JPH0784665B2 - Aluminum conversion treatment method - Google Patents
Aluminum conversion treatment methodInfo
- Publication number
- JPH0784665B2 JPH0784665B2 JP63072698A JP7269888A JPH0784665B2 JP H0784665 B2 JPH0784665 B2 JP H0784665B2 JP 63072698 A JP63072698 A JP 63072698A JP 7269888 A JP7269888 A JP 7269888A JP H0784665 B2 JPH0784665 B2 JP H0784665B2
- Authority
- JP
- Japan
- Prior art keywords
- liter
- aluminum
- conversion treatment
- ions
- degreasing
- 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
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
-
- 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
- C23C22/05—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 using aqueous solutions
- C23C22/06—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 using aqueous solutions using aqueous acidic solutions with pH less than 6
- C23C22/34—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
- C23C22/36—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
- C23C22/361—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing titanium, zirconium or hafnium compounds
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)
Description
【発明の詳細な説明】 産業上の利用分野 本発明はアルミニウムまたはその合金を迅速に化成処理
する方法に関する。TECHNICAL FIELD The present invention relates to a method for rapidly converting aluminum or its alloys.
従来の技術 アルミニウムまたはその合金(以下単にアルミという)
はシート状や飲料缶等として用いられる。Conventional technology Aluminum or its alloy (hereinafter simply referred to as aluminum)
Is used as a sheet or a beverage can.
缶の場合は、ドローイング・アンド・アイアニングと呼
ぶ引き抜き成形法により製造され、その際に用いられる
る潤滑剤や成形油が缶の表面に付着し、また、アルミニ
ウム粉が容器の内壁に残存付着する。このようなアルミ
の脱脂、洗浄、化成処理方法としては以下の技術が提案
されている。In the case of a can, it is manufactured by a drawing method called drawing and ironing, and the lubricant and molding oil used at that time adhere to the surface of the can, and aluminum powder remains and adheres to the inner wall of the container. . The following techniques have been proposed as such degreasing, cleaning, and chemical conversion treatment methods for aluminum.
特公昭53−28245ではアルミの脱脂、洗浄方法として、 PHが約1.0−1.8の 硫酸 約1〜10g/リットル、 フッ化水素酸 約0.005〜0.01g/リットル を含有する洗浄用水性液に温度 約43〜57℃で表面を接
触させることが; 特開昭59−133382では、アルミ容器に化成被膜を適用す
るため、容器の表面から油や屑その他の付着物を浄化及
びエッチングする方法として、実質的に 約6〜12g/リットルのアルカリ金属水酸化物、 約3〜6g/リットルのキレート剤から成る希釈アルカリ
性水溶液を約26〜54℃でスプレイして清浄な光輝表面を
形成することが;特開昭58−1078ではアルミ表面からア
ルミ細片を除去、溶解し且つ潤滑オイルを洗浄するため
の洗浄水溶液として 約0.5〜3g/リットルのアルカリ金属水酸化物、 約1〜5g/リットルのエチレンジアミンテトラ酢酸のア
ルカリ金属塩、 および約0.1〜10g/リットルの界面活性剤 及び、アルミニウム金属イオン封鎖剤としてグルコン酸
アルカリ金属塩他を含有する配合が; 特公昭56−33468では、アルミ上に沸騰水に対する黒色
抵抗性を有する被覆面を与えることができるコーチング
を形成するのに有効な、 PH 1.5〜4.0, 10PPM以上のジルコニウム,チタニウムあるいはこれら
の混合物、 10PPM以上のホスフエートおよび有効弗化物を含有する
配合が開示されている。In Japanese Examined Patent Publication No. 53-28245, as a method for degreasing and cleaning aluminum, a cleaning aqueous solution containing about 1 to 10 g / liter of sulfuric acid with a pH of about 1.0 to 1.8 and about 0.005 to 0.01 g / liter of hydrofluoric acid is used. The surface can be contacted at 43 to 57 ° C; in JP-A-59-133382, in order to apply a chemical conversion coating to an aluminum container, as a method for purifying and etching oil, debris and other deposits from the surface of the container, To spray a dilute alkaline aqueous solution of about 6 to 12 g / liter of alkali metal hydroxide and about 3 to 6 g / liter of chelating agent at about 26 to 54 ° C to form a clean bright surface; In Kaisho 58-1078, about 0.5 to 3 g / liter of an alkali metal hydroxide and about 1 to 5 g / liter of ethylenediamine tetra are used as a cleaning aqueous solution for removing and dissolving aluminum debris from the aluminum surface and cleaning the lubricating oil. Acetic acid alkali A combination containing a metal salt, a surfactant of about 0.1 to 10 g / liter, and an alkali metal salt of gluconate as an aluminum sequestering agent; Japanese Patent Publication No. 56-33468 discloses black resistance to boiling water on aluminum. Disclosed is a composition containing PH 1.5 to 4.0, zirconium, titanium or a mixture thereof of 10 PPM or more, a phosphate of 10 PPM or more and an effective fluoride effective for forming a coating capable of providing a coated surface having There is.
発明が解決しようとする問題点 本発明は品質水準を保持したまま、生産性を向上せしめ
るために、脱脂、洗浄、化成処理などを従来よりも高速
化することにある。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention The present invention is to accelerate degreasing, cleaning, chemical conversion treatment and the like in order to improve productivity while maintaining quality level.
問題点を解決するための手段 発明の構成 本発明の第一の化成処理方法は、(a)アルミニウムま
たはその合金に、1〜10g/リットルのPO4イオンと、0.1
〜3g/リットルのアルミニウムキレート化剤と、0.1〜5g
/リットルの界面活性剤とを含有し、アルカリ金属水酸
化物でpHを11〜13に調整した脱脂剤を4〜8秒間スプレ
ーすることにより脱脂を行い、次いで (b)0.01〜0.5g/リットルのZrイオンと、0.01〜0.5g/
リットルのPO4イオンと、0.001〜0.05g/リットルの有効
Fイオンとを含有し、pHを1.5〜4.0に調整した化成処理
剤を3〜7秒間スプレーすることを特徴とする。Means for Solving the Problems Constitution of the Invention The first chemical conversion treatment method of the present invention comprises: (a) aluminum or its alloy with 1 to 10 g / liter of PO 4 ions and 0.1
~ 3g / liter aluminum chelating agent, 0.1 ~ 5g
Degreasing is carried out by spraying a degreasing agent containing a surfactant / liter of which the pH is adjusted to 11 to 13 with an alkali metal hydroxide for 4 to 8 seconds, and then (b) 0.01 to 0.5 g / liter. Zr ions of 0.01-0.5g /
It is characterized in that a chemical conversion treatment agent containing liters of PO 4 ions and 0.001 to 0.05 g / liter of effective F ions and having a pH adjusted to 1.5 to 4.0 is sprayed for 3 to 7 seconds.
また本発明の第二の化成処理方法は、(a)アルミニウ
ムまたはその合金に、1〜10g/リットルのPO4イオン
と、0.1〜3g/リットルのアルミニウムキレート化剤と、
0.1〜5g/リットルの界面活性剤とを含有し、アルカリ金
属水酸化物でpHを11〜13に調整した脱脂剤で脱脂を行
い、次いで (b)0.01〜1g/リットルのVイオンと、0.01〜0.5g/リ
ットルのZrイオンと、0.01〜0.5g/リットルのPO4イオン
と、0.001〜0.05g/リットルの有効Fイオンとを含有
し、pHを1.5〜4.0に調整した化成処理剤を適用すること
を特徴とする。Further, the second chemical conversion treatment method of the present invention comprises (a) aluminum or an alloy thereof, 1 to 10 g / liter of PO 4 ion, and 0.1 to 3 g / liter of an aluminum chelating agent,
Degreasing is performed with a degreasing agent containing 0.1 to 5 g / liter of a surfactant and having a pH adjusted to 11 to 13 with an alkali metal hydroxide, and then (b) 0.01 to 1 g / liter of V ions and 0.01 ~ 0.5g / l Zr ion, 0.01-0.5g / l PO 4 ion, 0.001-0.05g / l effective F ion are contained, and the chemical conversion treatment agent whose pH is adjusted to 1.5-4.0 is applied. It is characterized by doing.
本発明で用いる脱脂剤はアルカリ金属水酸化物でPHを11
〜13に調整した PO4イオンとして 1〜10g/リットル アルミニウムキレート化剤 0.1〜3 g/リットル 界面活性剤 0.1〜5 g/リットル を含有する脱脂剤が好適であり、 PHを調整するアルカリ金属水酸化物としては水酸化ナト
リウム、水酸化カリウム、水酸化リチウム等が用いられ
る。The degreasing agent used in the present invention is an alkali metal hydroxide having a pH of 11
A degreasing agent containing 1 to 10 g / liter aluminum chelating agent 0.1 to 3 g / liter as a PO4 ion adjusted to 13 to 0.1 to 5 g / liter surfactant is suitable, and alkali metal hydroxide for adjusting PH is used. As the substance, sodium hydroxide, potassium hydroxide, lithium hydroxide or the like is used.
PHが11未満であると脱脂性、脱スマット性が不十分であ
り、また塗膜密着性が低下する。If the pH is less than 11, the degreasing and desmutting properties are insufficient, and the coating film adhesion decreases.
また、PHが13を越えるとエッチング量が多くなりすぎ、
外観不良(白化)および耐沸水黒変性も低下するため、
好ましくない。Also, if PH exceeds 13, the etching amount will be too large,
Since the poor appearance (whitening) and boiling water resistance to blackening also decrease,
Not preferable.
脱脂剤中におけるPO4イオンの供給源としては燐酸及び
その塩、特にオルト燐酸塩が好ましく例えば Na3PO4、Na2HPO4、(NH4)3PO4、K3PO4、K2HPO4等であ
り、その配合量はPO4換算で1g/リットル未満であると外
観が白化し、耐沸水黒変性も低下する。Phosphoric acid and its salts as a source of PO4 ions in the degreasing agent, especially Na 3 PO4 orthophosphate are preferred for example, Na 2 HPO 4, with (NH4) 3 PO 4, K 3 PO 4, K 2 HPO 4 , etc. If the blending amount is less than 1 g / liter in terms of PO 4 , the appearance will be whitened, and the blackening resistance to boiling water will be reduced.
また、10g/リットルを越えると塗膜との密着性が低下
し、浴の安定性も低下するので好ましくない。On the other hand, if it exceeds 10 g / liter, the adhesion to the coating film is deteriorated and the stability of the bath is also deteriorated, which is not preferable.
アルミニウムキレート化剤として用いられるものはグル
コン酸、ヘプトン酸、エチレンジアミン四酢酸およびそ
の塩等であり、その配合量は 0.1g/リットル未満であるとアルミニウムを溶解状態に
保持する能力が低く、浴の安定性も不十分でりある。ま
た、脱スマット性、塗膜との密着性が低下する。What is used as an aluminum chelating agent is gluconic acid, heptonic acid, ethylenediaminetetraacetic acid and its salts, etc., and the compounding amount of which is less than 0.1 g / liter has a low ability to hold aluminum in a dissolved state, The stability is also insufficient. Further, the desmutting property and the adhesion to the coating film are deteriorated.
また、3g/リットルを越えてもそれ以上の効果は認めら
れず、経済性が低下する。Further, even if it exceeds 3 g / liter, no further effect is observed, and the economical efficiency is lowered.
界面活性剤として用いられるものはノニオン系、アニオ
ン系、カチオン系いずれでも良いが、発泡性等を考慮す
るとノニオン系が好ましく、その配合量は0.1g/リット
ル未満であると脱脂性、脱スマット性が低下し、また処
理物への油分の残留が多くなる為、その後の化成処理で
均一な皮膜が生成されず、耐沸水黒変性、塗膜との密着
性も低下する。What is used as a surfactant may be any of nonionic, anionic, and cationic, but nonionic is preferable in consideration of foamability and the like, and if the compounding amount is less than 0.1 g / liter, degreasing and desmutting properties are obtained. In addition, since the amount of oil remaining on the treated product increases, a uniform film is not formed in the subsequent chemical conversion treatment, the blackening resistance to boiling water resistance and the adhesion to the coating film also decrease.
また、5g/リットルを越えても、それ以上の効果は認め
られず経済性および浴の発泡性、排水処理性を考えると
5g/リットルで十分である。Further, even if it exceeds 5 g / l, no further effect is observed, and considering the economy, the foamability of the bath, and the wastewater treatment property.
5 g / l is sufficient.
次に、化成処理剤(A)はPHが 1.5〜4.0であることが好ましく、PHが1.5未満であると
アルミニウムのエッチング反応が大きくなりすぎ皮膜が
生成しにくくなりまた、4.0を越えるとZr・Al−PO4の沈
澱が生じやすく、また、皮膜生成速度が遅くなり満足な
皮膜が生成されない。Next, the chemical conversion treatment agent (A) preferably has a pH of 1.5 to 4.0. When the pH is less than 1.5, the etching reaction of aluminum becomes too large and the film is hard to form. al-PO precipitation of 4 tends to occur, also, satisfactory coating slows film formation rate is not generated.
PHの調整は、硝酸、硫酸等の無機酸及び水酸化ナトリウ
ム、水酸化カリウム等の金属水酸化物及びアンモニア水
等を用いて行うのが好ましい。尚、燐酸の使用も不可能
ではないが、化成処理剤(A)中におけるPO4イオンの
量が特定の範囲(0.01〜0.5g/リットル)に規定されて
いるので、前期範囲内でしかPHの調整に燐酸を用いるこ
とができない。The pH is preferably adjusted using an inorganic acid such as nitric acid or sulfuric acid, a metal hydroxide such as sodium hydroxide or potassium hydroxide, or ammonia water. Although it is not impossible to use phosphoric acid, since the amount of PO4 ions in the chemical conversion treatment agent (A) is regulated within a specific range (0.01 to 0.5 g / liter), the pH of the Phosphoric acid cannot be used for conditioning.
Zrイオンの供給源としては、H2ZrF6、(NH4)2ZrF6、Na
2ZrF6、K2ZrF6、Zr(NO3)4、ZrO(NO3)2、Zr(S
O4)2、ZrOSO4等であり、その配合量が0.01g/リットル
未満であると満足な皮膜が生成されない。また、0.5g/
リットルを越えると、それ以上の効果はなく経済性が低
下する。The sources of Zr ions include H 2 ZrF 6 , (NH 4 ) 2 ZrF 6 and Na.
2 ZrF 6 , K 2 ZrF 6 , Zr (NO 3 ) 4 , ZrO (NO 3 ) 2 , Zr (S
O 4 ) 2 , ZrOSO 4, etc., and if the blending amount is less than 0.01 g / liter, a satisfactory film is not formed. Also, 0.5g /
Beyond liters, there is no further effect and economic efficiency declines.
化成処理剤(A)におけるPO4イオンの供給源としてはH
3PO4、NaH2PO4、(NH4)H2PO4等であり、その配合量は
0.01g/リットル未満であると塗膜との密着性が低下し、
また、0.5g/リットルを越えると耐沸水黒変性、塗膜と
の密着性が低下するうえ、Zr、Al−PO4の沈澱を生成す
る恐れが生じるので好ましくない。As a source of PO 4 ions in the chemical conversion treatment agent (A), H
3 PO 4 , NaH 2 PO 4 , (NH 4 ) H 2 PO 4, etc., and their compounding amounts are
If it is less than 0.01 g / liter, the adhesiveness with the coating film decreases,
On the other hand, if it exceeds 0.5 g / liter, the blackening resistance to boiling water and the adhesion to the coating film are deteriorated, and a precipitate of Zr or Al—PO 4 may be formed, which is not preferable.
有効Fイオンの供給源としてはHF、NA4F、NH4HF2、Na
F、NaHF2等であり、その配合量は0.001g/リットル未満
であるとアルミニウムのエッチング反応がほとんど起こ
らず、皮膜が生成しない。Sources of effective F ions are HF, NA 4 F, NH 4 HF 2 , Na
F, NaHF 2 and the like, and when the blending amount is less than 0.001 g / liter, the etching reaction of aluminum hardly occurs and a film is not formed.
また、0.05g/リットルを越えると皮膜生成速度よりもア
ルミニウムのエッチング反応の方が大きくなって、皮膜
が生成し難くなる。On the other hand, if it exceeds 0.05 g / liter, the etching reaction of aluminum becomes larger than the rate of film formation, and it becomes difficult to form a film.
また、皮膜が生成しても耐沸水黒変性の、塗膜との密着
性が低下する。Further, even if a film is formed, the resistance to blackening by boiling water and the adhesion to the coating film are reduced.
尚、化成処理剤中で遊離せずフッ素イオンを放出しない
フッ素化合物は,有効フッ素イオンの供給源として不適
である。A fluorine compound that does not release fluorine ions in the chemical conversion treatment agent is not suitable as a source of effective fluorine ions.
次に、化成処理剤(B)はPHが1.5〜4.0であることが好
ましく、PHが1.5未満であるとアルミニウムのエッチン
グ反応の方が大きくなりすぎ、皮膜が生成し難くなり、
また、4.0を越えるとZr、V、Al−PO4の沈澱が生じやす
くなり、また、皮膜生成速度が遅くなり、満足な皮膜が
生成されない。Next, the chemical conversion treatment agent (B) preferably has a PH of 1.5 to 4.0, and when the PH is less than 1.5, the etching reaction of aluminum becomes too large, which makes it difficult to form a film.
Further, if it exceeds 4.0 Zr, it becomes V, the precipitation of the Al-PO 4 prone, also slows film generation speed, satisfactory coating is not generated.
PHの調整は、硝酸、硫酸等の無機酸及び水酸化ナトリウ
ム、水酸化カリウム等の金属水酸化物及びアンモニア水
等を用いて行うのが好ましい。尚、燐酸の使用も不可能
ではないが、化成処理剤(B)中におけるPO4イオンの
量が特定の範囲(0.01〜0.5g/リットル)に規定されて
いるので、前期範囲内でしかPH調整に燐酸を用いること
ができない。The pH is preferably adjusted using an inorganic acid such as nitric acid or sulfuric acid, a metal hydroxide such as sodium hydroxide or potassium hydroxide, or ammonia water. It should be noted that it is not impossible to use phosphoric acid, but the amount of PO4 ions in the chemical conversion treatment agent (B) is regulated within a specific range (0.01 to 0.5 g / liter), so PH adjustment is possible only within the previous period. It is not possible to use phosphoric acid.
Vイオンの供給源としては、VHO3、NH4VO3、NaVO3等の
ハナジン酸及びその塩、硫酸バナジル、シュウ酸バナジ
ル等のバナジル塩、VF5のようなハロゲン化物等であ
り、その配合量は0.01g/リットル未満であると耐沸水黒
変性、塗膜密着性が不十分である。Sources of V ions include hanazic acid such as VHO 3 , NH 4 VO 3 and NaVO 3 and salts thereof, vanadyl salts such as vanadyl sulfate and vanadyl oxalate, and halides such as VF 5 and their combination. If the amount is less than 0.01 g / liter, blackening resistance to boiling water resistance and coating film adhesion are insufficient.
また、1g/リットルを越えてもそれ以上の効果が期待で
きない。Moreover, even if it exceeds 1 g / liter, no further effect can be expected.
Zrイオンの供給源としては、H2ZrF6、(NH4)2ZrF6、Na
2ZrE6、K2ZrE6、Zr(NO3)4、ZrO(NO3)2、Zr(S
O4)2、ZrOSO4等であり、その配合量は0.01g/リットル
未満であると満足な皮膜が生成されない。The sources of Zr ions include H 2 ZrF 6 , (NH 4 ) 2 ZrF 6 and Na.
2 ZrE 6 , K 2 ZrE 6 , Zr (NO 3 ) 4 , ZrO (NO 3 ) 2 , Zr (S
O 4 ) 2 , ZrOSO 4, etc., and if the blending amount is less than 0.01 g / liter, a satisfactory film is not formed.
また、0.5g/リットルを越えるとそれ以上の効果が期待
できない。If it exceeds 0.5 g / liter, no further effect can be expected.
化成処理剤(B)におけるPO4イオンの供給源として
は、H3PO4、NaH2PO4、(NH4)H2PO4等であり、その配合
量は0.01g/リットル未満であると塗膜との密着性が低下
し、また、0.5g/リットルを越えると耐沸水黒変性、塗
膜との密着性が低下するうえ、Zr、V,Al−PO4の沈澱を
生成しやすくなる。有効Fイオンの供給源としてはHF、 NH4F、NH4HF2、NaF、NaHF2等であり、その配合量は0.00
1g/リットル未満であるとアルミニウムのエッチング反
応がほとんど起こらず、皮膜が生成しない。Sources of PO 4 ions in the chemical conversion treatment agent (B) include H 3 PO 4 , NaH 2 PO 4 , (NH 4 ) H 2 PO 4, etc., and their blending amount is less than 0.01 g / liter. Adhesion to the coating film decreases, and if it exceeds 0.5 g / l, boiling water resistance to blackening, adhesion to the coating film decreases, and Zr, V, Al-PO 4 precipitates easily form. . Sources of effective F ions are HF, NH 4 F, NH 4 HF 2 , NaF, NaHF 2, etc., and their blending amount is 0.00
If the amount is less than 1 g / liter, the aluminum etching reaction hardly occurs and the film is not formed.
また、0.05g/リットルを越えると皮膜生成速度よりもア
ルミニウムのエッチング反応の方が大きくなって、皮膜
が生成し難くなる。On the other hand, if it exceeds 0.05 g / liter, the etching reaction of aluminum becomes larger than the rate of film formation, and it becomes difficult to form a film.
また、皮膜が生成しても耐沸水黒変性、塗膜との密着性
が低下する。Further, even if a film is formed, resistance to blackening by boiling water and adhesion to the coating film are reduced.
尚、化成処理剤中で遊離せずフッ素イオンを放出しない
フッ素化合物は,有効フッ素イオンの供給源として不適
である。A fluorine compound that does not release fluorine ions in the chemical conversion treatment agent is not suitable as a source of effective fluorine ions.
本発明方法が短時間処理を可能にした理由は、脱脂剤に
燐酸及びその塩を加え脱脂能力とエッチングのバランス
を取ったことにより、化成処理後の耐沸水黒変性、塗膜
との密着性が良好な表面を得ることができる。また、化
成処理を比較的PHの低い領域で濃い濃度の化成処理剤を
適用することによるものと推定される。The reason why the method of the present invention enables short-time treatment is that by adding phosphoric acid and its salt to a degreasing agent to balance degreasing ability and etching, boiling water resistance after chemical conversion treatment, adhesion to coating film Can obtain a good surface. It is also presumed that the chemical conversion treatment is performed by applying a high concentration chemical conversion treatment agent in a region where the pH is relatively low.
本発明の方法を適用することができるアルミニウム又は
その合金としては、アルミニウム、アルミニウム−銅合
金、アルミニウム−マンガン合金、アルミニウム−ケイ
素合金、アルミニウム−マグネシウム合金、アルミニウ
ム−マグネシウム−ケイ素合金、アルミニウム−亜鉛合
金、アルミニウム−亜鉛−マグネシウム合金などを挙げ
ることができ、板、棒、線、管などの任意の形で処理す
ることができる。特に、アルミニウム製飲料缶に好適で
ある。Examples of aluminum or an alloy thereof to which the method of the present invention can be applied include aluminum, aluminum-copper alloy, aluminum-manganese alloy, aluminum-silicon alloy, aluminum-magnesium alloy, aluminum-magnesium-silicon alloy, and aluminum-zinc alloy. , Aluminum-zinc-magnesium alloy, etc., and can be processed in any shape such as plate, rod, wire, tube and the like. In particular, it is suitable for aluminum beverage cans.
前記の脱脂剤や化成処理剤の処理条件は脱脂剤の場合、
50〜80℃で4〜8秒間スプレーを継続することにより行
われ、その後水洗される。In the case of the degreasing agent, the processing conditions of the degreasing agent and the chemical conversion treatment agent are
It is carried out by continuing spraying at 50 to 80 ° C. for 4 to 8 seconds, and then washing with water.
また、化成処理剤の場合、30〜60℃で3〜7秒間スプレ
ーを継続することにより行われ、その後水洗、純水洗後
乾燥されて塗装に供される。In the case of a chemical conversion treatment agent, spraying is continued at 30 to 60 ° C. for 3 to 7 seconds, followed by washing with water, washing with pure water, drying and application.
実施例1〜16、比較例1〜14 アルミニウム板(JISA3004)に絞り−しごき加工を施し
て得られた缶本体を、表1−1、1−2、1−3、及び
1−4で示す組成の脱脂剤、及び条件でスプレー脱脂
し、水洗後、表2−1、2−2、2−3、及び2−4に
示した組成の表面処理浴、及び条件でスプレー処理し
た。次いで、水洗及び脱イオン水による洗浄を行い、オ
ーブン中で200℃で乾燥した(実施例1〜16)。乾燥後
の缶について、外観、脱スマット、脱脂性、耐沸水黒変
性及び塗料密着性を測定し、評価した。結果を表3−
1、3−2、及び3−3に示す。Examples 1 to 16 and Comparative Examples 1 to 14 Can bodies obtained by subjecting an aluminum plate (JIS A3004) to drawing and ironing are shown in Tables 1-1, 1-2, 1-3, and 1-4. The composition was degreased by spraying with a degreasing agent and conditions, washed with water, and then spray-treated with surface treatment baths and conditions shown in Tables 2-1, 2-2, 2-3, and 2-4. Next, washing with water and washing with deionized water were carried out, and drying was performed in an oven at 200 ° C (Examples 1 to 16). The dried cans were evaluated for appearance, desmutting property, degreasing property, blackening resistance against boiling water and paint adhesion. The results are shown in Table 3-
1, 3-2, and 3-3.
同様に、アルミニウム板(JISA3004)に絞り−しごき加
工を施して得られた缶本体を、表4−1、4−2、及び
4−3で示す組成の脱脂剤、及び条件でスプレー脱脂
し、水洗後、表5−1、5−2、及び5−3に示した組
成の表面処理浴、及び条件でスプレー処理した。次い
で、水洗及び脱イオン水による洗浄を起い、オーブン中
で200℃で乾燥した(比較例1〜14)。乾燥後の缶につ
いて、外観、脱スマット、脱脂製、耐沸水黒変性及び塗
料密着を測定し、評価した。結果を表6−1、6−2、
及び6−3に示す。Similarly, a can body obtained by subjecting an aluminum plate (JIS A3004) to drawing-ironing is spray-degreased with a degreasing agent having the composition shown in Tables 4-1, 4-2, and 4-3, and conditions. After washing with water, spray treatment was carried out under the surface treatment baths and the conditions shown in Tables 5-1, 5-2, and 5-3. Then, washing with water and washing with deionized water were carried out, and drying was performed in an oven at 200 ° C (Comparative Examples 1 to 14). The dried cans were evaluated for appearance, desmutting, degreasing, boiling water black resistance and paint adhesion. The results are shown in Tables 6-1, 6-2,
And 6-3.
[評価方法] 外見 乾燥後の容器の光沢、(白さ)を目視判定 ◎ やや光沢あり ○ 光沢過剰;光沢あまりなし × 光沢なし 脱スマット性 乾燥後の容器内面にテープを装着、剥離、汚染の程度に
応じて5段階評価 ◎ 汚染なし ○ 痕跡程度の汚染 △ 僅微な汚染 × 中等な汚染 ×× 多大な汚染脱脂性 脱脂性 乾燥後の容器内面の残留油分(μg/缶)を測定し、残留
量に応じて5段階評価 ◎ 10未満 ○ 10以上20未満 △ 20以上30未満 × 30以上40未満 ×× 40以上耐沸水黒変性 耐沸水黒変性 水道水沸水30分後の黒変度(缶底) ◎ まったく黒変なし ○ ごくわずかに黒変 △ わずかに黒変 × かなり黒変 ×× 完全に黒変 塗膜密着性 容器内面にエポキシフェノール系塗料、を塗布、焼付乾
燥(215℃×3分)して試料とし、水道水の沸水に60分
浸漬後、ゴバン目試験を起い残ったコマ数により5段階
評価 ◎ 100 ; ○ 90〜99 △ 80〜89 ; × 70〜79 ×× 70未満 発明の効果 本発明は過度のエッチングを防止することにより、極め
て短時間で、化成処理後の耐沸水黒変性、塗膜との密着
性が従来以上の品質を得ることができ生産性を大幅に向
上することができたものである。 [Evaluation method] Appearance Visually judge the gloss and (whiteness) of the container after drying ◎ Slightly glossy ○ Excessive gloss; No too much gloss x No gloss Desmutting property Attach tape to the inner surface of the container after drying, peeling, and contamination Five-level evaluation according to the degree ◎ No pollution ○ Trace-level pollution △ Minor pollution × Moderate pollution × × Great pollution Degreasing Degreasing Measure the residual oil content (μg / can) on the inner surface of the container after drying, Five-level evaluation according to the residual amount ◎ Less than 10 ○ 10 or more and less than 20 △ 20 or more but less than 30 × 30 or more but less than 40 × × 40 or more Resistance to boiling water black modification Resistance to black boiling water modification Black water 30 minutes after boiling water (can Bottom) ◎ No blackening at all ○ Slightly blackening △ Slightly blackening × Quite blackening × × Completely blackening Coating adhesion Adhesion of epoxy phenolic paint to the inner surface of the container, baking and drying (215 ° C × 3 Minutes) and use it as a sample. Five-stage evaluation based on the number of remaining frames ◎ 100; ○ 90 to 99 △ 80 to 89; × 70 to 79 × less than 70 The effect of the present invention The present invention prevents formation of excessive etching to form a film in an extremely short time. The boiling water resistance after treatment and the adhesion to the coating film were able to obtain higher quality than before and the productivity could be greatly improved.
Claims (2)
〜10g/リットルのPO4イオンと、0.1〜3g/リットルのア
ルミニウムキレート化剤と、0.1〜5g/リットルの界面活
性剤とを含有し、アルカリ金属水酸化物でpHを11〜13に
調整した脱脂剤を4〜8秒間スプレーすることにより脱
脂を行い、次いで (b)0.01〜0.5g/リットルのZrイオンと、0.01〜0.5g/
リットルのPO4イオンと、0.001〜0.05g/リットルの有効
Fイオンとを含有し、pHを1.5〜4.0に調整した化成処理
剤を3〜7秒間スプレーすることを特徴とする化成処理
方法。1. To (a) aluminum or an alloy thereof, 1
And PO 4 ions to 10 g / l, contains an aluminum chelating agent 0.1 to 3 g / l, and a surfactant 0.1-5 g / l, and the pH was adjusted to 11-13 with an alkali metal hydroxide Degreasing is performed by spraying a degreasing agent for 4 to 8 seconds, and then (b) 0.01 to 0.5 g / liter Zr ions and 0.01 to 0.5 g / liter.
A chemical conversion treatment method comprising spraying a chemical conversion treatment agent containing liters of PO 4 ions and 0.001 to 0.05 g / liter of effective F ions and having a pH adjusted to 1.5 to 4.0 for 3 to 7 seconds.
〜10g/リットルのPO4イオンと、0.1〜3g/リットルのア
ルミニウムキレート化剤と、0.1〜5g/リットルの界面活
性剤とを含有し、アルカリ金属水酸化物でpHを11〜13に
調整した脱脂剤で脱脂を行い、次いで (b)0.01〜1g/リットルのVイオンと、0.01〜0.5g/リ
ットルのZrイオンと、0.01〜0.5g/リットルのPO4イオン
と、0.001〜0.05g/リットルの有効Fイオンとを含有
し、pHを1.5〜4.0に調整した化成処理剤を適用すること
を特徴とする化成処理方法。2. To (a) aluminum or an alloy thereof, 1
And PO 4 ions to 10 g / l, contains an aluminum chelating agent 0.1 to 3 g / l, and a surfactant 0.1-5 g / l, and the pH was adjusted to 11-13 with an alkali metal hydroxide Degreasing is performed with a degreasing agent, and then (b) 0.01 to 1 g / liter V ion, 0.01 to 0.5 g / liter Zr ion, 0.01 to 0.5 g / liter PO 4 ion, and 0.001 to 0.05 g / liter. And a chemical conversion treatment agent having a pH adjusted to 1.5 to 4.0.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63072698A JPH0784665B2 (en) | 1988-03-25 | 1988-03-25 | Aluminum conversion treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63072698A JPH0784665B2 (en) | 1988-03-25 | 1988-03-25 | Aluminum conversion treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01246370A JPH01246370A (en) | 1989-10-02 |
| JPH0784665B2 true JPH0784665B2 (en) | 1995-09-13 |
Family
ID=13496843
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63072698A Expired - Fee Related JPH0784665B2 (en) | 1988-03-25 | 1988-03-25 | Aluminum conversion treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0784665B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6193815B1 (en) | 1995-06-30 | 2001-02-27 | Henkel Corporation | Composition and process for treating the surface of aluminiferous metals |
| JP4408474B2 (en) * | 1999-01-25 | 2010-02-03 | トピー工業株式会社 | Aluminum alloy substrate coating method and wheel |
| WO2000061835A1 (en) * | 1999-04-12 | 2000-10-19 | Toyo Kohan Co., Ltd. | Method for production of surface treated steel sheet, surface treated steel sheet, and surface treated steel sheet coated with resin comprising surface treated steel sheet and organic resin coating the steel sheet |
| JP2008038184A (en) * | 2006-08-03 | 2008-02-21 | Denso Corp | Surface treatment method of aluminum-based material, and corrosion resistant structure |
| JP5520439B2 (en) | 2007-11-01 | 2014-06-11 | 日本パーカライジング株式会社 | Method for producing surface-adjusted aluminum casting |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3236247A1 (en) * | 1982-09-30 | 1984-04-12 | Metallgesellschaft Ag, 6000 Frankfurt | METHOD FOR SURFACE TREATMENT OF ALUMINUM |
| US4497667A (en) * | 1983-07-11 | 1985-02-05 | Amchem Products, Inc. | Pretreatment compositions for metals |
-
1988
- 1988-03-25 JP JP63072698A patent/JPH0784665B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01246370A (en) | 1989-10-02 |
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