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JP2945136B2 - Pickling method for metal products containing at least one titanium or a chemically similar element to titanium using a pickling bath - Google Patents
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JP2945136B2 - Pickling method for metal products containing at least one titanium or a chemically similar element to titanium using a pickling bath - Google Patents

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

Info

Publication number
JP2945136B2
JP2945136B2 JP2511471A JP51147190A JP2945136B2 JP 2945136 B2 JP2945136 B2 JP 2945136B2 JP 2511471 A JP2511471 A JP 2511471A JP 51147190 A JP51147190 A JP 51147190A JP 2945136 B2 JP2945136 B2 JP 2945136B2
Authority
JP
Japan
Prior art keywords
titanium
pickling
acid
chemically similar
oxidizing agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2511471A
Other languages
Japanese (ja)
Other versions
JPH04501139A (en
Inventor
アンリエ,ドミニク
ポール,ディディエ
プロスト,ローラン
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YUUJINU ASHE DO SHATEIYON E GUNYON
Original Assignee
YUUJINU ASHE DO SHATEIYON E GUNYON
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Publication of JPH04501139A publication Critical patent/JPH04501139A/en
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Publication of JP2945136B2 publication Critical patent/JP2945136B2/en
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Expired - Fee Related legal-status Critical Current

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Classifications

    • 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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  • Chemical & Material Sciences (AREA)
  • Metallurgy (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Materials For Medical Uses (AREA)
  • Chemical Treatment Of Metals (AREA)
  • Cosmetics (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The process for pickling in an acid bath containing an oxidant is distinguished in that, to increase the action of the pickling process, at least one peroxygenated compound of titanium or at least one element of the titanium family included in the product to be pickled is formed, with the metal ionised to a higher valency, the formation of the peroxygenated compound is monitored by measuring the redox potential and the quantity of oxidising agent is limited to conserve an oxy-reduction potential above the passivation potential of the metal product.

Description

【発明の詳細な説明】 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。
The present invention relates to a method of pickling a metal product containing at least one of titanium and / or an element chemically similar to titanium 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。
It is known in the metallurgy field that metal or alloy products that have been forged or heat treated during the manufacturing process are covered with rust skin (alamine). In order to improve the surface quality of the final product, it is necessary to remove all rust layers by pickling.

公知の酸洗処理では、硝酸HNO3と弗化水素酸HFとによ
って構成される酸洗浴(1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 a known pickling treatment, a pickling bath composed of nitric acid HNO 3 and hydrofluoric acid HF (a pickling bath having a ratio of 6 to 16% of nitric acid and 1 to 5% of hydrofluoric acid per one) is used. Pickle the final product. The working 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
NO2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(nitosamine)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
Based on nitric acid, which is extremely toxic
Generating a vapor of NO 2, the liquid waste contains a nitrogen compound (nitrite and nitrate) are. Although the maximum nitrate content allowed by law is relatively high, nitrites make the harmful substance nitrosamine, so their maximum content is much lower.

主成分として塩酸HCl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 also known to pickle titanium-based metallurgical products using a bath composed of a mixture of halogen acids containing hydrochloric acid HCl and hydrofluoric acid HF as the main components.

この方法の欠点は溶解時にチタンがIII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 upon dissolution, the titanium is reduced to valence III to form volatile compounds.

例えば、チタンを塩酸に溶解するとTiCl3に変換さ
れ、このTiCl3は80℃以下で昇華する。このTiCl3は下記
反応式に従って昇華の前にTiCl4+TiCl2に分解される: 2TiCl3→TiCl4+TiCl2 (I) TiCl4は特に揮発性が高く、その蒸気圧は50℃で42mm/
Hgである。
For example, it is converted to TiCl 3 when dissolved titanium in hydrochloric acid, the TiCl 3 sublimes at 80 ° C. or less. This TiCl 3 is decomposed to TiCl 4 + TiCl 2 before sublimation according to the following reaction equation: 2TiCl 3 → TiCl 4 + TiCl 2 (I) TiCl 4 is particularly volatile, and its vapor pressure is 42 mm / at 50 ° C.
Hg.

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点にある。
It is an object of the present invention to pickle a metallurgical product containing titanium or at least one chemically similar element of titanium in an acid medium by introducing an oxydant into the pickling bath which does not have the disadvantages of the above pickling process. It is an object of the present invention to provide a method for increasing the kinetics of pickling by using (1) titanium or at least one of titanium contained in the pickled product.
By forming at least one composeperoxygene of an element chemically similar to the two titaniums to make the metal a higher valent ion, and (2) measuring the redox potential (3) Limiting the amount of the oxidizing agent so that the oxidation-reduction potential is equal to or lower than the passivation potential of the metal product.

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、バナデート、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 underlying fact of this method is that the oxygenate of a metal becomes more aggressive when it becomes a higher valent ion than the metal itself and its lower valent oxide. is there. Higher valent ions mean in particular such ions as titanate, vanadate, zirconate, niobate, tantalate, uranate.

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−H2SO4のような鉱酸の混合物
を用いることもできる。
The above pickling bath is preferably a bath containing an acid selected from the group consisting of hydrofluoric acid, sulfuric acid, hydrochloric acid, phosphoric acid and formic acid. the mixture can also be used in the mineral acid such as the acid or HF-H 2 sO 4.

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。
In order to start the pickling reaction, an oxidizing agent having a strong oxidizing ability to form a peracid compound of at least one metal 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
ともに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(pers
el)を構成する。
It should be noted that titanium or an element chemically similar to titanium forms a peracid compound with the oxidizing agent. Depending on the degree of oxidation achieved, the following compounds are obtained: (Where M is Ti or a chemical analog of Ti) This compound is a particularly powerful oxidant, the persalt (pers).
el).

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 oxidizing agent is preferably selected from hydrogen peroxide, urea peroxide or a gas such as ozone or oxygen.

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。過酸化尿素は1.2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 less than 0.5% by weight. In addition, they can be introduced in the form of persalts or peracids which decompose in an acidic medium to give hydrogen peroxide. Urea peroxide can be used in amounts up to 1.2% by weight.

本発明は以下の説明からより容易に理解できよう。 The present invention will be more readily 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
の化学的類似元素、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 present invention relates to a method for pickling a metal or alloy product comprising titanium or at least one chemically similar element of titanium, in particular vanadium, zirconium, niobium, tantalum and uranium, 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
に取って詳細に説明する。
The mechanism of the pickling reaction is almost the same for each of the above metals and their alloys. Therefore, the pickling method for titanium will be described in detail as 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 underlying pickling bath is preferably a bath of hydrofluoric acid with a hydrofluoric acid concentration in the range of 0.2 to 10% by weight, but is chemically similar to titanium contained in the pickling product. Other acids, such as sulfuric acid, can be used as long as they contain the acid in the form of a peracid compound.

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→2TiF3+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Ti
F4に変換される。
In the example of pickling titanium, laboratory tests have shown that titanium oxide is attacked by hydrofluoric acid by the following reaction: 2Ti + 6HF → 2TiF 3 + 3H 2 ↑ (II) Excess HF If present, titanium trifluoride will be Ti tetrafluoride
It is converted to F 4.

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、ペルチタネートを形成する。
In the method of the present invention, at least one metal oxide is formed into higher valent ions in order to increase the rate of the pickling reaction. In the case of pickling titanium, it forms pertitanate, a peracid compound of titanium which is particularly aggressive for titanium and its oxides.

このペルチタネートは、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: Ti4++H2O2+2H2O→TiO4 2-+6H+ (III) 2TiO4 2-+Ti+16H+→3Ti4++8H2O (IV) 反応(IV)では超過なH2はなくなり、H2O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H+が入る作用が減少し、その結果、酸洗済の製品の
脆性化が少なくなる。
This pertitanate can be made by reacting hydrogen fluoride on titanium fluoride, for example, by the following reaction: Ti 4+ + H 2 O 2 + 2H 2 O → TiO 4 2- + 6H + (III) 2TiO 4 2 - + Ti + 16H + → 3Ti 4+ + 8H 2 O (IV) In the reaction (IV), excess H 2 disappears and H 2 O is formed, whereby H + is contained in the crystal lattice network of the pickled metal or alloy. There is less entry and consequently less brittleness of the pickled product.

ペルチタネートは、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。
Pertitanate can also be obtained by the action of urea peroxide, which produces hydrogen peroxide by decomposition. Urea peroxide is a solid and therefore easier to transport.

さらに、ペルチタネートは浴中へ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。この場合のペルチ
タネートの生成反応は以下の通りである: Ti4++O3+H2O→Ti4 2-+H2 + (V) 2TiO4 2-+Ti+16H+→3Ti4++8H2O (VI) オゾンの代わりに酸素を用いることもできる。
In addition, pertitanate can be formed by injecting ozone into the bath. The reaction of forming pertitanate in this case is as follows: Ti 4+ + O 3 + H 2 O → Ti 4 2- + H 2 + (V) 2TiO 4 2 + Ti + 16H + → 3Ti 4+ + 8H 2 O (VI) Oxygen can be used instead of ozone.

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、ペルチタネー
ト、ペルバナデート、ペルボレート等を挙げることがで
きる。
It is known that the introduction of a persalt into an acidic medium decomposes to produce hydrogen peroxide. Examples of persalts that can be used include permanganate, persulfate, pertitanate, pervanadate, perborate and the like.

さらに、酸性媒体中でH2O2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。
Further, a peracid compound which is decomposed into H 2 O 2 in an acidic medium can also be used. Examples of the peracid compound include perboric acid, titanium peroxide, peracetic acid, and persulfuric acid, which are used in other industrial fields.

TiO4 2-の形成は酸洗浴の酸化還元電位(potentiel de
oxydoreduction)を測定することによってコントロー
ルされる。この酸化還元電位(REDOX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。
The formation of TiO 4 2- depends on the oxidation-reduction potential of the pickling bath (potentiel de
oxydoreduction). This oxidation-reduction potential (REDOX potential) is a potential difference between a non-corrosive electrode (for example, a platinum electrode) immersed in a pickling bath to be measured and a reference electrode (for example, an Ag / AgCl or saturated calomel electrode). is there.

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/AgCl 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、チタンおよびそ
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 measurement characterizes the oxidizing power of the pickling bath.
The pickling bath can be readjusted to maintain the pickling bath at a predetermined oxidizing ability by introducing the compound based on the measured value. In order to pickle titanium or a titanium compound, the redox potential must be within the following range: (+150, -350) mV / Ag / AgCl In the method of the present invention, the main oxidizing agent is titanium or titanium. Pickling efficiency of titanium and its alloys, titanium and chemically similar elements and alloys using a standard bath containing preferably only a single acid Is to improve.

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40から80g/m2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 embodiment of the method of pickling titanium using the method of the present invention,
The weight loss of flat products is 40 to 80 g / m 2 . The surface condition obtained is comparable to that obtained using the nitric acid / hydrogen fluoride method and there is no excessive pickling bath action. When hydrogen peroxide is used, the treated surface 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 situ)すなわち系中
で”作るという点にある。
An important aspect of the method of the present invention is that the oxidizing agent is made "in situ" without adding harmful or contaminants.

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。
Since the pickling reaction is caused by titanium peroxide or a peroxide of an element chemically similar to titanium, 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 present invention does not cause air pollution and the wastewater can be treated and recycled, so that the service life of the pickling bath can be extended.

過酸化合物(ペルチタネート、ペルジルコネート、ペ
ルタンタレート、ペルニオベート、ペルウラネート、ペ
ルバナデート)の形成には生態学上問題のないH2O2を添
加するだけでよい。このH2O2は生物にとって好ましいH2
OとO2とに分解される。
For the formation of peracid compounds (pertitanate, perzirconate, pertantalate, perniobate, peruranate, pervanadate), it is only necessary to add H 2 O 2 which has no ecological problem. This H 2 O 2 is the preferred H 2 for living organisms
It is decomposed into O and O 2.

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 emission of harmful substances to the atmosphere and the outflow to wastewater, and further can 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。
The wastewater and the used pickling bath can be treated according to the regulations of industrial countries. For example, treatment with lime latex can precipitate metal hydroxides and prevent harmful anions from flowing out. On the contrary,
All of these are dissolved in water when nitrates are used. The method of the present invention is an economic 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, since the oxidizing agent bath can be used without generating excessive hydrogen, the diffusion of hydrogen into the metallographic network of the pickled product, which tends to occur in the reducing agent bath, is reduced, and the product after pickling is reduced. Is less brittle.

フロントページの続き (72)発明者 プロスト,ローラン フランス国 73400 ユージヌ リュ レオン エコフェ 151 (58)調査した分野(Int.Cl.6,DB名) C23G 1/10 Continued on the front page (72) Inventor Prost, Laurent 73400 Eugene Lou-Leon Ecofe 151 (58) Field surveyed (Int. Cl. 6 , DB name) C23G 1/10

Claims (12)

(57)【特許請求の範囲】(57) [Claims] 【請求項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。
1. A method of introducing a metal product or an alloy product containing at least one titanium or a chemically similar element of titanium into an acid bath containing an oxidizing agent and pickling in an acid bath, wherein a reaction rate of the pickling (1) Titanium or at least one titanium contained in the pickled product
Forming at least one kind of peracid compound of an element chemically similar to the two titanium atoms, turning the metal into an ion having a higher valence, and (2) measuring the oxidation-reduction potential to form the peracid compound. And (3) limiting the amount of the oxidizing agent so that the oxidation-reduction potential is equal to or lower than the passivation potential of the metal product.
【請求項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。
2. The method according to claim 1, wherein the acid bath is a bath containing one acid selected from the group consisting of hydrofluoric acid, sulfuric acid, hydrochloric acid, phosphoric acid and formic acid.
【請求項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。
3. The method according to claim 1, wherein the oxidizing agent is oxygen gas or ozone gas.
【請求項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。
4. The method according to claim 1, wherein the oxidizing agent is hydrogen peroxide or urea peroxide.
【請求項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,−350)mV/Ag/AgClの範囲中に
ある請求項1に記載の方法。
5. The method according to claim 1, wherein the redox potential at the time of pickling titanium or a titanium compound is in the range of (+150, -350) mV / Ag / AgCl.
【請求項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。
6. The amount of hydrogen peroxide introduced into the acid bath is 0.5
5. The method according to claim 4, which is less than or equal to% by weight.
【請求項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。
7. The method according to claim 4, wherein the amount of urea peroxide introduced into the acid bath is not more than 1.2% by weight.
【請求項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。
8. The method according to claim 1, wherein the oxidizing agent is a peroxide salt.
The method described in.
【請求項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。
9. The method according to claim 8, wherein the peroxide salt is a highly oxidizable peroxide salt of titanium or at least one element chemically similar to titanium contained in the pickled product.
【請求項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。
10. The method according to claim 1, wherein the oxidizing agent is a peracid compound.
【請求項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。
11. The method according to claim 10, wherein the peracid compound is titanium or a peracid compound of at least one element chemically similar to titanium contained in the pickled product.
【請求項12】チタンと化学的に類似な元素がバナジウ
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。
12. The method according to claim 1, wherein the element chemically similar to titanium is vanadium, zirconium, niobium, tantalum 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)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
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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JPH04501139A JPH04501139A (en) 1992-02-27
JP2945136B2 true JP2945136B2 (en) 1999-09-06

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CA (1) CA2037893C (en)
DE (1) DE69013447T2 (en)
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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.
JP3751324B2 (en) * 1993-12-10 2006-03-01 忠弘 大見 Substrate surface cleaning method and surface cleaning agent
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

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RU2168560C2 (en) 2001-06-10
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FR2650303A1 (en) 1991-02-01
ES2064686T3 (en) 1995-02-01
KR100191864B1 (en) 1999-06-15
JPH04501139A (en) 1992-02-27
ATE113080T1 (en) 1994-11-15
FI93371B (en) 1994-12-15
FI911398A0 (en) 1991-03-22
KR920701524A (en) 1992-08-11
AU634277B2 (en) 1993-02-18
CA2037893C (en) 2001-07-24
EP0415807B1 (en) 1994-10-19
FR2650303B1 (en) 1993-12-10
CA2037893A1 (en) 1991-01-27
EP0415807A2 (en) 1991-03-06
EP0415807A3 (en) 1991-03-20
DE69013447D1 (en) 1994-11-24
DE69013447T2 (en) 1995-02-23
WO1991002109A1 (en) 1991-02-21

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