JPS60211083A - Process for stripping thermal barrier coating - Google Patents
Process for stripping thermal barrier coatingInfo
- Publication number
- JPS60211083A JPS60211083A JP6787784A JP6787784A JPS60211083A JP S60211083 A JPS60211083 A JP S60211083A JP 6787784 A JP6787784 A JP 6787784A JP 6787784 A JP6787784 A JP 6787784A JP S60211083 A JPS60211083 A JP S60211083A
- Authority
- JP
- Japan
- Prior art keywords
- mineral acid
- thermal barrier
- barrier coating
- acid
- pref
- 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.)
- Granted
Links
Abstract
Description
【発明の詳細な説明】
発明の目的
本発明は、ジェットエンジンの燃焼室の噴射ガコーチン
グに際し、剥離が極めて困難な、元のサーマルバリヤー
コーチングの剥離法に関し、その目的とするところは温
和な条件下で簡易かつ完全な剥離を行なうための方法を
提供することにある。DETAILED DESCRIPTION OF THE INVENTION OBJECTS OF THE INVENTION The present invention relates to a method for removing the original thermal barrier coating, which is extremely difficult to remove, during injection gas coating of the combustion chamber of a jet engine. The object of the present invention is to provide a method for simple and complete peeling.
従来の技術
従来、アルカリ土類金属セラミックスおよび遷移金属セ
ラミックス、遷移金属合金よりなる単層/および多層コ
ーチングよりなるサーマルバリヤーコーチングの剥離法
としてはつぎの方法が挙げられる。すなわち、第一には
高温下で強酸溶液または強アルカリ溶液により処理し、
成分元素を塩の形として剥離させる方法であり、第二は
機械的な研磨法である。しかしながら、前記第一の方法
では高温を使用するにも拘わらず、剥離にかなりの長時
間を要し、剥離自体にも斑を生じやすい。BACKGROUND OF THE INVENTION Conventionally, the following methods have been used to remove thermal barrier coatings consisting of single-layer/multilayer coatings made of alkaline earth metal ceramics, transition metal ceramics, and transition metal alloys. That is, firstly, it is treated with a strong acid solution or a strong alkaline solution at high temperature,
The second method is to remove component elements in the form of salt, and the second method is mechanical polishing. However, although the first method uses high temperatures, it takes a considerable amount of time to peel off, and the peeling itself tends to cause spots.
また、母材の腐蝕などを生じやすい欠点があり、再コー
チングの密着性にも問題がある。さらには近時の省エネ
ルギー対策および廃蒸気や廃液処理など公害対策の面で
も問題がある。第二の方法で縮されるものの、母材の肉
厚減少による破壊事故や母材の変形などの問題がある。Additionally, it has the disadvantage that it tends to cause corrosion of the base material, and there are also problems with the adhesion of re-coating. Furthermore, there are also problems in terms of recent energy conservation measures and pollution control measures such as waste steam and waste liquid treatment. Although the second method reduces shrinkage, there are problems such as breakage accidents and deformation of the base material due to a decrease in the thickness of the base material.
さらに剥離後を生じ、第一の方法と同様に再コーチング
の密着性にも問題がある。Furthermore, peeling occurs, and as with the first method, there is also a problem in adhesion during recoating.
発明の構成
本発明者らは、これらの点に鑑みて鋭意検討した結果、
前記第一の方法において、塩化アンモニウムまたは臭化
アンモニウムを含む鉱酸酸性溶液が母材表面を損傷する
ことなく、コーチングの剥離を促進することを見出し、
本発明に到達したものである。すなわち、本発明はクロ
ム、コバルト、ニッケル、ジルコニア、イツトリウムな
どの周期表第4、第5、第6周期の遷移金属の合金/お
よびそのセラミックス誘導体ならびにアルカリ土類金属
セラミックスの単層/および多層コーチングよりなるサ
ーマルバリヤーコーチングを鉱酸溶液で前処理した後、
塩化アンモニウムまたは臭化アンモニウムを含む鉱酸酸
性溶液中において幹熱姓埋≠後処理りすることを特徴と
するサーマルバリヤーコーチングの剥離法である。Structure of the Invention As a result of intensive study in view of these points, the present inventors have found that:
In the first method, it has been discovered that a mineral acid solution containing ammonium chloride or ammonium bromide promotes peeling of the coating without damaging the base material surface,
This has led to the present invention. That is, the present invention relates to alloys of transition metals in periods 4, 5, and 6 of the periodic table, such as chromium, cobalt, nickel, zirconia, and yttrium, and ceramic derivatives thereof, and single-layer/and multi-layer coatings of alkaline earth metal ceramics. After pretreatment with mineral acid solution, the thermal barrier coating consists of
This is a stripping method for thermal barrier coatings, which is characterized by thermal embedding and post-treatment in a mineral acidic solution containing ammonium chloride or ammonium bromide.
本発明において、前処理における鉱酸溶液および後処理
における鉱酸酸性溶液の鉱酸は塩酸、硫酸、リン酸など
の無機酸である。本発明の1熱処理において、塩化アン
モニウムまたは臭化アンモニウムを使用することが必須
である。これは酸、アルカリに不溶性または難溶性の酸
化物などによるサーマルバリヤーコーチングをいったん
、可溶性あるいは易溶性のアンモニウム錯体に変換させ
る作用にもとすくものと考えられる。すなわち、従来の
酸、アルカリを用いた剥離法に代って特定のアンモニア
の化合物を用いることによって、サーマルバリヤーコー
チングの剥離がきわめて容易になる。In the present invention, the mineral acid in the mineral acid solution in pre-treatment and the mineral acid solution in post-treatment is an inorganic acid such as hydrochloric acid, sulfuric acid, or phosphoric acid. In one heat treatment of the present invention, it is essential to use ammonium chloride or ammonium bromide. This is thought to be due to the effect of converting the thermal barrier coating, which is an oxide that is insoluble or poorly soluble in acids and alkalis, into a soluble or easily soluble ammonium complex. That is, by using a specific ammonia compound in place of conventional acid or alkali stripping methods, stripping of thermal barrier coatings becomes extremely easy.
本発明において 8条件は、使用
されるアンモニアのハロゲン化物の酸性溶液によって適
宜選定されるが、水の還流下、100℃以下、好ましく
は80〜95℃で、5〜8時間程度加熱反応せしめれば
よい。その際の処理液量は原試料単位重量当り、5〜3
0容量、好ましくは15〜20容量程度である。また、
前処理および後処理における鉱酸の濃度は3〜35重量
%、好ましくは5〜20重量%程度である。鉱酸の濃度
が3重量%より低い場合は剥離が不充分となり、35重
量%より高い場合は装置の材質、廃水の問題から好まし
くない。さらに塩化アンモニウムまたは臭化アンモニウ
ムの濃度は3〜30重量%、好ましくは5〜20重量%
程度である。アンモニウム化合物の濃度が3重量%より
低い場合は剥離が不充分となり、30重量%より高くし
ても特に効果の向上は見られない。In the present invention, the 8 conditions are appropriately selected depending on the acidic solution of ammonia halide used, but the reaction is carried out under reflux of water at 100°C or lower, preferably 80 to 95°C, for about 5 to 8 hours. Bye. The amount of processing liquid at that time is 5 to 3 per unit weight of the original sample.
0 capacity, preferably about 15 to 20 capacity. Also,
The concentration of mineral acid in the pre-treatment and post-treatment is about 3 to 35% by weight, preferably about 5 to 20% by weight. If the concentration of mineral acid is lower than 3% by weight, peeling will be insufficient, and if it is higher than 35% by weight, it is not preferable due to problems with the material of the device and waste water. Furthermore, the concentration of ammonium chloride or ammonium bromide is 3 to 30% by weight, preferably 5 to 20% by weight.
That's about it. If the ammonium compound concentration is lower than 3% by weight, peeling will be insufficient, and if it is higher than 30% by weight, no particular improvement in effectiveness will be observed.
以下、実施例を挙げ本発明を更に具体的に説明する。実
施例中のチはすべて重量%を示す。Hereinafter, the present invention will be explained in more detail with reference to Examples. All numbers in the examples indicate weight %.
実施例 1゜
マグネシウムジルコネート、コバルト・クロムψアルミ
ニウムeイツトリウム合金からなる多層流する。該コー
チングを水洗後、さらに塩化アンモニウム15%を含む
5チ塩化水素水溶液にて90℃、3時間還流を行なう。Example 1 Multilayer flow consisting of magnesium zirconate, cobalt chromium ψ aluminum e yttrium alloy. After washing the coating with water, it is further refluxed at 90° C. for 3 hours in an aqueous solution of 5% hydrogen chloride containing 15% ammonium chloride.
′ 水洗したのち乾燥する。剥離 i会化薔けるコーチングの剥離は不充分かつ斑がある。 ′ Wash with water and then dry. Peeling The peeling of the coating is insufficient and patchy.
実施例 2゜
る。還流後、充分水洗し、乾燥させた試料の剥離表面は
第1図と同じ表面状態を有する。Example 2. After refluxing, the peeled surface of the sample, which was thoroughly washed with water and dried, had the same surface condition as shown in FIG.
実施例 3゜
流径、充分水洗し乾燥させた試料の剥離表面は第1図と
同じ表面状態を有する。Example 3 The peeled surface of a sample with a flow diameter of 3°, thoroughly washed with water and dried has the same surface condition as in FIG.
実施例 4゜
る。還流後、充分水洗し乾燥させた試料の剥離表面は第
1図と同じ状態を有する。Example 4. After refluxing, the peeled surface of the sample, which was thoroughly washed with water and dried, had the same condition as shown in FIG.
実施例 5゜
チングの剥離状態は良好で、腐蝕や粒界浸食の発生も認
められない。Example 5 The peeling state of the 5° scratch was good, and no corrosion or grain boundary erosion was observed.
実施例 6゜
90℃、2時間処理したのち、15%塩化アンモニウム
を含む5%*化水素水溶液Jo〜90℃、チングの剥離
状態は良好で、腐蝕や粒界浸食の発生も認められない。Example 6 After treatment at 90°C for 2 hours, a 5%* hydrogen hydride aqueous solution containing 15% ammonium chloride was heated to ~90°C. The peeling state of the tings was good, and no corrosion or grain boundary erosion was observed.
第1図は、本発明方法による剥離後の表面状態について
の顕微鏡写真(X100)を示す。
第2図は、剥離前のコーチング表面状態についての顕微
鏡写真(X100)を示す。
第3図A、Bは、従来法の濃塩酸水溶液(35重量%)
で5時間還流した後の剥離状態についての顕微鏡写真で
、A(X60)、B(X100)を示す。
第4図と第5図は、本発明方法による剥離後の断面の顕
微鏡写真(X500)を示す。
特許出願人 岩 1) 正 巳
図面の?’(’i!>(内rFに変更なし)Xso。
手続補正書(方式)
%式%
3、補正をする者
事件との関係 出 願 人
住所
へ名 震0正乙
4、代理人
5、補正命令の日付 昭和ゴ年 7月3I日(発送日)
明細書第8頁の図面の簡単な説明の欄を次のように補正
する。
「第1図は、本発明方法による剥離後の金属組織の表面
状態についての顕微鏡写真(X100)を示す。
第2図は、剥離前の金属組織のコーチング表面状態につ
いての顕微鏡写真(X100)を示す。
第6図A、Bは、従来法の濃塩酸水溶液(65重量%)
で5時間還流した後の剥離状態についての金属組織の顕
微鏡写真で、A’(X60)、B(X100)を示す。
第4図と第5図は、本発明方法による剥離後の金属組織
の断面の顕微鏡写真(X500)を示す。」FIG. 1 shows a micrograph (X100) of the surface condition after peeling according to the method of the present invention. FIG. 2 shows a micrograph (X100) of the coating surface condition before peeling. Figure 3 A and B show concentrated hydrochloric acid aqueous solution (35% by weight) of the conventional method.
A (X60) and B (X100) are micrographs showing the peeled state after refluxing for 5 hours. 4 and 5 show micrographs (X500) of the cross section after peeling according to the method of the present invention. Patent applicant Iwa 1) Masami drawing? '('i!>(no change in rF) Date of amendment order: July 31, Showa Go (shipping date)
The column for a brief description of the drawings on page 8 of the specification is amended as follows. "Figure 1 shows a micrograph (X100) of the surface condition of the metal structure after peeling by the method of the present invention. Figure 2 shows a micrograph (X100) of the coating surface condition of the metal structure before peeling. Figures 6A and B show concentrated hydrochloric acid aqueous solution (65% by weight) of the conventional method.
A' (X60) and B (X100) are micrographs of the metal structure in a peeled state after refluxing for 5 hours. FIGS. 4 and 5 show micrographs (X500) of cross-sections of metal structures after peeling according to the method of the present invention. ”
Claims (3)
マルバリヤーコーチングを鉱酸溶液で前処理した後、塩
化アンモニウムまたは臭化アンそニウムを含む鉱酸酸性
溶液中においてfl熱処理することを特徴とするサーマ
ルバリヤーコーチングの剥離方法。(1) A thermal barrier coating consisting of a single layer or/and a multilayer coating is pretreated with a mineral acid solution and then subjected to fl heat treatment in a mineral acid solution containing ammonium chloride or amthonium bromide. How to remove barrier coating.
れた少なくとも一種の酸である特許請求の範囲第1項に
記載の剥離方法。(2) The stripping method according to claim 1, wherein the mineral acid is at least one acid selected from inorganic acids such as hydrochloric acid, sulfuric acid, and phosphoric acid.
ウムを含む鉱酸酸性溶液の還流下で実施する特許請求の
範囲第1項に記載の剥離方法。(3) The peeling method according to claim 1, wherein the passion treatment is carried out under reflux of a mineral acid solution containing ammonium chloride or ammonium bromide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6787784A JPS60211083A (en) | 1984-04-05 | 1984-04-05 | Process for stripping thermal barrier coating |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6787784A JPS60211083A (en) | 1984-04-05 | 1984-04-05 | Process for stripping thermal barrier coating |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60211083A true JPS60211083A (en) | 1985-10-23 |
JPS6316466B2 JPS6316466B2 (en) | 1988-04-08 |
Family
ID=13357575
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6787784A Granted JPS60211083A (en) | 1984-04-05 | 1984-04-05 | Process for stripping thermal barrier coating |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60211083A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090220805A1 (en) * | 2006-04-05 | 2009-09-03 | Pirelli Tyre S.P.A. | Method for Processing a Crosslinkable Elastomeric Composition Comprising Silica |
-
1984
- 1984-04-05 JP JP6787784A patent/JPS60211083A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090220805A1 (en) * | 2006-04-05 | 2009-09-03 | Pirelli Tyre S.P.A. | Method for Processing a Crosslinkable Elastomeric Composition Comprising Silica |
US8444888B2 (en) * | 2006-04-05 | 2013-05-21 | Pirelli Tyre S.P.A. | Method for processing a crosslinkable elastomeric composition comprising Silica |
Also Published As
Publication number | Publication date |
---|---|
JPS6316466B2 (en) | 1988-04-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5705082A (en) | Roughening of metal surfaces | |
JP2004525254A5 (en) | ||
JP2007138934A (en) | Coating substrate forming method and stripping method | |
JP2000212783A5 (en) | ||
JP2000212783A (en) | Method for removing high temperature corrosion product from diffusion aluminide coating | |
JP2008174839A (en) | Method of surface treating metallic article, and solution system | |
US5205874A (en) | Process of protecting metallic and wood surfaces using silicate compounds | |
JP3023222B2 (en) | Hard austenitic stainless steel screw and its manufacturing method | |
GB2257395A (en) | Etching solution for removing metallic hot gas corrosion protective layers and hot gas reaction coatings from engine blades | |
CA2413640A1 (en) | Process for rejuvenating a diffusion aluminide coating | |
JPS60211083A (en) | Process for stripping thermal barrier coating | |
CN1047347A (en) | Hot dipping calorization process for low-carbon steel | |
CN106757236A (en) | Improve the method and palladium film layer of stainless steel surfaces palladium film layer decay resistance | |
JP3497483B2 (en) | Corrosion resistant coating material and method for producing the same | |
US3617345A (en) | Method of manufacturing aluminum coated ferrous base articles | |
JP2005518328A (en) | Method for metallizing titanate-based ceramics | |
KR100436597B1 (en) | Method for plating with molten aluminum | |
KR102605141B1 (en) | Plating processing method for surface treatment of metal | |
RU2569858C2 (en) | Preparation method of parts for soldering | |
JP2003034887A (en) | Method for removing oxidation resistant film on hot member surface | |
JPS61250180A (en) | Treatment for black coloring of stainless steel | |
JPS62263976A (en) | Treatment of aluminized surface | |
IT202100025232A1 (en) | METHOD OF REMOVING A CERAMIC THERMAL BARRIER COATING | |
JPH05214578A (en) | Production of noble metal electrocasting | |
JP2941560B2 (en) | Surface treatment method for polypropylene lining |