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JPH0633464B2 - Phosphate treatment liquid for composite structure and treatment method - Google Patents
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JPH0633464B2 - Phosphate treatment liquid for composite structure and treatment method - Google Patents

Phosphate treatment liquid for composite structure and treatment method

Info

Publication number
JPH0633464B2
JPH0633464B2 JP1308026A JP30802689A JPH0633464B2 JP H0633464 B2 JPH0633464 B2 JP H0633464B2 JP 1308026 A JP1308026 A JP 1308026A JP 30802689 A JP30802689 A JP 30802689A JP H0633464 B2 JPH0633464 B2 JP H0633464B2
Authority
JP
Japan
Prior art keywords
ion
fluorine
phosphate
ions
treatment
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 - Lifetime
Application number
JP1308026A
Other languages
Japanese (ja)
Other versions
JPH02277781A (en
Inventor
勝也 山本
賢一 福谷
庸夫 斉藤
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.)
Nissan Motor Co Ltd
Original Assignee
Nissan Motor Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nissan Motor Co Ltd filed Critical Nissan Motor Co Ltd
Priority to JP1308026A priority Critical patent/JPH0633464B2/en
Publication of JPH02277781A publication Critical patent/JPH02277781A/en
Publication of JPH0633464B2 publication Critical patent/JPH0633464B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/05Chemical 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 using aqueous solutions
    • C23C22/06Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
    • C23C22/364Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing also manganese cations
    • C23C22/365Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing also manganese cations containing also zinc and nickel cations

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  • 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)

Description

【発明の詳細な説明】Detailed Description of the Invention 【産業上の利用分野】[Industrial applications]

本発明は、鉄鋼板、亜鉛及びアルミニウム等の異質の素
材が一緒に組み合わされて構成されている自動車ボデ
ー、即ち複合構造物の表面を処理するためのリン酸塩処
理液及び処理方法に関するものである。
The present invention relates to a phosphate treatment liquid and a treatment method for treating a surface of an automobile body, that is, a composite structure, which is formed by combining different materials such as steel plate, zinc and aluminum together. is there.

【従来技術】[Prior art]

従来、アルミニウムを構成体の一部、即ちパーツとして
いる自動車ボデーをリン酸塩処理する場合には、そのア
ルミニウムパーツをボデーに取付ける前に、主として性
能上の理由からクロメート処理を行い、その後で鉄鋼板
及び亜鉛めっき鋼板からなる自動車ボデーに組付け、再
度リン酸塩処理を行い、続いてカチオン電着塗装を行っ
ている方法が周知である。この方法の特徴は、最初にア
ルミニウムパーツ上に生成させたクロメート皮膜が、後
で行うリン酸塩処理工程で、その一部のクロム及びアル
ミニウムの溶出が生じ、クロメート皮膜が不完全な皮膜
状態になり易く、又当然のことであるがリン酸塩皮膜の
生成も起こらないのである。
Conventionally, when a car body, which is made of aluminum as a part of the structural body, that is, a part, is subjected to a phosphate treatment, a chromate treatment is mainly performed for performance reasons before attaching the aluminum part to the body, and then a steel is used. A method is known in which a plate and a galvanized steel plate are mounted on an automobile body, subjected to phosphate treatment again, and then subjected to cationic electrodeposition coating. The feature of this method is that the chromate film formed on the aluminum part first elutes part of the chromium and aluminum in the phosphate treatment step performed later, resulting in an incomplete chromate film state. It tends to occur, and of course, the formation of a phosphate film does not occur.

【発明が解決しようとする課題】[Problems to be Solved by the Invention]

前記従来例の方法では、先にクロメート処理したアルミ
ニウムパーツが組み込まれているため、リン酸塩処理液
中にクロム及びアルミニウムの溶出が起き、クロメート
皮膜及びリン酸塩皮膜が不完全な皮膜状態となり、その
後の塗装処理を行った塗膜の密着性能が劣り、特に耐水
二次密着性が劣ると云う課題を有している。 又、自動車ボデーの製造工程では、パーツ組付け→表面
処理→塗装の一連の流れ工程において、前記従来例の工
程は、アルミニウムパーツのみ別工程で、水洗処理→ク
ロメート処理→水洗乾燥処理を必要とし、しかる後にパ
ーツ組付け→表面処理→塗装の工程を経なければなら
ず、作業性及びコストの面での課題も有している。 前記アルミニウムパーツをクロメート処理することなく
自動車ボデーに組付けてリン酸塩処理を行った場合に
は、従来公知の処理液では、アルミニウムパーツの表面
に満足な性能を有するリン酸塩皮膜、つまり塗装後の耐
糸サビ性及び耐水二次密着性に優れた皮膜を得ることが
できず、高い塗膜性能が要求されている自動車ボデーと
しては不向きな皮膜しか形成できない。同時に、その処
理工程において、リン酸塩処理液中にアルミニウムイオ
ンが溶出し、それによって異なった種類の素材が組み合
わされた自動車ボデーの表面全体に亘って化成されるリ
ン酸塩皮膜の性能が著しく低下すると云う大きな課題を
有することになる。
In the method of the conventional example, since the chromate-treated aluminum parts are incorporated in advance, chromium and aluminum are eluted in the phosphating solution, resulting in an incomplete film state of the chromate film and the phosphate film. However, there is a problem that the adhesion performance of the coating film subjected to the subsequent coating treatment is inferior, and particularly the water resistant secondary adhesion is inferior. Also, in the process of manufacturing an automobile body, in the series of process steps of assembly of parts → surface treatment → painting, the conventional example requires only aluminum parts as a separate process, that is, water washing treatment → chromate treatment → water washing drying treatment. After that, the process of assembly of parts → surface treatment → painting has to be performed, and there are problems in terms of workability and cost. In the case where the aluminum parts are assembled on an automobile body without chromate treatment and subjected to a phosphate treatment, a conventionally known treatment liquid produces a phosphate film having satisfactory performance on the surface of the aluminum parts, that is, a coating. It is not possible to obtain a film excellent in yarn rust resistance and water-resistant secondary adhesion afterwards, and only a film unsuitable for an automobile body requiring high film performance can be formed. At the same time, in the treatment process, aluminum ions are eluted in the phosphating solution, thereby significantly improving the performance of the phosphate film formed on the entire surface of the automobile body in which different kinds of materials are combined. It will have a big problem of decreasing.

【課題を解決するための手段】[Means for Solving the Problems]

前記従来例の種々の課題を解決する具体的手段として本
発明は、亜鉛イオン 0.3〜 2.0g/、ニッケルイオン
0.3〜 4.0g/、マンガンイオン 0.3〜 2.0g/、
ナトリウムイオン3〜10g/、カリウムイオン 0.1〜
10g/、リン酸イオン 5.0〜25.0g/、全フッ素イ
オン 0.1〜20g/、硝酸イオン 4.0g/以上及び亜
硝酸イオン0.01〜 1.0g/を主成分とし、pH 2.0〜
3.5で、且つ全フッ素イオン中に錯フッ素イオンがフッ
素として 0.1〜5g/であり、遊離フッ素イオンが
0.01〜2g/含まれていることを特徴とする複合構造
物用リン酸塩処理液、及び該処理液を用い、且つ酸性フ
ッ化ソーダと酸性フッ化カリウムの混合物を補給液とし
て、前記遊離フッ素イオン濃度を維持しながら複合構造
物を処理することを特徴とする処理方法を提供するもの
であり、一般的な製造工程を変更することなく適用して
も、複合構造物の表面に、カチオン電着塗装下地として
優れた皮膜を化成させることができるのである。 尚、処理液中に経時によりアルミニウムイオンが400ppm
以上含まれて来た場合、遊離フッ素イオンを 0.01 〜2
g/に維持すると、全フッ素イオンは1〜20g/の
範囲になってくる。
As a concrete means for solving various problems of the above-mentioned conventional example, the present invention provides zinc ion 0.3 to 2.0 g /, nickel ion
0.3 to 4.0 g /, manganese ion 0.3 to 2.0 g /,
Sodium ion 3 to 10 g /, potassium ion 0.1 to
10 g /, phosphate ion 5.0 to 25.0 g /, total fluorine ion 0.1 to 20 g /, nitrate ion 4.0 g / or more, and nitrite ion 0.01 to 1.0 g / as main components, pH 2.0 to
3.5, and the amount of complex fluoride ion in the total fluorine ion is 0.1 to 5 g / fluorine, and the free fluorine ion is
0.01 to 2 g / content of a phosphate treatment liquid for a composite structure, and the above-mentioned free fluorine using the treatment liquid and a mixture of acidic sodium fluoride and potassium acid fluoride as a replenishing liquid. The present invention provides a treatment method characterized by treating a composite structure while maintaining an ionic concentration. An excellent film can be formed as a coating base. It should be noted that aluminum ion in the treatment liquid is 400 ppm with time.
When it is included above, 0.01 to 2 of free fluorine ion
If maintained at g /, total fluorine ions will be in the range of 1 to 20 g /.

【作 用】[Work]

異なった素材例えば、アルミニウム、鉄、亜鉛めっき
(亜鉛合金めっき、合金化亜鉛めっき等を含む)等を一
緒に組付けた複合構造物に対し、リン酸亜鉛の同時処理
を可能とするには、異なった素材が共通して、塗装後
の塗膜性能が良いこと、アルミニウムを処理するため
にリン酸塩処理液中にアルミニウムが溶出し、アルミニ
ウムイオンの蓄積によって化成性が悪くなり、性能劣化
を招くので、アルミニウムイオンのコントロールを必要
とすること、が要求されるのである。 従って、前記処理液組成において、フッ素イオンの存
在、即ち全フッ素イオン中に錯フッ素イオンが 0.1〜5
g/であり、遊離フッ素イオン(全フッ素イオン量)
−(錯フッ素イオン中のフッ素量)−(AlF中のフ
ッ素量)=遊離フッ素イオン量が 0.01〜2g/含ま
れていることが不可欠の条件であり、この処理液を30
〜55℃にして、複合構造物を1〜5分浸漬して処理
し、該複合構造物の表面に化成されたリン酸亜鉛系皮膜
中にニッケル及びマンガンが夫々1〜10%の比率(好
ましくは4%程度)で含有していることに特徴がある。 処理液中にアルミニウムイオンが溶出して増加すると、
複合構造物の鉄鋼板及びアルミニウム表面上の皮膜化成
性を阻害する。特に、アルミニウムイオンが150 ppm
以上(遊離フッ素イオンの量に略対応)になると極端に
悪くなる。従って、前記処理液を用いて連続的に処理を
行うに当たっては次式、 Al+3+2KHF+NaHF →KNaAlF↓+3H の反応により、溶出アルミニウムイオン量に見合うKH
及びNaHFを適宜添加し(尚、Al+3+2KF
+NaF+3HF→KNaAlF↓+3Hでも同
様な反応であり、NaF及びKFとHFの添加でも同様
な効果がある)、遊離フッ素イオンを所定量の範囲に維
持することにより溶出アルミニウムイオンをコントロー
ルし、複合構造物の表面に生成するリン酸塩皮膜を適正
な皮膜にすることが可能になるのである。 この場合に、処理液中の遊離フッ素イオン量を制御する
ことでアルミニウムイオンをコントロールするのであっ
て、そのためにKHF及びNaHFを添加し、アル
ミニウムイオンをKNaAlFの形で沈澱させるの
である。そして、重要なことは、酸性フッ化ナトリウム
1分子量に対し、酸性フッ化カリウム2分子量の割合で
混合されていることであり、これらの成分を別々に添加
するのではなく、予め両者を混合させた混合物を処理液
中に連続的に又は間欠的に添加することである。このよ
うにすることによって、アルミニウム化合物の沈澱が瞬
時に生成し、遊離フッ素イオンの測定が正確に行え、コ
ントロールが容易となる。この場合の混合物は液体又は
固体であってもよい。 本発明のリン酸塩処理液を適用することによる性能的な
特徴としては、複合構造物の素材の内、鉄と亜鉛めっき
材に対しては一般的なリン酸亜鉛処理によるものとほと
んど差異のないリン酸塩皮膜が形成でき、アルミニウム
材に対しては形成された皮膜の性能向上の効果が著し
い。即ち、アルミニウム表面に生成するリン酸塩皮膜
は、リン酸、弗酸、亜鉛の三成分でもZn(PO
・4HOの生成は可能であるが、前記したように本
発明においては更にその皮膜中にニッケル及びマンガン
が夫々1〜10%の比率で含有していることで、皮膜結
晶が緻密化し、尚且つ耐水二次密着性及び屋外曝露性が
向上するのである。この場合の本発明に係る処理液を用
いて処理した皮膜性能を、塗装後において従来例と比較
した結果は表1の通りである。 従来例Zn系処理液組成 Zn 1.2g/ Na 7.0 〃 PO 15 〃 NO 7 〃 SiF 3 〃 NO 0.5 〃 pH 3.2 従来例クロム系処理液組成 CrO 7 g/ PO 10 〃 F 2 〃 pH 1.5 本発明処理液組成 Zn2+ 1.4g/ Ni2+ 1.5 〃 Mn2+ 0.5 〃 PO -3 15.5g/ SiF -2 3 g/ F 100 ppm NO 7 g/ K 0.5 〃 Na 7 〃 NO 0.2 〃 pH 3.2
In order to enable simultaneous treatment of zinc phosphate to a composite structure in which different materials such as aluminum, iron, zinc plating (including zinc alloy plating, alloyed zinc plating, etc.) are assembled together, Different materials are common, good coating performance after painting, aluminum elutes in the phosphate treatment liquid to treat aluminum, and aluminum ions accumulate, resulting in poor chemical conversion and deterioration of performance. Therefore, it is required to control aluminum ions. Therefore, in the composition of the treatment liquid, the presence of fluoride ions, that is, the complex fluoride ions in the total fluoride ions are 0.1 to 5 inclusive.
g /, free fluorine ion (total fluorine ion amount)
- (fluorine content in complex fluorine ions) - (fluorine content in AlF 3) = is an indispensable condition that the free fluorine ion content is contained 0.01 to 2 g /, the treatment liquid 30
The composite structure is dipped at 1 to 5 ° C. for 1 to 5 minutes to be treated, and the zinc phosphate-based coating formed on the surface of the composite structure contains nickel and manganese at a ratio of 1 to 10% each (preferably Is about 4%). When aluminum ions elute and increase in the processing liquid,
It inhibits the film formation on the steel and aluminum surfaces of the composite structure. Especially, aluminum ion is 150 ppm
Above (approximately corresponding to the amount of free fluorine ions), it becomes extremely bad. Therefore, in performing continuous treatment using the treatment liquid, the reaction of the following formula: Al +3 + 2KHF 2 + NaHF 2 → K 2 NaAlF 6 ↓ + 3H +
F 2 and NaHF 2 are added appropriately (Al +3 + 2KF
+ NaF + 3HF → K 2 NaAlF 6 ↓ + 3H + is the same reaction, and the same effect can be obtained by adding NaF and KF and HF), and controlling the elution aluminum ion by maintaining the free fluorine ion within a predetermined range. Thus, it becomes possible to make the phosphate film formed on the surface of the composite structure an appropriate film. In this case, the aluminum ion is controlled by controlling the amount of free fluorine ion in the treatment liquid. For that purpose, KHF 2 and NaHF 2 are added and the aluminum ion is precipitated in the form of K 2 NaAlF 6 . is there. And, what is important is that the acidic potassium fluoride is mixed in a ratio of 2 molecular weight with respect to 1 molecular weight of sodium acid fluoride, and these components are not mixed separately but mixed in advance. The above mixture is continuously or intermittently added to the treatment liquid. By doing so, precipitation of the aluminum compound is instantaneously generated, the free fluorine ion can be accurately measured, and control becomes easy. The mixture in this case may be liquid or solid. As a performance characteristic by applying the phosphating solution of the present invention, among the materials of the composite structure, for iron and galvanized material, there is almost no difference from the general zinc phosphate treatment. A non-phosphate coating can be formed, and the effect of improving the performance of the formed coating is remarkable for aluminum materials. That is, the phosphate film formed on the surface of aluminum contains Zn 3 (PO 4 ) even with the three components phosphoric acid, hydrofluoric acid and zinc.
Although 2.4H 2 O can be generated, as described above, in the present invention, since nickel and manganese are contained in the film at a ratio of 1 to 10% respectively, the film crystal is densified. In addition, the water-resistant secondary adhesion and outdoor exposure are improved. Table 1 shows the results of comparing the coating performance of the coating solution treated with the treatment liquid according to the present invention with the conventional example after coating. Conventional Zn-based treatment liquid composition Zn 1.2 g / Na 7.0 〃 PO 4 15 〃 NO 3 7 〃 SiF 6 3 〃 NO 2 0.5 〃 pH 3.2 conventional chromium-based treatment liquid composition CrO 4 7 g / PO 4 10 〃 F 2 〃 pH 1.5 Inventive treatment liquid composition Zn 2+ 1.4 g / Ni 2+ 1.5 〃 Mn 2+ 0.5 〃 PO 4 -3 15.5 g / SiF 6 -2 3 g / F 100 ppm NO 3 7 g / K + 0.5 〃 Na + 7 〃 NO 2 0.2 〃 pH 3.2

【実施例】【Example】

次に本発明の処理液及び処理方法について幾つかの実施
例を挙げ、従来例と比較してその効果を明らかにする。 実施例 1 (1)処理液組成 Zn2+ 1.1〜 1.2 g/ Ni2+ 0.9〜 1.0 〃 Mn2+ 0.4〜 0.6 〃 PO 3- 15.0〜15.5 〃 SiF 2- 2〜 3 〃 遊離F 0.08 〜 0.15 〃 NO 6〜 8 〃 K 0.05 〜 0.5 〃 Na 6.8 〜 7.8 〃 NO 0.15 〜 0.25 〃 pH 3.2〜 3.3 (2)処理条件 45℃、2分浸漬 上記処理条件で、5000系アルミニウム板と電気亜鉛めっ
き鋼板と亜鉛−ニッケルめっき鋼板と鉄鋼板とで構成さ
れる自動車ボディ(Fe:Al:Zn−Ni=6:1:
3)を、遊離フッ素が管理範囲になるように、遊離フッ
素を測定(遊離フッ素測定法……全フッ素量−錯体フッ
素中のフッ素量−AlF(Fとして)=遊離フッ素
量)して、含水率10%のKHF粉末2分子量とフレー
ク状NaHF1分子量との5%混合水溶液を添加しな
がら及び他成分も維持される様に補給剤を補給しながら
2m2/処理し、その時点で各試験片の性能をチェック
した結果を表2に示す。 比較例 1 KHFとNaHFの混合液のかわりに、5%NaH
を用いた以外は、実施例1と同条件で行った結果を
表2に示す。 比較例 2 遊離フッ素を0g/近辺で維持しながら行った以外
は、実施例1と同じ方法で行った結果を表2に示す。 配管系統の詰まりが、実施例1のときより多かった。 比較例 3 KHFとNaHFの混合液のかわりに5%KHF
を用いた以外は、実施例1と同条件で行った結果を表2
に示す。 比較例 4 実施例1の処理液からMn2+を除いた以外は、同条件で
行った。 比較例 5 実施例1の処理液からNi2+を除いた以外は、同条件で
行った。
Next, some examples of the treatment liquid and the treatment method of the present invention will be given, and the effect thereof will be clarified by comparison with the conventional example. Example 1 (1) treatment solution composition Zn 2+ 1.1~ 1.2 g / Ni 2+ 0.9~ 1.0 〃 Mn 2+ 0.4 to 0.6 〃 PO 4 3- from 15.0 to 15.5 〃 SiF 6 2- 2~ 3 〃 free F - 0.08 to 0.15 〃 NO 3 -. 6 to 8 〃 K + 0.05 ~ 0.5 〃 Na + 6.8 ~ 7.8 〃 NO 2 - 0.15 ~ 0.25 〃 pH 3.2 to 3.3 (2) processing conditions 45 ° C., for 2 minutes immersion the process conditions, Automobile body composed of 5000 series aluminum plate, electrogalvanized steel plate, zinc-nickel plated steel plate and steel plate (Fe: Al: Zn-Ni = 6: 1:
3), so that free fluorine is management range, free fluorine measurements (free fluorine assay ...... total fluorine content - as the amount of fluorine -alF 3 (F in complex fluorine) = free fluorine amount) to, 2m 2 / treatment while adding a 5% mixed aqueous solution of 2 molecular weight of KHF 2 powder having a water content of 10% and 1 molecular weight of flaky NaHF 2 and while supplementing with a replenisher so as to maintain other components as well. Table 2 shows the results of checking the performance of each test piece by. Comparative Example 1 5% NaH was used instead of the mixed solution of KHF 2 and NaHF 2.
Table 2 shows the results obtained under the same conditions as in Example 1 except that F 2 was used. Comparative Example 2 Table 2 shows the results obtained by the same method as in Example 1 except that the amount of free fluorine was maintained at 0 g / near. The clogging of the piping system was more than in Example 1. Comparative Example 3 KHF 2 and instead of the mixture of NaHF 2 5% KHF 2
Table 2 shows the results obtained under the same conditions as in Example 1 except that
Shown in. Comparative Example 4 The same conditions were used except that Mn 2+ was removed from the treatment liquid of Example 1. Comparative Example 5 The same conditions were used except that Ni 2+ was removed from the treatment liquid of Example 1.

【発明の効果】【The invention's effect】

以上説明したように本発明に係る複合構造物用リン酸塩
処理液及び処理方法は、リン酸亜鉛系処理液中に所定量
のNiイオン及びMnイオンを含み、遊離フッ素イオン
の含有量を所定の範囲に管理することで、アルミニウム
パーツを含む複合構造物であっても、連続処理が可能で
作業性が向上し、しかも複合構造物の表面に形成された
リン酸塩皮膜は、その後のカチオン電着塗装によって得
られた塗膜の屋外曝露後の密着性及び耐水二次密着性を
向上させると云う優れた効果を奏する。 又、アルミニウムパーツを含む複合構造物の連続処理に
おいて、弊害となる溶出アルミニウムイオンを順次KH
及びNaHFの混合物を添加し、アルミニウムイ
オンをKNaAlFの形で沈澱除去させるため、良
好なリン酸塩皮膜が得られると云う優れた効果を奏す
る。
As described above, the phosphate treatment solution and treatment method for a composite structure according to the present invention include a predetermined amount of Ni ions and Mn ions in the zinc phosphate-based treatment solution, and a predetermined content of free fluorine ions. By controlling within the range, even if it is a composite structure containing aluminum parts, continuous processing is possible and workability is improved, and the phosphate film formed on the surface of the composite structure is It has an excellent effect of improving the adhesiveness of a coating film obtained by electrodeposition coating after outdoor exposure and the water-resistant secondary adhesiveness. Also, in the continuous processing of the composite structure including aluminum parts, the dissolved aluminum ions, which are harmful, are sequentially subjected to KH.
Since a mixture of F 2 and NaHF 2 is added and aluminum ions are precipitated and removed in the form of K 2 NaAlF 6, an excellent effect that a good phosphate film is obtained can be obtained.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】亜鉛イオン 0.3〜 2.0g/、ニッケルイ
オン 0.3〜 4.0g/、マンガンイオン 0.3〜 2.0g/
、ナトリウムイオン3〜10g/、カリウムイオン
0.1〜10g/、リン酸イオン 5.0〜25.0g/、全フ
ッ素イオン 0.1〜20g/、硝酸イオン 4.0g/以上
及び亜硝酸イオン0.01〜 1.0g/を主成分とし、pH
2.0〜 3.5で、且つ全フッ素イオン中に錯フッ素イオン
がフッ素として 0.1〜5g/であり、下記式で現わさ
れる遊離フッ素イオンが 0.01〜2g/含まれている
ことを特徴とする鉄鋼、亜鉛めっき鋼及びアルミニウム
材を有する複合構造物用リン酸塩処理液。 全フッ素イオン(g/)−錯フッ素イオン中のフッ素
(g/)−AlF中のフッ素イオン(g/)=遊
離フッ素イオン(g/)
1. Zinc ion 0.3 to 2.0 g /, nickel ion 0.3 to 4.0 g /, manganese ion 0.3 to 2.0 g /
, Sodium ion 3-10g /, potassium ion
0.1-10 g /, phosphate ion 5.0-25.0 g /, total fluorine ion 0.1-20 g /, nitrate ion 4.0 g / or more and nitrite ion 0.01-1.0 g /
Steels characterized in that they are 2.0 to 3.5, and complex fluorine ions are 0.1 to 5 g / in fluorine as total fluorine ions, and 0.01 to 2 g / in free fluorine ions represented by the following formula. A phosphating solution for a composite structure having a galvanized steel and an aluminum material. Perfluorinated ion (g /) - fluorine in complex fluorine ions (g /) - Fluorine ions in AlF 3 (g /) = free fluorine ion (g /)
【請求項2】処理工程において、溶出するアルミニウム
イオンに対し、(過剰の)遊離フッ素イオンが含まれて
いることを特徴とする請求項 (1)記載の複合構造物用リ
ン酸塩処理液。
2. The phosphate treatment liquid for a composite structure according to claim 1, wherein in the treatment step, (excessive) free fluorine ions are contained with respect to the eluted aluminum ions.
【請求項3】カチオン電着塗装下地用皮膜を形成させる
ために適用される請求項 (1)記載の複合構造物用リン酸
塩処理液。
3. The phosphating solution for composite structures according to claim 1, which is applied to form a film for a cationic electrodeposition coating base.
【請求項4】亜鉛イオン 0.3〜 2.0g/、ニッケルイ
オン 0.3〜 4.0g/、マンガンイオン 0.3〜 2.0g/
、ナトリウムイオン3〜10g/、カリウムイオン
0.1〜10g/、リン酸イオン 5.0〜25.0g/、全フ
ッ素イオン 0.1〜20g/、硝酸イオン 4.0g/以上
及び亜硝酸イオン0.01〜 1.0g/を主成分とし、pH
2.0〜 3.5で、且つ全フッ素イオン中に錯フッ素イオン
がフッ素として 0.1〜5g/であり、遊離フッ素イオ
ンが 0.01〜2g/含まれている酸性処理液を用い、
酸性フッ化ナトリウムと酸性フッ化カリウムの混合物を
補給剤として、前記遊離フッ素イオン濃度を維持しなが
ら前記複合構造物を処理することを特徴とする処理方
法。
4. Zinc ion 0.3 to 2.0 g /, nickel ion 0.3 to 4.0 g /, manganese ion 0.3 to 2.0 g /
, Sodium ion 3-10g /, potassium ion
0.1-10 g /, phosphate ion 5.0-25.0 g /, total fluorine ion 0.1-20 g /, nitrate ion 4.0 g / or more and nitrite ion 0.01-1.0 g /
An acidic treatment liquid having a content of 2.0 to 3.5, a complex fluoride ion of 0.1 to 5 g / in terms of fluorine in a total fluoride ion, and a free fluoride ion of 0.01 to 2 g / is used.
A treatment method comprising treating the composite structure while maintaining the free fluorine ion concentration, using a mixture of sodium acid fluoride and potassium acid fluoride as a supplement.
【請求項5】混合物が、酸性フッ化ナトリウム1分子量
に対し、酸性フッ化カリウム2分子量の割合で混合され
ている液体又は固体である請求項 (4)記載の処理方法。
5. The treatment method according to claim 4, wherein the mixture is a liquid or a solid mixed in a ratio of 2 molecular weights of potassium acid fluoride to 1 molecular weight of sodium acid fluorides.
JP1308026A 1989-01-31 1989-11-28 Phosphate treatment liquid for composite structure and treatment method Expired - Lifetime JPH0633464B2 (en)

Priority Applications (1)

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JP2197589 1989-01-31
JP1-21975 1989-01-31
JP1308026A JPH0633464B2 (en) 1989-01-31 1989-11-28 Phosphate treatment liquid for composite structure and treatment method

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JPH02277781A JPH02277781A (en) 1990-11-14
JPH0633464B2 true JPH0633464B2 (en) 1994-05-02

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0483881A (en) * 1990-07-27 1992-03-17 Nippon Parkerizing Co Ltd Phosphate treatment method for composite structures
JP2695963B2 (en) * 1990-03-16 1998-01-14 マツダ株式会社 Phosphating of metal surfaces
JP2794013B2 (en) * 1990-10-24 1998-09-03 日本パーカライジング株式会社 Phosphate chemical conversion treatment solution for iron-aluminum metal sheet metal construction
JP2948370B2 (en) * 1991-08-26 1999-09-13 本田技研工業株式会社 Surface treatment method for combination products of aluminum and iron
JP2713002B2 (en) * 1991-11-25 1998-02-16 住友金属工業株式会社 Manufacturing method of galvanized steel sheet
JP3417653B2 (en) * 1994-05-11 2003-06-16 日本パーカライジング株式会社 Pretreatment method for painting aluminum material
JP4658339B2 (en) * 2001-01-17 2011-03-23 日本ペイント株式会社 Metal surface treatment method
JP5118275B2 (en) * 2001-08-22 2013-01-16 日本ペイント株式会社 Zinc phosphate treatment agent
ES2770152T3 (en) * 2017-04-21 2020-06-30 Henkel Ag & Co Kgaa Procedure for sludge-free zinc phosphating of metal components in series to form layers
RU2690876C1 (en) * 2018-06-14 2019-06-06 Закрытое Акционерное общество "ФК" (ЗАО " ФК") Phosphate coating production method

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3619300A (en) * 1968-11-13 1971-11-09 Amchem Prod Phosphate conversion coating of aluminum, zinc or iron
JPS60204889A (en) * 1984-03-29 1985-10-16 Nisshin Steel Co Ltd Zinc phosphate treatment of steel sheet plated with zn-al alloy
JPS6136588A (en) * 1984-07-27 1986-02-21 株式会社 応用地質調査事務所 Flexible pipe joining method in underground displacement measurement, etc. using inclinometer

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