JPS6041148B2 - Phosphate film conversion treatment method for metal surfaces - Google Patents
Phosphate film conversion treatment method for metal surfacesInfo
- Publication number
- JPS6041148B2 JPS6041148B2 JP52058482A JP5848277A JPS6041148B2 JP S6041148 B2 JPS6041148 B2 JP S6041148B2 JP 52058482 A JP52058482 A JP 52058482A JP 5848277 A JP5848277 A JP 5848277A JP S6041148 B2 JPS6041148 B2 JP S6041148B2
- Authority
- JP
- Japan
- Prior art keywords
- metal surface
- phosphate film
- water
- washing
- items
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/78—Pretreatment of the material to be coated
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Treatment Of Metals (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
【発明の詳細な説明】
本発明は金属表面にリン酸塩皮膜化成処理方法、更に詳
しくは、多段式水洗工程を有する金属表面洗浄処理装置
を用いて実施する場合にも特に有用な処理方法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for chemical conversion treatment of a metal surface with a phosphate film, and more particularly, to a treatment method which is particularly useful when carried out using a metal surface cleaning treatment apparatus having a multi-stage water washing process. .
なお、本発明にあって「金属表面」とは、鉄、亜鉛およ
びそれらの合金の表面を指称する。一般に、金属表面は
リン酸塩皮膜化成を行うにあたり、脱脂、水洗される。In the present invention, the term "metal surface" refers to surfaces of iron, zinc, and alloys thereof. Generally, metal surfaces are degreased and washed with water before forming a phosphate film.
脱脂された金属表面は、残留した脱脂液や油分を除去す
るため水洗され、次いで皮膜化成に供される。また、金
属表面に塗装下地として十分な性能を有するリン酸塩皮
膜を形成させるため、脱脂、水洗された金属表面は皮膜
化成に先立って前調整がなされることもある。例えば、
リン酸塩とチタン化合物を含む中性もしくは微アルカリ
性の水溶液を金属表面に接触せしめて、金属表面を活性
化しリン酸塩皮膜化成処理液との反応性を高めることに
より、均一微細な化成皮膜を形成する方法が行なわれて
いる(特公昭39−7125号参照)。しかしながら、
この方法では以下に示すような問題点が起生する。■
脱脂された金属表面は反応性に富んでいるため、金属表
面洗浄処理装置の設計や脱脂後の水洗条件によっては、
リン酸塩皮膜化成される前に発錆する問題がある。The degreased metal surface is washed with water to remove residual degreasing liquid and oil, and then subjected to film formation. Furthermore, in order to form a phosphate film having sufficient performance as a paint base on a metal surface, the degreased and water-washed metal surface is sometimes preconditioned prior to film formation. for example,
A neutral or slightly alkaline aqueous solution containing a phosphate and a titanium compound is brought into contact with the metal surface to activate the metal surface and increase its reactivity with the phosphate film chemical conversion treatment solution, thereby forming a uniform and fine chemical conversion film. A method of forming such a material has been used (see Japanese Patent Publication No. 39-7125). however,
This method causes the following problems. ■
Degreased metal surfaces are highly reactive, so depending on the design of the metal surface cleaning treatment equipment and the water washing conditions after degreasing,
There is a problem that rust occurs before the phosphate film is formed.
■ 脱脂された金属表面の温度が高かったり、各工程間
の移送時間が長いと、金属表面は皮膜化成工程に入る前
に水乾きして黄錆や点錆が生じ、不均一で粗な化成皮膜
が形成されることになる。■ 連続式金属表面洗浄処理
装置を用いての化成処理が途中で余儀なく休止した場合
には、脱脂一皮膜化成工程間で滞留した処理物は全面発
錆し、皮膜化成に供することができなくなる。■ If the temperature of the degreased metal surface is high or the transfer time between each process is long, the metal surface dries with water before entering the film formation process, causing yellow rust and spot rust, resulting in uneven and rough chemical formation. A film will be formed. ■ If chemical conversion treatment using a continuous metal surface cleaning treatment equipment is forced to stop midway through, the treated material that has remained between the degreasing and film formation processes will rust over the entire surface and cannot be used for film formation.
最近、洗浄用水の節約、排水処理量の軽減等に利する多
段式水洗装置や処理室内に排気設備を設け処理室内の空
気を排出せしめることにより余剰水量を蒸発除去せしめ
て該余剰水の廃水としての排出を減少もしくはなくす手
段と、多段水洗工程として供給水量を減少せしめる手段
を具備するクローズドシステム金属表面洗浄処理装置(
例えば特関昭48−69728号参照)等が当該リン酸
塩皮膜化成処理に広く採用されるようになっているが、
かかる装置を使用する場合に特に前掲の発錆が問題とな
っている。一方、このような情況下で、脱脂された金属
表面を皮膜化成に先立ちアルカリ性溶液で処理すること
により、金属表面の発錆を防止する方法が提供されてい
る(特開昭52一6343号参照)。Recently, multi-stage washing equipment and exhaust equipment have been installed in the processing chamber to save washing water and reduce the amount of wastewater to be treated, and by discharging the air in the processing chamber, the excess water is evaporated and removed, and the excess water is used as wastewater. Closed system metal surface cleaning treatment equipment (
For example, Tokusei No. 48-69728) has become widely adopted for the phosphate film chemical conversion treatment.
When such equipment is used, the above-mentioned rust formation is especially a problem. On the other hand, under such circumstances, a method has been proposed for preventing rust on the metal surface by treating the degreased metal surface with an alkaline solution prior to film formation (see JP-A-52-6343). ).
しかし、これも防錆効果は十分でなく、上述の多段式水
洗装置やクローズドシステム金属表面洗浄処理装置を使
用する時には金属表面の発錆は避け難く、またアルカリ
性溶液の皮膜化成処理槽への過剰量の特込みは、浴平衡
をくずし化成不良の原因となる。本発明はかかる問題点
を解消したもので、その目的は第1に、脱脂された金属
表面を水洗工程で防錆し、連続式金属表面洗浄処理装置
を用いての化成処理が途中で余儀なく休止した場合にも
、脱脂された金属表面が発錆することなく、多段式水洗
装置やクローズドシステム金属表面洗浄処理装置の使用
を可能とする金属表面のリン酸塩皮膜化成処理方法を提
供することにあり、第2に、金属表面の皮膜化成性を促
進し、皮膜化成工程に何らの悪影響を及ぼさず、特に霞
着塗装下地に適した均一繊密なリン酸塩皮膜を形成する
ことを可能とする金属表面のリン酸塩皮膜化成処理方法
を提供することにある。However, this also does not have a sufficient rust prevention effect, and when using the above-mentioned multi-stage water washing equipment or closed system metal surface cleaning equipment, it is difficult to avoid rusting on the metal surface, and excessive alkaline solution is added to the film conversion treatment tank. If the amount is too specific, the bath balance will be disrupted and this will cause poor chemical formation. The present invention solves these problems, and its first purpose is to prevent the degreased metal surface from rusting in the water washing process, thereby forcing the chemical conversion treatment using a continuous metal surface cleaning treatment device to stop midway through. To provide a method for chemically converting a phosphate film onto a metal surface, which enables the use of a multi-stage water washing device or a closed system metal surface cleaning treatment device, without causing rust on the degreased metal surface even when the metal surface is degreased. Second, it promotes the film formation properties of metal surfaces, does not have any negative effect on the film formation process, and makes it possible to form a uniform and dense phosphate film that is particularly suitable for use as a base for haze painting. An object of the present invention is to provide a method for chemically treating a metal surface with a phosphate film.
本発明者らは、上記目的を達成するため鋭意研究を進め
た結果、当該リン酸塩皮膜化成処理における一連の工程
において、脱脂工程と皮膜化成工程間に行なわれている
水洗工程として、単なる水を使用するのでなく、酸化性
物質0.01〜0.5(重量%、以下同様)を含有する
水溶液を使用することにより、所期目的のリン酸塩皮膜
化成処理方法が有効に実施されうろことを見出し、本発
明を完成するに至った。As a result of intensive research to achieve the above object, the present inventors found that in the series of steps in the phosphate film chemical conversion treatment, the water washing process that is carried out between the degreasing process and the film formation process is simply water-based. By using an aqueous solution containing 0.01 to 0.5 (wt%) of an oxidizing substance (the same applies hereinafter) instead of using a They discovered this and completed the present invention.
本発明の要旨は、金属表面を脱脂する工程、脱脂された
金属表面を酸化性物質0.01〜0.5%を含む水溶液
で洗浄する工程、金属表面にリン酸塩皮膜を化成する工
程、および化成された金属表面を水洗する工程からなる
ことを特徴とする金属表面のリン酸塩皮膜化成処理方法
に存する。The gist of the present invention is a step of degreasing a metal surface, a step of cleaning the degreased metal surface with an aqueous solution containing 0.01 to 0.5% of an oxidizing substance, a step of chemically forming a phosphate film on the metal surface, and a method for chemical conversion treatment of a phosphate film on a metal surface, comprising the steps of washing the chemically converted metal surface with water.
本発明方法における金属表面を脱脂する工程は、常法に
準じ溶剤脱脂、ェマルジョン脱脂、アルカリ脱脂または
これらの組合わせから適宜採用されてよいが、特にアル
カリ脱脂が一般的である。The step of degreasing the metal surface in the method of the present invention may be appropriately carried out by conventional methods such as solvent degreasing, emulsion degreasing, alkaline degreasing, or a combination thereof, with alkaline degreasing being particularly common.
このアルカリ脱脂の場合、通常の市販脱脂剤(例えば弱
アルカリ系脱脂剤として日本ペイント社製商品名「リド
リン#7卵−4一等、中アルカリ系脱脂剤として同社製
商品名「リドリン#100州−1一等、および強アルカ
リ系脱脂剤として同社製商品名「リドリン#5洲−4一
等)を通常1〜2%含む水溶液を使用し、温度40〜6
0℃、時間0.5〜5分の条件で実施すればよい。In the case of alkaline degreasing, use ordinary commercially available degreasers (for example, Nippon Paint Co., Ltd.'s product name "Ridrin #7 Egg-41" as a weak alkaline degreaser, and "Ridrin #100" manufactured by Nippon Paint Co., Ltd. as a medium alkaline degreaser). -1 grade, and a strong alkaline degreasing agent manufactured by the same company under the trade name "Ridrine #5-41 grade", using an aqueous solution containing usually 1 to 2%, and at a temperature of 40 to 6
It may be carried out at 0° C. for 0.5 to 5 minutes.
なお、脱脂浴には次工程に使用する酸化性物質(具体的
には後述するが、その中で例えば亜硝酸ナトリウムおよ
び過棚酸ナトリウム)を0.002%以上、好ましくは
0.01%以上含有させることが望ましい。本発明方法
における上記脱脂工程の次に実施される洗浄工程は、脱
脂された金属表面に残留する油分、溶剤、アルカリ性物
質等を除去することは勿論のこと、本発明の所期目的で
ある防錆効果を付与しうるものであって、酸化怪物質を
含む水溶液(以下、洗浄液と称す)を使用することを特
徴とする。The degreasing bath contains 0.002% or more, preferably 0.01% or more of oxidizing substances to be used in the next step (specifically described below, but among them, for example, sodium nitrite and sodium pershelate). It is desirable to include it. The cleaning step performed after the degreasing step in the method of the present invention not only removes oils, solvents, alkaline substances, etc. remaining on the degreased metal surface, but also removes oil, solvents, alkaline substances, etc., which is the intended purpose of the present invention. It is characterized by the use of an aqueous solution (hereinafter referred to as a cleaning solution) that can impart a rusting effect and contains an oxidizing substance.
上記酸イヒ性物質としては、リン酸塩皮膜化成の促進剤
として採用されているものであって、例えば函硝酸塩(
亜硝酸ナトリウムなど)、過酸化水素、過棚酸塩(過棚
酸ナトリウムなど)、芳香族ニトロ化合物(メタニトロ
ベンゼンスルフオン酸ナトリウムなど)、芳香族ニトロ
ソ化合物(ニトロソベンゼンなど)、硫酸ヒドロキシル
アミン、塩素酸ナトリウムおよび過硫酸アンモニウムが
挙げられ、これらの群から選ばれる少なくとも1種を用
に供する。The above-mentioned acidic substances include those that are used as accelerators for phosphate film formation, such as nitrate (
(e.g., sodium nitrite), hydrogen peroxide, persylates (e.g., sodium perselate), aromatic nitro compounds (e.g., sodium metanitrobenzene sulfonate), aromatic nitroso compounds (e.g., nitrosobenzene), hydroxylamine sulfate, Examples include sodium chlorate and ammonium persulfate, and at least one selected from these groups is used.
特に、亜硝酸ナトリウム、過酸化水素、過棚酸ナトリウ
ムが好適である。か)る洗浄液において、酸化性物質の
含有量は、好ましくは0.01〜0.5%の範囲で選定
する。この含有量が0.01%未満であると、脱脂され
た金属表面に十分な防錆効果を付与し難く、また0.5
%を越えてもそれ以上の防錆効果は得られない。なお、
上記酸化性物質以外に、例えば先の特公昭39−712
5号に開示のリン酸塩とチタン化合物(硫酸チタン、酸
化チタンなど)を含む中性もしくは微アルカリ性の水溶
液、即ち表面活性化剤を添加含有させてもよいM酸化性
物質と表面活性化剤の相剰効果により、皮膜化成性がよ
り一層改善され、特に電着塗装下地として適切な均一繊
密なリン酸塩皮膜が形成される。Particularly suitable are sodium nitrite, hydrogen peroxide, and sodium pershelate. In the above cleaning liquid, the content of the oxidizing substance is preferably selected in the range of 0.01 to 0.5%. If this content is less than 0.01%, it is difficult to impart a sufficient rust prevention effect to the degreased metal surface, and
%, no further rust prevention effect can be obtained. In addition,
In addition to the above-mentioned oxidizing substances, for example,
A neutral or slightly alkaline aqueous solution containing a phosphate and a titanium compound (titanium sulfate, titanium oxide, etc.) disclosed in No. 5, that is, an M oxidizing substance and a surface activator that may contain a surface activator. Due to the mutual effect of these, the film formation properties are further improved, and a uniform and dense phosphate film is formed, which is particularly suitable as a base for electrodeposition coating.
表面活性化剤の含有量は、通常チタニウム濃度がlop
pm以上、好ましくは脱脂後の最終洗浄液のチタニウム
濃度が10〜100ppmとなるような範囲で選定すれ
ばよい。チタニウム濃度が100ppmを越えると、金
属表面は過剰に活性化して化成不良を来たすことになる
。更に、次工程の皮膜化成に悪影響を及ぼさない範囲で
種々の界面活性化剤、有機酸、無機酸、アルカリ性物質
等を添加含有させてもよい。以上の如くして構成される
洗浄液は、通常4〜9のpH値に設定されていることが
望ましい。pHが4より低いと、脱脂された金属表面に
十分な防錆効果を付与し難く、また9より高いと、次工
程の皮膜化成性を阻害する。当該洗浄工程は、従来法の
水洗工程と同様1段または2段以上の多段数で行なって
よく、またその条件としては通常室温〜800○の温度
、0.5〜5分の時間が採用されてよい。The content of the surface activator is usually determined as the titanium concentration is lop
pm or more, preferably in a range such that the titanium concentration in the final cleaning solution after degreasing is 10 to 100 ppm. If the titanium concentration exceeds 100 ppm, the metal surface will be excessively activated, resulting in poor chemical formation. Furthermore, various surfactants, organic acids, inorganic acids, alkaline substances, etc. may be added to the extent that they do not adversely affect the film formation in the next step. It is desirable that the cleaning liquid configured as described above is usually set at a pH value of 4 to 9. If the pH is lower than 4, it is difficult to impart a sufficient antirust effect to the degreased metal surface, and if it is higher than 9, the film formation property in the next step is inhibited. The washing step may be carried out in one stage or in multiple stages, such as two or more stages, as in the conventional water washing step, and the conditions are usually a temperature of room temperature to 800° and a time of 0.5 to 5 minutes. It's fine.
従来法において水洗温度が40qC以上だと、脱脂、水
洗された金属表面は水乾きして発錆を招く結果となるが
、本発明の場合では同様に水乾きしても発錆は起こらず
、次工程の皮膜化成性に悪影響を及ぼすことがなく、洗
浄温度を特別管理する必要は免がれる。本発明方法にお
ける皮膜化成工程は、通常のリン酸鉄皮膜化成処理剤(
例えば日本ペイント社製商品名「ヂュリヂン#21船一
等)、リン酸亜鉛皮膜化成処理剤(例えば同社製商品名
「グラノヂソ#1鮒−2一等)、カルシウム変性リン酸
亜鉛皮膜化成処理剤(例えば同社製商品名「グラノヂン
#21N」等)が使用されてよく、それぞれの仕様に従
って通常の条件で実施すればよい。In the conventional method, if the water washing temperature is 40 qC or higher, the degreased and washed metal surface dries with water and causes rust, but in the case of the present invention, rust does not occur even if the metal surface is similarly dried with water. There is no adverse effect on the film formation properties in the next step, and there is no need to specially control the cleaning temperature. The coating chemical conversion step in the method of the present invention is performed using a common iron phosphate coating chemical conversion treatment agent (
For example, Nippon Paint Co., Ltd.'s product name "Durijin #21 Funa-1, etc.", zinc phosphate film chemical conversion treatment agent (for example, Nippon Paint's product name "Granodiso #1 Carp-21, etc."), calcium-modified zinc phosphate film chemical conversion treatment agent ( For example, products manufactured by the same company under the trade name "Granodin #21N" may be used, and the test may be carried out under normal conditions according to the respective specifications.
なお、カルシウム変性リン酸亜鉛皮膜化成を行なう場合
には、先の洗浄工程で酸化性物質として過棚酸ナトリウ
ムを使用し、且つこれにアルカリ性物質を添加してもよ
い。何故なら、カルシウム変性リン酸亜鉛皮膜化成は、
金属表面の影響を受け易く、わずかに発錆してし、ても
化成不良を生じる煩向が強いが、過柵酸ナトリウムとア
ルカリ性物質を含む洗浄液を適用すると、洗浄された金
属表面は皮膜化成工程前の発錆が防止されるのみならず
、カルシウム変性リン酸亜鉛皮膜化成性が極めて改善さ
れるからである。かかるアルカリ性物質としては、リン
酸塩皮膜化成において一般に使用されているものであっ
てよく、例えば水酸化ナトリウム、炭酸ナトリウム、重
炭酸ナトリウム、メタケィ酸ナトリウム、オルソケィ酸
ナトリウム、オルソリン酸ナトリウム、ピロリン酸ナト
リウム、トリポリリン酸ナトリウム、テトラリン酸ナト
リウムおよびへキサリン酸ナトリウムが挙げられる。上
述の三工程、即ち脱脂工程、1段または2段以上の洗浄
工程および皮膜化成工程をその順に従って連続的または
非連続的に通常の方式(スプレー法、浸漁法など)で行
なって本発明方法を実施し、次いで通常の1段または2
段以上の水洗工程および乾燥工程を行うことにより、最
終皮膜化成処理物が得られる。この最終品によれば、そ
の一連の処理工程途上および工程後の発錆は全く見られ
ず、結局において均一繊密で高品質の化成皮膜の形成が
認められる。次に、実施例および比較例を挙げて本発明
を具体的に説明する。In addition, when performing calcium-modified zinc phosphate film conversion, sodium pershelate may be used as the oxidizing substance in the previous cleaning step, and an alkaline substance may be added thereto. This is because calcium-modified zinc phosphate film conversion is
It is easily affected by metal surfaces and tends to rust slightly and cause poor chemical formation, but if a cleaning solution containing sodium peroxide and an alkaline substance is applied, the cleaned metal surface will not form a film. This is because not only rusting before the process is prevented, but also the chemical formation properties of the calcium-modified zinc phosphate film are greatly improved. Such alkaline substances may be those commonly used in phosphate film formation, such as sodium hydroxide, sodium carbonate, sodium bicarbonate, sodium metasilicate, sodium orthosilicate, sodium orthophosphate, and sodium pyrophosphate. , sodium tripolyphosphate, sodium tetraphosphate and sodium hexaphosphate. The method of the present invention is carried out by carrying out the above-mentioned three steps, that is, the degreasing step, one or more stages of cleaning step, and film formation step, continuously or discontinuously in that order by a conventional method (spray method, immersion method, etc.). and then the usual 1 or 2 steps.
By performing the water washing step and the drying step in stages or more, the final film chemical conversion treatment product is obtained. According to this final product, no rust was observed during or after the series of treatment steps, and the formation of a uniform, dense, and high quality chemical conversion coating was observed in the end. Next, the present invention will be specifically explained with reference to Examples and Comparative Examples.
実施例 1
本例は、スプレー型多段水洗式パイロットプラントで伶
延鋼板をリン酸亜鉛皮膜化成処理する。Example 1 In this example, a rolled steel sheet is subjected to a zinc phosphate coating chemical conversion treatment in a spray-type multi-stage water-washing pilot plant.
‘1} 処理工程(条件):脱脂(50〜600C、2
分)→第1洗浄(35〜40oo、1分)→第2洗浄(
35〜4000、1分)→第3洗浄(30〜3500、
1分)→皮膜化成(50〜55oo、2分)→第1水洗
(35〜4000、1分)→第2水洗(35〜40二0
、1分)→第3水洗(30〜35qo、1分)→乾燥。
1 脱脂液:弱アルカリ系脱脂剤(日本ペイント社製商
品名「リドリン#7州−4」)1.5%を含む水溶液を
使用。'1} Treatment process (conditions): Degreasing (50-600C, 2
minutes) → 1st wash (35-40oo, 1 minute) → 2nd wash (
35-4000, 1 minute) → 3rd cleaning (30-3500,
1 minute) → Film formation (50-55oo, 2 minutes) → First water washing (35-4000, 1 minute) → Second water washing (35-4000
, 1 minute) → Third washing (30-35 qo, 1 minute) → Drying.
1. Degreasing liquid: An aqueous solution containing 1.5% of a weak alkaline degreasing agent (product name: "Ridrin #7-4" manufactured by Nippon Paint Co., Ltd.) was used.
2 洗浄液:亜硝酸ナトリウム0.03%を含む水溶液
を使用。2 Cleaning liquid: Use an aqueous solution containing 0.03% sodium nitrite.
該洗浄液を3段目の洗浄槽に供給し、1段目の洗浄槽よ
りオーバーフローする。3 皮膜化成処理液:その組成
は以下の通りである。The cleaning liquid is supplied to the third-stage cleaning tank, and overflows from the first-stage cleaning tank. 3. Film chemical conversion treatment solution: Its composition is as follows.
組成
P043−・・・1.50%、Na十・・・0.43%
N03−・・・0.60%、N02−・・・0.013
〜0.016%Zn2十・・・0.16%、pH3.0
4 水洗液:水道水を3段目の水洗槽に供給し、1段目
の水洗槽よりオーバーフローする。Composition P043-...1.50%, Na+...0.43%
N03-...0.60%, N02-...0.013
~0.016%Zn20...0.16%, pH3.0
4. Rinsing liquid: Tap water is supplied to the third-stage washing tank, and overflows from the first-stage washing tank.
■ 結果:形成されるリン酸亜鉛皮膜は良好である。■ Result: The zinc phosphate film formed is good.
洗浄工程の各段での発錆は見られず、しかも連続操作を
途中で中断しても、処理物の発錆は無かった。実施例
2
本例は、実施例1と同じ処理設備および冷延鋼板を使用
しカルシウム変性リン酸亜鉛皮膜化成処理する。No rust was observed at any stage of the cleaning process, and even when the continuous operation was interrupted midway through, no rust was observed on the treated material. Example
2 In this example, the same treatment equipment and cold-rolled steel sheet as in Example 1 were used to carry out chemical conversion treatment for calcium-modified zinc phosphate film.
‘1} 処理工程(条件):皮膜化成の条件を75〜8
0℃、2分とする以外は実施例1に準ずる。'1} Treatment process (conditions): Film formation conditions 75-8
The procedure of Example 1 was followed except that the temperature was 0°C for 2 minutes.
1 脱脂液:強アルカリ系脱脂剤(日本ペイント社製商
品名「リドリン#5洲−4」)1%を含む水溶液を使用
。1. Degreasing liquid: An aqueous solution containing 1% of a strong alkaline degreasing agent (product name: "Ridrin #5-4" manufactured by Nippon Paint Co., Ltd.) was used.
2 洗浄液:週柵酸ナトリウム0.03%を含む水溶液
を使用。2. Cleaning solution: Use an aqueous solution containing 0.03% sodium palate.
3 皮膜化成処理液:その組成は以下の通りである。3. Film chemical conversion treatment solution: Its composition is as follows.
組成
PO43‐・・・0.49%、Na+・・・0.60%
N03−.・.3.60%、N02− ・・・0.
005〜0.01%Ca2十…0.59%、pH2.9
Zn2十…0.17%、4 水洗液:水道水を使用。Composition PO43-...0.49%, Na+...0.60%
N03-.・.. 3.60%, N02-...0.
005~0.01%Ca2...0.59%, pH2.9
Zn20...0.17%, 4 Washing liquid: Use tap water.
■ 結果:良品質のカルシウム変性リン酸亜鉛皮膜が形
成された。■ Result: A calcium-modified zinc phosphate film of good quality was formed.
実施例 3
本例は、スプレー式クローズドシステム金属表面洗浄処
理装置で片面亜鉛メッキ鋼板をリン酸亜鉛皮膜化成処理
する。Example 3 In this example, a single-sided galvanized steel sheet was subjected to a zinc phosphate coating chemical conversion treatment using a spray-type closed system metal surface cleaning treatment apparatus.
○} 処理工程(条件):脱脂(60qo、2分)→第
1洗浄(48〜5〆0、0.8分)→第2洗浄(43〜
470、0.5分)→第3洗浄(38〜420、0.5
分)→皮膜化成(50〜55o0、2分)→第1水洗(
35〜40qo、0.5分)→第2水洗(35〜40o
o、0.5分)→第3水洗(30〜35oo、0.5分
)→第4水洗(室温、0.5分)→乾燥。○} Treatment process (conditions): Degreasing (60qo, 2 minutes) → 1st cleaning (48~5〆0, 0.8 minutes) → 2nd cleaning (43~
470, 0.5 minutes) → 3rd cleaning (38-420, 0.5
minutes) → Film formation (50-55o0, 2 minutes) → First water washing (
35-40qo, 0.5 minutes) → 2nd water washing (35-40qo
o, 0.5 minutes) → 3rd water washing (30-35oo, 0.5 minutes) → 4th water washing (room temperature, 0.5 minutes) → drying.
1 脱脂液:中アルカリ系脱脂剤(日本ベイト社製商品
名「リドリン#100洲−1」)1.5%を含む水溶液
を使用。1. Degreasing liquid: An aqueous solution containing 1.5% of a medium alkaline degreasing agent (product name: "Ridrin #100S-1" manufactured by Nippon Bait Co., Ltd.) was used.
2 洗浄液:3段目の洗浄槽における亜硝酸ナトリウム
の含有量0.02%およびリン酸ナトリウムとチタン化
合物を含む表面活性化剤(日本ペイント社製商品名「フ
ィキソゲン#5」)の含有量0.1%で管理する。2 Cleaning liquid: Content of sodium nitrite in the third stage cleaning tank is 0.02% and content of surface activator containing sodium phosphate and titanium compound (trade name "Fixogen #5" manufactured by Nippon Paint Co., Ltd.) is 0. Manage at .1%.
3段目の洗浄液の供給量500そ/hr。Supply amount of third stage cleaning liquid is 500 so/hr.
3 皮膜化成処理液:その組成は以下の通りである。3. Film chemical conversion treatment solution: Its composition is as follows.
組成
P043−・・・1.10%、Na+・・・0.45%
N03−.・・0.70%、N02− ・・・0.
01〜0.015%Zn2十・・・0.05%、PH3
.44 水洗液:水道水を4段目の水洗槽に700と/
hrで供給し、皮膜化成工程で余剰水を蒸発せしめる。Composition P043-...1.10%, Na+...0.45%
N03-. ...0.70%, N02- ...0.
01~0.015%Zn20...0.05%, PH3
.. 44 Washing liquid: Add tap water to the 4th stage washing tank with 700 ml/
hr, and excess water is evaporated in the film formation process.
■ 結果:鉄面および亜鉛メッキ面共に亀着塗装下地と
して良好な均一繊密な皮膜が形成された。■Results: A uniform, dense film was formed on both the iron and galvanized surfaces, which was suitable as a base for coating.
脱脂工程後の洗浄工程で液温が4000以上となり、処
理物表面は水乾きしたにもかかわらず、発錆は認められ
なかった。比較例 1
実施例1のリン酸亜鉛皮膜化処理において、脱脂後の洗
浄工程の亜硝酸ナトリウム水溶液を水道水に代える以外
は同様な条件で実施した所、不均一で粗な化成皮膜が形
成された。Although the liquid temperature reached 4,000 or higher in the cleaning process after the degreasing process and the surface of the treated product was water-dried, no rust was observed. Comparative Example 1 When the zinc phosphate coating treatment of Example 1 was carried out under the same conditions except that the sodium nitrite aqueous solution in the cleaning step after degreasing was replaced with tap water, an uneven and rough chemical conversion coating was formed. Ta.
即ち、脱脂後の第2水洗および第3水洗後の金属表面に
点錆が認められ、また連続処理が途中で中断すると、脱
脂後の水洗工程で滞留した処理物は全面発錆した。比較
例 2実施例1のリン酸亜鉛皮膜化成処理において、脱
脂後の洗浄工程の亜硝酸ナトリウム水溶液を皮膜化成後
の第1水洗水に代える以外は同様な条件で実施した所、
均一なリン酸亜鉛皮膜は得られなかった。That is, dotted rust was observed on the metal surface after the second and third water washings after degreasing, and when the continuous treatment was interrupted midway, the treated material that remained in the water washing process after degreasing developed rust on the entire surface. Comparative Example 2 The zinc phosphate film chemical conversion treatment of Example 1 was carried out under the same conditions except that the sodium nitrite aqueous solution in the cleaning step after degreasing was replaced with the first washing water after film formation.
A uniform zinc phosphate film was not obtained.
即ち、希釈された皮膜化成処理液により部分的にリン酸
鉄系皮膜が形成され、後の皮膜化成が十分に行われなか
ったものと考えられる。また、脱脂後の第2水洗および
第3水洗後の金属表面に点錆が認められた。比較例 3
実施例1のリン酸亜鉛皮膜化成処理において、脱脂後の
洗浄工程の亜硝酸ナトリウム水溶液を、皮膜化成後の第
1水洗水を水酸化ナトリウムでpH7〜8に中和し沈殿
物を除去した液に代える以外は同様な条件で実施した所
、比較例1と同様に不均一で粗な化成皮膜が形成された
。That is, it is considered that an iron phosphate-based film was partially formed by the diluted film conversion treatment solution, and subsequent film formation was not performed sufficiently. Further, spot rust was observed on the metal surface after the second and third water washings after degreasing. Comparative Example 3 In the zinc phosphate film chemical conversion treatment of Example 1, the sodium nitrite aqueous solution in the cleaning step after degreasing and the first wash water after film formation were neutralized to pH 7 to 8 with sodium hydroxide to remove the precipitate. When the test was carried out under the same conditions except that the removed solution was used, a non-uniform and rough chemical conversion film was formed as in Comparative Example 1.
Claims (1)
化性物質0.01〜0.5重量%を含む水溶液で洗浄す
る工程、該水溶液で洗浄された金属表面にリン酸塩皮膜
を化成する工程、および化成された金属表面を水洗する
工程かな成ることを特徴とする金属表面のリン酸塩皮膜
化成処理方法。 2 酸化性物質が亜硝酸塩、過酸化水素、過硼酸塩、芳
香族ニトロ化合物、芳香族ニトロソ化合物および硫酸ヒ
ドロキシルアミンの群から選ばれる少なくとも1種であ
る上記第1項記載の方法。 3 亜硝酸ナトリウム、過酸化水素および過硼酸ナトリ
ウムの群から選ばれる少なくとも1種を0.01〜0.
5重量%で使用する上記第2項記載の方法。 4 各水洗工程を2段以上の多段水洗として供給水量を
減少せしめる手段を具備する金属表面洗浄処理装置にて
実施する上記第1項〜第3項のいずれかに記載の方法。 5 スプレー式処理室に排気設備を設け処理室内の空気
を排出せしめることにより、余剰水量を蒸発除去せしめ
て該余剰水の廃水としての排出を減少もしくはなくす手
段と、各水洗工程を2段以上の多段水洗として供給水量
を減少せしめる手段とを具備する金属表面洗浄処理装置
にて実施する上記第1項〜第3項のいずれかに記載の方
法。6 リン酸塩皮膜がリン酸鉄皮膜である上記第1項
〜第5項のいずれかに記載の方法。 7 リン酸塩皮膜がリン酸亜鉛皮膜である上記第1項〜
第5項のいずれかに記載の方法。 8 リン酸塩皮膜がカルシウム変性リン酸亜鉛皮膜であ
る上記第1項〜第5項のいずれかに記載の方法。 9 金属表面を脱脂する工程、脱脂された金属表面を酸
化性物質0.01〜0.5重量%とチタン化合物10〜
100ppm(チタニウム濃度換算)とを含む水溶液で
洗浄する工程、該水溶液で洗浄された金属表面にリン酸
塩皮膜を化成する工程、および化成された金属表面を水
洗する工程から成ることを特徴とする金属表面のリン酸
塩皮膜化成処理方法。 10 酸化性物質が亜硝酸塩、過酸化水素、過硼酸塩、
芳香族ニトロ化合物、芳香族ニトロソ化合物および硫酸
ヒドロキシルアミンの群から選ばれる少なくとも1種で
ある上記第9項記載の方法。 11 亜硝酸ナトリウム、過酸化水素および過硼酸ナト
リウムの群から選ばれる少なくとも1種を0.01〜0
.5重量%で使用する上記第10項記載の方法。 12 各水洗工程を2段以上の多段水洗として供給水量
を減少せしめる手段を具備す金属表面洗浄処理装置にて
実施する上記第9項〜第11項のいずれかに記載の方法
。 13 スプレー式処理室に排気設備を設け処理室内の空
気を排出せしめることにより、余剰水量を蒸発除去せし
めて該余剰水の廃水としての排出を減少もしくはなくす
手段と、各水洗工程を2段以上の多段水洗として供給水
量を減少せしめる手段とを具備する金属表面洗浄処理装
置にて実施する上記第9項〜第11項のいずれかに記載
の方法。 14 リン酸塩皮膜がリン酸鉄皮膜である上記第9項〜
第13項のいずれかに記載の方法。 15 リン酸塩皮膜がリン酸亜鉛皮膜である上記第9項
〜第13項のいずれかに記載の方法。 16 リン酸塩皮膜がカルシウム変性リン酸亜鉛皮膜で
ある上記第9項〜第13項のいずれかに記載の方法。 17 酸化性物質を含む水溶液が、過硼酸ナトリウムと
アルカリ性物質を含む第16項記載の方法。[Scope of Claims] 1 A step of degreasing a metal surface, a step of cleaning the degreased metal surface with an aqueous solution containing 0.01 to 0.5% by weight of an oxidizing substance, and a step of adding phosphorus to the metal surface cleaned with the aqueous solution. A method for chemically converting a phosphate film on a metal surface, comprising the steps of chemically converting a salt film and washing the chemically formed metal surface with water. 2. The method according to item 1 above, wherein the oxidizing substance is at least one selected from the group of nitrites, hydrogen peroxide, perborates, aromatic nitro compounds, aromatic nitroso compounds, and hydroxylamine sulfate. 3. At least one selected from the group of sodium nitrite, hydrogen peroxide, and sodium perborate in a concentration of 0.01 to 0.
The method according to item 2 above, wherein the amount is 5% by weight. 4. The method according to any one of items 1 to 3 above, wherein each water washing step is carried out in a metal surface cleaning treatment apparatus equipped with a means for reducing the amount of water supplied by performing two or more stages of water washing. 5. A method for reducing or eliminating the discharge of excess water as wastewater by evaporating excess water by installing exhaust equipment in the spray treatment chamber and discharging the air in the treatment chamber, and for each washing process to be carried out in two or more stages. The method according to any one of the above items 1 to 3, which is carried out in a metal surface cleaning treatment apparatus equipped with a means for reducing the amount of water supplied as multi-stage water washing. 6. The method according to any one of items 1 to 5 above, wherein the phosphate film is an iron phosphate film. 7 Item 1 above where the phosphate film is a zinc phosphate film
The method according to any of paragraph 5. 8. The method according to any one of items 1 to 5 above, wherein the phosphate film is a calcium-modified zinc phosphate film. 9 Step of degreasing the metal surface, degreasing the degreased metal surface with 0.01 to 0.5% by weight of an oxidizing substance and 10 to 10% of a titanium compound.
100 ppm (titanium concentration equivalent), a step of chemically forming a phosphate film on the metal surface cleaned with the aqueous solution, and a step of washing the chemically formed metal surface with water. Phosphate film conversion treatment method for metal surfaces. 10 Oxidizing substances include nitrite, hydrogen peroxide, perborate,
10. The method according to item 9, wherein the compound is at least one selected from the group consisting of aromatic nitro compounds, aromatic nitroso compounds, and hydroxylamine sulfate. 11 At least one selected from the group of sodium nitrite, hydrogen peroxide, and sodium perborate at 0.01 to 0
.. 11. The method of item 10 above, wherein the amount is 5% by weight. 12. The method according to any one of the above items 9 to 11, wherein each water washing step is carried out in a metal surface cleaning treatment apparatus equipped with means for reducing the amount of water supplied by performing two or more multi-stage washing steps. 13. A method for reducing or eliminating the discharge of excess water as wastewater by evaporating excess water by installing exhaust equipment in the spray treatment chamber and discharging the air in the treatment chamber, and for each washing process to be carried out in two or more stages. 12. The method according to any one of items 9 to 11 above, which is carried out in a metal surface cleaning treatment apparatus comprising means for reducing the amount of water supplied as multi-stage water washing. 14 Item 9 above, wherein the phosphate film is an iron phosphate film
The method according to any of paragraph 13. 15. The method according to any one of items 9 to 13 above, wherein the phosphate film is a zinc phosphate film. 16. The method according to any one of items 9 to 13 above, wherein the phosphate film is a calcium-modified zinc phosphate film. 17. The method according to item 16, wherein the aqueous solution containing an oxidizing substance contains sodium perborate and an alkaline substance.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52058482A JPS6041148B2 (en) | 1977-05-19 | 1977-05-19 | Phosphate film conversion treatment method for metal surfaces |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52058482A JPS6041148B2 (en) | 1977-05-19 | 1977-05-19 | Phosphate film conversion treatment method for metal surfaces |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53142934A JPS53142934A (en) | 1978-12-13 |
| JPS6041148B2 true JPS6041148B2 (en) | 1985-09-14 |
Family
ID=13085640
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52058482A Expired JPS6041148B2 (en) | 1977-05-19 | 1977-05-19 | Phosphate film conversion treatment method for metal surfaces |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6041148B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5623279A (en) * | 1979-07-31 | 1981-03-05 | Sumitomo Metal Ind Ltd | Surface activation treating method of zinc or zinc plated product |
| US5238506A (en) * | 1986-09-26 | 1993-08-24 | Chemfil Corporation | Phosphate coating composition and method of applying a zinc-nickel-manganese phosphate coating |
| US4793867A (en) * | 1986-09-26 | 1988-12-27 | Chemfil Corporation | Phosphate coating composition and method of applying a zinc-nickel phosphate coating |
| BRPI0417176B1 (en) * | 2003-12-04 | 2016-03-08 | Nippon Steel & Sumitomo Metal Corp | surface conditioning prior to chemical conversion treatment of a steel member |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49122440A (en) * | 1973-03-28 | 1974-11-22 | ||
| JPS529938B2 (en) * | 1974-05-30 | 1977-03-19 | ||
| DE2527853B2 (en) * | 1975-06-23 | 1981-04-09 | Metallgesellschaft Ag, 6000 Frankfurt | Process for improving the water balance in the phosphating of metals |
-
1977
- 1977-05-19 JP JP52058482A patent/JPS6041148B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53142934A (en) | 1978-12-13 |
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