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JP6931215B2 - Detergent for dissolving and removing iron rust and oxidation scale - Google Patents
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JP6931215B2 - Detergent for dissolving and removing iron rust and oxidation scale - Google Patents

Detergent for dissolving and removing iron rust and oxidation scale Download PDF

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JP6931215B2
JP6931215B2 JP2017034113A JP2017034113A JP6931215B2 JP 6931215 B2 JP6931215 B2 JP 6931215B2 JP 2017034113 A JP2017034113 A JP 2017034113A JP 2017034113 A JP2017034113 A JP 2017034113A JP 6931215 B2 JP6931215 B2 JP 6931215B2
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正登 山本
正登 山本
佐尾 俊生
俊生 佐尾
紀久士 常吉
紀久士 常吉
松下 亮
亮 松下
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株式会社ケミカル山本
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Description

本発明は、火力発電プラント等の主蒸気管系統及び再熱蒸気管系統等の内部に成長した水蒸気酸化スケールを化学洗浄液にて溶解除去する方法に関し、特に常温近傍で溶解除去する方法に関する。 The present invention relates to a method of dissolving and removing steam oxidation scale grown inside a main steam pipe system of a thermal power plant or the like and a reheated steam pipe system or the like with a chemical cleaning liquid, and particularly to a method of dissolving and removing at around room temperature.

火力発電プラントの水側及び蒸気側の系統図を図−1に示す。8.タービンから戻った蒸気は、1.復水器で冷却され凝縮して給水となる。給水は、1.復水器から図示されていない復水ポンプ及び復水ブースタポンプを通して2.低圧給水加熱器へ運ばれ、加熱される。その後、3.脱気器で酸素が除去される。次に図示されていない高圧給水ポンプを通して4.高圧給水加熱器、5.節炭器で加熱昇温されて6.ボイラへ運ばれ、加熱されて蒸気が発生する。蒸気は、7.過熱器で更に加熱されて14.主蒸気管で連結された10.MSV(主蒸気止め弁)及び11.CV(加減弁)を通り、8.タービン(高圧)へ供給される。8.タービン(高圧)で仕事をした蒸気は、15.低温再熱蒸気管で連結された9.再熱器へ送られ再度加熱された後、16.高温再熱蒸気管で連結された12.RSV(再熱蒸気止め弁)及び13.ICV(インターセプト弁)を通り、8.タービン(中圧及び低圧)へ送られ、8.タービン(中圧及び低圧)で仕事をした後、1.復水器へ戻り、冷却・凝縮されて給水となり循環を繰り返す。 Figure 1 shows the system diagram of the water side and steam side of the thermal power plant. 8. The steam returned from the turbine is 1. It is cooled by a condenser and condensed to supply water. Water supply is 1. 2. From the condenser through a condenser pump and a condenser pump (not shown). It is transported to a low-pressure feed water heater and heated. After that, 3. Oxygen is removed by the deaerator. Next, through a high-pressure water pump (not shown) 4. High-pressure feed water heater, 5. 6. The temperature is raised by heating with an economizer. It is carried to a boiler and heated to generate steam. Steam is 7. Further heated by a superheater 14. 10. Connected by the main steam pipe. MSV (main steam stop valve) and 11. Pass through CV (control valve), 8. It is supplied to the turbine (high pressure). 8. The steam that worked in the turbine (high pressure) is 15. 9. Connected by a low temperature reheat steam pipe. After being sent to the reheater and reheated, 16. 12. Connected by high temperature reheat steam pipe. RSV (reheat steam stop valve) and 13. Pass through the ICV (intercept valve), 8. It is sent to the turbine (medium pressure and low pressure), 8. After working with turbines (medium and low pressure), 1. Return to the condenser, cool and condense to supply water, and repeat circulation.

このような火力発電プラントの過熱器に内蔵された過熱器管、再熱器に内蔵された再熱器管、主蒸気管、低温再熱蒸気管、高温再熱蒸気管等の伝熱管、蒸気配管及び各種弁類は、耐熱性のあるクロム含有鋼材料が使用され、その蒸気側の面には運転時間が長くなるにつれ、水蒸気酸化スケールが生成・成長する。スケールの厚さが厚くなると部分的な剥離を生じ、後流側へ飛散してタービン等の損傷原因となるので、主蒸気管、低温再熱蒸気管、高温再熱蒸気管に生成した水蒸気酸化スケールについては、化学洗浄により溶解除去されている。 Superheater tubes built into superheaters of such thermal power plants, reheater tubes built into reheaters, main steam tubes, low temperature reheat steam tubes, heat transfer tubes such as high temperature reheat steam tubes, steam Heat-resistant chromium-containing steel material is used for piping and various valves, and steam oxidation scale is generated and grows on the surface on the steam side as the operation time becomes longer. If the scale becomes thicker, partial peeling will occur and it will scatter to the wake side and cause damage to the turbine, etc., so steam oxidation generated in the main steam pipe, low temperature reheat steam pipe, and high temperature reheat steam pipe. The scale is dissolved and removed by chemical cleaning.

クロムを含有する鋼管の内面に生成する水蒸気酸化スケールは、内層と外層からなる二層構造となっている。外層(蒸気側)スケールは酸化鉄(マグネタイト)が主体であり、内層スケール(母材側)はクロムリッチの酸化スケールである。 The water vapor oxidation scale generated on the inner surface of the chromium-containing steel pipe has a two-layer structure consisting of an inner layer and an outer layer. The outer layer (steam side) scale is mainly iron oxide (magnetite), and the inner layer scale (base material side) is a chromium-rich oxide scale.

ボイラの蒸発管内面に生成するスケールは、ボイラへ持ち込まれた不純物がスケール化したものであり、通常の塩酸洗浄或いはクエン酸洗浄により比較的容易に除去することが可能であるが、前記水蒸気酸化スケールは、管材自体が酸化(自己酸化)して生成した強固な難溶性のスケールであり、通常の酸洗浄法で溶解除去することは困難である。 The scale generated on the inner surface of the evaporation pipe of the boiler is a scale of impurities brought into the boiler, and can be relatively easily removed by ordinary hydrochloric acid washing or citric acid washing. The scale is a strong sparingly soluble scale produced by oxidizing (self-oxidizing) the pipe material itself, and it is difficult to dissolve and remove it by a normal acid washing method.

水蒸気酸化スケールが生成した蒸気配管を洗浄する際は、洗浄対象部と非洗浄部を切断して切り離し、洗浄対象部のみを仮設配管で繋ぎ込み洗浄液を循環して水蒸気酸化スケールを溶解除去している。 When cleaning the steam pipe generated by the steam oxidation scale, the cleaning target part and the non-cleaning part are cut and separated, and only the cleaning target part is connected by a temporary pipe and the cleaning liquid is circulated to dissolve and remove the steam oxidation scale. There is.

これらの洗浄に用いられる洗浄剤としては、EDTAのアンモニウム塩等のキレート洗浄剤或いはクエン酸等の洗浄液を用いて高温(100℃前後)で、しかも長時間(30〜90時間)の循環洗浄が行われている。 As the cleaning agent used for these cleanings, a chelate cleaning agent such as an ammonium salt of EDTA or a cleaning liquid such as citric acid is used for circulating cleaning at a high temperature (around 100 ° C.) and for a long time (30 to 90 hours). It is done.

水蒸気酸化スケールが生成した蒸気止め弁等の弁類については、循環洗浄が難しいため、取り外した後、グラインダー等を用いて物理的な除去作業が行われている。
また、過熱器管及び再熱器管内面に生成した水蒸気酸化スケールについては、循環洗浄する際、構造的に管内流速の調整(平均的に流すこと)が難しく、剥離スケールの排出が困難であるため、洗浄方法を適用できず、定期的に新管切り替え工事(切断・溶接)が行われている。
Since it is difficult to circulate and clean valves such as steam stop valves generated by steam oxidation scale, after removing them, physical removal work is performed using a grinder or the like.
Further, regarding the steam oxidation scale generated on the inner surface of the superheater tube and the reheater tube, it is structurally difficult to adjust the flow velocity in the tube (flow on average) during circulation cleaning, and it is difficult to discharge the peeling scale. Therefore, the cleaning method cannot be applied, and new pipe switching work (cutting / welding) is being carried out on a regular basis.

従来の洗浄方法は、水蒸気酸化スケールに対する溶解力が乏しいため、100℃前後の高温で、しかも長時間(20〜100時間)の洗浄を行う必要があり、安全面及び施工面で問題であった。 Since the conventional cleaning method has poor dissolving power for steam oxidation scale, it is necessary to perform cleaning at a high temperature of about 100 ° C. for a long time (20 to 100 hours), which is a problem in terms of safety and construction. ..

高温での洗浄を行うため、循環系統を構成して昇温する必要があり、洗浄対象(主蒸気管、高温再熱蒸気管、低温再熱蒸気管)の大口径配管の切断加工、仮設配管施工及び洗浄後の復旧工事等の工事費用が過大となっていた。 In order to perform cleaning at high temperature, it is necessary to configure a circulation system to raise the temperature. Construction costs such as restoration work after construction and cleaning were excessive.

また、洗浄対象の大口径の蒸気管を洗浄する際は、従来の洗浄方法では仮設配管を含む洗浄系統の保有水量が多く、洗浄液の購入費用及び廃液処理費用が過大となっていた。 Further, when cleaning a large-diameter steam pipe to be cleaned, the conventional cleaning method has a large amount of water held in the cleaning system including the temporary pipe, and the purchase cost of the cleaning liquid and the waste liquid treatment cost are excessive.

水蒸気酸化スケールが生成した蒸気配管については、上記方法で循環洗浄を行うことが可能であるが、蒸気系統に設置されている水蒸気酸化スケールの生成したバルブ類(主蒸気止め弁、蒸気加減弁及び再熱蒸気止め弁等)の単体ものについては、循環系統で洗浄することは難しいため、取り外して物理的な方法でスケールの除去処理が行われている。しかしながら作業中に母材を傷つける等の問題があり、施工性が悪くなり処理作業に長時間を要していた。 The steam pipes generated by the steam oxidation scale can be circulated and cleaned by the above method, but the valves (main steam stop valve, steam control valve and steam control valve) generated by the steam oxidation scale installed in the steam system are installed. Since it is difficult to clean a single unit (reheat steam stop valve, etc.) in the circulation system, it is removed and the scale is removed by a physical method. However, there are problems such as damage to the base material during the work, and the workability deteriorates, and the processing work takes a long time.

そこで、本発明は、クロム含有鋼材料の表面に形成された酸化クロム含有量の多い下層(母材側)と、酸化鉄を主体とする上層(蒸気側)を含んだ二層構造の水蒸気酸化スケールを常温で溶解除去できる洗浄剤及び洗浄方法を提供することを目的とする。 Therefore, in the present invention, steam oxidation of a two-layer structure including a lower layer (base material side) having a high chromium oxide content formed on the surface of a chromium-containing steel material and an upper layer (steam side) mainly composed of iron oxide. An object of the present invention is to provide a cleaning agent and a cleaning method capable of dissolving and removing scale at room temperature.

本発明は、ヨウ素化合物を含むことを特徴とする鉄さび及び酸化スケールを溶解除去する洗浄剤と該洗浄剤を用いた洗浄方法を提供するものである。 The present invention provides a cleaning agent for dissolving and removing iron rust and oxidation scale, which is characterized by containing an iodine compound, and a cleaning method using the cleaning agent.

本発明の洗浄剤は、無機酸及び有機酸の少なくとも1種以上からなる酸成分と、ヨウ素化合物及びフッ素化合物を混合して成ることを特徴とする。 Cleaning agent of the present invention an acid component consisting of at least one or more inorganic acids and organic acids, that formed by mixing the iodine compound and a fluorine compound, wherein.

本発明の洗浄剤において、無機酸として塩酸、硫酸、硝酸、リン酸、ホウ酸、フッ化水素酸、スルファミン酸より選択された少なくとも1種を含むことを特徴とする。 The cleaning agent of the present invention is characterized by containing at least one selected from hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, boric acid, hydrofluoric acid, and sulfamic acid as the inorganic acid.

本発明の洗浄剤において、有機酸としてクエン酸、シュウ酸、酢酸、ギ酸、グリコール酸、酒石酸より選択された少なくとも1種を含むことを特徴とする。 The cleaning agent of the present invention is characterized by containing at least one selected from citric acid, oxalic acid, acetic acid, formic acid, glycolic acid and tartaric acid as organic acids.

本発明の洗浄剤において、ヨウ素化合物としてヨウ素、ヨウ化水素酸、ヨウ化カリウム、ヨウ化ナトリウム、ヨウ化リチウム、ヨウ化銅、ヨウ化アンモニウム、ヨウ化亜鉛、ヨウ化マグネシウム、ヨウ化セシウム、ヨウ化ストロンチウム、ヨウ化バリウム、ヨウ素酸水溶液、ヨウ素酸カリウム、ヨウ素酸ナトリウム、ヨウ素酸カルシウムより選択された少なくとも1種を含むことを特徴とする。 In the cleaning agent of the present invention, the iodine compounds include iodine, hydroiodic acid, potassium iodide, sodium iodide, lithium iodide, copper iodide, ammonium iodide, zinc iodide, magnesium iodide, cesium iodide, and iodine. It is characterized by containing at least one selected from strontium iodide, barium iodide, aqueous iodate, potassium iodate, sodium iodate, and calcium iodate.

本発明の洗浄剤において、フッ素化合物としてフッ化アンモニウム、酸性フッ化アンモニウム、フッ化ナトリウム、酸性フッ化ナトリウム、フッ化カリウム、酸性フッ化カリウムより選択された少なくとも1種を含むことを特徴とする。 The cleaning agent of the present invention is characterized by containing at least one selected from ammonium fluoride, acidic ammonium fluoride, sodium fluoride, sodium fluoride, potassium fluoride, and acidic potassium fluoride as the fluorine compound. ..

本発明の洗浄方法において、請求項1記載の洗浄剤を用いて、常温で浸漬或いは循環洗浄を行うことを特徴とする。 The cleaning method of the present invention is characterized in that the cleaning agent according to claim 1 is used to perform immersion or circulation cleaning at room temperature.

本発明の洗浄方法において、請求項1記載の洗浄剤を用いて洗浄を行う際、洗浄剤を加熱昇温することで洗浄速度をアップすることが出来る。 In the cleaning method of the present invention, when cleaning is performed using the cleaning agent according to claim 1, the cleaning speed can be increased by heating and raising the temperature of the cleaning agent.

本発明の洗浄方法において、毛細管現象を利用して請求項1記載の洗浄剤を被洗浄部へ供給することを特徴とする。 The cleaning method of the present invention is characterized in that the cleaning agent according to claim 1 is supplied to a portion to be cleaned by utilizing the capillary phenomenon.

本発明の洗浄方法において、塗布或いは保水性を有するスポンジ状の材料に請求項1記載の洗浄剤を含浸させて被洗浄部へ供給し、洗浄を行うことが出来る。 In the cleaning method of the present invention, a sponge-like material having coating or water retention can be impregnated with the cleaning agent according to claim 1 and supplied to a part to be cleaned for cleaning.

本発明の洗浄方法において、吸水性樹脂に請求項1記載の洗浄剤を含浸させて被洗浄部へ供給し、洗浄を行うことが出来る。 In the cleaning method of the present invention, the water-absorbent resin can be impregnated with the cleaning agent according to claim 1 and supplied to the part to be cleaned for cleaning.

本発明のクロム含有鋼材料のスケール除去方法では、クロム含有鋼材料表面におけるクロムリッチな下層と酸化鉄を主体とした上層とを有した二層構造のスケールを除去する際、常温でしかも比較的短時間での除去が可能であり、安全面および施工面で大幅に改善される。 In the scale removing method of the chromium-containing steel material of the present invention, when removing the scale of a two-layer structure having a chromium-rich lower layer and an iron oxide-based upper layer on the surface of the chromium-containing steel material, the scale is relatively at room temperature. It can be removed in a short time, which greatly improves safety and construction.

二層構造の水蒸気酸化スケールを常温で溶解除去できるため、循環系統構成にかかる大口径配管の切断加工、仮設配管施工及び洗浄後の復旧工事等の工事費用が大幅に削減できる。 Since the steam oxidation scale having a two-layer structure can be dissolved and removed at room temperature, construction costs such as cutting of large-diameter pipes related to the circulation system configuration, temporary pipe construction, and restoration work after cleaning can be significantly reduced.

循環系統構成にかかる大口径配管の切断加工、仮設配管施工及び洗浄後の復旧工事等の洗浄前後における工事が省略できるため、工事期間が大幅に短縮できる。 Since the work before and after cleaning, such as cutting of large-diameter pipes related to the circulation system configuration, temporary pipe construction, and restoration work after cleaning, can be omitted, the construction period can be significantly shortened.

水蒸気酸化スケールが生成したバルブ(弁)類等の単体については、常温での浸漬洗浄(部分洗浄)が可能であり、準備作業が低減されるため、比較的短時間で二層構造の水蒸気酸化スケールを溶解除去できる。また、物理的な処理方法を併用することも可能であり、施工性が向上する。 For simple substances such as valves generated by steam oxidation scale, immersion cleaning (partial cleaning) at room temperature is possible and preparatory work is reduced, so steam oxidation of a two-layer structure takes a relatively short time. The scale can be dissolved and removed. It is also possible to use a physical treatment method together, which improves workability.

水蒸気酸化スケールが生成した部位は、既にスケールが剥離した部位と残留した部位が混在しているが、本発明による方法では、毛細管現象等を利用して水蒸気酸化スケールの残留部位(付着部位)のみを対象に部分的な洗浄が可能である。
また、部分的な洗浄が可能となるため、他の作業との同時並行作業が可能となり、工程管理面で有利である。
The part where the water vapor oxidation scale is generated is a mixture of the part where the scale has already peeled off and the part where the scale remains. Partial cleaning is possible for the target.
In addition, since partial cleaning is possible, simultaneous parallel work with other work is possible, which is advantageous in terms of process control.

部分洗浄が可能であるため、循環洗浄に比較して洗浄液量が極端に少なくなるため、洗浄液にかかる費用が大幅に低減できる。 Since partial cleaning is possible, the amount of cleaning liquid is extremely small as compared with circulating cleaning, so that the cost of cleaning liquid can be significantly reduced.

化学洗浄工事においては、洗浄後の廃液処理費用の占める割合(洗浄工事の約50%)が大きいが、本発明の洗浄方法によれば、循環洗浄に比較して洗浄廃液量が極端に少なくなるため、廃液処理費用が大幅に低減できる。 In chemical cleaning work, the ratio of waste liquid treatment cost after cleaning is large (about 50% of cleaning work), but according to the cleaning method of the present invention, the amount of cleaning waste liquid is extremely small as compared with circulating cleaning. Therefore, the waste liquid treatment cost can be significantly reduced.

この図は本発明を説明するための発電プラントにおける水及び蒸気側の循環系統図である。This figure is a circulation system diagram on the water and steam side in a power plant for explaining the present invention. この図は本発明の実施例5に係る4個の試験片の黒皮の除去に伴う重量減と27%りん酸水溶液に対する12.7%ヨウ素溶液の配合割合との関係を示したグラフである。This figure is a graph showing the relationship between the weight loss associated with the removal of the black skin of the four test pieces according to Example 5 of the present invention and the mixing ratio of the 12.7% iodine solution to the 27% phosphoric acid aqueous solution. ..

本発明の実施の形態の一例として、水蒸気酸化スケールの浸漬洗浄方法、毛細管現象を利用して洗浄剤を被洗浄部へ供給する洗浄方法及び保水性を有する材料に洗浄剤を含浸させて洗浄剤を被洗浄部へ供給する洗浄方法とその効果等を実施例により説明する。 As an example of the embodiment of the present invention, a cleaning method of dipping and cleaning the steam oxidation scale, a cleaning method of supplying the cleaning agent to the part to be cleaned by utilizing the capillary phenomenon, and a cleaning agent by impregnating a water-retaining material with the cleaning agent. The cleaning method and its effect and the like will be described with reference to Examples.

火力発電所で使用されていた蒸気止め弁に付着した水蒸気酸化スケールをハンマーで物理的に剥し、剥離した二層スケールを溶解試験用のサンプルとした。
この二層スケールサンプルの厚さは、0.47〜0.55mmであった。下層スケールの厚さは、0.22〜0.23mmであり、上層スケールの厚さは、0.25〜0.32mmであった。
200mlのガラスビーカーを6個準備し、これに下記に示す6種類の各試験液を50mlずつ計り取り、常温でビーカースケールでの溶解試験に供した。薬品の濃度は、重量%である。
CASE.1 5%塩酸
CASE.2 5%クエン酸
CASE.3 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液
CASE.4 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を9:1の割合で混合した試験液
CASE.5 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を8:2の割合で混合した試験液
CASE.6 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を7:3の割合で混合した試験液
それぞれの試験液中に水蒸気酸化スケールのサンプル(0.035〜0.055g)を投入し、常温での浸漬溶解試験を開始した。
試験開始から16時間経過後、サンプルの外観状況を確認した。結果の概要は以下の通りである。
CASE.1 スケール溶解状況:×(水蒸気酸化スケールの外観変化は全く無し)
CASE.2 スケール溶解状況:×(水蒸気酸化スケールの外観変化は全く無し)
CASE.3 スケール溶解状況:×(水蒸気酸化スケールの外観変化は全く無し)
CASE.4 スケール溶解状況:△(水蒸気酸化スケールが微細化)
CASE.5 スケール溶解状況:△(水蒸気酸化スケールが更に微細化)
CASE.6 スケール溶解状況:○(水蒸気酸化スケールが殆ど溶解した。)
備考)スケール溶解状況の評価
×:溶解能力無し
△:溶解能力が認められる
○:良好な溶解能力が認められる
The steam oxidation scale attached to the steam stop valve used in the thermal power plant was physically peeled off with a hammer, and the peeled two-layer scale was used as a sample for the dissolution test.
The thickness of this two-layer scale sample was 0.47 to 0.55 mm. The thickness of the lower scale was 0.22 to 0.23 mm, and the thickness of the upper scale was 0.25 to 0.32 mm.
Six 200 ml glass beakers were prepared, and 50 ml of each of the six types of test solutions shown below was weighed and subjected to a dissolution test on a beaker scale at room temperature. The concentration of the chemical is% by weight.
CASE. 15% Hydrochloric Acid CASE. 25% citric acid CASE. 3 A mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid CASE. 4 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 9: mixed test liquid CASE 1 ratio. 5 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 8: 2 mixed test liquid CASE in proportion. 6 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 7: the steam oxidation scale samples (0.035~0.055g) was placed in test solution each test solution were mixed in a ratio of 3, the immersion dissolution test at room temperature It started.
After 16 hours from the start of the test, the appearance of the sample was confirmed. The summary of the results is as follows.
CASE. 1 Scale dissolution status: × (No change in appearance of steam oxidation scale)
CASE. 2 Scale dissolution status: × (No change in appearance of steam oxidation scale)
CASE. 3 Scale dissolution status: × (No change in appearance of steam oxidation scale)
CASE. 4 Scale dissolution status: △ (water vapor oxidation scale becomes finer)
CASE. 5 Scale dissolution status: △ (water vapor oxidation scale becomes finer)
CASE. 6 Scale dissolution status: ○ (Steam oxidation scale was almost dissolved.)
Remarks) Evaluation of scale dissolution status ×: No dissolution ability △: Dissolution ability is recognized ○: Good dissolution ability is recognized

火力発電所で使用されていた蒸気止め弁の水蒸気酸化スケールが付着(二層スケール)した弁体の3か所を選定し、溶解試験用のテスト面(30mm×30mm)とした。
弁体の洗浄テスト面のスケール厚さは不明であるが、洗浄テスト面近傍から採取した二層スケールサンプルの厚さは、実施例1で用いた二層スケールと同程度であった。
200mlのガラスビーカーを3個準備し、これに下記に示す3種類の試験液を50mlずつ計り取り、常温でビーカースケールでの溶解試験に供した。
CASE.1 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を9:1の割合で混合した試験液
CASE.2 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を8:2の割合で混合した試験液
CASE.3 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を7:3の割合で混合した試験液
蒸気止め弁の3か所に設けた溶解試験用テスト面近傍に試験液の入ったビーカーを設置し、これに適量ガーゼを入れて試験液を含浸させ、ガーゼの一端で黒皮の表面を覆い、常温での溶解試験を開始した。
22時間後、溶解試験用テスト面のガーゼを取り外し、スケールの溶解状況を確認した。結果の概要は以下の通りである。
CASE.1 スケールの溶解状況:△(上層スケールと下層スケールの一部が溶解)
CASE.2 スケールの溶解状況:△(上層スケールと下層スケールの一部が溶解し
、材部の一部が露出していた)
CASE.3 スケールの溶解状況:○(上層スケールと下層スケールが溶解し、テス
ト面の母材部が殆ど露出していた)
備考)スケール溶解状況の評価
×:溶解能力無し
△:溶解能力が認められる
○:良好な溶解能力が認められる
Three locations of the valve body to which the steam oxidation scale of the steam stop valve used in the thermal power plant was attached (two-layer scale) were selected and used as the test surface (30 mm × 30 mm) for the dissolution test.
Although the scale thickness of the cleaning test surface of the valve body is unknown, the thickness of the two-layer scale sample collected from the vicinity of the cleaning test surface was about the same as the two-layer scale used in Example 1.
Three 200 ml glass beakers were prepared, and 50 ml of each of the three types of test solutions shown below was weighed and subjected to a dissolution test on a beaker scale at room temperature.
CASE. 1 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 9: mixed test liquid CASE 1 ratio. 2 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 8: 2 mixed test liquid CASE in proportion. 3 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 7: The beaker was placed with the test surface near a dissolution test provided in three places of test fluid steam stop valve in a mixing ratio of 3 test liquid, to which a suitable amount gauze Was impregnated with the test solution, the surface of the black skin was covered with one end of gauze, and the dissolution test at room temperature was started.
After 22 hours, the gauze on the test surface for the dissolution test was removed, and the dissolution status of the scale was confirmed. The summary of the results is as follows.
CASE. Dissolution status of 1 scale: △ (part of upper scale and lower scale is dissolved)
CASE. 2 Scale dissolution status: △ (Part of the upper scale and lower scale are dissolved
, A part of the material part was exposed)
CASE. 3 Scale dissolution status: ○ (Upper scale and lower scale are dissolved, test
Most of the base material on the surface was exposed)
Remarks) Evaluation of scale dissolution status ×: No dissolution ability △: Dissolution ability is recognized ○: Good dissolution ability is recognized

黒皮付き(黒皮の厚さ:20μm)の炭素鋼板を溶解試験用のサンプルとした。黒皮が付着した面を溶解試験の対象とした。
200mlのガラスビーカーを3個準備し、これに下記に示す3種類の試験液を入れ、黒皮の溶解試験に供した。
CASE.1 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を9:1の割合で混合した試験液
CASE.2 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を8:2の割合で混合した試験液
CASE.3 酸性フッ化アンモニウム7%、硝酸9%及び硫酸18%の混合液と
12.7%ヨウ素溶液を7:3の割合で混合した試験液
3枚の黒皮付き炭素鋼板を準備し、3種類の試験液をそれぞれガーゼに含浸させ、ガーゼの一端で黒皮の表面を覆い、常温での溶解試験を開始した。
試験開始から30分経過後、黒皮の表面のガーゼを取り外し、黒皮の溶解状況を確認した。結果の概要は以下の通りである。
CASE.1 スケールの溶解状況:○(ガーゼで覆ったテスト面の黒皮は殆ど溶解)
CASE.2 スケールの溶解状況:○(ガーゼで覆ったテスト面の黒皮は殆ど溶解)
CASE.3 スケールの溶解状況:○(ガーゼで覆ったテスト面の黒皮は殆ど溶解)
備考)スケール溶解状況の評価
×:溶解能力無し
△:溶解能力が認められる
○:良好な溶解能力が認められる
A carbon steel sheet with a black skin (thickness of the black skin: 20 μm) was used as a sample for the dissolution test. The surface to which the black skin was attached was the subject of the dissolution test.
Three 200 ml glass beakers were prepared, and the following three types of test solutions were added thereto and subjected to a black skin dissolution test.
CASE. 1 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 9: mixed test liquid CASE 1 ratio. 2 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 8: 2 mixed test liquid CASE in proportion. 3 With a mixed solution of 7% acidic ammonium fluoride, 9% nitric acid and 18% sulfuric acid
The 12.7% iodine solution 7: the three test solution in a mixing ratio of 3 to prepare a black unpeeled carbon steel, impregnated three test solution in gauze each of mill scale at one end of the gauze The surface was covered and a dissolution test at room temperature was started.
After 30 minutes from the start of the test, the gauze on the surface of the black skin was removed, and the dissolution status of the black skin was confirmed. The summary of the results is as follows.
CASE. Dissolution status of 1 scale: ○ (The black skin on the test surface covered with gauze is almost dissolved)
CASE. 2 scale dissolution status: ○ (The black skin on the test surface covered with gauze is almost dissolved)
CASE. Dissolution status of 3 scales: ○ (The black skin on the test surface covered with gauze is almost dissolved)
Remarks) Evaluation of scale dissolution status ×: No dissolution ability △: Dissolution ability is recognized ○: Good dissolution ability is recognized

黒皮付き(黒皮の厚さ:20μm)の炭素鋼板を溶解試験用のサンプルとした。黒皮が付着した面を溶解試験の対象とした。
200mlのガラスビーカーを3個準備し、これに下記に示す3種類の試験液を入れ、黒皮の溶解試験に供した。
CASE.1 酸性フッ化アンモニウム7%、クエン酸9%及び硫酸18%の混合
液と12.7%ヨウ素溶液を7:3の割合で混合した試験液
CASE.2 酸性フッ化アンモニウム7%、グリコール酸9%及び硫酸18%の
混合液と12.7%ヨウ素溶液を7:3の割合で混合した試験液
CASE.3 酸性フッ化アンモニウム7%、クエン酸4.5%、グリコール酸4
.5%及び硫酸18%の混合液と12.7%ヨウ素溶液を7:3の
割合で混合した試験液
3枚の黒皮付き炭素鋼板を準備し、3種類の試験液をそれぞれガーゼに含浸させ、ガーゼの一端で黒皮の表面を覆い、常温での溶解試験を開始した。
試験開始から60分経過後、黒皮の表面のガーゼを取り外し、黒皮の溶解状況を確認した。結果の概要は以下の通りである。
CASE.1 スケールの溶解状況:〇(ガーゼで覆ったテスト面の黒皮は殆ど溶解)
CASE.2 スケールの溶解状況:〇(ガーゼで覆ったテスト面の黒皮は殆ど溶解)
CASE.3 スケールの溶解状況:〇(ガーゼで覆ったテスト面の黒皮は殆ど溶解)
備考)スケール溶解状況の評価
×:溶解能力無し
△:溶解能力が認められる
〇:良好な溶解能力が認められる
A carbon steel sheet with a black skin (thickness of the black skin: 20 μm) was used as a sample for the dissolution test. The surface to which the black skin was attached was the subject of the dissolution test.
Three 200 ml glass beakers were prepared, and the following three types of test solutions were added thereto and subjected to a black skin dissolution test.
CASE. 1 Mixing of 7% acidic ammonium fluoride, 9% citric acid and 18% sulfuric acid
Liquid and 12.7% iodine solution 7: mixed test liquid CASE at 3. 2 Acidic ammonium fluoride 7%, glycolic acid 9% and sulfuric acid 18%
Mixture and 12.7% iodine solution 7: 3 test solutions CASE in a mixing ratio of. 3 Acidic ammonium fluoride 7%, citric acid 4.5%, glycolic acid 4
.. A mixture of 5% and 18% sulfuric acid and a 12.7% iodine solution at a ratio of 7: 3.
Prepare the mixed test solution three black unpeeled carbon steel at a ratio, the three test solution was impregnated respectively gauze, covering the surface of the mill scale at one end of the gauze, start dissolution test at room temperature bottom.
After 60 minutes from the start of the test, the gauze on the surface of the black skin was removed, and the dissolution status of the black skin was confirmed. The summary of the results is as follows.
CASE. Dissolution status of 1 scale: 〇 (The black skin on the test surface covered with gauze is almost dissolved)
CASE. 2 scale dissolution status: 〇 (The black skin on the test surface covered with gauze is almost dissolved)
CASE. Dissolution status of 3 scales: 〇 (The black skin on the test surface covered with gauze is almost dissolved)
Remarks) Evaluation of scale dissolution status ×: No dissolution ability △: Dissolution ability is recognized 〇: Good dissolution ability is recognized

黒皮付き(黒皮の厚さ:20μm)の炭素鋼板を溶解試験用のサンプルとした。黒皮が付着した面を溶解試験の対象とした。
200mlのガラスビーカーを4個準備し、これに下記に示す4種類の試験液を入れ、黒皮の溶解試験に供した。
CASE.1 りん酸27%水溶液
CASE.2 りん酸27%水溶液と12.7%ヨウ素溶液を9:1の割合で混合
た試験液
CASE.3 りん酸27%水溶液と12.7%ヨウ素溶液を8:2の割合で混合
た試験液
CASE.4 りん酸27%水溶液と12.7%ヨウ素溶液を7:3の割合で混合
た試験液
4枚の黒皮付き炭素鋼板を準備し、4種類の試験液をそれぞれガーゼに含浸させ、ガーゼを黒皮の表面を覆い、常温での溶解試験を開始した。
試験開始から60分経過後、黒皮の表面のガーゼを取り外し、黒皮の溶解状況を確認した。
図2に黒皮付き炭素鋼板の試験後の重量減少結果を示す。りん酸水溶液にヨウ素を添加することで、黒皮の除去速度が速くなる傾向を示した。またヨウ素の混合比率(ヨウ素添加率)が高くなるほど、黒皮の除去速度が速くなる傾向を示した。
A carbon steel sheet with a black skin (thickness of the black skin: 20 μm) was used as a sample for the dissolution test. The surface to which the black skin was attached was the subject of the dissolution test.
Four 200 ml glass beakers were prepared, and the following four types of test solutions were added thereto and subjected to a black skin dissolution test.
CASE. 1 Phosphoric acid 27% aqueous solution CASE. 2 A 27% aqueous solution of phosphoric acid and a 12.7% iodine solution are mixed at a ratio of 9: 1.
The test solution CASE. 3 A 27% aqueous solution of phosphoric acid and a 12.7% iodine solution are mixed at a ratio of 8: 2.
The test solution CASE. 4 A 27% aqueous solution of phosphoric acid and a 12.7% iodine solution are mixed at a ratio of 7: 3.
And were prepared test solution four black unpeeled carbon steel, 4 types of test liquid impregnated respectively gauze, covering the surface of the mill scale gauze began dissolution test at room temperature.
After 60 minutes from the start of the test, the gauze on the surface of the black skin was removed, and the dissolution status of the black skin was confirmed.
FIG. 2 shows the results of weight reduction after the test of the carbon steel sheet with black skin. The addition of iodine to the aqueous phosphoric acid solution tended to increase the removal rate of black skin. In addition, the higher the iodine mixing ratio (iodine addition rate), the faster the black skin removal rate tended to be.

産業上の利用の可能性Possibility of industrial use

火力発電プラントの蒸気側の配管や弁類に生成する強固で難溶性の水蒸気酸化スケールを、常温で溶解する程の強力な洗浄剤であるため、火力発電プラントはもとより、原子力発電プラントなど、高温蒸気を用いるプラントのメンテナンスに利用できる。その他鉄鋼の黒皮(酸化スケール)や鉄さび除去にも利用できる。 Since it is a powerful cleaning agent that dissolves the strong and sparingly soluble steam oxidation scale generated in the steam side pipes and valves of thermal power plants at room temperature, it is a high temperature not only in thermal power plants but also in nuclear power plants. It can be used for maintenance of plants that use steam. It can also be used to remove black skin (oxidation scale) and iron rust on steel.

1復水器、2低圧給水加熱器、3脱気器、4高圧給水加熱器、5節炭器、6ボイラ、7過熱器、8タービン、9再熱器、10MSV(主蒸気止め弁)、11CV(加減弁)、12RSV(再熱蒸気止め弁)、13ICV(インターセプト弁)、14主蒸気管、15低温再熱蒸気管、16高温再熱蒸気管
実線は、給水系統の配管ライン
点線は、蒸気系統の配管ライン
1 water recovery device, 2 low-pressure feed water heater, 3 deaerator, 4 high-pressure feed water heater, 5-concrete heater, 6 boiler, 7 superheater, 8 turbine, 9 reheater, 10 MSV (main steam stop valve), 11CV (control valve), 12RSV (reheat steam stop valve), 13ICV (intercept valve), 14 main steam pipe, 15 low temperature reheat steam pipe, 16 high temperature reheat steam pipe Solid line is the piping line of the feed water system. Steam system piping line

Claims (1)

塩酸、硫酸、硝酸、リン酸、ホウ酸、フッ化水素酸、スルファミン酸からなる無機酸及びクエン酸、シュウ酸、酢酸、ギ酸、グリコール酸、酒石酸からなる有機酸の少なくとも1種以上からなる酸成分と
ヨウ素、ヨウ化水素酸、ヨウ化カリウム、ヨウ化ナトリウム、ヨウ化リチウム、ヨウ化銅、ヨウ化アンモニウム、ヨウ化亜鉛、ヨウ化マグネシウム、ヨウ化セシウム、ヨウ化ストロンチウム、ヨウ化バリウム、ヨウ素酸水溶液、ヨウ素酸カリウム、ヨウ素酸ナトリウム、ヨウ素酸カルシウムより選択された少なくとも1種を含むヨウ素化合物と、
フッ化アンモニウム、酸性フッ化アンモニウム、フッ化ナトリウム、酸性フッ化ナトリウム、フッ化カリウム、酸性フッ化カリウムより選択された少なくとも1種を含むフッ素化合物と、
から構成されることを特徴とする鉄さび及び酸化スケールの溶解除去用洗浄剤。
An inorganic acid consisting of hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, boric acid, hydrofluoric acid, and sulfamic acid, and an acid consisting of at least one organic acid consisting of citric acid, oxalic acid, acetic acid, formic acid, glycolic acid, and tartaric acid. and the component,
Iodine, hydroiodic acid, potassium iodide, sodium iodide, lithium iodide, copper iodide, ammonium iodide, zinc iodide, magnesium iodide, cesium iodide, strontium iodide, barium iodide, aqueous iodic acid , potassium iodate, sodium iodate, and iodine compounds containing at least one selected from iodate calcium,
Fluorine compounds containing at least one selected from ammonium fluoride, acidic ammonium fluoride, sodium fluoride, sodium acidic fluoride, potassium fluoride, and acidic potassium fluoride .
A cleaning agent for dissolving and removing iron rust and oxide scale, which is characterized by being composed of.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12227693B2 (en) 2022-09-09 2025-02-18 Saudi Arabian Oil Company Aqueous fluid compositions and barite scale removal therewith

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12227693B2 (en) 2022-09-09 2025-02-18 Saudi Arabian Oil Company Aqueous fluid compositions and barite scale removal therewith

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