295605 五、發明説明(1 ) 本發明是一種有關於鋁或鋁合金的電解成灰色系列的 電解發色方法:在各種的鋁或鋁合金,使用交流電的電解 發色方法中,使之產生灰色系列的方法中,以使用鋅及錫 的金屬鹽類的合金是最易於操作及控制。 由於鋅及錫的氧化還原半電位(E ° )差距極大 Zn+2 + 2e_ 二 Zn E° 二-0.7628,Sn+2 + 2e_ = Sn Κ〇 二·〇· 136 若直接使用在陰極電解發色中要產生合金,在方法上有其 困難,爲了解決此困難點,我們朝著1.提升錫(Sn+2 )的氧 化還原半電位;2.降低鋅CZn+2 )的氧化還原半電位;3. 拉大鋅及錫的離子濃度比,來克服之。 在使用鋅錫合金的電解發色方法中,有英丨魂的專利C Brit· pat. 14 08859 )中,由於使用的硫酸亞錫在5克/升 以上,所以PH必需控制在1〜1 . 5之間方可產生灰色, 但由於PH的調整,使得電解液的電解度〔Conduct i vi ty;^-高,而使得使用該法帶產生1.表面硬質皮膜產生軟化濺落 ;2.顏色深淺變化快不利於生產中的控制。在生產上有其 困難。 經濟部中央榡爭局只工消費合作杜印^ 本方法的最大特點,在使用硼酸和硫酸鋅作用,生成 鋅的錯鹽後,而降低鋅CZn+2 )的氧化還原半電位,並提咼 Zn+ 2 /Sn + 2離子濃度比在8 : 1以上,並且盡量減少使用 過多的藥品,使電解液易於管埋及控制。 由於硼酸有其溶解度的限制,所以本方法由硼酸爲基 點,來求出其他組成份的使用量··硼酸在常溫下溶解度大 約在50克/升,但爲求操作上的方便,大部分採由30〜4〇 第一頁 本紙張尺度適用中國國家標準(CNS ) Λ4規格(2!()><297公缝) 經濟部中央標隼局員工消費合作社印製 A7 B7五、發明説明(2 ) 克/升由硼酸濃度來算出硫酸鋅(ZnS04 ·7Η2〇)使用濃度爲 50〜70克/升間,若再增加硫酸鋅濃度對於灰色的發色上 並無多大幫助,反而增加成本上的浪費,再由加大鋅/錫 濃度上,由Λ驗上得知硫酸亞錫的濃度應在5克/升以下 ,在生產上才能很容易的生產出均一灰色系列的電解鋁或 鋁合金。爲了增加電解發色時的抛力(Throwing power)我 們使用硫酸CH2S04) »爲了使在電解發色中電流分佈的均 勻,由實驗中,得知硫酸濃度應在10〜50克/升之間,若 少於11)克/升間會產生:1·著色不易;2.陰極效率過低; 3.著色不均勻;4.著色時間過長,若高於50克/升會產生 :1.氧化化皮膜鬆化;2.發色後水洗前有褪色現象。 因爲使用硫酸亞錫爲避免錫(Sn+ 2)的安定,故使用硫 酸亞錫安定劑,如多元有機酸CP〇ly base Carboxylic Acid)或芳香族有機酸(Aromatic Carboxylic Acid)、 磺酸(Sul f on ic Acid),其濃度大約在4克/升以下。 在操作條件上溫度可採用常溫操作,電流密度經多次 試驗,應在0·4〜1.4A/dm2之間,若低於0.4A/dm2時,因 發色時間過長會影響生產產量,若大於1 · 4A/dm2時,常 會使硬質皮膜破裂的缺點。 實施例: 例1. 鋁或鋁合金經:1.脫脂:在30 %硝酸脫脂、淸水洗; 2·鹼蝕(Etching) : 1〇 %氫氧化鈉鹸蝕,淸水洗;3.中和 :10 %硝酸中和,淸水洗;及4.陽極處理·· 18〇克/升硫 本紙張尺度適用中國國家標準(CNS > Λ4規格(210X297公嫠) 第二貝 A7 H7 崎满部屮失愫!?-局.,=^_消贫合作仆印製 A、發明説明(3 ) 酸溶液中18 °c直流電壓17 V,時間25分鐘陽極處理,淸水 洗等上述之前處理後,在如下的電解發色的槽液組成份及 方法,並使用交流電發色: 槽液組成份: 硼酸(h3bo3) 40 克/升 硫酸鋅CZnS04 ·7Η20) 60 克/升 硫酸 ch2so4) 25 克/升 硫酸亞錫(SnS04 ) 2.5 克/升 酒石酸(H00CCCH0H)2 C00H) 1. 5 克/升 發色條# : 對應電極:碳電極 溫度 :25 °C 電流密度:().8A/dm2 時間 :9分 著色外觀:呈現出極美的灰色外觀 例2. 前處理過程同例1. 槽液組成份: 硼酸 30 克/升 硫酸鋅 50 克/升 硫酸亞錫 3 克/升 硫酸 30 克/升 ΐ黃化水楊酸(Su 1 fosa 1 icylic Acid) 3 克/升 發色條件: 對應電極:不銹鋼電極 溫度 :25 °c 電流密度:0.7A/dm2 時間 :10分 , 本纸张尺度谪用中阈阈家標年(CNS ) AWUS ( 2丨Οχ 2()7公筇) 第三頁 A7 B7 五、發明説明(4) 著色外觀:呈現極美的灰色外觀 例3. 前處理過程同例1. 槽液組成份: 硼酸 硫酸鋅 硫酸亞錫 硫酸 檸檬酸(Citric Acid) 發色條件: 對應電極 電流密度 著色外觀 碳電極。 0.8A/dm 2 呈現極美的灰色外觀 30克/升 5〇克/升 1.5克/升 2〇克/升 3克/升 溫度:25 °C 時間:9分 ("尤閱ifil'::而之';,,;沾f'f!"-,A-'',;,本打) 經濟部中央標準扃負工消费合作社印製 本案與GB14 08 859案比較》如下表 • 到開始呈 現灰色所 需時間 由開始呈現 灰色到呈現 黑色間所需 時間 3» 明 ητυ 本 案 6分 12分 由於單位時間顏色變化小,在生 產岛,易於控制均一顏色 GB1408859 案 27分 3分 由於單位時間顏色變化大,在生 產時,不易控制均一顏色,且發 色時間過長,鋁的表面氧化皮膜 易於產生鬆化及脫落。 木氓择上度璃m中罔Η家樣牟(CNS ) Λ4忧格Ο丨0 X2^公鏵) 第四頁295605 V. Description of the invention (1) The present invention is an electrolytic color development method related to the electrolysis of aluminum or aluminum alloys into gray series: in various aluminum or aluminum alloys, the electrolytic color development method using alternating current is used to produce gray Among the series of methods, alloys using metal salts of zinc and tin are the easiest to operate and control. Due to the great difference between the oxidation-reduction half-potentials (E °) of zinc and tin Zn + 2 + 2e_ 2 Zn E ° 2 -0.7628, Sn + 2 + 2e_ = Sn Κ〇 二 · 〇 · 136 If used directly at the cathode electrolysis color To produce alloys in the process, there are difficulties in the method. In order to solve this difficulty, we are toward 1. Raising the redox half potential of tin (Sn + 2); 2. Decreasing the redox half potential of zinc (CZn + 2); 3. Increase the ion concentration ratio of zinc and tin to overcome it. In the electrolytic color development method using zinc-tin alloys, there is the British patent C Brit · pat. 14 08859), because the use of stannous sulfate is more than 5 grams / liter, so the PH must be controlled at 1 ~ 1. Between 5 and 5 can produce gray, but due to the adjustment of PH, the electrolytic degree of the electrolyte [Conduct i vity; ^ -high, and the use of this method band produces 1. The surface hard film produces softening splashes; 2. Color depth Quick changes are not conducive to control in production. There are difficulties in production. The Ministry of Economic Affairs of the Central Committee of the Central Committee of the Ministry of Economic Affairs and Labor Cooperation Du Yin ^ The biggest feature of this method is that after the use of boric acid and zinc sulfate to form the wrong salt of zinc, the redox half potential of zinc (CZn + 2) is reduced, and The Zn + 2 / Sn + 2 ion concentration ratio is above 8: 1, and the use of too many drugs should be minimized, making the electrolyte easy to embed and control. Since boric acid has its solubility limitation, this method uses boric acid as the base point to find the usage of other components. · The solubility of boric acid is about 50 g / L at room temperature, but for the convenience of operation, most of the From 30 to 40, the first page of this paper scale is applicable to the Chinese National Standard (CNS) Λ4 specification (2! () ≫ < 297 male sewing) Printed by the Ministry of Economic Affairs Central Standard Falcon Bureau Employee Consumer Cooperatives A7 B7 V. Description of the invention (2) g / l. The zinc sulfate (ZnS04 · 7Η2〇) is calculated from the boric acid concentration. The use concentration is between 50 and 70 g / l. If the zinc sulfate concentration is increased, it will not help the gray hair color, but will increase the cost. The waste of the above, and then by increasing the concentration of zinc / tin, it is known from the Λ test that the concentration of stannous sulfate should be below 5 grams / liter, and only a gray series of electrolytic aluminum or aluminum can be easily produced in production alloy. In order to increase the throwing power (Throwing power) during electrolytic hair coloring, we use sulfuric acid CH2S04) »In order to make the current distribution in the electrolytic hair color uniform, from the experiment, we know that the sulfuric acid concentration should be between 10 ~ 50 g / l, If it is less than 11) g / L, it will produce: 1. Coloring is not easy; 2. Cathode efficiency is too low; 3. Coloring is uneven; 4. Coloring time is too long, if it is higher than 50 g / L, it will produce: 1. Oxidation Loosening film; 2. Fading after hair color before washing. Because stannous sulfate is used to avoid the stability of tin (Sn + 2), stannous sulfate stabilizers are used, such as the polybasic organic acid CP〇ly base Carboxylic Acid) or aromatic organic acids (Aromatic Carboxylic Acid) and sulfonic acid (Sul f on ic Acid), its concentration is about 4 g / L or less. Under operating conditions, the temperature can be operated at room temperature. The current density should be between 0.4 and 1.4A / dm2 after multiple tests. If it is lower than 0.4A / dm2, the production time will be affected due to the long color development time. If it is more than 1.4A / dm2, it will often cause the hard film to break. Examples: Example 1. Aluminum or aluminum alloy: 1. Degreasing: degreasing in 30% nitric acid, washing with rubbing water; 2. Etching: Etching with 10% sodium hydroxide, washing with rubbing water; 3. Neutralization: Neutralized with 10% nitric acid, washed with water; and 4. Anodic treatment ·· 18〇g / liter of sulfur This paper standard is applicable to Chinese national standard (CNS > Λ4 specification (210X297 gong)) Second shell A7 H7 Qimanbei lost愫!?-局., = ^ _ Poverty-reduction cooperative printing A. Description of the invention (3) 18 ° c DC voltage 17 V in acid solution, anodizing for 25 minutes, washing with water, etc. After the above previous treatments, the following The composition and method of the electrochromic bath solution, and the color development using alternating current: The composition of the bath solution: Boric acid (h3bo3) 40 g / l zinc sulfate CZnS04 · 7Η20) 60 g / l sulfuric acid ch2so4) 25 g / l subsulfuric acid Tin (SnS04) 2.5 g / l tartaric acid (H00CCCH0H) 2 C00H) 1. 5 g / l color bar #: Corresponding electrode: carbon electrode temperature: 25 ° C current density: (). 8A / dm2 time: 9 minutes coloring Appearance: presents a beautiful gray appearance Example 2. The pretreatment process is the same as Example 1. Composition of bath solution: Boron 30 g / l zinc sulfate 50 g / l stannous sulfate 3 g / l sulfuric acid 30 g / l l Yellow 1 salicylic acid (Su 1 fosa 1 icylic Acid) 3 g / l Hair color condition: Corresponding electrode: stainless steel Electrode temperature: 25 ° c Current density: 0.7A / dm2 Time: 10 minutes, this paper uses the middle threshold threshold standard year (CNS) AWUS (2 丨 Οχ 2 () 7 Gongqi) Third page A7 B7 V. Description of invention ( 4) Coloring appearance: presenting a beautiful gray appearance Example 3. The pre-treatment process is the same as Example 1. Composition of bath solution: Zinc borate sulfate stannous sulfate citric acid Color development condition: Corresponding electrode current density color appearance carbon electrode . 0.8A / dm 2 presents a beautiful gray appearance 30g / l 50g / l 1.5g / l 20g / l 3g / l Temperature: 25 ° C Time: 9 minutes (" 尤 读 ifil ':: And '; ,,; dip f'f! &Quot;-, A-' ',;, Ben)) The case printed by the Ministry of Economic Affairs Central Standards Consumer Labor Cooperative and the case of GB14 08 859 "as shown in the table below The time required to display gray from the start of gray to black 3 »Ming ητυ 6 minutes and 12 minutes in this case because the color change per unit time is small, and it is easy to control the uniform color on the production island GB1408859 27 minutes and 3 minutes in the case due to the color per unit time The change is large. It is difficult to control a uniform color during production, and the color development time is too long. The aluminum oxide film is prone to loosening and falling off. The hooligan chooses to go to the top of the glass m in the 罔 Η family like Mou (CNS) Λ4 worry grid 丨 丨 X2 ^ Gonghua) Page 4