JPH04501139A - Pickling method using a pickling bath for metal products containing titanium or at least one element chemically similar to titanium - Google Patents

Pickling method using a pickling bath for metal products containing titanium or at least one element chemically similar to titanium

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JPH04501139A
JPH04501139A JP2511471A JP51147190A JPH04501139A JP H04501139 A JPH04501139 A JP H04501139A JP 2511471 A JP2511471 A JP 2511471A JP 51147190 A JP51147190 A JP 51147190A JP H04501139 A JPH04501139 A JP H04501139A
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titanium
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アンリエ,ドミニク
ポール,ディディエ
プロスト,ローラン
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ユージヌ,アシエ ドゥ シャティヨン エ グニョン
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • C23G1/10Other heavy metals
    • C23G1/106Other heavy metals refractory metals
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions

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  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
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Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 発明の名称 チタンまたはチタンと化学的に類似な元素を少なくとも1つ含む金属製品の酸洗 浴を用いた酸洗方法本発明はチタンまたはまたはチタンと化学的に類似な元素を 少なくとも1つ含む金属製品を酸浴中で酸洗する方法に関するものである。[Detailed description of the invention] name of invention Pickling of metal products containing titanium or at least one element chemically similar to titanium Pickling method using a bath The present invention uses titanium or an element chemically similar to titanium. The present invention relates to a method for pickling a metal product containing at least one metal product in an acid bath.

冶金分野では、製造過程において鍛造加工や熱処理を受けた金属製品または合金 製品はさび皮(alamine)で被われているということは知られている。最 終製品の表面品質を良くするためには、酸洗処理によって全てのさび皮層を取り 除く必要がある。In the metallurgical field, metal products or alloys that have undergone forging or heat treatment during the manufacturing process. It is known that the product is covered with alumine. most In order to improve the surface quality of the finished product, all rust layers must be removed by pickling. need to be removed.

公知の酸洗処理では、硝酸HNO,と弗化水素酸HFとによって構成される酸洗 浴(11当たり硝酸が6〜16%、弗化水素酸が1〜5%の比率の酸洗浴)中に 最終製品を漬ける。この場合の酸洗浴の使用温度は40℃〜60℃である。In the known pickling treatment, pickling is composed of nitric acid, HNO, and hydrofluoric acid, HF. in a pickling bath with a ratio of 6 to 16% nitric acid and 1 to 5% hydrofluoric acid per 11 Soak the final product. The operating temperature of the pickling bath in this case is 40°C to 60°C.

チタンの酸洗に最も多く用いられる酸洗浴の1つは、硝酸をベースとしたもので あるが、硝酸は極めて有毒なNO3の蒸気を発生し、廃液中には窒素化合物(亜 硝酸塩および硝酸塩)が含まれる。法律で許容される硝酸塩の最大含有量は比較 的に高いが、亜硝酸塩は有害物質であるニトロザミン(nitosan+1ne )を作るため、その最大含有量ははるかに低い。One of the most commonly used pickling baths for pickling titanium is nitric acid-based. However, nitric acid generates extremely toxic NO3 vapor, and the waste liquid contains nitrogen compounds (nitrous oxide). nitrates and nitrates). The maximum content of nitrates allowed by law is However, nitrite is a toxic substance, nitrosamine (nitosan + 1ne). ), its maximum content is much lower.

主成分として塩酸HCIと弗化水素酸HFとを含むハロゲン酸の混合で構成され る浴を用いてチタンをベースとした冶金製品を酸洗する方法も公知である。It is composed of a mixture of halogen acids containing hydrochloric acid HCI and hydrofluoric acid HF as the main components. Methods for pickling titanium-based metallurgical products using baths are also known.

この方法の欠点は溶解時にチタンが■価に還元されて揮発性の化合物を形成する 点にある。The disadvantage of this method is that during dissolution, titanium is reduced to its valence and forms a volatile compound. At the point.

例えば、チタンを塩酸に溶解するとTiC1sに変換され、このTiC1−は8 0℃以下で昇華する。このTiC1sは下記反応式に従って昇華の前にTiCl 4+TiC1iに分解される:2 TiC1s−TiCl4+TiC1i (I  )TIC14は特に揮発性が高く、その蒸気圧は50℃で42m/Hgである 。For example, when titanium is dissolved in hydrochloric acid, it is converted to TiC1s, and this TiC1- is 8 Sublimes below 0℃. This TiCls is converted into TiCl before sublimation according to the reaction formula below. Decomposed into 4+TiC1i: 2 TiC1s-TiCl4+TiC1i (I ) TIC14 is particularly volatile, and its vapor pressure is 42 m/Hg at 50°C. .

本発明の目的は上記の酸洗方法の欠点が無い酸化剤(oxydant)を酸洗浴 中に導入してチタンまたはチタンの化学的類似元素を少なくとも1つ含む冶金製 品を酸性媒体中で酸洗する方法を提供することにあり、本発明の特徴は酸洗の反 応速度(cinetique)を増加させるために、 (1)被酸洗製品に含まれるチタンまたは少なくとも1つのチタンと化学的に類 似な元素の少なくとも1種の過酸化合物(composeperoxygene )を形成して、金属を原子価がより高いイオンとし、(2)酸化還元(レドック ス)電位を測定することによって上記過酸化合物の形成を制御し、 (3)酸化還元電位が金属製品のバッジバージョン電位以下となるように酸化剤 の量を制限する点にある。The object of the present invention is to add an oxidant to a pickling bath that does not have the drawbacks of the above-mentioned pickling methods. metallurgical product containing at least one titanium or chemically similar element to titanium It is an object of the present invention to provide a method for pickling products in an acidic medium. In order to increase the cinetique, (1) Titanium or at least one chemically similar to titanium contained in the product to be pickled; At least one peroxygene of similar elements ) to make the metal a higher valence ion, and (2) redox (redox). b) controlling the formation of said peracid compound by measuring the potential; (3) Oxidizing agent so that the redox potential is below the badge version potential of the metal product. The point is to limit the amount of

この方法の基礎となる事実は、金属の酸素物は原子価がより高いイオンになった 時には、その金属自体および原子価がより低いその金属の酸化物に較べてより攻 撃的になるということである。原子価がより高いイオンとは、特にチタネート、 ノイナデート、ジルコネート、ニオベート、タンタレート、ウラネートのイオン のようなものを意味する。The fact underlying this method is that the metal's oxygen species have become ions with higher valences. Sometimes more aggressive than the metal itself and its lower valence oxides. It means being aggressive. Ions with higher valences are especially titanates, Ions of noinadate, zirconate, niobate, tantalate, uranate means something like

上記酸洗浴は基本的に弗化水素酸、硫酸、塩酸、燐酸および蟻酸によって構成さ れる群の中から選択される酸を含んだ浴であるのが好ましいが、酸化チタンを酸 洗可能なその他の酸またはHF−H,SO,のような鉱酸の混合物を用いること もできる。The above pickling bath basically consists of hydrofluoric acid, sulfuric acid, hydrochloric acid, phosphoric acid and formic acid. Preferably, the bath contains an acid selected from the group consisting of: Using other washable acids or mixtures of mineral acids such as HF-H, SO, You can also do it.

酸洗反応を開始させるためには、少なくとも1つの金属の過酸化合物を形成する ような酸化能の強い酸化剤を酸洗浴中に導入する。To initiate the pickling reaction, a peroxide compound of at least one metal is formed. An oxidizing agent with strong oxidizing ability is introduced into the pickling bath.

チタンまたはチタンと化学的に類似な元素は酸化剤ととも1こ過酸化合物を形成 するということに注目すべきことである。達成される酸化の程度に応じて下記の 化合物が得られる=(ここで、MはTiまたはTiの化学的類似元素である)こ の化合物は特に強力な酸化物質である過酸塩(persel)を構成する。Titanium or elements chemically similar to titanium form monoperoxide compounds with oxidizing agents. It is worth noting that. Depending on the degree of oxidation achieved, the following A compound is obtained = (where M is Ti or a chemically similar element of Ti) The compounds constitute persels, which are particularly strong oxidizing substances.

上記酸化剤は過酸化水素、過酸化尿素またはオゾンや酸素のようなガスの中から 選択するのが好ましい。The above oxidizing agents can be hydrogen peroxide, urea peroxide or gases such as ozone and oxygen. Preferably.

過酸化水素は0.5重量%以下の量で酸洗浴に直接に導入される。さらに、酸性 媒体中で分解して過酸化水素を生じるような過酸塩または過酸の形で導入するこ ともできる。過酸化尿素G11.2重量%以下の量で用いることができる。Hydrogen peroxide is introduced directly into the pickling bath in an amount of up to 0.5% by weight. Additionally, acidic It may be introduced in the form of a persalt or peracid, which decomposes in the medium to produce hydrogen peroxide. Can also be done. Urea peroxide G can be used in an amount of 11.2% by weight or less.

本発明は以下の説明からより容易に理解できよう。The invention will be more easily understood from the following description.

本発明方法は、チタンまたは少なくとも1つのチタンのイヒ学的類似元素、特に バナジウム、ジルコニウム、ニオブ、タンタルおよびウラニウムを含む金属また は合金の製品を酸洗浴中で酸洗する方法に関するものである。The method according to the invention comprises titanium or at least one chemically similar element of titanium, in particular titanium. metals including vanadium, zirconium, niobium, tantalum and uranium; relates to a method for pickling alloy products in a pickling bath.

酸洗反応の機構は上記の各金属の場合でも、その合金の場合でもほぼ同じである ので、チタンの酸洗方法を例暑こ取って詳細に説明する。The pickling reaction mechanism is almost the same for each of the above metals and their alloys. Therefore, I will explain in detail how to pickle titanium using an example.

基礎となる酸洗浴は、弗化水素酸の濃度が0.2〜10重量%の範囲である弗化 水素酸の浴であるのが好ましいが、被酸洗製品中に含まれるチタンの化学的類似 元素を過酸化合物の形で含むという条件さえ満たせば、その他の酸、例えば硫酸 を用いることもできる。The basic pickling bath is a fluorinated pickling bath with a concentration of hydrofluoric acid ranging from 0.2 to 10% by weight. A bath of hydrogen acid, preferably a bath of chemically similar titanium contained in the pickled product. Other acids, such as sulfuric acid, can be used as long as they contain the element in the form of a peracid. You can also use

チタンの酸洗の例では、酸化チタンが下記の反応によって弗化水素酸によって攻 撃されることが実験室でのテストで確認されている: 2Ti+6HF → 2’riF’3 +3H2↑ (II)過剰なHFが存在 すると三フッ化チタンは四フッ化物7iF4に変換される。In the example of pickling titanium, titanium oxide is attacked by hydrofluoric acid by the following reaction: Laboratory tests have confirmed that: 2Ti+6HF → 2'riF'3 +3H2↑ (II) Excess HF exists Titanium trifluoride is then converted to tetrafluoride 7iF4.

本発明方法では、酸洗反応の速度を増加させるために、原子価がより高いイオン に成った少なくとも1つの金属酸化物を形成する。チタンの酸洗の場合には、チ タンとその酸化物に対して特に攻撃的であるチタンの過酸化合物、ベルチタネー トを形成する。In the method of the invention, ions of higher valence are used to increase the rate of the pickling reaction. forming at least one metal oxide having a composition of at least one metal oxide; In the case of pickling titanium, Vertitane, a titanium peroxide compound that is particularly aggressive towards titanium and its oxides. form a grid.

このベルチタネートは、例えば下記反応によって、チタンのフッ化物に過酸化水 素を作用させて作ることができる=TI”+ HJ* + 2H*0 → Ti O4”−+ 6H” (III)2 TiO4”−+ Ti + 16H+→  3Ti’◆+8H,0(IV)反応(IV)では超過なH″はなくなり、H30 が形成され、それによって被酸洗金属または合金の結晶格子網の中にH4が入る 作用が減少し、その結果、酸洗浴の製品の脆性化が少なくなる。This vertitanate is produced by adding water peroxide to titanium fluoride, for example, by the following reaction. It can be made by interacting with the elements = TI” + HJ* + 2H*0 → Ti O4"-+ 6H" (III) 2 TiO4"-+ Ti + 16H+→ 3Ti'◆+8H,0(IV) In the reaction (IV), there is no excess H'', and H30 is formed, thereby allowing H4 to enter the crystal lattice network of the pickled metal or alloy. The effect is reduced, resulting in less brittleness of the product in the pickling bath.

ベルチタネートは、分解によって過酸化水素を生じる過酸化尿素の作用で得るこ ともできる。過酸化尿素は固体であるので運搬がより容易になる。Vertitanate can be obtained through the action of urea peroxide, which decomposes to produce hydrogen peroxide. Can also be done. Urea peroxide is a solid, which makes it easier to transport.

さらに、ベルチタネートは浴中ヘオゾンを注入することによって形成させること もできる。この場合のベルチタネートの生成反応は以下の通りである: Ti” + Os + HtO→Ti4”−+ H2” (V)2Ti04”− + Ti + 16H”→3Ti”+ 8HiO(VI)オゾンの代わりに酸素 を用いることもできる。Additionally, vertitanate can be formed by injecting heozone into the bath. You can also do it. The reaction for producing vertitanate in this case is as follows: Ti" + Os + HtO → Ti4"-+ H2" (V)2Ti04"- + Ti + 16H" → 3Ti" + 8HiO (VI) Oxygen instead of ozone You can also use

酸性媒体の中へ過酸塩を導入すると、分解して過酸化水素を生じることは知られ ている。使用可能な過酸塩としては特に過マンガン酸塩、過硫酸塩、ベルチタネ ート、ベルバナデート、ベルボレート等を挙げることができる。It is known that when persalts are introduced into acidic media, they decompose to form hydrogen peroxide. ing. Persalts that can be used include permanganates, persulfates, and vertitanes, among others. Examples include berbanate, bervanadate, berborate, and the like.

さらに、酸性媒体中でHa Oxに分解される過酸化合物を用いることもできる 。この過酸化合物としては特に、他の産業分野で使われている過硼酸、過酸化チ タン、過酢酸、過硫酸を挙げることができる。Additionally, peracid compounds that decompose into HaOx in acidic media can also be used. . Examples of peracid compounds include perboric acid and titanium peroxide, which are used in other industrial fields. Mention may be made of tan, peracetic acid and persulfuric acid.

T1042″の形成は酸洗浴の酸化還元電位(potentiel de ox ydo−reduct 1on)を測定することによってコントロールされる。The formation of T1042″ is caused by the redox potential of the pickling bath. controlled by measuring the ydo-reduct 1on).

この酸化還元電位(RBIIOX電位)は、被測定対象の酸洗浴中に浸漬した非 腐食性電極(例えば、白金電極)と基準電極(例えば、Ag/AgClまたは飽 和カロメル電極)との間の電位差である。This oxidation-reduction potential (RBIIOX potential) is determined by A corrosive electrode (e.g. platinum electrode) and a reference electrode (e.g. Ag/AgCl or saturated Calomel electrode).

この測定値は酸洗浴の酸化能を特徴づける値である。また、この測定値に基づい て上記化合物を導入して酸洗浴を所定の酸化能力に維持するために酸洗浴を再調 整することができる。チタンまたはチタン化合物を酸洗するためには、上記酸化 還元電位は下記の範囲内にある必要がある: (+150.−350)mV/Ag/AgC1本発明方法では、主酸化剤がチタ ンまたはチタンと化学的に類似な元素要の過酸化合物である好ましくは単一の酸 のみしか含まない標準浴を用いて、チタンふよびその合金、チタンと化学的に類 似な元素およびその合金を酸洗効率を向上させるものである。This measured value is a value that characterizes the oxidizing ability of the pickling bath. Also, based on this measurement The pickling bath is reconditioned by introducing the above-mentioned compounds to maintain the pickling bath at the desired oxidation capacity. can be adjusted. In order to pickle titanium or titanium compounds, the above oxidation The reduction potential must be within the following range: (+150.-350) mV/Ag/AgC1 In the method of the present invention, the main oxidant is titanium. peroxide compound, preferably a single acid, containing an element chemically similar to titanium or titanium. Using a standard bath containing only titanium, titanium and its alloys, which are chemically similar to titanium, It improves the pickling efficiency of similar elements and their alloys.

本発明方法を使ったチタンの酸洗法の一実施例では、平らな製品の重量損失は4 0から80g/m”である。得られた表面状態は硝酸/弗化水素法を用いて得ら れたものに匹敵し、過剰な酸洗浴作用はない。過酸化水素を用いた場合の処理面 は白くなり審美的に好ましい外観になる。In one example of pickling titanium using the method of the invention, the weight loss of the flat product was 4. 0 to 80 g/m''.The obtained surface condition was obtained using the nitric acid/hydrogen fluoride method. Comparable to those prepared in this way, and does not have an excessive pickling bath effect. Surface treated with hydrogen peroxide becomes white and has an aesthetically pleasing appearance.

本発明方法の重要な点は、有害物質または汚染物質を添加せずに酸化剤を“その 場(in 5itu)すなわち系中で”作るという点にある。An important aspect of the method of the invention is that the oxidizing agent is It lies in the fact that it is “created in situ”, that is, in the system.

酸洗反応は過酸化チタンまたはチタンと化学的に類似な元素の過酸化物によって 起こるので、弗化水素酸の消費量が減る。The pickling reaction is carried out by titanium peroxide or peroxides of elements chemically similar to titanium. occurs, so the consumption of hydrofluoric acid is reduced.

本発明方法は大気汚染を引き起こさず、廃水は処理して再循環できるので、酸洗 浴の使用寿命を延ばすことができる。The method of the invention does not cause air pollution and the wastewater can be treated and recycled, so pickling The service life of the bath can be extended.

過酸化合物(ベルチタネート、ベルジルコネート、ベルタンタレート、ベルニオ ベート、ベルウラネート、ベルバナデート)の形成には生態学上問題のないH, O□を添加するだけでよい。Peracid compounds (Vertitanate, Verzirconate, Vertanthalate, Bernio) H, which has no ecological problems in the formation of bate, beluranate, belbanadate). Just add O□.

このH,O□は生物にとって好ましいH,Oと02とに分解される。This H, O□ is decomposed into H, O and 02, which are favorable for living things.

従って、本発明方法は有害物質の大気へ放出や廃水への流出が減少でき、さらに は、これらを全く無くすこともできる。Therefore, the method of the present invention can reduce the release of harmful substances into the atmosphere and into wastewater, and furthermore, You can also eliminate these altogether.

この廃水と使用後の酸洗浴は、工業国の規制に従って処理することができる。例 えば、石灰乳液で処理することによって金属水酸化物を沈殿させて、有害な陰イ オンが流出するのを防止することができる。これに対して、硝酸塩を用いた場合 にはこれら全てが水に溶けてしまう。本発明方法はエコノロジカルな方法である 。This waste water and the used pickling bath can be treated in accordance with the regulations of industrialized countries. example For example, treatment with lime emulsion can precipitate metal hydroxides and remove harmful anions. It is possible to prevent on from flowing out. In contrast, when using nitrates All of these dissolve in water. The method of the present invention is an ecological method. .

本発明方法では、過剰な水素を発生させずに酸化剤浴が使用できるので、還元剤 浴で起こり易い被酸洗品の金属組織網中への水素の拡散が減少し、酸洗後の製品 の脆性化が少なくなる。In the method of the present invention, an oxidizing agent bath can be used without generating excess hydrogen, so a reducing agent can be used. The diffusion of hydrogen into the metal network of the product to be pickled, which tends to occur in baths, is reduced, and the product after pickling is becomes less brittle.

国際調査報告 −ポー一+^―−IN、PCT/FR90100564国際調査報告 FR9000564international search report -Poichi+^--IN, PCT/FR90100564 International Search Report FR9000564

Claims (1)

【特許請求の範囲】 1.酸化剤を含む酸浴中にチタンまたはチタンの化学的類似元素を少なくとも1 つ含む金属製品または合金製品を導入して酸浴中で酸洗する方法において、 酸洗の反応速度を増加させるために、 (1)被酸洗製品に含まれるチタンまたは少なくとも1つのチタンと化学的に類 似な元素の少なくとも1種の過酸化合物を形成して、金属を原子価がより高いイ オンとし、(2)酸化還元電位を測定することによって上記過酸化合物の形成量 を制御し、 (3)酸化還元電位が金属製品のパッシバーション電位以下となるように酸化剤 の量を制限する ことを特徴とする方法。 2.酸浴が弗化水素酸、硫酸、塩酸、燐酸、蟻酸によって構成される群の中から 選択された1つの酸を含む浴である請求項1に記載の方法。 3.酸化剤が酸素ガスまたはオゾンガスである請求項1または2に記載の方法。 4.酸化剤が過酸化水素または過酸化尿素である請求項1から3に記載の方法。 5.チタンまたはチタン化合物の酸洗時の上記酸化還元電位が(+150,−3 50)mV/Ag/AgClの範囲中にある請求項1に記載の方法。 6.酸浴中に導入される過酸化水素の量が0.5重量%以下である請求項4に記 載の方法。 7.酸浴に導入される過酸化尿素の量が1.2重量%以下である請求項4に記載 の方法。 8.酸化剤が過酸化塩である請求項1または2に記載の方法。 9.過酸化塩が被酸洗製品中に含まれるチタンまたはチタンと化学的に類似な少 なくとも1つの元素の酸化能の強い過酸化塩である請求項8に記載の方法。 10.酸化剤が過酸化合物である請求項1または2に記載の方法。 11.過酸化合物が被酸洗製品中に含まれるチタンまたはチタンと化学的に類似 な少なくとも1つの元素の過酸化合物である請求項10に記載の方法。 12.チタンと化学的に類似な元素かバナジウム、ジルコニウム、ニオブ、タン タルまたはウラニウムである請求項1〜11のいずれか1項に記載の方法。[Claims] 1. At least one titanium or chemically similar element to titanium is added to an acid bath containing an oxidizing agent. In the method of pickling in an acid bath by introducing a metal product or an alloy product containing To increase the reaction rate of pickling, (1) Titanium or at least one chemically similar to titanium contained in the product to be pickled; The formation of at least one peroxide compound of similar elements to bind metals to higher valence atoms. (2) The amount of peracid compound formed by measuring the redox potential control, (3) Oxidizing agent so that the redox potential is below the passivation potential of the metal product. limit the amount of A method characterized by: 2. From the group in which the acid bath consists of hydrofluoric acid, sulfuric acid, hydrochloric acid, phosphoric acid, and formic acid 2. The method of claim 1, wherein the bath comprises one selected acid. 3. The method according to claim 1 or 2, wherein the oxidizing agent is oxygen gas or ozone gas. 4. 4. A method according to claims 1 to 3, wherein the oxidizing agent is hydrogen peroxide or urea peroxide. 5. The above redox potential during pickling of titanium or titanium compound is (+150, -3 50) The method of claim 1 in the range of mV/Ag/AgCl. 6. Claim 4, wherein the amount of hydrogen peroxide introduced into the acid bath is 0.5% by weight or less. How to put it on. 7. Claim 4, wherein the amount of urea peroxide introduced into the acid bath is 1.2% by weight or less. the method of. 8. 3. The method according to claim 1 or 2, wherein the oxidizing agent is a peroxide salt. 9. If the peroxide salt contains titanium or a small amount chemically similar to titanium in the pickled product, 9. The method according to claim 8, wherein the peroxide salt has a strong oxidizing ability of at least one element. 10. The method according to claim 1 or 2, wherein the oxidizing agent is a peracid compound. 11. The peroxide compound is chemically similar to titanium or titanium contained in the pickled product. 11. The method according to claim 10, wherein the peroxide compound is a peroxide compound of at least one element. 12. Elements chemically similar to titanium or vanadium, zirconium, niobium, tan 12. The method according to any one of claims 1 to 11, wherein the metal is tal or uranium.
JP2511471A 1989-07-26 1990-07-25 Pickling method for metal products containing at least one titanium or a chemically similar element to titanium using a pickling bath Expired - Fee Related JP2945136B2 (en)

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FR8910093A FR2650303B1 (en) 1989-07-26 1989-07-26 PROCESS FOR ACIDIC STRIPPING OF METAL PRODUCTS CONTAINING TITANIUM OR AT LEAST ONE CHEMICAL ELEMENT OF THE TITANIUM FAMILY
FR89/10093 1989-07-26

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995016277A1 (en) * 1993-12-10 1995-06-15 Tadahiro Ohmi Surface cleaning method and surface cleaning agent of substrate

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1255855B (en) * 1992-10-12 1995-11-17 Cesare Pedrazzini PICKLING AND PASSIVATION PROCESS FOR TITANIUM SHEETS IN TAPE, WITHOUT THE USE OF NITRIC ACID.
IT1288407B1 (en) * 1996-12-09 1998-09-22 Sviluppo Materiali Spa METHOD FOR PICKLING METAL ALLOY PRODUCTS CONTAINING IRON AND TITANIUM AND ITS ALLOYS
IT1290947B1 (en) * 1997-02-25 1998-12-14 Sviluppo Materiali Spa METHOD AND DEVICE FOR THE PICKLING OF METALLIC ALLOY PRODUCTS IN THE ABSENCE OF NITRIC ACID AND FOR THE RECOVERY OF EXHAUSTED SOLUTIONS
RU2151822C1 (en) * 1998-07-21 2000-06-27 Акционерное общество открытого типа "Уральский завод гражданской авиации" Solution for cleaning components of titanium alloys from high-temperature deposits
US7611588B2 (en) 2004-11-30 2009-11-03 Ecolab Inc. Methods and compositions for removing metal oxides
RU2496819C1 (en) * 2012-05-30 2013-10-27 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Национальный исследовательский Томский политехнический университет" Titanium etchant
KR101669718B1 (en) 2014-07-01 2016-10-27 김동회 Incubator with multi-directional angle structure

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB360126A (en) * 1929-10-19 1931-11-05 Hirsch Kupfer & Messingwerke Method of pickling oxidised metals
US3258429A (en) * 1963-09-19 1966-06-28 Ronald D Weed Decontamination solution and method
JPS526853B2 (en) * 1972-12-22 1977-02-25
DE2358683A1 (en) * 1973-11-24 1975-06-05 Kalman Von Dipl Phys Soos Pickling, etching or cleaning of metals, esp. steel - using ozone accelerator in addn. to the other chemicals
JPS549120A (en) * 1977-06-24 1979-01-23 Tokai Electro Chemical Co Method of controlling acid cleaning liquid for stainless steel
SU992179A1 (en) * 1981-09-17 1983-01-30 Фрунзенский политехнический институт Percussion-action machine
FR2587369B1 (en) * 1985-09-19 1993-01-29 Ugine Gueugnon Sa PROCESS OF ACID STRIPPING OF STAINLESS STEEL PRODUCTS
JPS6277489A (en) * 1985-09-30 1987-04-09 Nippon Mining Co Ltd Method for pickling metallic material
JPS62109998A (en) * 1985-11-07 1987-05-21 Kobe Steel Ltd Pretreatment of valve metal before anodic oxidation
EP0259533A1 (en) * 1986-09-11 1988-03-16 Eka Nobel Aktiebolag Method of reducing the emission of nitrogen oxides from a liquid containing nitric acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995016277A1 (en) * 1993-12-10 1995-06-15 Tadahiro Ohmi Surface cleaning method and surface cleaning agent of substrate

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