式的に示したものである。図中、1は過熱器入り口弁取り合い座、2は主蒸気止め弁取り合い座、3はスラッジ捕集装置、4はヒーター、5は循環ポンプ、6は薬品溶解タンク、7は薬品溶解注入ポンプ、8はスラッジ計測装置、9は二次過熱器、10は主蒸気管をそれぞれ示す。   FIG. 1 schematically shows a cleaning system according to the first aspect of the present invention. In the figure, 1 is a superheater inlet valve joint seat, 2 is a main steam stop valve joint seat, 3 is a sludge collecting device, 4 is a heater, 5 is a circulation pump, 6 is a chemical dissolution tank, 7 is a chemical dissolution injection pump, 8 is a sludge measuring device, 9 is a secondary superheater, and 10 is a main steam pipe.

第一態様発明を実施するには、まず、過熱器入口弁を洗浄液入口、主蒸気止め弁を洗浄液出口とすることが必要である。過熱器入り口弁は、ゲート弁が一般的であり、この弁と取り合う場合は、バルブボンネットを開放し、弁対を抜き取った後、弁の洗浄液通水側は開口を有する板を、また、洗浄液を閉止する側には、閉止板をそれぞれタンバックルで接続し、その両サイドを突張る突張力で閉止側を閉止すればよい。更に、弁フランジ部に仮設フランジを取付け取り合うことにより化学洗浄液の循環が可能となる。   In order to implement the first aspect of the invention, it is first necessary to set the superheater inlet valve as the cleaning liquid inlet and the main steam stop valve as the cleaning liquid outlet. The superheater inlet valve is generally a gate valve. When the valve is connected with the valve, the valve bonnet is opened and the valve pair is removed. It is only necessary to connect the closing plates to the side to be closed with tan buckles, and close the closing side with the thrust that stretches both sides. Further, the chemical cleaning liquid can be circulated by attaching and mounting the temporary flange to the valve flange portion.

上記の化学洗浄液の循環は、洗浄装置を用いて行われる。この洗浄装置は、少なくともスラッジ捕集装置3、薬品溶解タンク6と薬品溶解注入ポンプ7を備えた化学洗浄液注入装置8および循環ポンプ5を具備したものである。   The chemical cleaning liquid is circulated using a cleaning device. This cleaning device includes at least a sludge collecting device 3, a chemical cleaning liquid injection device 8 including a chemical dissolution tank 6 and a chemical dissolution injection pump 7, and a circulation pump 5.

このうち、スラッジ捕集装置3は、化学洗浄液による洗浄工程で各配管から除去・脱落・溶解した主に鉄のスラッジ成分を、その後の正方向あるいは逆方向の水洗により微細な粒子として収集するものであり、サイクロンセパレーター等が利用できる。   Among these, the sludge collection device 3 collects mainly iron sludge components removed, dropped, and dissolved from each pipe in a cleaning process with a chemical cleaning solution as fine particles by subsequent forward or reverse water washing. A cyclone separator or the like can be used.

また、この洗浄装置には、化学洗浄液を加温するためのヒーター4が備えられていることが好ましく、このヒーター4としては、蒸気により化学洗浄液を直接加熱するミキシングヒータや、間接加熱するパネル式ヒーターが利用できる。   The cleaning device is preferably provided with a heater 4 for heating the chemical cleaning liquid. As the heater 4, a mixing heater for directly heating the chemical cleaning liquid with steam, or a panel type for indirect heating is used. A heater is available.

更に、配管中のスラッジの残存状態、特に二次過熱器9のUチューブなどの屈曲管部分のスラッジ堆積状況を常時把握するため、非破壊方式の測定装置8を取り付けておくことが好ましい。このような、非破壊方式の測定装置としては、超音波を利用する装置や、X線を利用する装置等が利用できる。   Furthermore, it is preferable to attach a non-destructive measuring device 8 in order to constantly grasp the remaining state of sludge in the piping, particularly the sludge accumulation state of the bent pipe portion such as the U tube of the secondary superheater 9. As such a non-destructive measurement apparatus, an apparatus using ultrasonic waves, an apparatus using X-rays, or the like can be used.

一方、本発明において使用する化学洗浄液は、その主剤としてキレート形成性化合物、有機酸および還元剤を含有するものである。このうち、キレート形成性化合物は、付着スケール溶解後のスラッジ粒子の微細化をはかり、後の水洗工程でのスラッジ搬出を容易にするものである。このようなキレート形成性化合物としては、エチレンジアミン四酢酸(EDTA)またはその塩が好ましく、特に、EDTAのナトリウム塩およびアンモニウム塩が好ましい。このキレート形成性化合物の添加量は、2.5〜12.5質量%程度が好ましい。   On the other hand, the chemical cleaning liquid used in the present invention contains a chelate-forming compound, an organic acid and a reducing agent as its main components. Among these, the chelate-forming compound is intended to make the sludge particles finer after the adhesion scale is dissolved, and facilitates the removal of sludge in the subsequent water washing step. As such a chelate-forming compound, ethylenediaminetetraacetic acid (EDTA) or a salt thereof is preferable, and a sodium salt and an ammonium salt of EDTA are particularly preferable. The amount of the chelate-forming compound added is preferably about 2.5 to 12.5% by mass.

また、有機酸としては、クエン酸、グルコン酸等が好ましく、この有機酸の添加により、化学洗浄剤のPHを、4〜10、特に、4〜6の範囲とすることが好ましい。この有機酸は、キレート形成性化合物1に対し、重量比で0.4〜0.7とすることが望ましい。   Moreover, as an organic acid, a citric acid, gluconic acid, etc. are preferable, and it is preferable to make PH of a chemical cleaning agent into the range of 4-10, especially 4-6 by addition of this organic acid. The organic acid is preferably used in a weight ratio of 0.4 to 0.7 with respect to the chelate-forming compound 1.

更に、化学洗浄剤中に含まれる還元剤としては、L−アスコルビン酸、エリソルビン酸等を使用することが好ましい。この還元剤は3価のFeを溶解し易い2価に還元するものである。この還元剤の配合量は、化学洗浄剤液量の0.2〜2w/v%とすることが好ましい。   Furthermore, it is preferable to use L-ascorbic acid, erythorbic acid or the like as the reducing agent contained in the chemical detergent. This reducing agent reduces trivalent Fe into a divalent which is easy to dissolve. The blending amount of the reducing agent is preferably 0.2 to 2 w / v% of the chemical detergent liquid amount.

また、化学洗浄剤中に腐食抑制剤を添加することにより、洗浄時の洗浄対象配管の腐食抑制をはかることが可能である。   In addition, by adding a corrosion inhibitor to the chemical cleaning agent, it is possible to suppress the corrosion of the piping to be cleaned during cleaning.

上記化学洗浄剤を使用した化学洗浄は、80〜95℃の範囲の洗浄温度で実施できる。また、洗浄時間は、原則として、スケール付着量、成分組成により異なり、洗浄液中のFe溶出濃度が飽和するまで実施するのが好ましい。更に、洗浄時の特に過熱器管Uチューブ部での線流速は、最低1.3m/secであることが好ましい。   Chemical cleaning using the chemical cleaning agent can be performed at a cleaning temperature in the range of 80 to 95 ° C. Further, in principle, the washing time varies depending on the scale adhesion amount and the component composition, and is preferably carried out until the Fe elution concentration in the washing liquid is saturated. Furthermore, it is preferable that the linear flow velocity at the superheater tube U tube portion at the time of cleaning is at least 1.3 m / sec.

一方、図2は、第二態様発明の洗浄系統を模式的に示したものである。図中、3〜8、13および14は、図1と同じものを示し、21は再熱器入り口弁取り合い座、22は再熱蒸気止め弁取り合い座、23は再熱器、24は再熱蒸気管をそれぞれ示す。   On the other hand, FIG. 2 schematically shows the cleaning system of the second aspect of the invention. In the figure, 3 to 8, 13 and 14 are the same as in FIG. 1, 21 is a reheater inlet valve mating seat, 22 is a reheat steam stop valve mating seat, 23 is a reheater, and 24 is reheat. Each steam pipe is shown.

本発明の第二態様発明を実施するには、まず、再熱器入口弁を洗浄液入口、再熱蒸気止め弁を洗浄液出口とすることが必要である。再熱器入り口弁と取り合う場合、再熱器入り口弁も、ゲート弁が一般的であるので、このバルブボンネットを開放し、弁対を抜き取った後、弁の洗浄液通水側は開口を有する板を、また、洗浄液を閉止する側には、閉止板をそれぞれタンバックルで接続し、その両サイドを突張る突張力で閉止側を閉止すればよい。更に、弁フランジ部に仮設フランジを取付け取り合うことにより化学洗浄液の循環が可能となる。   In order to implement the second aspect of the present invention, it is first necessary to use the reheater inlet valve as the cleaning liquid inlet and the reheat steam stop valve as the cleaning liquid outlet. When engaging with the reheater inlet valve, the reheater inlet valve is also generally a gate valve. Therefore, after opening the valve bonnet and extracting the valve pair, the cleaning liquid water-flowing side of the valve has a plate with an opening. In addition, it is only necessary to connect the closing plates to the side that closes the cleaning liquid with tumbles and close the closing side with the thrust that stretches both sides. Further, the chemical cleaning liquid can be circulated by attaching and mounting the temporary flange to the valve flange portion.

上記の化学洗浄液の循環は、基本的に第一態様発明で説明したのと同様にして行われる。すなわち、洗浄装置は、第一態様発明で使用するものと同一であり、当該装置を構成する各機器も、第一態様発明で説明したのと同じ機能を有するものである。   The circulation of the chemical cleaning solution is basically performed in the same manner as described in the first aspect of the invention. That is, the cleaning apparatus is the same as that used in the first aspect invention, and each device constituting the apparatus has the same function as described in the first aspect invention.

また、再熱器配管中の、屈曲管部分でのスラッジ堆積状況を常時把握するため、非破壊方式の測定装置8を取り付けておくことが好ましいことも同様である。   Similarly, it is preferable to attach a non-destructive measuring device 8 in order to always grasp the sludge accumulation state in the bent pipe portion in the reheater pipe.

更に、第二態様発明で使用する化学洗浄液も、第一態様発明で使用するものと同一であり、これを構成する各成分やその配合量、あるいはその作用も同一である。   Furthermore, the chemical cleaning liquid used in the second aspect invention is also the same as that used in the first aspect invention, and the components constituting the chemical cleaning liquid, the blending amount thereof, or the action thereof are also the same.

更にまた、化学洗浄の条件も、再熱器や再熱蒸気管中のスケールの発生度合いにもよるが、ほぼ第一態様発明と同一でよい。   Furthermore, chemical cleaning conditions may be substantially the same as in the first aspect of the invention, although depending on the degree of scale generation in the reheater or reheat steam pipe.

次に実施例、比較例および試験例を挙げ、本発明を更に詳しく説明するが、本発明はこれら実施例等に何ら制約されるものではない。   EXAMPLES Next, although an Example, a comparative example, and a test example are given and this invention is demonstrated in more detail, this invention is not restrict | limited at all by these Examples.

実 施 例
本発明化学洗浄液の調製:
EDTA−4NHを8w/v%、クエン酸を4w/v%、L−アスコルビン酸を0.2w/v%、腐食抑制剤を0.3w/v%となるようそれぞれ水に加え、化学洗浄剤(本発明品)を調製した。
EXAMPLE Preparation of the present chemical cleaning solution:
EDTA-4NH 3 the 8w / v%, citric acid 4w / v%, L- ascorbic acid 0.2 w / v%, was added a corrosion inhibitor, each water so as to be 0.3 w / v%, chemical cleaning An agent (product of the present invention) was prepared.

比 較 例
比較化学洗浄剤の調製:
ぎ酸を2w/v%、グリコール酸を4w/v%、L−アスコルビン酸を0.2w/v%、腐食抑制剤を0.3w/v%となるようそれぞれ水に加え、化学洗浄剤(比較品)を調製した。
Comparative Example Preparation of a comparative chemical cleaner:
Formic acid was added to water at 2 w / v%, glycolic acid at 4 w / v%, L-ascorbic acid at 0.2 w / v%, and corrosion inhibitor at 0.3 w / v%. Comparative product) was prepared.

試 験 例
スケール洗浄性試験:
実施例1で得た本発明品および比較例で得た比較品について、スケールが発生している同じ再熱蒸気管を試料としてスケール洗浄性を調べた。試験は、本発明品および比較品の温度を85〜95℃の間に保持し、これに試料を44時間浸漬し、試料の腐食量、生じたスラッジ量およびスラッジの形態を調べることにより行った。この結果を表1に示す。
Test example Scale cleanability test:
About the present invention product obtained in Example 1 and the comparative product obtained in the comparative example, the scale removability was examined using the same reheat steam pipe in which the scale was generated as a sample. The test was performed by maintaining the temperature of the product of the present invention and the comparative product between 85-95 ° C., immersing the sample in this for 44 hours, and examining the amount of corrosion of the sample, the amount of sludge generated and the form of sludge. . The results are shown in Table 1.

Figure 2006183902
Figure 2006183902

この結果から明らかなように、本発明品を用いた場合のスラッジの形態は、微粉状であり、スラッジの流し出しが容易と判断されたのに対し、比較品を用いた場合は、薄片上のスラッジが観察され、これらの流し出しは困難と考えられた。また、比較品を用いた場合は、本発明品を用いた場合に比べ、試料の腐食量やスラッジ量が多かった。   As is apparent from the results, the sludge form when using the product of the present invention is fine powder, and it was judged that the sludge flowed out easily. Sludge was observed, and it was considered difficult to drain them. Further, when the comparative product was used, the amount of corrosion and sludge of the sample was larger than when the product of the present invention was used.

本発明方法によれば、貫流型ボイラーの過熱器・再熱器・主蒸気管・高、低温再熱蒸気管の等の洗浄対象系統の配管を切断せずに一括し、同時に洗浄することが可能となり、洗浄効率を向上させることができる。   According to the method of the present invention, the pipes of the system to be cleaned such as the superheater / reheater / main steam pipe / high / low temperature reheat steam pipe of the once-through boiler can be cleaned at the same time without being cut. This makes it possible to improve the cleaning efficiency.

また、本発明で用いる化学洗浄剤は、キレート形成性化合物および有機酸の他、還元剤も含まれているものであるため、従来の付着スケール溶解機構と異なる方法でスラッジを除去できるものである。すなわち、溶解後のスラッジ粒子の微細化をはかり、後の水洗工程でのスラッジ搬出を容易にすることが可能である。   In addition, the chemical cleaning agent used in the present invention contains a reducing agent in addition to the chelate-forming compound and the organic acid, so that sludge can be removed by a method different from the conventional adhesion scale dissolution mechanism. . That is, it is possible to make the sludge particles after dissolution finer and facilitate the sludge unloading in the subsequent water washing step.

従って本発明は、貫流ボイラーの洗浄方法として有利に利用することができるものである。   Therefore, the present invention can be advantageously used as a method for cleaning a once-through boiler.

第一態様発明の過熱器・主蒸気管一括洗浄時の洗浄系統図Cleaning system diagram at the time of batch cleaning of the superheater and main steam pipe of the first aspect invention 第二態様発明の再熱器・再熱蒸気管一括洗浄時の洗浄系統図Cleaning system diagram for batch cleaning of reheater and reheat steam pipe of the second aspect invention

符号の説明Explanation of symbols

1 … … 過熱器入り口弁取り合い座
2 … … 主蒸気止め弁取り合い座
3 … … スラッジ捕集装置
4 … … ヒーター
5 … … 循環ポンプ
6 … … 薬品溶解タンク
7 … … 薬品溶解注入ポンプ
8 … … スラッジ計測装置
9 … … 二次過熱器
10 … … 主蒸気管
11 … … 一次過熱器
12 … … ケージ壁
13 … … 高圧タービン
14 … … 中圧タービン
21 … … 再熱器入り口弁取り合い座
22 … … 再熱蒸気止め弁取り合い座
23 … … 再熱器
24 … … 再熱蒸気管
以 上
1…… Superheater inlet valve mating seat 2…… Main steam stop valve mating seat 3…… Sludge collector 4…… Heater 5…… Circulation pump 6…… Chemical dissolution tank 7…… Chemical dissolution injection pump 8…… Sludge measuring device 9…… Secondary superheater 10…… Main steam pipe 11…… Primary superheater 12…… Cage wall 13…… High pressure turbine 14…… Medium pressure turbine 21…… Reheater inlet valve mating seat 22… ... Reheat steam stop valve joint seat 23 ... ... Reheater 24 ... ... Reheat steam pipe
more than

Claims (15)

過熱器入口弁を洗浄液入口、主蒸気止め弁を洗浄液出口として取り合い、この間をスラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置を用い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄することを特徴とする貫流型ボイラーの一括化学洗浄方法。   A superheater inlet valve is used as a cleaning liquid inlet and a main steam stop valve is used as a cleaning liquid outlet, and a chelating agent, an organic acid, and a reducing agent are used in the meantime using a cleaning device equipped with a sludge collection device, a chemical cleaning solution injection device and a circulation pump. A batch chemical cleaning method for a once-through boiler, characterized by circulating cleaning with a chemical cleaning agent containing 再熱器入口弁を洗浄液入口、再熱蒸気止め弁を洗浄液出口として取り合い、この間をスラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置を用い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄することを特徴とする貫流型ボイラーの一括化学洗浄方法。   The reheater inlet valve is used as a cleaning liquid inlet, and the reheat steam stop valve is used as a cleaning liquid outlet. Between these, a cleaning device equipped with a sludge collector, a chemical cleaning liquid injection device and a circulation pump is used. A batch chemical cleaning method for a once-through boiler, characterized by circulating cleaning with a chemical cleaning agent containing a reducing agent. 洗浄液の循環洗浄の後、更に水を洗浄液と正方向または逆方向に流して洗浄する請求項1または請求項2記載の貫流型ボイラーの一括化学洗浄方法。   3. The once-through chemical cleaning method for a once-through boiler according to claim 1 or 2, wherein, after circulating cleaning of the cleaning liquid, cleaning is further performed by flowing water in a forward or reverse direction with respect to the cleaning liquid. 洗浄装置が、更に加熱手段を有する請求項1ないし3のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   The method of batch chemical cleaning of a once-through boiler according to any one of claims 1 to 3, wherein the cleaning device further includes a heating means. 洗浄装置の化学洗浄液注入装置が、薬品溶解タンクおよび薬品注入ポンプを含むものである請求項1ないし4のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   5. The batch chemical cleaning method for a once-through boiler according to claim 1, wherein the chemical cleaning liquid injection device of the cleaning device includes a chemical dissolution tank and a chemical injection pump. 更に、二次過熱器または再熱器内の屈曲管に洗浄対象物より剥離、除去されたスラッジの堆積の有無を非破壊方式の計測装置により確認する請求項1ないし5のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   Furthermore, the non-destructive measuring device is used to confirm whether or not the sludge that has been peeled off and removed from the object to be cleaned on the bent pipe in the secondary superheater or reheater is accumulated. Batch chemical cleaning method for once-through boilers. 化学洗浄液が、更に腐蝕抑制剤を含有するものである請求項1ないし6のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   The method for batch chemical cleaning of a once-through boiler according to any one of claims 1 to 6, wherein the chemical cleaning liquid further contains a corrosion inhibitor. 化学洗浄液に含有されるキレート形成化合物が、EDTAのアンモニウム塩またはナトリウム塩である請求項1ないし7のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   The method for batch chemical cleaning of a once-through boiler according to any one of claims 1 to 7, wherein the chelate-forming compound contained in the chemical cleaning solution is an ammonium salt or sodium salt of EDTA. 化学洗浄液に含有される有機酸が、クエン酸またはグルコン酸である請求項1ないし8のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   The method for batch chemical cleaning of a once-through boiler according to any one of claims 1 to 8, wherein the organic acid contained in the chemical cleaning liquid is citric acid or gluconic acid. 化学洗浄液に含有される還元剤が、L−アスコルビン酸および/またはL−ソルビン酸である請求項1ないし9のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   The method for batch chemical cleaning of a once-through boiler according to any one of claims 1 to 9, wherein the reducing agent contained in the chemical cleaning liquid is L-ascorbic acid and / or L-sorbic acid. 化学洗浄液のpHが、4ないし10である請求項1ないし10のいずれかの項記載の貫流型ボイラーの一括化学洗浄方法。   The method for batch chemical cleaning of a once-through boiler according to any one of claims 1 to 10, wherein the pH of the chemical cleaning solution is 4 to 10. スラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置で、過熱器入口弁を洗浄液入口、主蒸気止め弁を洗浄液出口として取り合い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄可能としてなる貫流型ボイラーの一括化学システム。   A cleaning device equipped with a sludge collector, a chemical cleaning liquid injection device, and a circulation pump, with a superheater inlet valve as a cleaning liquid inlet and a main steam stop valve as a cleaning liquid outlet, containing a chelating compound, an organic acid and a reducing agent A batch chemical system for once-through boilers that can be circulated with chemical cleaners. 更に、水を洗浄液と正方向または逆方向に流すことを可能とした請求項12の貫流型ボイラーの一括化学洗浄システム。   Furthermore, the collective chemical cleaning system for a once-through boiler according to claim 12, wherein water can flow in a forward direction or a reverse direction with respect to the cleaning liquid. スラッジ捕集装置、化学洗浄液注入装置および循環ポンプを備えた洗浄装置で、再熱器入口弁を洗浄液入口、再熱蒸気止め弁を洗浄液出口として取り合い、キレート形成性化合物、有機酸および還元剤を含有する化学洗浄剤で循環洗浄可能としてなる貫流型ボイラーの一括化学洗浄システム。   A cleaning device equipped with a sludge collector, a chemical cleaning fluid injection device, and a circulation pump. The reheater inlet valve is used as a cleaning fluid inlet, and the reheat steam stop valve is used as a cleaning solution outlet, and a chelating compound, organic acid, and reducing agent are mixed. A batch chemical cleaning system for once-through boilers that can be circulated and cleaned with chemical cleaning agents. 更に、水を洗浄液と正方向または逆方向に流すことを可能とした請求項14の貫流型ボイラーの一括化学洗浄システム。

Furthermore, the collective chemical cleaning system for a once-through boiler according to claim 14, wherein water can flow in a forward direction or a reverse direction with respect to the cleaning liquid.

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JP2010159932A (en) * 2009-01-09 2010-07-22 Sharp Corp Heating cooker and method of cleaning steam generator
JP2011212591A (en) * 2010-03-31 2011-10-27 Kurita Water Ind Ltd Descaling method and descaling agent
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JP2012184742A (en) * 2011-03-08 2012-09-27 Chugoku Electric Power Co Inc:The Exhaust path formation method for steam and drain in drying operation of reheater
JP2015102278A (en) * 2013-11-25 2015-06-04 三菱日立パワーシステムズ株式会社 Chemical washing method for boiler piping
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WO2020246065A1 (en) * 2019-06-07 2020-12-10 三菱重工業株式会社 Method and device for detecting sludge accumulation spot and program for detecting sludge accumulation spot

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010159932A (en) * 2009-01-09 2010-07-22 Sharp Corp Heating cooker and method of cleaning steam generator
JP2011212591A (en) * 2010-03-31 2011-10-27 Kurita Water Ind Ltd Descaling method and descaling agent
KR101139886B1 (en) 2010-07-28 2012-05-02 한국전력공사 Clening system and cleaning method of steam touched boilers
JP2012184742A (en) * 2011-03-08 2012-09-27 Chugoku Electric Power Co Inc:The Exhaust path formation method for steam and drain in drying operation of reheater
JP2015102278A (en) * 2013-11-25 2015-06-04 三菱日立パワーシステムズ株式会社 Chemical washing method for boiler piping
JP2018021684A (en) * 2016-08-01 2018-02-08 栗田エンジニアリング株式会社 Chemical cleaning method of boiler
WO2020246065A1 (en) * 2019-06-07 2020-12-10 三菱重工業株式会社 Method and device for detecting sludge accumulation spot and program for detecting sludge accumulation spot
JP2020201076A (en) * 2019-06-07 2020-12-17 三菱重工業株式会社 Method and system of detecting a sludge deposit, and sludge deposit detection program
JP7349269B2 (en) 2019-06-07 2023-09-22 三菱重工業株式会社 Method and device for detecting sludge accumulation locations, and sludge accumulation location detection program

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